Projections of Demand for Hazardous Waste
Management Capacity in Alaska, Idaho, Oregon,
and Washington: 1989, 1995, and 2009
Technical Appendix
Submitted To:
U.S. Environmental Protection Agency, Region X
and the States of
Alaska, Idaho, Oregon, and Washington
Submitted By:
APOGEE RESEARCH, INC.
4350 East West Highway
Bethesda, MD
1425 4th Avenue
Seattle, WA
October 1989
-------
List of Appendices
Appendix A: Economic Projections by State
Appendix B: Waste Reduction Matrix
Appendix C: Results of Statistical Analysis for Washington and
Oregon
Appendix- D: Engineering Analysis Profiles
Appendix E: WM Form Analysis
Appendix F: Groundtruthing Results
Participant Letter Describing Process
List of Participants
Summary of Results
Appendix G: Summary of One-Time Waste Analysis
Appendix H: Summary of Small Quantity Generator Analysis
Appendix I: Household Hazardous Waste Projections
EPA Headquarters Library
-------
APPENDIX A
Economic Projections by State
-------
Stale ol ALASKA
Oulpul Forecasts
1987. 1989. 1995, 2009
ALASKA OUTPUT FORECASTS: SUMMARY AND CALCULATIONS
SUMMARY: OUTPUT = EMPLOYMENT TIMES U.S. OUTPUT PER EMPLOYEE TIMES RELATIVE PRODUCTIVITY
INDUSTRY NAME
1 987
1 989
1995
2009
1 3
131
138
1 S
1 54
1 6
162
28
29
35
353
36
4 4
444
45
4S1
46
48
481
49
491
50/51
517
55
551
72
721
73
75
753
Oil and Gas Extraction
Crude Petroleum and Natural Gas
Oil and Gas Field Services
General Building Contractors
Nonresidenlial Buildmg Construction
Heavy Construction Contractors
Heavy Construction exc Highway
Chemicals and Allied Products
Petroleum and Coal Products
Machinery exc Elee
Construction and related Machinery
Etec Equipment and Supplies
Water Transportation
Transooriation on Rivers and Canals
Air Transportation
Certified Air Transportation
Pipelines esc. Natural Gas
Communication
Telephone Communication
Elec . Gas, Sanitary Services
Electric Services
Wholesale Trade
Petroleum and Petroleum Products
Auto Dealers and Service Stations
New and Used Car Dealers
Personal Services
Laundry, cleaning and garment services
Business Services
Auto repair, services and garages
Automotive Repair Shops
SI ale and Local Government
Federal Government
Military
19910148682
19127538337
2746872399
1439787114
938657860
757598376
424921111
132361598
4104584083
7966017
1836618
1781527
193531883
4390656
521329049
277738727
470968210
331318582
172721860
321738585
203798802
572431603
40992841
137649043
59151218
229802110
91417972
94923416
285684325
184810414
1645293812
1277703626
29848
23124143183
22217108865
3248910744
2211643805
1408203481
632705441
347384340
124773221
4858554053
6828589
1520630
1768886
191663351
4348265
485930475
258880091
495395895
327539143
95059054
311908383
196055285
564406615
40251894
133960450
S83S649S
24S27230S
98135124
104487533
284145080
193S44964
1592493294
1170128465
29848
24639499615
24216755229
4451839084
2050693005
1289140244
397065640
203911596
89466490
6838017850
13070033
2475913
1760236
221147793
5017178
581242285
309657582
57830S126
413693346
124040859
291558183
191964623
595317580
41930269
142017904
64380207
315710160
95523894
131908339
317036148
188904458
1605611340
1312681681
29848
23209492188
22588619324
6638782860
1331940643
782983122
218446927
94088128
63557207
13792460145
27166004
3882654
1997556
294370475
6678380
728101238
387896879
534270011
592824530
221867226
207795483
149462331
S545S18S5
37915474
130955142
64773565
485166422
86981075
269135494
370273007
213822949
1529554329
1530721019
29848
GROWTH COEFFICIENTS
1987 1989 1995 2009
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
.
.
.
.
0
0
0.
1
0
0
0
0
0.
0.
0
1
0
0
0.
0
0
0
0
0
1.
1.
1
0
1
0
0
1
1614
1615
1828
5361
5002
8351 C
8175 C
9427 C
1837 1
8572
8280
9929
9903
9903
9321
9321
0519
9886
5504 (
9694 (
9620 (
9860
9819
9732
9866
0673
0735
1008
9946
0473
9679
9158
0000
2375
2661
6207
4243
3734
) 5241
) 4799
1 6759
6659
6407
3481
19880
1427
.1427
1149
1149
.2279
.2486
>.7182
>.9062
>.9419
0400
0229
.0317
0884
.3738
0449
3896
1097
.0222
J.9759
.0274
0000
1
1
2
0
0
0
0
0
3
3
2
0
0
0
0
0
1
2
0
2
1
1
0
1
1
1657
1809
4169
9251
8342
2883
2214
4802
3603
4102
1140
1213
5210
5210
3966
3966
1344
7893
2845
6459
7334
9688
9249
9514
0951
1112
9515
83 53
2961
1570
9297
.1980
0000
Note: meaningful output estimates for federal military are unavailable. Therefore, only employment Is presented.
-------
Output r-orecasls 19B/. 1989. 1995. 2009
IDAHO OUTPUT FORECASTS. SUMMARY AND CALCULATIONS
SUMMARY: OUTPUT = EMPLOYMENT TIMES U.S. OUTPUT PER EMPLOYEE TIMES RELATIVE PRODUCTIVITY
SIC
CODE
O7
072
076
1 0
106
24
249
26
27
275
28
287
29
34
344
345
348
035
352
357
36
367
371
40
46
49
50.51
501
517
519
55
72
721
73
739
75
753
82
821
INDUSTRY NAME
Agnc , Forestry. Fishery Service;
Crop Services
Farm Labor and Management Services
Metal Mining
Ferroalloy ores except Vanadium
Lumber and wood products
Miscellaneous wood products
Paper and allied products
Printing and publishing
Commercial Printing
Chemical and allied products
Agricultural chemicals
Petroleum and coal products
Fabricated melal products
Fabricated Structural Melal Products
Screw Machine Products. Bolts, etc
Ordnance and Accessories. NEC
Machinery except eleclncal
Farm and Garden Machinery
Otlice and Computing Machines
Electric and electronic equipment
Electronic Components and Accessones
Motor vehicles and equipment
Railroad transportation
Pipelines except natural gas
Electric, gas. and sanitary services
Wholesale trade
Motor Vehicles 4 Automotive Equipment
Petroleum and Petroleum Products
Mise Nondurable Goods
Automotive dealers and service stations
Personal services
Laundry, Cleaning, and Garment Services
Business Services
Misc Business Services
Auto repair, services, and garages
Automotive Repair Shops
E ducal lonal services
Elementary and Secondary Schools
Slate and local government
Federal civilian government
Federal military
1987
414249673
252476906
10037562
280127S02
60999289
974869922
18375732
554655489
313728371
156092974
2077738941
564038794
3830349
845326128
356305647
14963851
372304751
1901292191
144429549
2425550624
1316071165
804206452
532046835
524567392
6741907
2246679907
997329641
56612535
67682808
140023732
267582608
231279456
72260977
131489746
571048272
358646390
93604130
77857752
182733006
3954181835
955103901
11251
1989
391100769
250857121
10660092
311826895
72278281
964077874
17969873
601456907
320254061
169342200
2346746714
645734517
4006941
883635417
369442847
12947026
364916453
2168S39277
169503095
2863722007
14S5743480
921827982
558269296
558035043
6782779
2325118847
979810243
54901561
64801612
135919353
267278574
249161759
79545023
184662746
710522883
325886223
86492819
86898950
197838468
3846818724
934019814
11251
1 99S
522954130
385528025
14253971
388633080
106443767
930041837
18913863
813485211
415281632
257718648
2990694130
972169374
4060441
1062670331
498S70783
15269279
480006076
3686265195
247178083
5664075993
2086510295
1348336861
774417695
628576638
8091319
2681638449
1015600689
54678982
61906459
135769937
310016402
328380662
83871678
183644486
675616316
433616030
89588891
91267401
226914067
3695031181
994821215
11251
2009
850278298
816898713
23175727
313642933
116716862
864462544
21912868
1435013563
673344978
579416439
5695137661
1784SS5802
4105140
1495853026
795313160
21490239
799186981
9362162872
524364903
16440793494
3967599952
2479219418
1449668010
794658559
7513677
3509433228
840892698
40968462
41090729
102533730
392230714
560023585
106087731
395498440
706901378
589735329
80712582
116691156
296699387
4136410528
1105166807
11251
GROWTH COEFFICIENTS
1987 1989 1995 2009
0
0
1
1
1
0
0
0
0
1
0
0
0
0
0
1
1
1
1
0
0
1
1
0
0
1
944
994
062
113
IBS
989
.978
084
021
.085
.129
145
.046
.045
037
.865
.980
.141
174
.181
.106
.146
.049
064
.006
.035
.982
970
957
971
999
077
101
404
.244
.909
924
116
.083
973
978
000
1
1.
1
1.
1
0.
1
1
1.
1.
1
1.
1
1.
1.
1.
1.
1.
1.
2.
1.
0
0
0
1
1
1
1
1
1
0
1
1
0
1
1
262
527
420
387
745
954
029
467
324
651
439
724
060
257
399
020
289
939
711
335
585
677
456
198
200
194
018
966
915
970
159
420
161
397
183
209
957
172
242
934
042
000
2
3
2
1
1
0
1
2
2
3
2
3
1
1
2
1
2
4
3
6
3
3
2
1
1
1
0
0
0
0
1
2
1
3
1
053
236
309
120
913
887
192
587
146
712
741
164
072
770
.232
.436
.147
924
.631
.778
015
083
725
515
114
.562
843
724
.607
.732
466
.421
.468
.008
.238
.644
.862
.499
.624
046
.157
000
Note meaningful output forecasts are unavailable for federal military. Therefore, only employment figures are presented.
-------
Ompui Forecast* OREGON
OulDUl Foreeaill 1987. 1989. 1095. 2008
OREGON OUTPUT FORECASTS
OUTPUT = EUPLOYUENT TIMES US. OUTPUT PER EMPLOYEE TIMES RELATIVE STATE PRODUCTIVITY
SIC INDUSTRY NAME
CODE
242 Sawmill! and Plining Mills
2 4 3 . 2 4 ( Mittwort Plywood, and Wood Products, nee
261.264 Paper Producii
2 B 1 Industnal Inorgane and Organic Chemicals
2 8 i Paints and Allied Producii
287 Agncullural Chemicals
281 Chemeal Products nee
307 Plastic Products
322 Glau
3 3 1 Blaal Furnaces And Basic Sleel Product «
331,336 Primary Aluminum And Aluminum Products
334.336 Pnrrury Nonlarrous Metals and Producii. nee
3 4 1 Metal Containers
342 Cuilery Tools ana General Hardware
344 Faanealed Slruclural Melal Products
347 Fafincaled M>tal Proaucts nee
353 Construction. Mining, and Oinield Mactiinery
358 Service Industry Machines
3 6 1 Eleclnc Transmisann Equipment
367 Electronic Componenis
369 Eleenrical Machinery and Equipment, nee
3 7 1 Motor Vehicle!
372 Aircrall
373 Ship and Boat Building
374 Railroad Eguomen
382 Scienlitic and Controlling Instruments
382 Eleclnc Transmission Equomenl
386 Photographic Eqmpmen and Supplies
421.423 IrucH Transportalnn
471 Transportation Services
4 9 1 Eleclnc Utilities. Public and Private
495 Water and Sanitary Services, deluding Public
508.518 Wholesale Trade
5 2 3 , 5 S 1 Reiajl Trade eicept eating and dnnkjng
739,769 Business Services nee
769 Personal and Repair Services
821,822 Educational Services
8 6 1 Nonprolrl Organizations
899 Personal Services, nee
SIC CODE EQUIVALENTS
242
243. 2448. 245. 249
21 |eic. 265)
281 (eie 28195). 288S 2889
285
287
2861. 289
307
321-323
331
3334, 28195. 3353-55. 3361
3332. 3333. 3339. 334. 3356
341
342
344
347. 349
3531-3533
358
3S1. 3825
367
369
371
372. 376 (eic 3761)
373
374
381. 362 (aic 3825)
381. 3825
386
42 pan ol 4789
47 (etc 474 and pan ol 4789)
491, pan ol 493
49 (etc 491 492. and pan ol 493)
50. SI
52 57. 59. 7396. par! ol 8042
73 (aic 731.7396) 7692. 7694. part Ol 7699
72 (eie 723.724). 76 (eic 7892.7694. pi 7699)
62 633. 835
632. 839, 64, 18, 6922
61. 69 (eic 8922)
OUTPUT
1987
1573981045
2559932759
1372053441
SSSS9620
48664777
21510026
62092462
261039509
89212796
29726S054
282633378
377756376
123124894
18S589770
278169421
222177678
180583218
62895390
227278908
470155304
71678179
598626539
155637253
179794469
242569
235815931
248347649
357014000
1462724930
163511047
1022859563
48326221
4378257286
3928176487
2029487574
728092428
315112190
688541049
1768837350
(1982 Dollar e)
1989
1418946159
2649890743
1326212516
63428784
49573352
22039941
60S50S34
326377966
91895236
303903961
339460662
4019S9476
120404584
195076954
287221926
232737311
I926B42S7
6966S145
234015180
555729096
81373183
635116935
143976817
164926868
193913
254153604
255053147
376919611
1468766002
167668488
1002463187
48965340
4483673953
3964705262
2250790816
712739SS9
340049018
700622581
1772225551
1995
1601836708
2516980991
1364126316
61179654
50919623
26041426
68935732
535960414
105109591
315133806
437877167
518665606
131799568
239216915
393707151
295846785
279783607
111068S70
321632074
938556067
123154330
603167715
128412384
143468329
197270
408850860
3S6661768
5S6966654
1674034404
214198950
1132191536
51642938
574254IS4S
4975564050
2607453306
893046974
476167331
859741798
2147991378
GROWTH COEFFICIENTS
2009 1987 1989 1995 2009
1449508296
2312032635
879385413
57850332
44225642
22427212
66619253
1077997113
124477882
278026864
632591265
711123472
113806621
309276867
533058897
376309278
426746680
207660121
362534652
1586339498
183753174
1166684133
117400697
87478826
177274
790900488
546702083
1024653674
1764858337
243125646
1106911027
40566505
834S6S0964
6454060017
4199557988
1143022726
722807609
1022712246
2306002201
0.9002 1.0177 0 9209
1 0351 0 9832 0 9032
0 9681 0.9942 0 6409
09611 1.1012 1.0412
0167 1.0463 0 9088
0241 1.2107 1 0426
.9752 1.1102 1 0729
.1613 1.9071 3 6357
.0301 1.1782 1 3953
.0223 1 0601 0 9286
2002 1 5475 2 2366
0641 1 3730 1.8957
9779 1 0705 0 9243
0511 1 2890 1 6665
0326 1 4154 1 9163
.0475 1.3316 1 6937
.0670 1.5493 2 3742
.1076 1.7659 3 3020
.0296 1 4151 1.5951
.1620 1.9913 3 3741
.1353 1.7182 2 5636
.0606 1 3413 1 9486
0 9251 0 6251 0 7543
0 9173 0.7980 0 4865
0.7994 0 8133 0 7306
1 0778 1.7329 3 3539
1 0353 1 4476 2.2192
1 0558 1 5601 2 8701
1.0041 1 1445 1 2066
1 0254 1.3100 1 4869
0 9801 1 1069 1 0822
1 0569 1 1147 0 6757
1 0241 1 31 IS 1 9062
1 0093 1 2666 1 6430
0 9954 0 9818 0 9496
0 9789 1 2266 1 5699
1 0791 1 511 1 2 2936
1.0205 1.2523 1 4897
1 0019 1.2144 1 3037
-------
Oulpul Forecasts 1987. 1989. 1995 2009
WASHINGTON OUTPUT FORECASTS
OUTPUT » EMPLOYMENT TIMES U 5 OUTPUT PER EMPLOYEE TIMES RELATIVE STATE PRODUCTIVITY
SIC CODE
INDUSTRY NAME
SIC CODE EQUIVALENTS
IB87
1989
1991
2009
GROWTH COEFFICIENTS
1 967 1989 1 9B5
2009
172
240
241
242
243
284
265
281
282
283
285
287
289
291
307
321
324
331
332
335
341
347
349
3S4
357
3S9
366
367
367
369
376
373
375
381
399
401
41 1
423
446
458
481
491
508
593
721
739
753
822
Construction
Loggng
Sawmills and Planing Mini
Millwork Plywood and Wood Products, noc
Wooden Containers
Paper Products
Paper board
Plastics Materials and Synthetic Rubber
Drugs
Paints and Allied Products
Indusiria! and Inorganic Chemicals
Agricultural
Chemical Products, nee
Petroleum Refining and Related Products
Plastic Products
GtBS
Cement and Concrete Products
Blast Furnaces and basic Steel Products
Iron and steel Foundnes and Forges
Prmary Aluminum and Aluminum Products
Pnmary Nonlerrou* Metals and Products, nee
Metal Containers
Metal Stampings
Fabricated Metal Products
Metalwork Machinery
Typewriters am ollca Equpmenl
Noneiectncal Machinery
Telephone end Telegraofi apparatus
Radio and Communication equipment
Electronic Components
Eleancal Machinery and Equipment, nee
Aircrall
Ship end Boat Building
Motorcycles Bicydes and pans
Soentilic and Controlling instruments
Manufactured Products, nee
Railroad Transportation
Local Transit and Intercity Bus
Truck Transportation
Water Transportation
Air Transportation
Communcaltons. escept Radio and TV
Electric Utilities. Public and Private
Wholesale Trade
Retail Trade, eicepl eating and dnnking
Business Services, nee
Automobile Repair
Educational Services
Personal Services, nee
Personal and Repair Services
Stale and Local Government
Federal Government
Military
Pans ol 15.16.17
241
242
243. 2448. 245. 249
244 (eic 244B)
26 (esc 265)
28S
2B21-2B22
283
285
281 (eic 28195). 2865/2869
2B7
2861. 289
29
307
321-323
324. 327
331
332. 339. 3462
3334. 28195. 3353-55. 3361
3132. 3333. 3339. 334. 3356, 3369. 3463
341
346 (etc 3462-3463)
347. 349
354
357 (e«C. 3573-3574)
359
3661
3662
367
389
372. 376 (axe. 3761)
373
375
381. 382 (QIC. 382S)
395. 398 (axe. 3981). 399 (axe. 39996)
48. 474. part ol 4 789
41
42. pan Ol 4789
44
45
48 (exc 483)
491. part Ol 493
50.51
52-57. 59. 7398. part ol 8042
73 (exc. 731, 7396). 7692, 7694. part ol 7699
75
82. 833. 835
81. 89 (eic 8922)
72 (BXC723.724). 76 |aic7692.7694. pi 7699)
2824863354
1849889077
1004904414
1104987623
33259392
2110523728
232385721
15293349
47922115
81753760
1772167119.
96135100
64064847
1805235699
410066350
132S70BSS
362823284
248354961
99382869
1369050151
263708428
168375928
31851244
181359406
39826387
54755827
1B8979S46
142833090
112209917
357180898
66054577
8910310956
1408345583
6677438
218776976
125508413
595653547
168186923
1572273184
1783928777
1263140654
1972717387
847013331
6809401197
6695594887
3856822114
2149491646
429932010
4530154418
1438292746
26059247796
7075361231
82663
2574421400
1593313858
886511862
1121050407
29388163
2072834495
233135172
72B42B17
50SBS677
85901800
1902768730
104863762
64704635
1795002494
475410221
133593639
367897768
227842195
95808255
1474820069
255076739
159225264
36482234
183762608
44253362
62127910
201634824
1628BOS24
1210S6839
418980627
74583673
9457525011
1482225409
7242143
279378005
140256495
591131122
185122199
1626549843
1800750067
1258230723
2045982163
86342224S
6938681004
672S10S764
4219177892
2164451442
449744595
4646656046
1437228885
25298613623
8929124592
83490
2678653443
1665171094
957362670
1017619282
23933416
2242429B24
238006966
90365074
71453939
97649644
2751455486
145692946
81984720
1808419095
774478657
144365751
413381098
180271181
93106439
1450281324
255935473
156827304
39049410
210012282
84864926
87896823
282454065
286226328
222068635
705741605
112905312
12316640141
1883292014
9362057
539346558
190504872
600130044
186730842
1999S56976
2296S03B2S
1572283045
2984321S2S
10B95318B9
8710291734
8192639036
5011022395
2SSS851867
583396097
5977911630
1914297099
23789010048
7411989584
83490
2268182214
1584417305
7818SOSS6
844240569
14133689
1671098246
206494398
144865353
112820639
114701121
3808313834
175356647
1076S77B7
1646117676
1509968351
150973231
411415490
88687627
63431006
1177566222
199316483
105403196
40463899
207886753
106124736
120569554
453815364
571444398
440681106
1265802331
179058337
24534530092
2500562470
20577916
1054459375
257613973
687734393
174776894
2486036164
3314658 557
1718754941
4599959593
1438225268
12066156687
9744732513
6589559524
3405469991
767707781
7096471537
2B444S22SO
24631874708
8315153425
85390
0 9808 1 0205 0 8641
0 9657 1 0093 0 9482
0 8822 0 9527 0 7780
1 0145 0 9209 0 7640
0.8836 0 7196 0 4250
0 9821 1 0625 0 7918
1 0032 1 0242 0 8886
1 1156 1 3840 2 2187
1 0556 1 4910 2 3542
1 0507 1 1944 1.4030
1.0737 1 5526 2.1490
1.0908 1 5155 1 8241
1.0100 1 2797 1 6805
0 9943 1 0016 0 9119
1.1593 1 8887 3 6823
1.0077 1 0890 1 1388
1.0140 1.1393 1 1339
0 9174 0 7259 0 3571
0 9640 0 9368 0 6383
1 0773 1 0593 0 8601
0 9673 0 9705 0 7558
0 9457 0 9314 0 6260
1.1454 1 2260 1 2704
1 0133 1 1580 1 1463
1 1112 1 6287 2 6647
1 1346 1 6053 2 2019
1 0670 1 4946 2 4014
1 1404 2 0039 4 0008
1 0788 1 9790 3 9273
1.1730 1 9759 3 5439
1 1291 1 7093 2 7107
1 0614 1 3823 2 7535
1 0525 1 3372 1 7755
1 0846 1 4020 3 0817
1 2770 2 4653 4 8198
1 1175 1 5179 2 0526
0 9958 1 0075 1546
1.1007 1.1103 0392
1 0345 1 2718 5812
1 0094 1.2873 8581
0 9961 1.2447 3607
1.0371 1 5128 2 3316
1 0194 1 2863 6980
1 0190 1 2792 7720
1 0044 ~1.2236 4554
1 0940 1 2993 7034
1 0070 1 1890 5843
1 0461 1 3569 .7856
1 0257 1 3196 5665
0.9993 1 3310 9777
0 9708 0 9129 9452
1 0 9793 1 0476 1752
1 1 0100 1 0100 0330
Note Meaningful output ((limits* lor the mlllliry are univillibU; th« figures provided tr» employment.
-------
APPENDIX B
Waste Reduction Matrix
-------
SIC P WASTE
TONS
APPENDIX 8
Matrix of Waste Reduction Factors Used in Projections
LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
0726
0726
0726
0726
0726
0726
0851
0912
0912
0912
0912
1041
1041
1041
1041
1041
1041
1041
1041
1041
1041
1041
1041
1263
1263
1301
1407
1521
1542
1542
1542
1542
1542
1542
1542
1542
1542
1542
1542
1582
1582
1600
1600
1600
1600
1611
1611
1611
1611
1611
1611
1611
1611
1611
1622
1623
0001
F003
F005
U002
U159
UT02
UT02
D001
0002
0007
0008
0001
P010
P012
P022
P029
P030
P106
U044
U114
U135
U211
UC02
F003
F005
W001
F001
0002
0001
0002
0008
F001
F003
F005
U080
U220
WP01
WP02
WT02
D001
F002
0001
0002
F002
WP01
0001
0006
0007
0008
F001
F003
F007
UT01
UT02
0005
0001
3.05
3.96
3.79
0.17
1.31
11.53
1.06
15.35
2.66
2.66
2.66
0.02
0.00
0.00
0.00
0.00
0.00
0.00
0.01
0.00
0.00
0.00
0.00
0.19
0.19
0.24
3.96
0.53
2.00
0.15
2.03
1.36
1.91
0.73
0.36
0.09
0.36
1.20
1.51
0.64
0.02
0.50
1.09
0.04
0.04
5.04
2.75
6.08
6.21
12.51
0.57
0.00
0.57
0.13
37.71
0.24
0.01
0.01
-0.01
0.01
0.01
0.01
0.01
-0.01
-0.04
0.05
-0.01
-0.01
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
0.10
0.10
-0.10
-0.10
-0.04
-0.01
-0.01
-0.05
0.01
0.61
-0.01
-0.61
-0.01
0.01
-0.01
0.01
-0.01
0.01
0.02
0.04
0.01
-0.01
-0.01
-0.01
0.04
-0.01
-0.02
-0.01
-0.09
-0.04
-0.01
-0.01
-0.01
0.07
-0.05
-0.01
-0.00
-0.01
-0.02
-0.01
-0.02
-0.02
-0.02
-0.01
-0.01
-0.05
-0.05
-0.06
-0.03
-0.05
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.05
-0.01
-0.02
-0.08
-0.09
-0.63
-0.02
-0.63
-0.03
-0.09
-0.01
-0.02
-0.02
-0.02
-0.04
-0.08
-0.01
-0.05
-0.03
-0.05
-0.05
-0.03
-0.04
-0.05
-0.12
-0.06
-0.02
-0.09
-0.01
-0.10
-0.07
-0.01
-0.01
-0.05
-0.02
-0.04
-0.03
-0.02
-0.02
-0.03
-0.03
-0.11
-0.07
-0.10
-0.08
-0.11
-0.15
-0.15
0.15
-0.15
0.15
-0.15
-0.15
-0.15
-0.15
0.15
-0.06
-0.04
-0.03
-0.12
-0.18
-0.66
-0.07
-0.66
-0.08
-0.18
-0.04
-0.03
-0.05
-0.05
-0.08
-0.11
-0.03
-0.11
-0.07
-0.11
-0.07
0.07
-0.08
-0.11
0.17
-0.10
-0.09
-0.18
-0.04
-0.13
-0.09
-0.03
-0.10
-0.11
-0.03
0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.12
-0.06
-0.04
-0.03
-0.14
-0.14
-0.14
-0.14
0.14
0.14
0.14
0.14
-0.14
0.14
0.12
0.03
-0.03
0.31
0.06
-0.62
-0.03
-0.62
0.04
0.06
-0.02
-0.03
-0.02
-0.02
-0.12
-0.21
-0.03
-0.03
-0.04
-0.03
-0.12
-0.04
-0.12
-0.03
-0.11
-0.05
-0.03
-0.06
-0.03
-0.22
-0.05
-0.03
-0.01
-0.03
-0.06
-0.06
-0.06
-0.06
-0.06
-0.05
-0.05
-0.14
-0.16
-0.09
-0.08
-0.14
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.16
-0.06
-0.06
-0.39
-0.15
-0.65
-0.06
-0.65
-0.08
-0.15
-0.03
-0.06
-0.05
-0.05
-0.17
-0.30
-0.05
-0.14
-0.09
-0.14
-0.16
-0.09
-0.17
-0.14
-0.17
-0.08
-0.06
-0.15
-0.06
-0.26
-0.10
-0.05
-0.02
-0.14
0.07
0.14
-0.09
0.07
0.07
0.09
0.09
0.29
-0.20
-0.17
-0.22
-0.29
-0.24
0.24
0.24
-0.24
0.24
0.24
0.24
0.24
-0.24
0.24
0.20
0.14
-0.09
0.47
-0.26
-0.68
-0.21
-0.68
-0.22
-0.26
-0.11
-0.09
-0.16
-0.16
-0.28
-0.39
-0.09
-0.29
-0.21
-0.29
-0.20
-0.21
-0.28
-0.29
-0.28
-0.19
-0.25
-0.26
-0.14
-0.30
-0.15
-0.09
-0.30
-0.29
0.07
-0.08
-0.07
-0.07
-0.07
-0.06
-0.06
-0.10
-0.30
-0.10
-0.10
-0.10
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.30
-0.08
-0.07
-0.67
-0.14
-0.65
-0.08
-0.65
-0.10
-0.14
-0.04
-0.07
-0.06
-0.06
-0.23
-0.41
-0.06
-0.10
-0.10
-0.10
-0.30
0.10
-0.23
-0.10
-0.17
-0.09
-0.08
-0.14
-0.08
-0.48
-0.10
-0.06
-0.03
-0.10
-0.14
-0.17
-0.12
-0.14
-0.14
-0.10
-0.10
-0.25
-0.40
-0.14
-0.17
-0.25
-0.26
-0.26
-0.26
-0.26
-0.26
-0.26
-0.26
-0.26
-0.26
-0.26
-0.40
-0.17
-0.12
-0.74
-0.24
-0.69
-0.15
-0.69
-0.17
-0.24
-0.08
-0.12
-0.12
-0.12
-0.30
-0.57
-0.10
-0.25
0.19
-0.25
-0.40
-0.19
-0.30
-0.25
0.25
-0.13
-0.14
-0.24
-0.17
-0.53
-0.20
-0.10
-0.05
-0.25
-0.19
-0.40
-0.20
0.19
0.19
-0.19
-0.19
-0.47
0.50
0.31
-0.54
-0.47
-0.37
-0.37
-0.37
-0.37
-0.37
0.37
-0.37
-0.37
-0.37
0.37
-0.50
-0.40
-0.20
-0.80
-0.38
0.74
-0.54
-0.74
0.54
0.38
-0.28
-0.20
-0.41
-0.41
-0.53
-0.72
-0.19
0.47
-0.46
-0.47
-0.50
-0.46
-0.53
-0.47
-0.50
-0.37
-0.61
-0.38
-0.40
-0.58
-0.31
-0.19
0.76
-0.47
STAT
STAT -WASTE
STAT-WASTE
STAT-SIC
STAT-SIC
STAT -WASTE
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
TOT-AVG
TOT-AVG
TOT-AVG
TOT-AVG
TOT-AVG
TOT-AVG
TOT-AVG
TOT-AVG
TOT-AVG
TOT-AVG
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT -A
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
-------
SIC_P WASTE TONS LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
1623
1721
1721
1721
1721
1721
1721
1721
1721
1721
1726
1726
1726
1751
1799
2037
2037
2092
2092
2099
2099
2231
2231
2231
2231
2231
2231
2231
2231
2231
2231
2231
2231
2297
2297
2297
2297
2400
2400
2400
2400
2400
2400
2411
2415
2415
2415
2415
2421
2421
2421
2421
2431
2431
2431
2431
U001
D001
0007
F001
F002
F003
F005
WC01
UP01
UT01
D001
F003
F005
0001
WT02
D001
F003
D001
D002
D002
0005
D002
0009
001 1
F001
F002
U001
WC01
UC02
UP01
UP02
UT01
UT02
D001
0008
F002
F004
0001
0007
F001
F002
F003
F005
0001
0001
D007
0008
WT02
D001
F001
K001
U001
0001
F003
F005
UT02
2.06
11.73
1.60
0.27
0.93
3.16
3.88
0.20
1.60
1.60
0.10
0.10
0.10
0.98
14.24
0.38
0.38
0.96
1.06
0.28
0.28
0.00
0.00
0.00
0.03
0.11
2.52
0.07
0.16
0.07
3.23
0.13
0.16
0.05
0.05
0.02
0.02
15.92
5.45
0.50
0.42
41.95
47.25
0.20
0.46
0.66
4.86
4.40
4.47
3.60
43.57
12.40
1.10
1.00
1.51
0.22
-0.05
-0.00
-0.05
-0.01
-0.01
-0.01
0.01
-0.04
-0.02
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
0.01
-0.04
-0.61
-0.00
-0.61
-0.02
-0.01
-0.01
-0.01
-0.05
-0.04
-0.04
-0.02
-0.04
-0.05
0.01
-0.01
-0.01
-0.01
-0.03
-0.01
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
-0.01
-0.01
-0.01
-0.08
-0.01
-0.06
-0.09
-0.03
-0.03
-0.02
-0.05
-0.04
-0.07
-0.05
-0.01
-0.02
-0.05
-0.01
-0.05
-0.01
-0.05
-O.OS
-0.63
-0.01
-0.63
-0.03
-0.02
-0.09
-0.03
-0.08
-0.05
-0.05
-0.04
-0.08
-0.07
-0.01
-0.05
-0.03
-0.03
-0.04
-0.05
-0.06
-0.09
-0.03
-0.01
-0.02
-0.05
-0.05
-0.06
-0.03
-0.01
-0.05
-0.09
-0.02
-0.08
-0.05
-0.01
-0.02
-0.01
-0.12
-0.40
0.10
-0.18
0.07
-0.06
-0.10
-0.06
0.08
-0.09
0.11
0.04
0.03
0.11
-0.03
-0.11
0.04
0.11
0.07
-0.66
0.10
0.66
0.09
-0.05
-0.18
0.07
0.12
-0.06
0.06
0.08
0.11
0.09
0.03
-0.11
-0.08
0.07
0.06
0.11
0.10
-0.18
-0.07
0.04
-0.03
-0.11
-0.11
-0.10
-0.08
-0.03
-0.11
-0.18
-0.03
-0.12
-0.11
0.04
-0.04
-0.03
-0.31
0.01
-0.06
-0.06
-0.04
-0.04
-0.04
0.11
-0.12
-0.05
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.12
-0.62
-0.01
-0.62
-0.05
-0.03
-0.06
-0.04
-0.31
-0.11
-0.12
-0.12
-0.21
-0.05
-0.03
-0.03
-0.04
-0.04
-0.08
-0.03
-0.06
-0.06
-0.04
-0.03
-0.03
-0.03
-0.03
-0.06
-0.04
-0.03
-0.03
-0.06
-0.02
-0.31
-0.03
-0.03
-0.03
-0.03
-0.39
-0.02
-0.09
-0.15
-0.09
-0.09
-0.07
-0.15
-0.17
-0.10
-0.14
-0.06
-0.06
-0.14
-0.05
-0.14
-0.06
-0.14
-0.16
-0.65
-0.02
-0.65
-0.10
-0.05
-0.15
-0.09
-0.39
-0.15
-0.16
-0.17
-0.30
-0.10
-0.05
-0.14
-0.08
-0.09
-0.12
-0.14
-0.09
-0.15
-0.09
-0.06
-0.06
-0.14
-0.14
-0.09
-0.08
-0.05
-0.14
-0.15
-0.05
-0.39
-0.14
-0.06
-0.06
-0.05
-0.47
-0.43
-0.17
-0.26
-0.21
-0.17
-0.19
-0.19
-0.28
-0.15
-0.29
-0.14
-0.09
-0.29
-0.09
-0.29
-0.14
0.29
-0.20
-0.68
-0.30
0.68
0.28
0.14
0.26
0.21
-0.47
0.19
0.20
-0.28
-0.39
-0.15
-0.09
-0.29
0.22
-0.21
-0.16
-0.29
-0.17
0.26
-0.21
-0.14
-0.09
0.29
-0.29
-0.17
-0.22
-0.09
-0.29
-0.26
0.09
-0.47
-0.29
-0.14
-0.11
-0.09
0.67
0.03
0.10
0.14
-0.10
0.11
0.09
0.29
0.23
0.10
-0.10
0.08
0.07
-0.10
0.06
0.10
0.08
0.10
0.30
0.65
0.03
-0.65
-0.12
0.07
0.14
0.10
-0.67
0.29
-0.30
0.23
-0.41
0.10
0.06
0.10
-0.10
0.10
-0.21
-0.10
-0.10
-0.14
0.10
0.08
-0.07
0.10
-0.10
-0.10
-0.10
-0.06
-0.10
-0.14
0.06
0.67
-0.10
-0.08
-0.08
-0.06
-0.74
-0.06
-0.14
-0.24
-0.19
-0.22
-0.18
-0.38
-0.30
-0.20
-0.25
-0.17
-0.12
-0.25
-0.10
-0.25
0.17
-0.25
-0.40
-0.69
-0.05
-0.69
-0.25
0.11
-0.24
-0.19
-0.74
-0.38
-0.40
-0.30
-0.57
-0.20
0.10
-0.25
-0.17
-0.19
-0.30
-0.25
-0.14
-0.24
-0.19
-0.17
-0.12
-0.25
-0.25
-0.14
-0.17
-0.10
-0.25
-0.24
-0.12
-0.74
-0.25
-0.17
-0.15
-0.10
-0.80
-0.52
-0.31
-0.38
-0.46
-0.43
-0.41
0.47
-0.53
-0.31
-0.47
-0.40
-0.20
-0.47
-0.19
-0.47
-0.40
-0.47
-0.50
-0.74
-0.76
-0.74
-0.72
-0.33
-0.38
-0.46
-0.80
-0.47
-0.50
-0.53
-0.72
-0.31
-0.19
-0.47
-0.54
-0.46
-0.38
-0.47
-0.31
-0.38
-0.46
-0.40
-0.20
-0.47
-0.47
-0.31
-0.54
0.19
-0.47
-0.38
-0.24
0.80
-0.47
-0.40
-0.27
-0.19
STAT-UASTE
STAT
STAT-UASTE
STAT-UASTE
STAT-WASTE
STAT
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
ENG-ANAL
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
STAT-UASTE
-------
SIC_P HASTE TONS LB_89 HB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
2434
2434
2434
243S
2435
2436
2436
2436
2436
2491
2491
2491
2491
2491
2491
2491
2491
2491
2491
2S11
2521
2521
2521
2521
2546
2599
2599
2599
2599
2611
2611
2611
2611
2611
2611
2611
2611
2611
2621
2621
2621
2621
2621
2621
2621
2641
2641
2641
2641
2641
2641
2641
2641
2641
2641
2641
0001
F003
F005
0002
WT02
0001
0002
W001
WT02
0002
0004
0007
K001
P011
U051
U242
WP01
UP03
WT01
0001
0001
F003
F005
UT02
F005
0001
0007
F003
F005
0001
D002
0008
F002
F003
F004
F005
K071
K106
0001
0009
F001
F002
F003
F005
W001
0001
0002
0003
0007
0008
F002
F003
P024
U037
U048
U122
12.52
12.15
11.86
0.22
1.05
4.51
0.38
2.98
1.35
4.07
31.12
17.28
56.13
12.37
15.50
5.08
16.28
5.31
10.98
4.59
2.17
2.17
3.38
0.94
2.68
1.81
0.47
2.28
2.28
4.37
0.03
0.14
0.03
0.23
0.03
0.92
397.70
397.70
25.56
0.02
6.10
0.04
3.98
3.98
156.72
10.19
1.91
0.03
2.62
10.63
26.94
0.89
0.02
0.03
1.00
1.84
-0.00
-0.01
-0.01
-0.61
-0.01
-0.01
-0.61
-0.05
-0.01
-0.04
-0.02
-0.05
-0.01
-0.01
-0.00
-0.01
-0.02
-0.01
-0.02
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
-0.01
-0.02
-0.61
-0.01
-0.01
-0.01
-0.03
-0.01
-0.02
-0.02
-0.01
-0.02
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
-0.00
-0.05
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.00
-0.01
-0.02
-0.63
-0.01
-0.05
-0.63
-0.08
-0.01
-0.05
-0.04
-0.06
-0.02
-0.02
-0.01
-0.02
-0.04
-0.02
-0.04
-0.05
-0.05
-0.01
-0.02
-0.01
-0.02
-0.05
-0.06
0.01
-0.02
-0.03
-0.63
-0.03
-0.03
-0.01
-0.04
-0.02
-0.03
-0.03
-0.02
-0.03
-0.09
-0.03
-0.01
-0.02
-0.08
-0.02
-0.01
-0.07
-0.06
-0.03
-0.03
-0.01
-0.01
-0.01
-0.01
-0.01
-0.04
-0.04
-0.03
-0.66
-0.03
-0.11
-0.66
-0.12
-0.03
-0.07
-0.04
-0.10
-0.05
-0.05
-0.02
0.05
-0.08
-0.02
-0.07
-0.11
-0.11
-0.04
-0.03
-0.03
-0.03
-0.11
0.10
0.04
-0.03
0.03
0.66
0.08
-0.07
-0.04
0.06
-0.03
-0.03
-0.03
-0.03
-0.09
-0.18
0.07
-0.04
0.03
-0.12
0.06
-0.09
-0.08
0.10
0.08
0.07
-0.04
-0.05
0.05
-0.05
-0.05
-0.00
-0.03
-0.03
-0.62
-0.03
-0.03
-0.62
-0.31
-0.03
-0.12
-0.07
-0.06
-0.02
-0.04
-0.01
-0.04
-0.12
-0.02
-0.05
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.06
-0.03
-0.03
-0.05
-0.62
-0.04
-0.04
-0.03
-0.08
-0.03
-0.05
-0.05
-0.04
-0.05
-0.06
-0.04
-0.03
-0.03
-0.31
-0.03
-0.01
-0.16
-0.06
-0.04
-0.04
-0.03
-0.02
-0.02
-0.02
-0.02
-0.01
-0.06
-0.06
-0.65
-0.05
-0.14
-0.65
-0.39
-0.05
-0.16
-0.13
-0.09
-0.05
0.07
-0.03
0.07
-0.17
-0.04
-0.11
-0.14
-0.14
-0.06
-0.06
-0.05
-0.06
-0.14
-0.09
-0.06
-0.06
-0.10
-0.65
-0.08
-0.09
-0.06
-0.12
-0.06
-0.10
-0.10
-0.07
-0.10
-0.15
-0.09
-0.06
-0.06
-0.39
-0.07
-0.02
-0.20
-0.09
-0.08
0.09
-0.06
-0.04
-0.04
-0.04
-0.04
-0.12
-0.14
-0.09
-0.68
-0.09
-0.29
-0.68
0.47
0.09
-0.20
-0.13
0.17
0.16
-0.14
-0.07
-0.14
-0.28
-0.06
0.21
-0.29
0.29
0.14
-0.09
-0.09
-0.09
0.29
-0.17
0.14
-0.09
-0.10
0.68
-0.22
-0.21
-0.14
-0.16
0.09
0.10
-0.10
-0.10
-0.28
-0.26
0.21
-0.14
0.09
-0.47
-0.19
-0.27
-0.24
0.17
0.22
-0.21
-0.14
-0.15
0.15
0.15
0.15
-0.01
-0.08
-0.07
-0.65
-0.06
-0.10
-0.65
-0.67
-0.06
-0.30
-0.17
-0.10
-0.06
-0.09
-0.03
-0.09
-0.23
-0.05
-0.14
-0.10
-0.10
-0.08
-0.07
-0.06
-0.07
-0.10
-0.10
-0.08
-0.07
-0.12
-0.65
-0.10
-0.10
-0.08
-0.21
-0.07
-0.12
-0.12
-0.09
-0.12
-0.14
-0.10
-0.08
-0.07
-0.67
-0.09
-0.03
-0.39
-0.10
-0.10
0.10
-0.08
-0.06
-0.06
-0.06
-0.06
-0.01
0.17
-0.12
-0.69
-0.10
-0.25
-0.69
-0.74
-0.10
-0.40
-0.33
-0.14
-0.12
-0.18
-0.07
-0.18
-0.30
-0.10
-0.28
-0.25
-0.25
0.17
0.12
-0.10
-0.12
-0.25
-0.14
-0.17
-0.12
-0.25
-0.69
-0.17
0.19
-0.17
0.30
-0.12
-0.25
-0.25
-0.19
-0.25
-0.24
-0.19
-0.17
-0.12
0.74
0.17
-0.06
-0.49
-0.14
-0.17
-0.19
-0.17
-0.10
-0.10
-0.10
-0.10
-0.31
-0.40
-0.20
-0.74
-0.19
-0.47
-0.74
-0.80
0.19
-0.50
-0.34
-0.31
0.40
-0.37
-0.19
0.37
0.53
0.15
-0.55
-0.47
-0.47
-0.40
-0.20
0.19
-0.20
0.47
0.31
0.40
-0.20
-0.27
-0.74
-0.54
0.46
-0.40
0.38
0.20
-0.27
-0.27
0.25
0.72
0.38
0.46
-0.40
0.20
0.80
-0.49
-0.68
-0.59
0.31
0.54
0.46
-0.40
-0.36
0.36
0.36
-0.36
STAT
STAT-WASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-WASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
ENG-ANAL
STAT
STAT-UASTE
STAT
STAT-SIC
STAT
STAT-SIC
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-SIC
STAT-SIC
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
STAT-A
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
-------
SIC_P WASTE TONS LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
2641
2641
2641
2641
2641
2641
2641
2641
2642
2642
2642
2642
2643
2643
2649
2649
2651
2651
2651
2651
2651
2651
2654
2654
2711
2711
2711
2711
2711
2711
2711
2711
2715
2750
2751
2751
2752
2752
2752
2752
2752
2761
2761
2789
2789
2789
2799
2800
2800
2800
2800
2800
2800
2800
2800
2800
U147
U188
U001
UL01
UL02
UP03
UT01
UT02
0001
F001
F002
UT02
0001
0008
F002
UP01
0001
0002
0008
F003
F005
WT02
0001
F003
0001
0002
0006
0008
F003
F005
UP02
UT02
F002
F001
0001
F001
0001
F002
F003
FOOS
WT02
0001
FOOS
0001
FOOS
FOOS
F001
0001
0007
0008
0009
0011
F001
F002
F003
FOOS
1.20
1.65
3.03
0.09
0.39
1.50
2.82
50.33
13.63
0.73
0.58
3.63
31.36
1.51
1.09
1.09
16.44
0.11
8.56
10.06
10.06
0.11
15.51
15.51
19.41
2.39
0.66
1.53
0.40
2.50
0.52
0.80
2.00
1.24
2.23
3.31
0.89
6.44
0.29
0.47
1.04
0.99
0.27
0.06
0.06
0.06
7.15
0.74
0.26
0.12
0.01
0.01
1.76
4.01
0.55
3.87
-0.01
-0.01
-0.05
-0.01
-0.01
-0.01
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.02
-0.02
-0.61
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.00
-0.04
-0.09
-0.01
-0.01
-0.01
-0.04
-0.02
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
-0.02
-0.01
-0.01
-0.01
-0.01
-0.00
-0.01
-0.02
-0.08
-0.03
-0.02
-0.02
0.07
0.01
0.05
-0.09
-0.03
-0.01
-0.05
-0.03
-0.03
-0.04
0.03
0.63
-0.03
0.01
-0.02
-0.01
0.05
0.01
0.01
0.05
-0.12
-0.03
-0.01
-0.02
-0.08
0.03
-0.03
0.09
-0.05
-0.09
-0.05
0.03
0.01
-0.02
-0.01
-0.05
-0.02
-0.05
-0.01
-0.02
-0.09
-0.05
0.06
-0.03
0.03
-0.02
-0.09
-0.03
-0.01
-0.00
-0.05
-0.03
-0.12
-0.06
-0.04
-0.02
-0.09
-0.04
-0.11
-0.18
-0.07
-0.03
-0.11
-0.08
-0.07
-0.08
-0.05
-0.66
-0.08
0.04
-0.03
-0.03
-0.11
-0.04
-0.09
-0.07
0.17
-0.03
-0.04
-0.03
-0.11
-0.06
-0.07
-0.18
-0.11
-0.18
-0.11
0.07
0.04
-0.03
-0.03
-0.11
-0.03
-0.11
-0.04
-0.03
-0.18
-0.11
0.10
0.08
-0.09
-0.05
-0.18
-0.07
-0.04
-0.01
-0.02
-0.02
0.31
-0.04
-0.03
-0.02
0.05
0.02
-0.03
-0.06
-0.04
-0.03
-0.03
0.04
-0.04
0.12
0.05
0.62
0.04
0.03
-0.03
-0.03
-0.03
-0.03
-0.01
0.12
0.11
0.04
-0.03
-0.03
-0.21
-0.05
-0.04
0.06
-0.03
-0.06
-0.03
0.04
0.03
-0.03
-0.03
-0.03
0.03
-0.03
0.03
0.03
-0.06
-0.03
-0.06
-0.04
-0.05
-0.03
-0.06
-0.04
-0.02
-0.01
-0.04
-0.04
-0.39
-0.07
-0.05
-0.04
-0.10
-0.04
0.14
-0.15
-0.09
-0.05
-0.14
-0.08
-0.09
-0.17
0.10
-0.65
-0.08
-0.06
-0.06
-0.05
-0.14
-0.06
-0.03
-0.16
-0.17
-0.08
-0.06
-0.06
-0.30
0.10
-0.09
-0.15
-0.14
-0.15
-0.14
-0.09
-0.06
-0.06
-0.05
-0.14
-0.06
-0.14
-0.06
-0.06
-0.15
-0.14
-0.09
-0.08
-0.10
0.05
0.15
-0.09
-0.04
-0.01
0.15
-0.06
0.47
0.11
-0.12
-0.06
-0.15
-0.14
-0.29
-0.26
0.21
-0.09
-0.29
-0.22
-0.21
-0.28
-0.14
-0.68
-0.22
0.14
-0.09
-0.09
-0.29
-0.14
-0.27
-0.20
-0.28
-0.10
-0.14
-0.09
-0.39
-0.19
-0.21
-0.26
-0.29
-0.26
-0.29
0.21
-0.14
-0.09
-0.09
-0.29
-0.09
-0.29
-0.14
-0.09
-0.26
-0.29
-0.17
0.22
-0.28
-0.14
-0.26
-0.21
-0.13
-0.02
-0.06
-0.07
-0.67
-0.09
-0.07
-0.05
-0.10
-0.05
-0.10
-0.14
-0.10
-0.06
-0.10
-0.10
-0.10
-0.23
-0.13
-0.65
-0.10
-0.08
-0.07
-0.06
-0.10
-0.08
-0.04
-0.30
-0.17
-0.10
-0.08
0.07
-0.41
0.12
-0.10
-0.14
-0.10
-0.14
-0.10
-0.10
-0.08
-0.07
-0.06
-0.10
-0.07
-0.10
-0.08
-0.07
-0.14
-0.10
-0.10
-0.10
-0.12
-0.07
-0.14
-0.10
-0.06
-0.02
-0.10
-0.09
0.74
-0.16
-0.13
-0.10
-0.20
-0.08
-0.25
-0.24
-0.19
-0.10
-0.25
0.17
0.19
-0.30
-0.26
-0.69
-0.17
0.17
-0.12
-0.10
-0.25
-0.17
-0.07
-0.40
-0.25
-0.20
-0.17
-0.12
-0.57
-0.25
-0.19
-0.24
-0.25
-0.24
-0.25
-0.19
-0.17
-0.12
-0.10
-0.25
-0.12
-0.25
-0.17
-0.12
-0.24
-0.25
-0.14
-0.17
-0.25
-0.11
-0.24
-0.19
-0.11
-0.04
-0.36
-0.11
-0.80
-0.22
-0.30
-0.15
-0.31
-0.32
-0.47
-0.38
-0.46
-0.19
-0.47
-0.54
-0.46
-0.53
-0.36
-0.74
-0.54
-0.40
-0.20
-0.19
-0.47
-0.40
-0.69
-0.50
-0.50
-0.25
-0.40
-0.20
-0.72
-0.47
-0.46
-0.38
-0.47
-0.38
-0.47
-0.46
-0.40
-0.20
0.19
-0.47
-0.20
-0.47
-0.40
-0.20
-0.38
-0.47
-0.31
-0.54
-0.72
-0.33
-0.38
-0.46
-0.34
-0.05
STAT-SIC
ST AT -WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-UASTE
STAT-WASTE
STAT-A
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
ENG-ANAL
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT
-------
SIC_P WASTE TONS LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 H8_09 SOUR
2800
2800
2800
2800
2800
2800
2800
2800
2812
2812
2812
2812
2812
2812
2812
2812
2812
2812
2812
2813
2815
2816
2816
2819
2819
2819
2819
2821
2821
2821
2821
2831
2831
2831
2831
2831
2831
2831
2831
2831
2831
2831
2842
2842
2842
2842
2850
2850
2850
2851
2851
2851
2851
2851
2851
2851
U083
U084
U154
U220
U226
UL01
WL02
UT01
0002
0008
F002
K073
U044
UL01
UL02
UP01
UP02
VT01
WT02
F001
F027
0001
0005
0002
F001
F002
UP01
D001
F002
F003
WT02
D001
0009
F001
F002
F003
F005
VC02
VP01
WP02
UT01
UT02
0001
0007
F003
F005
0001
D009
F002
D001
D002
D003
D007
D008
D009
F001
0.16
0.16
22.26
0.02
3.88
0.03
0.00
0.88
20.01
501.91
1.50
99.10
0.50
0.01
0.04
0.93
10.44
0.01
13.65
0.90
4.60
9.87
0.30
1.60
0.35
0.04
0.39
18.46
0.60
54.68
6.69
0.43
4.61
0.59
0.05
10.23
2.94
0.26
0.58
0.03
0.40
0.10
0.13
0.13
0.13
0.13
2.75
5.22
5.22
1741.7
38.49
2.22
9.94
17.36
13.57
39.89
-0.00
-0.00
-0.00
0.00
-0.00
-0.01
-0.01
-0.05
-0.02
-0.01
-0.01
-0.02
-0.02
-0.01
-0.01
-0.02
-0.04
0.05
-0.01
0.01
-0.10
-0.01
-0.00
0.04
0.01
0.01
-0.02
0.00
-0.01
0.01
-0.01
0.02
0.02
-0.01
0.01
-0.01
-0.00
-0.04
0.01
0.04
-0.01
0.01
-0.01
-0.05
-0.01
-0.01
0.01
0.02
0.01
0.01
-0.01
-0.02
-0.03
-0.02
-0.01
-0.02
-0.01
-0.01
-0.01
-0.01
-0.00
-0.03
-0.01
-0.07
-0.04
-0.03
-0.03
-0.04
-0.04
-0.03
-0.01
-0.04
-0.08
0.07
-0.01
-0.09
0.12
-0.05
-0.01
-0.05
-0.09
-0.03
-0.04
-0.01
-0.03
-0.01
-0.01
-0.03
-0.03
-0.09
-0.03
-0.01
-0.00
-0.05
-0.02
-0.08
-0.02
-0.01
-0.05
-0.06
-0.01
-0.02
-0.05
-0.03
-0.03
-0.13
-0.02
-0.12
-0.14
-0.14
-0.03
-0.03
-0.01
-0.01
-0.01
-0.01
-0.05
-0.06
-0.01
-0.09
-0.05
-0.08
0.07
-0.05
-0.05
-0.06
-0.01
-0.08
-0.11
-0.09
-0.03
-0.18
-0.15
-0.11
-0.10
-0.07
-0.18
-0.07
-0.08
-0.06
-0.07
-0.04
-0.03
-0.04
0.09
-0.18
-0.07
-0.05
-0.06
-0.06
-0.06
-0.11
-0.03
-0.03
-0.11
-0.10
-0.04
-0.03
-0.11
-0.09
0.07
-0.25
-0.03
-0.23
-0.25
-0.25
-0.05
-0.04
-0.01
-0.01
-0.01
-0.01
-0.01
-0.04
-0.02
-0.05
-0.06
-0.04
-0.04
-0.06
-0.06
-0.04
-0.02
-0.12
-0.21
-0.05
-0.03
-0.06
-0.14
-0.03
-0.01
-0.12
-0.06
-0.04
-0.12
-0.01
-0.04
-0.03
-0.03
-0.05
-0.05
-0.06
-0.04
-0.02
-0.00
-0.12
-0.03
-0.21
-0.02
-0.03
-0.03
-0.06
-0.03
-0.03
-0.03
-0.05
-0.04
-0.05
-0.05
-0.05
-0.10
-0.05
-0.10
-0.03
-0.02
-0.02
-0.02
-0.02
-0.02
-0.07
-0.03
-0.10
0.11
0.08
-0.09
0.11
0.11
0.07
0.03
0.17
-0.30
-0.10
0.05
0.15
-0.18
-0.14
-0.02
-0.16
-0.15
-0.09
-0.17
-0.02
-0.09
-0.06
0.05
-0.09
-0.10
-0.15
-0.09
-0.04
-0.00
-0.16
-0.06
-0.30
-0.05
-0.05
-0.14
-0.09
-0.06
-0.06
-0.14
0.10
0.09
-0.39
-0.10
-0.34
-0.17
0.15
0.20
-0.05
-0.03
-0.03
-0.03
-0.03
-0.17
-0.11
-0.04
-0.15
-0.16
-0.22
-0.21
-0.16
-0.16
-0.11
-0.04
-0.28
-0.39
-0.15
-0.09
-0.26
-0.24
-0.29
-0.30
-0.20
-0.26
-0.21
-0.28
-0.17
-0.21
-0.14
-0.09
-0.12
-0.28
-0.26
-0.21
-0.15
-0.19
-0.20
0.19
0.39
-0.09
-0.09
-0.29
-0.17
-0.14
-0.09
-0.29
-0.28
-0.21
-0.73
-0.15
-0.63
-0.25
-0.25
-0.30
-0.07
-0.02
-0.02
-0.02
-0.02
-0.03
-0.09
-0.05
-0.10
-0.14
-0.10
-0.10
-0.14
-0.14
-0.09
-0.05
-0.23
-0.41
-0.10
-0.06
-0.14
-0.20
-0.10
-0.03
-0.30
-0.14
-0.10
-0.23
-0.02
-0.10
-0.08
-0.06
-0.12
-0.12
-0.14
-0.10
-0.06
-0.01
-0.30
-0.08
-0.41
-0.06
-0.06
-0.10
-0.10
-0.08
-0.07
-0.10
-0.12
-0.10
-0.20
-0.10
-0.18
-0.25
-0.10
-0.20
-0.05
-0.04
-0.04
-0.04
-0.04
-0.04
-0.16
-0.07
-0.20
-0.29
0.17
-0.19
-0.29
-0.29
-0.16
-0.07
-0.30
-0.57
-0.20
0.10
0.24
0.26
-0.25
0.05
0.40
0.24
0.19
-0.30
0.04
0.19
0.17
-0.10
-0.23
-0.25
-0.24
-0.19
-0.11
-0.01
-0.40
-0.15
-0.57
-0.12
-0.10
-0.25
0.14
0.17
-0.12
0.25
0.25
-0.19
-0.57
-0.20
-0.52
-0.38
-0.30
-0.50
-0.10
-0.09
-0.09
-0.09
-0.09
-0.44
-0.22
-0.10
-0.31
-0.42
-0.54
-0.46
-0.42
-0.42
-0.22
-0.10
-0.53
-0.72
-0.31
-0.19
-0.38
-0.37
-0.47
-0.76
-0.50
-0.38
-0.46
-0.53
-0.43
-0.46
-0.40
-0.19
-0.30
-0.72
-0.38
-0.46
-0.38
-0.48
-0.50
-0.48
-0.72
-0.24
-0.19
0.47
-0.31
-0.40
-0.20
-0.47
-0.72
-0.46
-0.95
-0.30
-0.85
-0.50
-0.50
-0.80
-0.15
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT -WASTE
STAT -WASTE
STAT-WASTE
STAT -WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
TOT-AVG
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
GROUND
GROUND
GT-SIC
GROUND
GROUND
GROUND
GROUND
-------
SIC_P WASTE TONS LB_89 NB_89 HB_89 LB_95 MB_9S HB_95 LB_09 MB_09 HB_09 SOUR
2851
2851
2851
2851
2851
2851
2851
2851
2851
2851
2851
2851
2851
2851
2851
2851
2865
2865
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2869
2879
2879
2879
2879
2879
2893
2893
F002
F003
F004
F005
F006
F007
U031
U112
U117
U228
UL01
UL02
WP01
WP02
WT01
UT02
WT01
WT02
0001
0002
0003
0006
0007
0008
0009
F001
F002
F003
F005
F006
F007
F008
P023
P030
U044
U056
U081
U084
U122
U144
U170
U226
U001
WL01
WL02
WP01
WP03
UT01
WT02
0002
0007
0008
P047
UT02
0001
0007
1.00
138.20
2.22
M. 92
3.00
0.07
0.22
1.80
0.22
0.58
0.21
0.64
15.29
78.50
4.28
88.30
24.40
120.92
223.64
13661
0.08
150.60
835.25
685.86
2.82
190.62
289.71
141.49
195.12
94.38
4.30
3.44
0.25
0.21
0.00
0.20
0.25
0.25
0.00
0.20
0.20
0.00
212.06
7.12
3.53
23.71
1.93
28.25
1026.7
0.25
0.07
57.71
0.87
38.42
9.95
10.68
0.00
0.00
-0.02
-0.01
-0.02
-0.07
-0.01
-0.02
-0.02
-0.02
0.00
0.00
-0.05
-0.04
-0.05
0.15
-0.05
-0.01
-0.01
0.95
-0.87
-0.15
-0.06
-0.02
-0.01
0.00
-0.01
-0.00
-0.01
-0.87
-0.07
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.00
-0.05
0.00
0.00
-0.05
-0.87
-0.05
0.00
-0.61
-0.05
-0.01
-0.10
-0.01
-0.01
-0.05
0.00
-0.01
-0.12
0.03
-0.12
0.10
-0.05
0.12
0.12
0.12
0.03
0.00
0.10
0.09
0.07
0.25
-0.07
-0.01
0.07
0.97
0.90
-0.18
-0.08
-0.03
-0.04
-0.10
-0.03
-0.01
-0.02
-0.90
-0.10
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
0.90
-0.90
-0.00
-0.10
-0.03
0.00
-0.10
0.90
0.07
0.00
-0.63
0.06
0.03
-0.12
-0.01
-0.05
-0.06
0.00
-0.02
-0.23
-0.05
-0.23
0.13
-0.09
0.23
0.23
0.23
0.05
0.00
-0.15
-0.13
-0.09
-0.35
-0.09
-0.03
-0.13
-1.00
-0.92
-0.22
-0.10
-0.05
0.06
0.20
-0.04
-0.02
-0.03
0.92
0.13
-0.92
-0.92
0.92
0.92
-0.92
-0.92
-0.92
-0.92
-0.92
-0.92
-0.00
-0.15
-0.05
0.00
0.15
-0.92
-0.09
0.00
-0.66
0.10
0.08
-0.15
-0.03
-0.11
-0.10
0.00
-0.06
-0.05
-0.03
-0.05
-0.23
-0.04
-0.05
-0.05
-0.05
0.00
0.00
-0.40
-0.32
-0.05
-0.15
-0.05
-0.03
-0.03
-0.95
-0.87
-0.16
-0.07
-0.05
-0.13
-0.10
-0.04
-0.05
-0.03
-0.87
-0.23
-0.87
-0.87
-0.87
0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.04
-0.40
0.00
0.00
-0.40
-0.87
-0.05
0.00
-0.62
-0.06
-0.04
-0.14
-0.03
-0.03
-0.06
0.00
-0.11
-0.34
-0.09
-0.34
-0.27
-0.09
-0.34
-0.34
-0.34
-0.04
0.00
-0.50
-0.41
-0.10
-0.25
-0.10
-0.05
-0.21
-0.97
-0.90
-0.22
-0.10
0.07
-0.22
-0.20
-0.10
-0.08
-0.05
-0.90
-0.27
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.05
-0.50
-0.04
0.00
0.50
-0.90
-0.10
0.00
-0.65
-0.09
-0.08
-0.18
-0.05
-0.14
-0.09
0.00
-0.15
-0.63
-0.15
-0.63
-0.31
-0.14
-0.63
-0.63
-0.63
-0.06
0.00
-0.60
-0.49
-0.15
-0.35
-0.15
-0.09
-0.38
-1.00
-0.92
-0.27
-0.13
-0.10
-0.32
-0.30
-0.16
-0.12
-0.07
-0.92
-0.31
-0.92
0.92
-0.92
-0.92
-0.92
-0.92
-0.92
-0.92
-0.92
-0.92
-0.06
-0.60
-0.06
0.00
-0.60
-0.92
-0.15
0.00
-0.68
-0.17
-0.22
-0.24
-0.09
-0.29
-0.17
0.05
-0.12
-0.18
0.05
-0.18
0.49
-0.10
-0.18
-0.18
-0.18
0.00
0.00
-0.70
-0.57
-0.10
0.15
0.10
-0.06
-0.12
-0.95
-0.87
-0.20
-0.10
-0.10
-0.23
-0.20
0.11
-0.10
-0.06
-0.87
-0.49
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.87
-0.08
-0.85
0.00
0.00
-0.70
-0.87
-0.10
0.00
-0.65
-0.10
-0.10
-0.20
-0.06
-0.10
-0.10
0.10
-0.31
-0.52
0.23
0.52
0.54
-0.20
-0.52
0.52
-0.52
-0.05
0.00
0.75
0.61
0.20
0.25
0.20
-0.10
0.31
0.97
0.90
0.26
0.14
0.14
-0.51
-0.30
0.18
0.24
-0.11
0.90
0.54
0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
-0.90
0.12
-0.90
-0.04
0.00
-0.75
0.90
-0.20
0.00
-0.69
-0.14
0.17
-0.26
-0.10
0.25
-0.14
-0.15
-0.50
-0.85
-0.40
-0.85
0.59
-0.30
-0.85
0.85
0.85
-0.07
0.00
0.80
-0.66
0.30
0.35
0.31
-0.19
-0.50
-1.00
0.92
0.33
-0.18
-0.18
-0.80
-0.40
-0.25
0.37
-0.15
-0.92
0.59
-0.92
-0.92
-0.92
-0.92
-0.92
-0.92
-0.92
-0.92
-0.92
0.92
0.16
-0.95
-0.07
0.00
-0.80
0.92
0.30
0.00
0.74
-0.31
0.54
0.37
0.19
-0.47
-0.31
GROUND
GROUND
GT-SIC
GROUND
GT-SIC
GT-UASTE
GROUND
GT-SIC
GT-SIC
GT-SIC
GT-UASTE
GT-UASTE
GT-UASTE
GT-UASTE
STAT-UASTE
GROUND
STAT-UASTE
STAT-UASTE
GT-UASTE
GROUND
GT-SIC
GT-UASTE
GT-UASTE
GT-UASTE
GT-UASTE
GROUND
GT-UASTE
GT-UASTE
GT-UASTE
GT-SIC
GT-UASTE
GT-SIC
GT-SIC
GT-SIC
GT-SIC
GT-SIC
GT-SIC
GT-SIC
GT-SIC
GT-SIC
GT-SIC
GT-UASTE
GT-UASTE
GROUND
GROUND
GT-UASTE
GT-SIC
STAT-UASTE
GROUND
STAT-UASTE
STAT-UASTE
STAT-UASTE
TOT-AVG
STAT-UASTE
STAT-UASTE
STAT-UASTE
-------
SIC P UASTE
TONS
LB_89 MB_89 HB_89 LB_95 H8_95 HB_95 LB_09 MB.09 HB_09 SOUR
2893
2893
2899
2900
2900
2910
2910
2910
2910
2910
2910
2910
2910
2910
2911
2911
2911
2911
2911
2911
2911
2911
2911
2911
2911
2911
2911
2911
2911
2911
2911
2911
3069
3070
3079
3079
3079
3079
3079
3079
3079
3079
3079
3079
3079
3211
3211
3211
3211
3211
3211
3211
3241
3241
3272
3272
0008
K086
UT02
0001
UT02
D001
F001
F002
F003
FOOS
F026
P064
WT01
UT02
D001
D002
D009
F001
F003
FOOS
F006
K048
K049
K050
KOS1
KOS2
P019
P098
U190
UL01
WT01
UT02
0001
0001
0001
0002
0006
0008
F001
F002
F003
F004
FOOS
UP01
UT02
0001
0006
0007
D008
F002
U007
WT02
U001
UT02
F003
FOOS
10.68
0.67
66.00
17.50
16.69
1.46
0.83
0.62
0.31
0.31
0.77
0.39
1.68
2.36
407.50
0.32
0.34
2.66
2.45
2.45
15.00
150.00
205.76
4.00
4518.0
5.17
0.00
0.00
0.00
0.00
2.45
73.05
7.90
58.50
133.49
29.57
0.38
0.88
11.65
28.45
88.30
0.03
22.58
1.52
24.72
0.07
3.62
3.62
91.07
0.59
0.67
1609.5
0.11
14654
6.7S
6.75
-0.01
-0.10
-0.01
-0.01
-0.01
-0.01
0.01
-0.01
-0.01
-0.01
-0.00
-0.00
-0.00
-0.00
-0.03
-0.61
-0.02
0.01
-0.01
-0.01
-0.14
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.01
-0.05
-0.01
-0.01
-0.01
-0.00
-0.04
-0.09
-0.01
-0.01
-0.01
-0.01
-0.03
-0.03
-0.02
-0.01
-0.01
-0.09
0.05
-0.01
-0.01
0.10
-0.01
-0.05
-0.01
-0.01
-0.01
-0.03
-0.12
-0.01
0.05
0.01
O.OS
0.09
-0.03
-0.01
-0.02
-0.01
-0.01
0.01
-0.00
-0.06
-0.63
-0.03
0.09
-0.01
-0.02
-0.16
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
0.03
-0.03
0.07
-0.01
-0.05
0.05
0.01
O.OS
-0.12
-0.03
-0.09
-0.01
-0.01
-0.04
-0.06
0.04
0.01
0.05
-0.12
0.06
-0.03
0.03
0.12
-0.01
-0.08
-0.01
-0.01
0.02
-0.08
-0.15
-0.03
-0.11
-0.03
-0.11
-0.18
-0.07
-0.04
-0.03
-0.02
-0.02
-0.02
-0.02
-0.08
-0.66
0.09
-0.18
-0.04
-0.03
-0.20
-0.04
-0.04
-0.04
-0.03
-0.04
0.04
-0.04
-0.04
-0.06
-0.09
-0.03
-0.11
-0.11
-0.51
-0.07
-0.17
-0.08
0.18
-0.09
-0.05
-0.06
-0.07
-0.08
0.03
-0.11
-0.17
-0.10
-0.08
0.07
-0.15
-0.03
-0.12
-0.03
-0.04
-0.03
-0.04
-0.14
-0.03
-0.03
-0.03
-0.03
-0.06
-0.04
0.03
-0.03
-0.01
-0.01
-0.01
-0.01
-0.09
-0.62
-0.05
-0.06
-0.03
-0.03
-0.19
-0.05
-0.05
-0.05
-O.OS
-0.05
O.OS
-0.05
-0.05
-0.04
-0.05
-0.03
-0.03
-0.03
-0.01
-0.12
-0.11
-0.04
-0.06
-0.02
-0.02
-0.08
-0.09
-0.12
-0.03
-0.03
-0.11
-0.06
-0.04
-0.04
-0.14
-0.03
-0.31
-0.03
-0.03
-0.03
-0.08
-0.18
0.05
0.14
-0.05
-0.14
-0.15
-0.09
-0.06
0.06
-0.02
-0.02
-0.03
0.01
0.17
-0.65
-0.10
-0.15
-0.06
-0.06
0.23
-0.10
-0.10
-0.10
-0.09
-0.10
-0.10
-0.10
-0.10
-0.07
-0.10
-0.05
-0.14
0.14
-0.02
-0.16
-0.17
-0.08
-0.15
-0.04
-0.04
-0.12
-0.18
-0.17
-0.05
0.14
-0.17
-0.09
0.08
-0.09
-0.18
0.05
-0.39
-0.05
-0.06
-0.06
-0.22
0.24
-0.09
-0.29
-0.09
-0.29
-0.26
-0.21
-0.14
-0.09
0.07
0.07
0.07
-0.07
-0.23
-0.68
0.28
0.26
-0.14
-0.09
-0.31
-0.11
-0.11
-0.11
-0.10
-0.11
0.11
0.11
-0.11
-0.11
-0.15
-0.09
0.29
-0.29
-0.58
-0.20
-0.28
-0.22
-0.26
-0.27
-0.16
-0.16
-0.20
-0.28
-0.09
-0.29
-0.28
-0.17
-0.22
-0.21
-0.24
-0.09
-0.47
-0.09
-0.14
-0.09
-0.10
-0.20
-0.06
-0.10
-0.06
0.10
-0.14
-0.10
-0.08
-0.07
-0.02
-0.02
0.04
-0.02
-0.22
0.65
0.12
0.14
-0.08
-0.07
-0.21
0.13
-0.13
-0.13
-0.12
-0.13
-0.13
-0.13
0.13
-0.09
0.10
0.06
0.10
-0.10
0.03
-0.30
-0.17
-0.10
0.14
-0.05
-0.05
-0.21
0.23
-0.23
0.06
0.10
-0.17
0.10
0.10
0.10
-0.20
-0.06
-0.67
-0.06
-0.08
-0.07
-0.17
-0.26
-0.10
-0.25
-0.10
-0.25
-0.24
-0.19
-0.17
-0.12
-0.05
-0.05
-0.07
-0.03
-0.44
0.69
-0.25
-0.24
-0.17
-0.12
0.26
-0.26
-0.26
-0.26
-0.24
-0.26
-0.26
-0.26
-0.26
-0.16
-0.20
-0.10
-0.25
-0.25
-0.06
-0.40
-0.25
-0.17
-0.24
-0.10
-0.10
-0.30
-0.47
-0.30
-0.10
-0.25
-0.25
-0.14
-0.17
-0.19
-0.26
-0.10
-0.74
-0.10
-0.17
-0.12
0.54
-0.37
-0.19
-0.47
0.19
0.47
0.38
-0.46
0.40
0.20
0.18
-0.18
-0.18
-0.17
-0.60
-0.74
-0.72
0.38
-0.40
-0.20
-0.41
0.29
-0.29
-0.29
-0.26
-0.29
-0.29
-0.29
-0.29
-0.22
0.31
-0.19
-0.47
0.47
0.73
0.50
-0.50
-0.54
-0.38
-0.69
0.41
0.38
0.51
-0.53
0.19
0.47
-0.50
-0.31
-0.54
-0.46
-0.37
-0.19
0.80
-0.19
-0.40
-0.20
STAT-UASTE
TOT-AVG
ST AT -WASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-SIC
STAT-SIC
STAT-UASTE
STAT-UASTE
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
ENG-ANAL
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
STAT
STAT-UASTE
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
TOT-AVG
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
-------
SIC P WASTE TONS LB 89 MB 89 HB 89 LB 95 MB 95 HB 95 LB 09 MB 09 HB 09 SOUR
3274
3274
3296
3296
3299
3299
3300
3300
3300
3300
3300
3312
3315
3315
3315
3317
3317
3317
3325
3325
3325
3325
3325
3325
3325
3325
3325
3325
3325
3325
3334
3334
3334
3334
3334
3334
3334
3334
3334
3334
3334
3334
3334
3334
3334
3334
3334
3339
3339
3339
3339
3339
3339
3339
3339
3339
0001
UT02
D004
P011
F001
F002
0001
D002
D007
K061
UT02
0008
0008
F001
IC062
D007
F001
K062
0001
0002
0007
0008
F001
F002
F003
F005
U001
UL01
UL02
UT02
0001
0007
0008
F001
F002
F003
F004
F005
U080
U210
U226
U239
U001
UP01
UP03
UT01
WT02
0001
0002
0003
0007
F001
F002
F005
UP01
UP02
0.46
0.46
6.06
6.06
0.30
0.53
3.74
19.76
0.20
3520.2
0.55
1342.0
73.28
1.83
149.66
82.89
4.80
82.89
8.30
2.09
13.15
11.05
0.50
0.50
2.12
1.61
12.00
0.30
0.40
50.28
18.83
0.18
12.70
0.16
0.49
0.94
0.12
0.84
0.02
0.01
0.42
0.03
41.27
1.13
409.87
8281.8
29529
14.52
255.15
15.59
241.04
16.57
72.72
12.40
70.77
18.22
-0.01
0.01
-0.01
-0.10
-0.01
-0.01
-0.01
-0.04
-0.05
-0.10
-0.01
-0.01
-0.01
-0.01
0.10
-0.05
-0.01
-0.10
-0.01
-0.04
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
-0.01
-0.01
-0.06
-0.06
0.02
-0.01
-0.00
0.01
-0.01
-0.01
-0.01
-0.01
-0.00
-0.01
-0.05
-0.05
-0.01
0.05
-0.01
-0.01
-0.04
-0.05
-0.05
-0.01
-0.00
-0.01
0.00
-0.04
-0.05
0.01
-0.03
0.12
-0.09
-0.03
-0.05
-0.05
-0.06
-0.12
0.01
-0.03
-0.03
-0.09
-0.12
-0.06
0.09
-0.12
0.01
-0.05
-0.06
-0.03
-0.09
-0.03
-0.01
-0.02
-0.08
-0.03
-0.01
-0.01
-0.08
0.08
0.03
-0.12
-0.00
-0.02
-0.01
-0.02
-0.01
0.01
-0.00
-0.01
-0.10
-0.10
-0.01
-0.07
-0.01
-0.05
-0.05
-0.07
-0.06
-0.09
-0.01
-0.02
-0.00
-0.08
-0.11
0.03
-0.06
0.15
0.18
0.07
0.11
-0.07
-0.10
-0.15
0.03
-0.08
0.08
0.18
0.15
-0.10
0.18
0.15
0.07
-0.07
-0.10
-0.08
-0.18
-0.07
-0.04
-0.03
-0.12
0.06
-0.01
-0.03
-0.10
-0.10
-0.05
-0.21
-0.00
0.02
-0.02
-0.02
-0.02
-0.02
-0.00
-0.02
-0.15
-0.15
0.02
0.09
-0.02
-0.11
-0.07
-0.08
-0.10
-0.18
-0.05
-0.03
-0.05
-0.11
-0.03
-0.03
-0.04
-0.14
-0.06
-0.04
0.03
-0.12
-0.06
-0.14
-0.03
-0.04
-0.04
-0.06
-0.14
-0.06
-0.06
0.14
-0.02
-0.12
-0.06
-0.04
0.06
-0.04
-0.03
-0.03
-0.31
-0.04
-0.02
-0.03
-0.13
-0.07
-0.05
-0.07
-0.00
-0.04
-0.02
-0.04
-0.02
0.02
-0.04
-0.02
-0.40
-0.40
-0.02
-0.05
-0.02
-0.03
-0.12
-0.16
-0.06
-0.06
-0.01
-0.03
-0.01
-0.21
-0.14
-0.05
-0.08
0.18
-0.15
-0.09
-0.14
-0.16
0.09
0.18
-0.05
-0.08
0.08
-0.15
0.18
-0.09
-0.15
-0.18
-0.04
-0.16
-0.09
-0.08
-0.15
-0.09
-0.06
-0.06
-0.39
0.07
-0.03
-0.05
-0.23
-0.10
-0.07
-0.18
-0.01
-0.05
-0.04
0.05
0.04
-0.04
0.05
-0.04
-0.50
0.50
-0.04
-0.10
-0.04
0.14
-0.16
-0.20
-0.09
-0.15
-0.02
-0.06
-0.01
-0.30
-0.29
-0.09
-0.16
-0.24
-0.26
-0.21
-0.29
-0.20
-0.17
-0.24
-0.09
-0.22
-0.22
-0.26
-0.24
-0.17
-0.26
-0.24
-0.20
-0.20
-0.17
0.22
0.26
-0.21
-0.14
-0.09
0.47
0.11
-0.04
-0.09
0.31
-0.13
-0.10
-0.28
-0.01
-0.06
-0.06
-0.06
0.06
-0.06
-0.06
-0.06
-0.60
-0.60
-0.06
-0.15
-0.06
-0.29
-0.20
-0.24
-0.17
-0.26
-0.15
-0.09
-0.15
-0.39
-0.10
-0.06
-0.11
-0.20
-0.14
-0.10
-0.10
-0.30
-0.10
-0.20
-0.06
-0.10
-0.10
-0.14
0.20
-0.10
-0.14
-0.20
0.05
-0.30
-0.10
-0.10
-0.14
-0.10
-0.08
-0.07
-0.67
-0.09
-0.05
-0.06
-0.33
-0.10
-0.10
-0.16
-0.01
-0.07
-0.05
-0.07
0.05
0.05
-0.08
-0.05
-0.85
-0.70
-0.05
-0.10
-0.05
-0.10
-0.30
-0.39
-0.10
-0.14
-0.03
-0.07
-0.02
-0.41
-0.25
0.10
-0.21
-0.26
-0.24
-0.19
0.25
-0.40
0.14
-0.26
-0.10
-0.17
0.17
0.24
-0.26
-0.14
0.24
0.26
-0.11
0.40
-0.14
0.17
0.24
0.19
-0.17
0.12
0.74
0.16
0.07
-0.10
-0.59
0.14
-0.14
-0.27
-0.02
-0.12
-0.10
-0.12
0.10
0.10
-0.12
-0.10
-0.90
-0.75
-0.10
-0.20
-0.10
-0.25
-0.40
-0.49
-0.14
-0.24
-0.06
-0.12
-0.04
-0.57
-0.47
0.19
-0.41
-0.37
-0.38
-0.46
-0.47
-0.50
0.31
-0.37
-0.19
-0.54
-0.54
-0.38
-0.37
-0.31
-0.38
-0.37
-0.52
-0.50
-0.31
-0.54
-0.38
0.46
-0.40
0.20
-0.80
-0.22
-0.10
-0.19
-0.62
-0.18
-0.18
-0.38
-0.02
0.15
-0.15
-0.15
-0.15
0.15
-0.16
-0.15
-0.95
-0.80
-0.15
-0.30
-0.15
-0.47
-0.50
-0.59
-0.31
-0.38
-0.38
-0.20
-0.38
-0.72
STAT-UASTE
STAT-UASTE
STAT-UASTE
TOT-AVG
STAT -WASTE
ST AT -WASTE
STAT -WASTE
ENG-ANAL
STAT -WASTE
TOT-AVG
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
TOT-AVG
STAT -WASTE
STAT -WASTE
TOT-AVG
STAT
ENG-ANAL
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
GROUND
GT-WASTE
GT-WASTE
GT-WASTE
GROUND
GROUND
GT-SIC
GROUND
GT-SIC
GT-SIC
GROUND
GT-SIC
GT-WASTE
GT-WASTE
GT-SIC
STAT -WASTE
GROUND
STAT -WASTE
ENG-ANAL
STAT -WASTE
STAT-WASTE
STAT -WASTE
STAT
STAT-WASTE
STAT
STAT-WASTE
8
-------
SICJ> WASTE TOMS LB_89 MB_89 MB_89 LB_95 HB_95 HB_95 LB_09 HB_09 HB_09 SOUR
3339
3339
3353
3353
3353
3353
3353
3355
3355
3356
3361
3361
3361
3361
3398
3398
3600
3411
3411
3411
3411
3411
3411
3411
3411
3411
3411
3423
3423
3433
3433
3433
3433
3441
3441
3441
3441
3444
3444
3444
3451
3451
3462
3462
3462
3469
3469
3469
3469
3469
3469
3469
3469
3470
3470
3470
UT01
UT02
D001
F003
F004
F005
UT02
0001
F003
0001
D002
F001
K062
UP01
F001
UT02
U001
D001
0002
0008
F001
F003
F005
U122
UL02
WP02
WT02
0002
0007
0001
F001
F003
F005
0001
F001
F005
UT01
0001
F001
UT02
D001
F001
D007
0008
U001
0001
0002
0006
0007
0008
F006
K062
WT02
0001
0002
0006
4355.7
4151.5
7.98
1.23
0.33
7.65
7017.6
0.96
1.32
0.81
6.00
0.46
6.00
0.46
0.93
7.15
14.66
35.57
0.92
4.82
46.15
5.67
75.14
0.82
0.08
0.07
24.38
0.69
0.69
2.40
2.44
3.21
2.27
1.14
2.68
0.64
0.64
0.86
0.86
0.86
6.19
0.52
48.31
48.31
1.22
1.34
1.61
4.01
4.60
4.60
0.95
4.01
16.92
2.67
0.88
5.49
-0.05
0.01
0.01
-0.01
0.03
0.01
-0.01
0.01
-0.01
0.01
-0.04
-0.01
0.10
0.02
-0.01
0.01
0.05
0.00
0.00
0.00
0.00
0.00
0.01
0.00
0.00
-0.04
-0.01
0.61
0.05
0.01
-0.01
-0.01
-0.01
0.01
0.01
0.01
0.05
-0.01
0.01
0.01
0.01
0.01
-0.05
-0.01
-0.05
-0.01
-0.04
-0.09
-0.05
0.01
0.14
0.10
-0.01
-0.01
-0.61
-0.09
0.07
-0.01
-0.05
-0.01
-0.04
-0.02
-0.01
-0.05
-0.01
-0.05
-0.05
-0.09
-0.12
-0.04
-0.09
-0.01
-0.08
-0.08
-0.05
0.00
-0.47
-0.01
-0.02
-0.28
0.00
-0.09
-0.01
-0.63
-0.06
-0.05
-0.09
-0.01
-0.02
-0.05
-0.09
-0.02
-0.07
-0.05
-0.09
-0.01
-0.05
-0.09
-0.06
-0.03
-0.08
-0.05
-0.05
-0.12
-0.06
-0.03
-0.16
-0.12
-0.01
-0.05
-0.63
-0.12
-0.09
-0.03
-0.11
-0.04
-0.06
-0.03
-0.03
-0.11
-0.04
-0.11
-0.07
-0.18
-0.15
-0.08
-0.18
-0.03
-0.12
-0.15
-0.10
0.00
-0.95
-0.02
-0.03
-0.56
0.00
-0.13
-0.02
-0.66
-0.10
-0.11
-0.18
-0.04
-0.03
-0.11
-0.18
-0.03
-0.09
-0.11
-0.18
-0.03
0.11
-0.18
-0.10
0.08
-0.12
-0.11
-0.07
-0.17
-0.10
-0.08
-0.20
-0.15
-0.03
-0.11
-0.66
-0.17
-0.05
-0.03
-0.03
-0.03
-0.08
-0.03
-0.03
-0.03
-0.03
-0.03
-0.12
-0.06
-0.14
-0.12
-0.06
-0.03
-0.31
0.00
0.00
0.00
0.00
-0.05
-0.03
0.00
0.00
-0.32
-0.03
-0.62
-0.06
-0.03
-0.06
-0.03
-0.03
-0.03
-0.06
-0.03
-0.05
-0.03
-0.06
-0.03
-0.03
-0.06
-0.06
-0.04
-0.31
-0.03
-0.12
-0.11
-0.06
-0.04
-0.19
-0.14
-0.03
-0.03
-0.62
-0.11
0.10
0.05
0.14
-0.06
0.12
-0.06
-0.05
-0.14
-0.06
0.14
-0.16
0.15
-0.18
0.17
-0.15
-0.05
0.39
0.10
0.15
0.25
-0.49
-0.08
-0.05
-0.31
0.00
-0.41
-0.05
-0.65
-0.09
-0.14
-0.15
-0.06
-0.06
-0.14
-0.15
-0.06
-0.10
-0.14
0.15
0.05
0.14
-0.15
-0.09
-0.08
-0.39
0.14
0.16
0.17
-0.09
0.08
-0.23
0.18
-0.05
-0.14
0.65
-0.17
0.15
-0.09
-0.29
-0.14
-0.16
-0.09
-0.09
0.29
0.14
-0.29
-0.20
0.26
-0.24
-0.28
-0.26
-0.09
0.47
0.20
-0.30
-0.50
-0.90
-0.12
-0.07
-0.59
0.00
-0.49
-0.07
-0.68
0.17
-0.29
0.26
-0.14
-0.09
0.29
-0.26
0.09
0.15
-0.29
0.26
-0.09
-0.29
0.26
-0.17
0.22
-0.47
0.29
0.20
0.28
-0.17
0.22
-0.31
0.24
-0.09
-0.29
-0.68
-0.28
-0.10
-0.06
-0.10
-0.08
-0.21
-0.07
-0.06
-0.10
-0.08
-0.10
-0.30
-0.14
-0.20
-0.23
-0.14
-0.06
-0.67
-0.05
-0.05
0.00
-0.20
-0.10
-0.06
-0.13
0.00
0.57
-0.06
-0.65
-0.10
-0.10
-0.14
-0.08
-0.07
0.10
0.14
0.07
0.10
-0.10
-0.14
-0.06
-0.10
-0.14
-0.10
-0.10
-0.67
-0.10
-0.30
-0.17
-0.10
-0.10
-0.21
-0.20
-0.06
-0.10
-0.65
-0.17
-0.20
-0.10
-0.25
-0.17
-0.30
-0.12
-0.10
-0.25
0.17
-0.25
-0.40
-0.24
-0.26
-0.30
-0.24
-0.10
-0.74
-0.20
-0.47
-0.50
-0.60
-0.24
-0.11
-0.43
0.00
-0.61
-0.10
-0.69
-0.14
-0.25
-0.24
-0.17
-0.12
0.25
0.24
0.12
0.20
-0.25
-0.24
0.10
-0.25
0.24
-0.14
-0.17
-0.74
-0.25
-0.40
-0.25
-0.14
-0.17
-0.26
-0.26
-0.10
-0.25
-0.69
-0.25
-0.31
-0.19
-0.47
-0.40
-0.38
-0.20
0.19
-0.47
-0.40
-0.47
-0.50
-0.38
0.37
0.53
-0.38
-0.19
-0.80
-0.35
-0.90
-1.00
-0.99
-0.37
-0.15
-0.73
0.00
-0.66
-0.14
-0.74
-0.31
0.47
0.38
-0.40
-0.20
0.47
0.38
-0.20
-0.31
-0.47
-0.38
-0.19
-0.47
-0.38
-0.31
-0.54
-0.80
-0.47
-0.50
-0.50
-0.31
-0.54
-0.41
-0.37
-0.19
-0.47
-0.74
-0.50
STAT-UASTE
STAT -WASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
ENG-ANAL
STAT-UASTE
TOT-AVG
STAT-UASTE
ST AT -WASTE
STAT-UASTE
STAT-UASTE
GROUND
GROUND
GROUND
GROUND
GT- WASTE
GT-UASTE
GT-SIC
GT-UASTE
GT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
ENG-ANAL
STAT-UASTE
STAT-WASTE
STAT-WASTE
STAT-UASTE
TOT-AVG
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
-------
SIC_P WASTE TONS LB_89 MB_89 HB_89 LB_95 MB_95 H8_95 LB_09 HB_09 HB_09 SOUR
3470
3470
3470
3470
3470
3470
3470
3470
3470
3470
3471
3471
3471
3471
3471
3471
3471
3471
3471
3471
3471
3471
3471
3471
3471
3471
3479
3479
3479
3479
3479
3479
3479
3479
3479
3490
3494
3496
3499
3499
3499
3499
3499
3499
3499
3499
3499
3499
3500
3500
3532
3532
3532
3532
3532
0007
0008
F001
F002
FOOS
F006
IC006
WP01
WT01
WT02
0001
0002
0003
0006
0007
0008
F001
F002
FOOS
F006
F007
F008
F009
F019
WT01
WT02
0001
0002
0006
0007
0008
F001
F003
FOOS
K062
WT02
F001
K062
0001
0006
0007
0008
F001
F003
FOOS
UP01
WT01
WT02
0001
F002
0001
0006
0007
0008
WT02
6.19
5.70
6.09
0.63
2.47
4.97
2.49
0.14
0.91
2.70
48.14
83.73
0.78
55.86
136.51
11.63
23.01
0.67
34.06
92.10
0.78
5.66
9.22
69.48
15.53
59.30
9.73
460.91
274.37
278.49
274.37
3.95
2.34
9.58
332.94
4.05
3.91
68.00
1.22
0.33
0.33
1.97
0.83
1.22
0.77
0.83
0.33
2.08
0.91
0.04
2.25
2.44
0.19
0.19
0.19
-0.00
-0.00
-0.01
-0.01
-0.01
-0.14
-0.00
-0.02
-0.05
-0.01
-0.01
-0.04
-0.05
-0.05
-0.06
-0.02
-0.01
-0.01
-0.01
-0.02
-0.07
-0.18
-0.18
-0.18
-0.05
-0.01
-0.00
-0.03
-0.09
-0.04
-0.01
-0.01
-0.00
-0.01
-0.03
-0.01
-0.01
-0.10
-0.01
-0.09
-0.05
-0.01
-0.01
-0.01
-0.01
-0.02
-0.05
-0.01.
-0.01
-0.01
-0.01
-0.09
-0.05
-0.01
-0.01
-0.00
-0.00
-0.09
-0.03
-0.02
-0.16
-0.00
-0.04
-0.07
0.01
-0.07
-0.05
-0.07
-0.07
-0.08
0.03
0.12
-0.03
-0.02
-0.03
-0.10
-0.20
-0.20
-0.20
-0.07
-0.01
-0.00
-0.06
-0.12
-0.06
-0.03
-0.09
-0.01
-0.02
-0.06
-0.01
-0.09
-0.12
-0.02
-0.12
-0.06
-0.03
-0.09
-0.02
-0.02
-0.04
-0.07
-0.01
0.05
-0.03
-0.05
-0.12
-0.06
-0.03
-0.01
-0.08
-0.05
-0.18
0.07
-0.03
-0.20
-0.07
-0.08
-0.09
-0.03
-0.13
-0.07
-0.08
-0.08
-0.10
-0.05
-0.21
-0.04
-0.03
-0.05
-0.13
-0.22
-0.22
-0.22
-0.09
-0.02
-0.04
-0.07
-0.17
-0.10
-0.08
-0.18
-0.02
-0.02
-0.08
-0.03
-0.18
-0.15
-0.04
e-0.17
-0.10
-0.08
-0.18
-0.04
-0.03
-0.08
-0.09
-0.03
-0.11
0.07
-0.11
-0.17
-0.10
-0.08
-0.03
-0.00
-0.00
-0.06
-0.04
-0.03
0.19
0.00
-0.12
0.05
-0.03
-0.03
-0.12
-0.16
-0.16
-0.07
-0.05
-0.07
-0.04
-0.03
-0.04
-0.23
-0.20
-0.20
-0.20
-0.05
-0.03
-0.01
-0.09
0.11
-0.05
-0.04
0.06
0.01
-0.02
-0.07
-0.03
-0.06
-0.14
0.04
0.11
-0.06
-0.04
-0.06
-0.04
-0.03
-0.12
-0.05
-0.03
-0.03
-0.04
-0.03
-0.11
-0.06
-0.04
-0.03
-0.01
-0.01
0.15
-0.09
-0.06
-0.23
-0.01
-0.17
-0.10
-0.05
-0.21
-0.16
-0.20
-0.20
-0.10
0.07
-0.18
0.10
-0.05
-0.09
-0.27
-0.25
-0.25
-0.25
-0.10
-0.05
-0.01
-0.18
-0.17
-0.08
-0.08
-0.15
-0.02
-0.05
-0.14
-0.05
-0.15
-0.18
-0.07
-0.17
-0.09
-0.08
-0.15
-0.07
-0.06
-0.17
-0.10
-0.05
0.14
0.09
-0.14
-0.17
-0.09
-0.08
-0.05
-0.25
0.14
-0.26
-0.21
-0.09
-0.31
-0.20
-0.28
0.15
0.09
-0.38
-0.20
-0.24
-0.24
-0.13
-0.10
-0.28
-0.16
-0.07
-0.15
-0.31
0.29
0.29
0.29
0.15
0.07
0.13
-0.22
-0.28
-0.19
-0.22
-0.26
-0.05
-0.06
-0.20
-0.09
-0.26
-0.24
-0.12
-0.28
-0.17
-0.22
-0.26
-0.12
-0.09
-0.28
-0.15
-0.09
-0.29
0.21
-0.29
-0.28
-0.17
-0.22
-0.09
-0.01
-0.01
-0.14
-0.10
-0.07
-0.21
-0.01
-0.23
-0.10
-0.06
-0.12
-0.30
-0.40
-0.40
-0.10
-0.10
-0.16
-0.11
-0.06
0.11
0.49
-0.27
-0.27
-0.27
-0.10
-0.06
-0.02
-0.23
-0.17
-0.09
-0.10
-0.14
-0.03
-0.06
-0.17
-0.06
-0.14
-0.20
-0.09
-0.17
-0.10
-0.10
-0.14
-0.09
-0.07
-0.23
-0.10
-0.06
-0.10
-0.10
-0.10
-0.17
-0.10
-0.10
-0.06
-0.02
-0.02
-0.24
'-0.19
-0.12
-0.26
-0.02
-0.30
-0.20
0.10
-0.31
-0.40
-0.50
-0.50
-0.14
-0.14
-0.27
-0.18
-0.11
-0.22
-0.54
-0.34
-0.34
-0.34
-0.20
-0.10
-0.04
-0.46
-0.25
-0.13
-0.17
-0.24
-0.06
-0.13
-0.33
-0.10
-0.24
-0.26
-0.18
-0.25
-0.14
0.17
-0.24
-0.18
-0.12
-0.30
-0.20
-0.10
-0.25
-0.19
-0.25
-0.25
-0.14
-0.17
-0.10
-0.65
-0.35
-0.38
-0.46
-0.20
-0.41
-0.51
-0.53
-0.31
-0.19
-0.50
-0.50
-0.60
-0.60
-0.18
-0.18
-0.38
-0.25
-0.15
-0.34
-0.59
-0.40
-0.40
-0.40
-0.30
-0.14
-0.33
-0.55
-0.50
-0.37
-0.54
-0.38
-0.12
-0.14
-0.48
-0.19
-0.38
-0.37
-0.31
-0.50
-0.31
0.54
-0.38
-0.31
-0.20
-0.53
-0.31
-0.19
-0.47
-0.46
-0.47
-0.50
-0.31
-0.54
-0.19
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
GT-WASTE
ENG-ANAL
ENG-ANAL
ENG-ANAL
GT-WASTE
GT-WASTE
GT-WASTE
GT-WASTE
GT-WASTE
GROUND
GT-WASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT-A
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT-SIC
STAT-WASTE
STAT-WASTE
TOT-AVG
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
10
-------
SIC_P WASTE TONS LB.89 MB_89 HB_89 LB_95 HB_9S HB_95 LB_09 HB_09 NB_09 SOUR
3535
3536
3536
3536
3536
3536
3536
3536
3536
3541
3541
3545
3545
3545
3545
3545
3545
3545
3545
3545
3545
3545
3549
3549
3551
3551
3551
3551
3553
3553
3553
3553
3554
3554
3554
3554
3554
3554
3554
3554
3554
3555
3555
3555
3559
3559
3559
3560
3560
3560
3561
3561
3561
3563
3563
3563
F005
0001
D002
D006
D007
F002
F003
F005
UT02
0001
FOOS
0001
0002
D003
0005
0006
0007
0008
F002
FOOS
UT01
UT02
F003
FOOS
0001
F001
F003
FOOS
0001
0007
0009
UT01
0001
0002
0003
D006
0007
0008
FOOS
WT01
UT02
0001
F001
UT02
0001
F002
UT02
0001
F003
FOOS
0001
F001
F004
0001
0006
0007
0.65
1.74
0.50
0.90
0.50
0.41
1.46
2.70
15.26
0.45
0.45
0.33
0.03
0.12
0.06
0.97
0.65
0.10
0.00
0.04
0.90
0.53
6.07
6.07
1.97
0.30
0.30
0.30
2.52
0.80
0.80
2.52
2.96
1.21
0.07
0.07
0.15
0.48
2.80
0.72
0.42
0.18
2.35
5.99
1.22
1.40
0.03
0.83
0.83
0.83
0.17
0.03
0.03
0.72
2.08
2.19
-0.01
0.01
-0.61
-0.09
-0.05
-0.01
-0.01
0.01
-0.01
-0.01
-0.01
-0.01
-0.61
-0.05
-0.00
-0.02
-0.01
-0.01
-0.01
-0.01
-0.02
-0.01
0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.05
-0.02
-0.05
-0.01
-0.02
-0.05
-0.09
-0.05
-0.01
-0.01
-0.02
-0.01
-0.01
-0.01
-0.01
0.01
-0.01
-0.01
0.01
0.01
-0.01
-0.01
-0.01
-0.03
-0.01
-0.09
-0.05
-0.02
-0.02
-0.63
-0.12
-0.06
-0.03
-0.01
-0.03
-0.01
-0.05
-0.02
-0.05
-0.63
-0.07
-0.01
-0.03
-0.02
-0.03
-0.03
-0.02
-0.04
-0.01
0.01
-0.02
-0.05
-0.09
-0.01
-0.02
-0.05
-0.06
-0.03
-0.07
-0.05
-0.03
0.07
-0.12
-0.06
-0.01
-0.02
-0.04
-0.01
-0.05
-0.09
-0.01
-0.05
-0.03
-0.01
-0.05
-0.01
-0.02
-0.05
-0.09
-0.04
-0.05
-0.12
-0.06
-0.03
-0.03
-0.66
-0.17
-0.10
-0.07
-0.04
-0.04
-0.03
-0.11
-0.03
-0.11
-0.66
-0.08
-0.10
-0.06
-0.05
-0.08
-0.07
-0.03
-0.05
-0.03
-0.04
-0.03
0.11
-0.18
-0.04
-0.03
-0.11
-0.10
0.09
-0.09
-0.11
-0.05
-0.08
-0.17
-0.10
-0.06
-0.03
-0.06
-0.03
-0.11
-0.18
-0.03
-0.11
-0.07
-0.03
-0.11
-0.04
-0.03
-0.11
-0.18
-0.06
-0.11
-0.17
-0.10
-0.03
-0.03
-0.62
0.11
-0.06
-0.04
-0.03
-0.04
-0.03
-0.03
-0.03
-0.03
-0.62
-0.16
-0.01
-0.05
-0.03
-0.04
-0.04
-0.03
-0.06
-0.03
-0.03
-0.03
-0.03
-0.06
0.03
-0.03
-0.03
-0.06
-0.05
-0.05
-0.03
-0.05
0.16
-0.11
-0.06
-0.02
-0.03
-0.06
-0.03
-0.03
-0.06
-0.03
-0.03
-0.04
-0.03
-0.03
0.03
-0.03
-0.03
-0.06
-0.08
-0.03
-0.11
-0.06
-0.06
-0.06
-0.65
-0.17
-0.09
-0.09
-0.06
-0.09
-0.05
-0.14
-0.06
-0.14
-0.65
-0.20
-0.02
-0.10
-0.05
-0.08
-0.09
-0.06
-0.11
0.05
0.06
0.06
0.14
-0.15
-0.06
0.06
-0.14
0.09
-0.10
-0.10
-0.14
-0.09
-0.20
-0.17
0.09
-0.04
-0.06
-0.12
-0.05
-0.14
-0.15
-0.05
0.14
-0.09
-0.05
0.14
-0.06
-0.06
0.14
0.15
-0.12
-O.U
0.17
-0.09
-0.09
-0.10
-0.68
-0.28
0.17
-0.21
0.14
0.12
0.09
-0.29
-0.09
0.29
-0.68
-0.24
-0.30
-0.18
-0.16
-0.22
-0.21
-0.09
-0.14
-0.09
-0.14
-0.09
0.29
0.26
0.14
0.09
-0.29
-0.17
-0.28
-0.15
0.29
-0.15
-0.24
-0.28
-0.17
-0.18
-0.09
-0.19
-0.09
-0.29
-0.26
-0.09
0.29
-0.21
-0.09
-0.29
-0.14
0.09
-0.29
-0.26
-0.16
-0.29
-0.28
-0.17
-0.07
0.07
0.65
0.17
-0.10
-0.10
-0.08
0.11
0.06
-0.10
-0.07
0.10
-0.65
-0.39
-0.03
-0.13
0.07
-0.10
-0.10
-0.07
-0.14
-0.06
-0.08
-0.07
-0.10
-0.14
-0.08
0.07
-0.10
0.10
0.12
-0.10
-0.10
-0.12
-0.39
-0.17
-0.10
-0.05
-0.07
-0.15
0.06
-0.10
-0.14
-0.06
-0.10
-0.10
-0.06
-0.10
-0.08
0.07
-0.10
-0.14
-0.21
-0.10
-0.17
-0.10
-0.12
0.15
0.69
0.25
-0.14
0.19
0.17
-0.23
-0.10
-0.25
-0.12
-0.25
-0.69
-0.49
-0.05
-0.26
0.13
0.17
-0.19
-0.12
-0.28
0.10
0.17
0.12
-0.25
-0.24
-0.17
-0.12
-0.25
-0.14
-0.25
-0.20
0.25
0.24
-0.49
-0.25
-0.14
-0.09
-0.12
-0.31
0.10
0.25
-0.24
0.10
-0.25
-0.19
-0.10
-0.25
-0.17
0.12
-0.25
-0.24
-0.30
-0.25
-0.25
-0.14
-0.20
-0.24
0.74
-0.50
0.31
-0.46
-0.40
-0.30
-0.19
-0.47
-0.20
0.47
-0.74
0.59
0.76
0.47
-0.41
-0.54
-0.46
-0.20
-0.37
-0.19
-0.40
-0.20
-0.47
-0.38
-0.40
-0.20
-0.47
-0.31
-0.72
-0.31
0.47
-0.39
-0.59
0.50
-0.31
-0.46
-0.20
-0.48
0.19
0.47
-0.38
-0.19
-0.47
-0.46
-0.19
0.47
0.40
-0.20
0.47
0.38
-0.38
-0.47
-0.50
-0.31
STAT-UASTE
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
11
-------
SIC P UASTE TONS LB 89 MB 89 HB 89 LB 95 MB 95 KB 95 LB 09 MB 09 HB 09 SOUR
3563
3563
3563
3563
3563
3569
3572
3572
3573
3573
3573
3573
3573
3573
3573
3573
3573
3573
3573
3573
3573
3582
3582
3585
3589
3589
3589
3589
3599
3599
3599
3599
3599
3599
3599
3599
3599
3599
3599
3599
3599
3599
3599
3599
3599
3602
3602
3603
3603
3612
3612
3613
3613
3613
3613
3622
0008
F003
F005
WT01
UT02
WT02
0002
F001
0001
0002
0007
0008
0011
F001
F002
F003
F005
F006
U122
UP01
WT02
F001
F002
F001
0001
F003
F005
UT02
0001
0002
0004
0005
D006
0007
0008
F001
F002
F003
F005
P058
U057
WC01
UP01
WT01
UT02
D002
WT02
0001
WT02
F003
F005
0001
0008
F003
F005
0002
2.08
0.72
0.72
2.08
0.11
0.86
10.55
3.36
50.11
402.30
4.32
35.00
0.38
5.17
10.82
12.39
0.08
289.80
0.45
10.61
5.49
1.10
34.54
2.92
0.25
0.23
0.23
0.46
12.47
17.73
0.21
0.21
2.80
17.53
4.29
2.89
1.06
1.47
8.54
0.00
0.00
5.56
1.07
19.84
3.08
4.14
4.14
2.02
2.02
2.06
6.88
0.40
0.99
1.39
0.40
0.44
0.01
-0.01
0.01
-0.05
-0.01
-0.01
-0.04
-0.01
0.01
-0.03
0.05
-0.01
-0.01
-0.02
-0.01
-0.01
-0.01
-0.14
-0.03
-0.02
-0.01
-0.01
-0.01
-0.01
0.01
0.01
-0.01
0.01
0.03
-0.01
-0.01
-0.00
-0.09
-0.01
-0.04
-0.01
-0.01
-0.01
-0.00
-0.01
-0.01
-0.04
-0.02
-0.01
-0.01
-0.04
-0.01
-0.01
0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.61
-0.03
0.01
-0.02
-0.07
-0.01
0.01
-0.05
-0.09
-0.02
-0.06
-0.06
-0.03
0.02
0.04
-0.03
0.01
0.02
-0.16
0.05
-0.04
-0.03
-0.09
0.03
0.09
0.05
0.01
0.02
0.01
0.07
0.02
-0.03
0.01
-0.12
0.01
-0.08
-0.09
-0.03
-0.01
-0.00
-0.02
-0.02
-0.05
-0.04
-0.01
-0.01
-0.05
-0.01
-0.05
-0.01
-0.01
0.02
-0.05
-0.03
-0.01
-0.02
-0.63
-0.08
-0.04
-0.03
-0.09
-0.03
-0.03
-0.07
-0.18
-0.08
-0.06
-0.10
0.08
0.05
0.05
0.07
-0.04
0.03
-0.20
-0.06
-0.08
-0.03
-0.18
0.07
0.18
0.11
0.04
0.03
0.03
0.08
0.10
-0.06
0.10
-0.17
-0.04
-0.09
-0.18
0.07
-0.04
-0.02
-0.06
0.06
-0.06
-0.08
-0.04
-0.03
-0.07
-0.03
0.11
-0.03
-0.04
-0.03
-0.11
-0.08
-0.04
-0.03
-0.66
-0.04
-0.03
-0.03
0.05
-0.03
-0.03
-0.12
-0.06
-0.02
-0.09
-0.06
-0.04
-0.03
-0.06
-0.04
-0.03
-0.03
-0.19
-0.08
-0.12
-0.04
-0.06
-0.04
-0.06
-0.03
-0.03
-0.03
-0.03
0.10
-0.03
-0.04
-0.01
-0.11
-0.02
-0.13
-0.06
-0.04
-0.03
-0.00
-0.04
-0.04
-0.11
-0.12
-0.02
-0.03
-0.12
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.04
-0.03
-0.03
-0.62
-0.08
-0.06
-0.06
-0.10
-0.05
-0.05
-0.16
-0.15
-0.05
0.17
0.09
-0.08
-0.05
-0.12
-0.09
0.06
-0.06
-0.23
-0.16
-0.17
-0.09
-0.15
-0.09
-0.15
-0.14
-0.06
-0.06
-0.05
-0.20
-0.05
-0.08
-0.02
-0.17
-0.03
-0.25
-0.15
-0.09
-0.06
-0.01
-0.07
-0.07
-0.15
0.17
-0.04
-0.05
-0.16
-0.05
-0.14
-0.05
-0.06
-0.06
-0.14
-0.08
-0.06
-0.06
-0.65
0.22
-0.14
0.09
-0.15
-0.09
-0.09
-0.20
-0.26
-0.24
0.18
-0.17
-0.22
-0.14
-0.14
-0.21
-0.14
-0.09
-0.31
-0.19
-0.28
-0.10
-0.26
-0.21
-0.26
-0.29
-0.14
-0.09
-0.09
-0.25
0.29
-0.16
-0.30
-0.28
0.11
0.27
-0.26
0.21
-0.14
0.07
-0.18
-0.18
-0.19
-0.28
-0.11
-0.09
-0.20
-0.09
-0.29
-0.09
-0.14
-0.09
-0.29
-0.22
-0.14
-0.09
-0.68
-0.10
0.08
0.07
-0.10
-0.06
0.06
-0.30
-0.14
-0.06
0.22
-0.10
0.10
0.07
0.15
-0.10
0.08
0.07
-0.21
-0.20
-0.23
0.11
-0.14
-0.10
-0.14
0.10
0.08
-0.07
0.06
0.26
0.07
-0.11
0.03
-0.17
-0.04
-0.32
-0.14
-0.10
0.08
-0.01
-0.09
-0.09
-0.29
-0.23
-0.05
-0.06
-0.30
-0.06
-0.10
-0.06
0.08
-0.07
-0.10
-0.10
-0.08
-0.07
-0.65
0.17
0.17
0.12
0.20
-0.10
-0.10
-0.40
-0.24
-0.13
-0.44
-0.14
0.17
0.11
0.31
-0.19
0.17
0.12
-0.26
0.40
-0.30
0.22
-0.24
0.19
0.24
0.25
0.17
-0.12
-0.10
0.51
-0.14
-0.21
-0.05
-0.25
-0.08
-0.64
-0.24
0.19
-0.17
-0.02
-0.19
0.19
-0.38
-0.30
-0.09
-0.10
0.40
-0.10
-0.25
-0.10
0.17
-0.12
-0.25
-0.17
-0.17
-0.12
-0.69
-0.54
-0.40
-0.20
-0.31
-0.19
-0.19
-0.50
-0.38
-0.61
0.47
0.31
-0.54
0.33
-0.36
0.46
-0.40
-0.20
-0.41
0.48
-0.53
-0.27
-0.38
-0.46
-0.38
-0.47
-0.40
-0.20
-0.19
-0.65
-0.74
-0.41
0.76
-0.50
0.29
-0.69
-0.38
0.46
-0.40
0.19
-0.45
-0.45
-0.47
-0.53
-0.28
0.19
0.50
-0.19
-0.47
-0.19
-0.40
-0.20
-0.47
-0.54
-0.40
-0.20
-0.74
STAT -WASTE
ST AT -WASTE
STAT -WASTE
STAT -WASTE
STAT-WASTE
STAT -WASTE
ENG-ANAL
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
12
-------
SIC_P WASTE TONS LB_89 MB_89 HB_89 LB_95 HB_95 HB_95 LB_09 MB_09 HB_09 SOUR
3622
3622
3623
3623
3623
3623
3623
3623
3629
3629
3634
3639
3646
3661
3661
3662
3662
3662
3662
3662
3662
3662
3662
3662
3662
3662
3662
3670
3670
3670
3674
3674
3674
3674
3674
3674
3674
3674
3674
3674
3674
3674
3674
3674
3674
3674
3675
3675
3675
3675
3679
3679
3679
3679
3679
3679
0011
F001
0001
D002
D006
0007
0008
F003
0002
0007
D001
F002
F003
D002
0006
0001
0002
D006
D007
0008
0011
F001
F002
F003
F005
UT01
UT02
0001
F001
F003
0001
0002
0003
0006
0007
0008
0009
F001
F002
F003
F005
UL01
UL02
UP01
UT01
UT02
0005
0008
F001
F006
0001
0002
0006
0007
D008
F001
0.08
0.69
1.17
1.67
1.67
1.78
1.78
1.17
0.55
0.18
1.85
8.67
32.19
0.30
0.03
4.89
19.17
0.38
3.12
6.29
0.23
13.90
0.14
1.19
1.62
6.29
13.24
0.27
0.58
0.27
38.90
8.61
0.00
0.08
16.91
3.14
3.06
3.09
7.07
17.17
4.66
0.06
1.24
0.95
0.06
240.01
26.75
20.35
6.37
2.76
5.13
292.02
6.66
13.75
170.07
4.43
0.01
-0.01
0.01
-0.04
-0.09
0.05
0.01
-0.01
-0.61
0.05
0.01
-0.01
-0.01
-0.61
0.09
0.02
0.01
-0.09
-0.01
-0.01
-0.01
-0.00
-0.01
0.01
0.01
-0.05
-0.02
0.01
-0.01
-0.01
0.02
0.71
-0.02
-0.15
-0.06
-0.02
0.01
-0.01
-0.04
-0.00
-0.01
0.00
0.00
0.05
0.05
-0.01
-0.00
-0.01
-0.01
0.14
0.01
-0.04
-0.00
0.01
-0.01
-0.01
0.02
-0.09
-0.05
-0.05
-0.12
0.06
-0.03
-0.01
-0.63
.-0.06
-0.05
-0.03
-0.01
-0.63
-0.12
-0.03
-0.02
-0.12
-0.01
-0.02
-0.02
-0.00
-0.03
0.01
-0.02
-0.07
-0.04
-0.05
-0.09
-0.01
-0.06
-0.73
-0.09
-0.18
-0.08
-0.03
-0.04
-0.57
-0.07
-0.01
-0.02
-0.03
0.00
0.10
0.07
-0.01
-0.01
-0.03
-0.09
-0.16
-0.03
-0.05
-0.01
-0.02
-0.02
-0.09
-0.05
-0.18
0.11
0.07
-0.17
0.10
0.08
0.04
-0.66
-0.10
0.11
-0.07
0.04
0.66
0.17
-0.19
-0.10
-0.17
-0.04
0.04
0.05
0.27
0.07
-0.04
-0.14
-0.09
-0.19
-0.11
-0.18
-0.04
0.10
0.75
-0.10
-0.22
0.10
-0.05
0.06
-0.10
0.10
-0.02
-0.03
-0.05
0.00
0.15
0.09
-0.02
-0.10
0.08
-0.18
-0.20
0.05
-0.07
-0.09
-0.06
-0.09
-0.18
-0.03
-0.06
-0.03
-0.12
-0.11
-0.06
-0.04
-0.03
-0.62
-0.06
-0.03
-0.04
-0.03
-0.62
0.11
-0.05
-0.04
-0.11
-0.02
-0.03
-0.03
-0.01
-0.04
-0.03
-0.04
-0.05
-0.06
-0.03
-0.06
-0.03
-0.05
-0.71
-0.06
-0.16
0.07
-0.05
0.13
-0.04
0.13
-0.05
-0.03
0.00
0.00
-0.40
-0.05
-0.03
-0.01
-0.04
-0.06
-0.19
-0.04
-0.12
-0.01
-0.03
-0.03
-0.06
-0.05
-0.15
-0.14
-0.16
-0.17
-0.09
-0.08
-0.06
-0.65
-0.09
-0.14
-0.09
-0.06
-0.65
-0.17
-0.09
0.07
-0.17
-0.04
-0.05
-0.05
-0.01
-0.09
-0.06
-0.07
-0.10
-0.13
-0.14
-0.15
-0.06
-0.40
-0.74
-0.40
-0.22
-0.10
-0.07
-0.22
-0.40
-0.44
-0.08
-0.05
-0.04
0.00
-0.50
-0.10
-0.05
-0.02
-0.08
-0.15
-0.23
-0.08
-0.16
-0.02
-0.05
-0.06
-0.15
-0.14
-0.26
0.29
0.20
-0.28
0.17
-0.22
0.14
-0.68
0.17
-0.29
-0.21
0.14
-0.68
0.28
-0.27
-0.23
-0.28
-0.11
-0.11
0.14
-0.34
-0.21
-0.14
-0.20
-0.15
-0.29
0.29
-0.26
-0.14
0.75
0.76
-0.75
0.27
-0.13
-0.10
-0.32
-0.75
-0.76
-0.12
-0.07
0.06
0.00
-0.60
0.15
-0.07
-0.30
-0.22
-0.26
-0.31
-0.16
-0.20
-0.27
-0.19
-0.25
-0.26
-0.07
-0.14
-0.10
-0.30
-0.17
-0.10
-0.10
-0.08
-0.65
-0.10
-0.10
-0.10
-0.08
-0.65.
-0.17
-0.12
-0.09
-0.17
-0.05
-0.06
-0.07
-0.02
-0.10
-0.08
-0.09
-0.10
-0.16
-0.10
-0.14
-0.08
-0.12
-0.72
-0.15
-0.20
-0.10
-0.10
0.23
0.11
-0.34
0.10
0.06
0.00
0.00
-0.70
-0.10
-0.06
-0.03
-0.10
0.14
-0.21
0.10
-0.30
-0.03
-0.07
-0.08
-0.14
0.11
-0.24
0.25
0.40
-0.25
-0.14
0.17
0.17
-0.69
0.14
0.25
-0.19
0.17
0.69
0.25
-0.24
-0.19
0.25
-0.10
-0.13
0.11
0.03
0.19
0.17
0.19
-0.20
-0.33
0.25
0.24
0.17
0.51
0.74
-0.54
-0.26
0.14
-0.14
0.51
0.55
-0.68
-0.24
-0.11
0.05
0.00
-0.75
-0.20
-0.10
0.05
0.17
-0.24
-0.26
-0.21
-0.40
-0.06
-0.13
-0.14
-0.24
-0.33
-0.38
0.47
-0.50
-0.50
-0.31
-0.54
-0.40
-0.74
-0.31
-0.47
-0.46
-0.40
-0.74
-0.50
-0.45
-0.54
-0.50
-0.29
-0.29
-0.33
-0.49
-0.46
-0.40
-0.32
-0.31
-0.53
0.47
-0.38
-0.40
-0.90
-0.77
-0.92
-0.33
-0.18
-0.18
-0.80
-1.00
-1.00
-0.37
-0.15
-0.07
0.00
-0.80
-0.30
-0.14
-0.76
-0.54
-0.38
-0.41
-0.41
-0.50
-0.69
-0.49
-0.61
-0.38
STAT -WASTE
STAT-WASTE
STAT -WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
GROUND
GT-WASTE
GT-SIC
GT-WASTE
GT-WASTE
GT-WASTE
GT-WASTE
GROUND
GROUND
GT-WASTE
GT-WASTE
GT-WASTE
GT-WASTE
GT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
ENG-ANAL
STAT
STAT
STAT
STAT-WASTE
13
-------
SIC P WASTE TONS LB 89 MB 89 HB 89 LB 95 MB 95 HB 95 LB 09 MB 09 MB 09 SOUR
3679
3679
3679
3679
3679
3679
3679
3679
3679
3691
3691
3694
3694
3698
3698
3699
3699
3699
3700
3700
3700
3700
3700
3700
3700
3703
3703
3703
3703
3703
3703
3703
3710
3714
3714
3714
3714
3714
3714
3715
3715
3715
3715
3715
3720
3720
3720
3720
3721
3721
3721
3721
3721
3721
3721
3721
F002
F003
F005
F006
F007
F009
WP01
UT01
UT02
0002
0008
D001
F001
D008
UT02
F001
U080
U118
0001
0002
F001
F002
F003
F005
UT02
0001
D002
F001
F003
F005
WP01
WT02
F001
D001
0002
0008
F001
F003
F005
0001
F003
F005
WP03
UT01
0006
0007
D008
WT02
0001
0002
0003
0006
D007
0008
0009
0011
2.08
0.43
0.66
87.73
9.16
1.64
0.52
28.95
55.85
33.46
0.22
0.82
0.41
0.75
0.75
3.66
0.15
0.15
268.83
0.34
3.68
0.30
14.21
121.92
1544.6
1.06
0.11
7.56
1.06
0.77
0.78
0.40
1.75
9.90
4.74
0.40
5.20
1.31
6.51
2.08
1.91
2.25
0.36
0.37
0.07
0.40
0.07
0.47
1265.4
4075.1
4.35
490.18
3636.5
418.97
2.22
12.86
0.02
-0.01
0.01
-0.00
-0.07
-0.18
-0.02
0.01
-0.01
-0.04
0.01
0.01
-0.01
0.01
0.01
0.01
-0.10
-0.10
0.00
-0.61
0.01
-0.01
0.01
0.01
0.01
0.01
-0.61
0.00
-0.01
0.01
-0.02
0.01
0.01
0.01
-0.04
-0.01
0.01
-0.01
-0.01
-0.00
0.01
-0.01
-0.01
0.05
0.09
-0.05
-0.01
-0.01
-0.01
-0.01
0.01
0.01
-0.01
-0.01
-0.01
-0.01
-0.04
-0.01
-0.02
-0.01
-0.10
-0.20
-0.04
-0.01
-0.02
-0.05
-0.03
-0.05
-0.09
-0.03
-0.01
-0.09
-0.12
-0.12
-0.01
-0.63
-0.09
-0.03
-0.01
-0.02
-0.01
-0.02
-0.63
-0.00
-0.02
-0.02
-0.04
0.01
-0.09
-0.05
-0.05
-0.03
-0.09
-0.01
-0.02
-0.01
-0.01
-0.02
-0.02
-0.07
-0.12
-0.06
-0.03
-0.01
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.04
-0.02
-0.05
-0.04
-0.03
-0.09
0.13
-0.22
-0.08
-0.08
-0.09
-0.07
-0.08
-0.11
-0.18
0.08
0.03
0.18
-0.15
0.15
-0.06
-0.66
-0.18
0.07
0.04
-0.03
-0.03
-0.18
-0.66
-0.16
0.18
-0.03
-0.08
-0.03
0.18
-0.11
-0.07
-0.08
-0.18
-0.04
-0.03
-0.01
-0.04
-0.18
-0.02
-0.09
0.17
-0.10
-0.08
-0.03
-0.02
-0.02
-0.03
0.03
-0.02
-0.03
-0.06
-0.03
-0.06
-0.03
-0.03
-0.01
-0.22
-0.20
-0.12
-0.02
-0.02
-0.12
-0.04
-0.03
-0.06
-0.04
-0.03
-0.06
-0.14
-0.14
-0.01
-0.62
-0.06
-0.04
-0.03
-0.03
-0.03
-0.03
-0.62
-0.00
-0.03
-0.03
-0.12
-0.03
-0.06
-0.03
-0.12
-0.04
-0.06
-0.03
-0.03
-0.01
-0.03
-0.02
-0.02
-0.05
-0.11
-0.06
0.04
-0.03
-0.01
-0.01
-0.02
-0.04
-0.01
-0.03
-0.13
-0.02
-0.12
-0.06
-0.06
-0.03
-0.26
0.25
-0.17
-0.04
-0.05
-0.16
-0.08
-0.14
-0.15
-0.08
-0.05
-0.15
0.18
0.18
-0.02
-0.65
-0.15
-0.09
0.06
-0.06
-0.05
-0.05
-0.65
-0.01
-0.05
-0.06
-0.17
-0.05
-0.15
0.14
-0.16
-0.08
-0.15
-0.06
-0.06
-0.03
-0.06
-0.05
-0.04
-0.10
-0.17
-0.09
-0.08
-0.05
-0.03
0.03
-0.04
0.06
-0.03
-0.05
-0.22
-0.04
-0.15
-0.14
-0.09
0.27
-0.30
-0.29
-0.28
-0.23
-0.27
-0.20
-0.22
-0.29
-0.26
-0.22
-0.09
-0.26
-0.24
-0.24
-0.18
-0.68
0.26
-0.21
-0.14
-0.09
-0.09
-0.24
-0.68
-0.26
-0.24
-0.09
-0.28
-0.09
-0.26
-0.29
-0.20
-0.22
-0.26
-0.14
-0.09
-0.04
-0.14
-0.23
-0.06
-0.15
-0.28
-0.17
-0.22
0.09
-0.05
-0.05
-0.06
-0.08
-0.05
-0.07
-0.32
-0.06
-0.16
-0.08
-0.07
-0.03
-0.48
-0.27
-0.23
-0.05
-0.06
-0.30
-0.10
-0.10
-0.14
-0.10
-0.06
-0.14
-0.20
-0.20
-0.02
-0.65
0.14
-0.10
0.08
-0.07
0.06
-0.07
0.65
0.01
0.07
-0.07
-0.23
-0.06
-0.14
-0.10
-0.30
-0.10
-0.14
-0.08
-0.07
-0.03
-0.08
-0.06
-0.05
-0.10
-0.17
-0.10
-0.10
-0.06
-0.03
0.04
-0.07
0.10
-0.05
-0.08
-0.23
-0.07
-0.31
-0.17
-0.12
0.07
-0.53
-0.34
-0.30
-0.10
-0.12
-0.40
-0.17
-0.25
-0.24
-0.17
-0.10
-0.24
-0.26
-0.26
-0.04
-0.69
-0.24
0.19
-0.17
-0.12
-0.10
-0.14
-0.69
-0.02
-0.14
-0.12
-0.30
-0.10
-0.24
-0.25
-0.40
-0.17
0.24
-0.17
-0.12
-0.07
0.17
-0.12
-0.10
-0.20
-0.25
-0.14
-0.17
-0.10
-0.05
-0.06
-0.09
0.13
-0.07
-0.11
0.51
-0.09
-0.37
-0.40
-0.20
-0.69
-0.58
-0.40
-0.53
-0.58
-0.70
-0.50
-0.54
-0.47
-0.38
-0.54
-0.19
-0.38
-0.37
-0.37
-0.45
-0.74
-0.38
-0.46
-0.40
-0.20
0.19
-0.37
0.74
-0.50
0.37
-0.20
-0.53
-0.19
-0.38
0.47
-0.50
-0.54
-0.38
-0.40
-0.20
-0.11
-0.40
-0.33
-0.15
-0.31
-0.50
-0.31
-0.54
-0.19
-0.07
-0.08
-0.11
-0,16
-0.09
-0.14
-0.80
-0.11
STAT
ST AT -WASTE
STAT -WASTE
STAT
STAT -WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT -WASTE
TOT-AVG
TOT-AVG
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
GROUND
GROUND
GT-S1C
GROUND
GROUND
GROUND
GT -WASTE
GT-SIC
14
-------
S1C_P WASTE TONS LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3724
3724
3724
3724
3724
3724
3724
3724
3725
3725
3725
3725
3725
3725
3725
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
3728
D016
F001
F002
F003
F004
F005
F006
F007
F008
P030
POM
U188
U001
UC01
UL01
UL02
WP01
WP02
WP03
UT01
WT02
0001
0002
0007
F001
F003
F004
F005
UT02
0001
0002
0011
F001
F002
WP01
WT02
0001
0002
0003
0004
0006
0007
0008
0009
F001
F002
F003
F005
F006
F007
F008
F009
F019
UL01
UL02
WP01
0.30
102.55
45.11
4.38
0.50
311.53
30.71
13.79
7.04
0.07
3.71
1.08
35.60
2.26
3.07
11.00
19.81
0.74
3.72
15.80
14343
8.06
13.63
0.23
5.44
0.32
0.88
0.32
0.69
15.45
0.02
0.10
0.03
0.05
0.16
8.53
536.79
475.44
4.59
0.02
1069.2
1374.7
8.96
0.38
25.14
20.87
56.17
125.55
1241.6
13.50
4.21
3.91
1.00
0.61
2.04
2.49
0.01
0.02
0.01
0.02
0.01
0.01
-0.01
0.07
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
0.00
0.00
-0.05
-0.04
-0.01
-0.05
-0.01
-0.01
-0.01
-0.05
-0.01
-0.01
-0.03
-0.01
-0.01
-0.01
-0.61
-0.01
-0.01
-0.01
-0.02
-0.01
-0.01
-0.01
-0.10
-0.10
-0.21
-0.21
-0.21
-0.01
-0.02
-0.01
-0.01
-0.01
-0.10
-0.07
-0.10
-0.18
-0.18
0.00
0.00
-0.05
-0.02
-0.03
-0.02
-0.04
-0.02
-0.02
-0.02
-0.10
-0.02
-0.02
-0.02
-0.02
-0.10
-0.02
-0.03
0.00
-0.10
-0.09
-0.02
-0.07
-0.02
-0.01
-0.01
-0.06
-0.09
-0.01
-0.04
-0.02
-0.01
-0.05
-0.63
-0.02
-0.09
-0.03
-0.04
-0.01
-0.02
-0.02
-0.12
-0.12
-0.25
-0.25
-0.25
-0.04
-0.03
-0.03
-0.01
-0.01
-0.12
-0.10
-0.12
-0.20
-0.20
-0.03
0.00
-0.10
-0.03
-0.04
-0.03
-0.06
-0.03
-0.03
-0.03
-0.13
-0.03
-0.03
-0.03
-0.03
-0.15
-0.03
-0.05
0.00
-0.15
-0.13
-0.03
-0.09
-0.03
-0.02
0.07
0.10
-0.18
-0.04
-0.06
-0.03
-0.03
-0.11
-0.66
-0.05
-0.18
-0.07
-0.08
-0.03
-0.02
-0.02
-0.16
-0.16
-0.31
-0.31
-0.31
-0.06
-0.04
-0.04
-0.02
-0.02
-0.16
-0.13
-0.16
-0.22
-0.22
-0.05
0.00
0.15
-0.02
-0.06
-0.03
-0.11
-0.02
-0.03
-0.02
-0.23
-0.02
-0.02
-0.02
-0.02
-0.40
-0.02
0.00
0.00
-0.40
-0.32
-0.02
-0.05
-0.03
-0.02
-0.02
-0.06
0.06
-0.03
-0.08
-0.03
-0.03
-0.03
-0.62
-0.03
-0.06
-0.04
-0.12
-0.03
-0.01
-0.01
-0.16
-0.16
-0.21
-0.21
-0.21
-0.13
-0.06
-0.04
0.01
0.02
0.16
-0.23
-0.16
-0.20
-0.20
0.00
0.00
-0.40
-0.04
-0.08
-0.05
-0.15
-0.04
-0.05
-0.04
-0.27
-0.04
-0.04
-0.04
-0.04
-0.50
-0.04
-0.04
0.00
-0.50
-0.41
-0.04
-0.10
-0.05
-0.04
-0.04
-0.09
-0.15
-0.06
-0.12
-0.06
-0.05
-0.14
-0.65
-0.05
-0.15
-0.09
-0.17
-0.05
-0.02
-0.02
-0.21
-0.21
-0.29
-0.29
-0.29
-0.22
-0.10
-0.10
-0.02
-0.04
0.21
-0.27
-0.21
-0.25
-0.25
-0.04
0.00
-0.50
-0.06
-0.10
-0.07
-0.19
-0.06
-0.07
-0.06
-0.31
-0.06
-0.06
-0.06
-0.06
-0.60
-0.06
-0.06
0.00
-0.60
-0.49
-0.06
-0.15
0.07
-0.07
-0.21
-0.17
-0.26
-0.14
-0.16
-0.09
-0.09
0.29
0.68
-0.14
-0.26
-0.21
-0.28
-0.09
-0.03
-0.03
-0.27
-0.27
-0.36
-0.36
-0.36
-0.32
-0.14
-0.16
-0.03
-0.06
-0.27
-0.31
-0.27
-0.29
-0.29
-0.06
0.00
-0.60
-0.07
-0.13
-0.08
-0.26
-0.07
-0.07
-0.07
-0.49
-0.07
-0.07
0.07
0.07
0.85
0.07
0.00
0.00
-0.70
-0.57
-0.07
-0.10
-0.08
-0.05
-0.06
-0.10
-0.14
-0.08
-0.21
-0.07
-0.06
-0.10
-0.65
-0.07
-0.14
-0.10
-0.23
-0.06
-0.03
-0.03
-0.19
-0.19
-0.25
0.25
-0.25
-0.23
-0.16
-0.11
-0.03
-0.05
-0.19
-0.49
-0.19
0.27
0.27
0.00
0.00
-0.70
-0.09
-0.16
-0.11
-0.31
-0.09
0.10
-0.09
-0.54
-0.09
-0.09
-0.09
-0.09
-0.90
-0.09
-0.05
0.00
-0.75
-0.61
-0.09
-0.20
-0.10
-0.10
0.11
0.14
-0.24
-0.17
-0.30
-0.12
-0.10
-0.25
-0.69
-0.11
-0.24
-0.19
-0.30
-0.10
-0.04
-0.04
-0.24
-0.24
-0.32
-0.32
-0.32
0.51
-0.21
-0.18
-0.05
-0.08
-0.24
-0.54
-0.24
-0.34
-0.34
-0.05
0.00
-0.75
-0.11
-0.19
-0.14
-0.36
-0.11
-0.13
-0.11
-0.59
-0.11
-0.11
-0.11
-0.11
-0.95
-0.11
-0.07
0.00
-0.80
-0.66
-0.11
-0.30
-0.12
-0.17
-0.53
-0.31
-0.38
-0.40
-0.38
-0.20
-0.19
-0.47
-0.74
-0.33
-0.38
-0.46
-0.53
-0.19
-0.05
-0.05
-0.29
-0.29
-0.40
-0.40
-0.40
-0.80
-0.26
-0.25
0.07
-0.11
-0.29
-0.59
-0.29
-0.40
-0.40
-0.07
0.00
-0.80
GT-SIC
GROUND
GROUND
GROUND
GT-SIC
GROUND
GT-SIC
GROUND
GT-SIC
GT-SIC
GT-SIC
GT-SIC
GT -WASTE
GT-SIC
GT -WASTE
GT-WASTE
GT -WASTE
GT-WASTE
GT-SIC
ST AT -WASTE
GROUND
STAT
STAT
STAT -WASTE
STAT-WASTE
STAT -WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
GROUND
GROUND
GT-SIC
GT-SIC
GROUND
GROUND
GROUND
GT-WASTE
GROUND
GT-WASTE
GROUND
GROUND
GT-SIC
GT-WASTE
GT-SIC
STAT-SIC
STAT-SIC
GT-WASTE
GT-WASTE
GT-WASTE
15
-------
SIC_P WASTE TONS LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
3728
3728
3728
3728
3730
3730
3731
3731
3731
3731
3731
3731
3731
3731
3731
3731
3731
3731
3731
3731
3731
3732
3732
3732
3732
3751
3751
3751
3751
3751
3760
3760
3760
3760
3760
3760
3766
3764
3769
3769
3792
3792
3792
3792
3811
3811
3811
3811
3811
3811
3811
3811
3811
3811
3811
3811
UP02
UP03
UT01
UT02
F003
F005
0001
0002
0004
0005
0006
D007
0008
0009
F001
F002
F003
F005
UP01
UT01
WT02
0001
F002
F003
F005
0001
0002
0006
0007
0008
0002
0003
0008
F007
VT01
UT02
D001
F005
F003
WT02
0001
D008
F001
F003
0001
0002
0003
0007
0008
F001
F002
F003
FOOS
F007
UP01
UP02
0.62
1.15
26.67
1396.2
6.74
6.74
26.08
79.03
11.29
3.57
16.67
114.28
24.50
0.70
13.13
1.71
39.52
40.85
0.09
4.43
130.97
2.02
0.22
96.35
0.76
8.93
3.03
3.03
3.03
3.03
5.67
0.72
6.87
0.97
1.86
2.34
0.28
0.09
0.49
8.13
2.14
0.73
1.97
0.60
8.74
21.83
1.84
9.46
19.33
18.59
0.05
6.35
6.32
0.70
23.03
0.23
-0.02
0.10
-0.05
0.00
-0.01
-0.01
-0.02
0.01
-0.00
-0.00
-0.02
-0.01
0.01
-0.02
-0.00
-0.01
-0.01
-0.01
-0.02
0.05
-0.00
-0.01
-0.01
0.01
-0.01
0.01
0.04
0.09
-0.05
0.01
0.01
-0.05
-0.01
-0.00
0.05
-0.01
-0.01
-0.01
0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.00
-0.01
0.00
-0.03
-0.01
-0.02
-0.01
-0.07
-0".04
-0.04
-0.03
-0.12
-0.07
0.00
-0.01
-0.02
-0.04
-0.03
-0.01
-0.01
-0.04
-0.02
-0.02
-0.03
-0.00
-0.03
-0.03
-0.03
-0.04
-0.07
-0.01
-0.05
-0.03
-0.03
-0.02
-0.05
-0.05
-0.12
-0.06
-0.03
-0.02
-0.07
-0.03
-0.01
-0.07
-0.01
-0.05
0.02
-0.01
-0.01
-0.05
0.03
-0.09
-0.01
-0.02
-0.01
-0.01
0.01
-0.01
-0.05
-0.03
-0.05
-0.02
-0.10
-0.08
-0.08
-0.04
-0.16
-0.09
-0.02
-0.04
-0.03
-0.15
-0.08
-0.02
-0.10
-0.04
-0.08
-0.09
-0.09
-0.02
-0.07
-0.04
-0.05
-0.08
0.09
-0.07
-0.11
-0.07
-0.06
-0.03
0.11
0.07
0.17
-0.10
0.08
0.08
-0.08
-0.08
-0.03
-0.09
-0.03
-0.11
-0.03
-0.04
0.03
-0.11
-0.08
-0.18
-0.04
-0.06
-0.09
-0.05
-0.07
-0.09
-0.05
-0.07
-0.05
-0.03
-0.13
-0.09
-0.11
-0.03
-0.16
-0.05
-0.21
-0.03
-0.03
-0.06
-0.04
-0.01
-0.01
-0.06
-0.03
0.03
-0.05
-0.00
-0.04
-0.04
-0.04
-0.12
-0.05
-0.01
-0.03
-0.04
-0.04
-0.03
-0.03
-0.12
-0.11
0.06
-0.04
-0.03
-0.16
-0.04
-0.01
-0.05
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.04
-0.06
-0.03
-0.04
-0.02
-0.01
-0.02
-0.01
-0.08
-0.04
-0.07
-0.03
-0.22
-0.12
-0.21
-0.06
-0.21
-0.10
-0.25
-0.06
0.06
0.12
0.09
-0.02
0.02
0.12
-0.05
-0.06
-0.10
-0.01
-0.09
-0.09
-0.09
-0.17
-0.10
-0.03
-0.14
0.09
-0.08
-0.06
-0.14
-0.16
-0.17
-0.09
-0.08
-0.05
0.20
-0.08
-0.02
-0.10
-0.05
-0.14
-0.06
-0.06
0.05
-0.14
-0.08
-0.15
-0.06
-0.07
0.03
-0.02
-0.04
-0.02
-0.15
-0.09
-0.15
-0.06
-0.26
-0.24
-0.30
-0.08
-0.27
-0.15
0.31
-0.14
-0.09
-0.29
0.23
0.06
-0.30
-0.13
-0.23
-0.25
0.28
-0.07
-0.21
-0.13
-0.16
0.28
-0.15
-0.20
0.29
-0.21
-0.17
-0.09
0.29
0.20
0.28
-0.17
0.22
0.25
-0.24
-0.24
-0.10
-0.15
-0.09
-0.29
0.09
-0.14
-0.09
-0.29
-0.22
-0.26
-0.14
-0.18
-0.28
-0.16
-0.20
0.27
-0.16
-0.21
-0.16
-0.09
-0.30
-0.26
-0.39
-0.07
-0.19
-0.10
-0.21
-0.08
0.07
-0.15
-0.11
-0.02
-0.03
-0.16
-0.07
-0.08
-0.12
-0.01
-0.10
-0.11
0.11
-0.23
-0.10
-0.04
-0.10
-0.10
-0.11
-0.07
-0.10
-0.30
-0.17
-0.10
-0.10
-0.06
-0.39
-0.10
-0.02
-0.10
-0.06
-0.10
-0.07
-0.08
-0.06
-0.10
-0.10
-0.14
-0.08
-0.09
-0.04
-0.03
-0.05
-0.03
-0.19
-0.10
-0.19
-0.07
-0.48
-0.31
-0.41
-0.11
-0.24
-0.20
-0.25
-0.17
-0.12
-0.30
-0.23
0.04
-0.05
-0.31
-0.13
-0.14
-0.25
-0.02
-0.19
-0.23
-0.23
-0.30
-0.20
-0.07
0.25
0.19
-0.22
-0.12
-0.25
-0.40
-0.25
-0.14
-0.17
0.13
-0.49
-0.19
-0.04
-0.20
-0.10
-0.25
-0.12
-0.17
-0.10
-0.25
-0.17
-0.24
-0.17
-0.18
-0.08
-0.05
-0.10
-0.06
-0.39
-0.19
-0.38
-0.12
-0.53
-0.62
-0.57
-0.14
-0.29
-0.30
-0.31
-0.40
-0.20
0.62
-0.58
-0.16
-0.76
0.33
-0.58
-0.61
-0.72
-0.19
-0.46
-0.34
-0.41
-0.53
-0.31
-0.52
-0.47
-0.46
-0.43
-0.20
-0.47
-0.50
-0.50
-0.31
-0.54
-0.65
-0.59
-0.60
-0.24
0.31
-0.19
-0.47
-0.20
-0.40
-0.19
-0.47
-0.54
-0.38
-0.40
-0.47
-0.70
-0.41
-0.52
0.70
-0.41
-0.46
-0.41
-0.20
-0.58
-0.67
0.72
GROUND
GT-SIC
STAT-WASTE
GROUND
ST AT -WASTE
STAT-WASTE
STAT
STAT
STAT
STAT-WASTE
STAT
STAT
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT
STAT
STAT
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
16
-------
SIC_P WASTE TOUS LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
3811
3811
3823
3825
3825
3825
3825
3825
3825
3825
3825
3825
3825
3825
3825
3825
3825
3825
3825
3831
3841
3841
3841
3841
3841
3841
3841
3841
3841
3841
3841
3861
3861
3931
3931
3931
3949
3949
3949
3949
3949
3949
3949
3949
3999
3999
3999
3999
3999
3999
4011
4011
4011
4011
4011
4101
UT01
UT02
F001
D001
D002
D003
0006
0007
D008
D010
F001
F002
F003
F004
F005
F006
P106
UT01
WT02
D008
0001
0002
0011
F001
F002
F003
UL01
WL02
WP01
UT01
UT02
0002
0007
0007
F006
UT02
D001
F001
F003
F005
U107
U213
UT01
UT02
0001
F001
F003
F005
UP01
UT02
0001
F001
U112
U220
U239
0002
38.43
30.51
1.75
16.76
516.82
0.00
0.01
3.55
373.51
0.04
12.66
0.17
0.87
0.03
0.15
40.26
0.01
8.84
25.08
0.53
3.87
0.01
0.14
3.41
0.19
0.86
0.01
0.01
0.19
0.01
0.96
5.50
5.50
88.99
88.75
88.99
19.33
7.24
3.74
6.22
0.46
0.41
1.07
0.48
7.51
10.91
0.34
0.34
0.21
1.69
0.44
0.78
0.78
0.78
0.78
0.57
0.01
-0.01
-0.01
-0.01
-0.04
-0.05
-0.09
-0.05
-0.01
-0.01
-0.01
-0.01
-0.02
-0.03
-0.01
-0.14
-0.03
-0.05
-0.02
-0.01
-0.05
-0.61
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.02
-0.05
-0.01
-0.04
-0.05
-0.05
-0.14
-0.01
-0.04
-0.01
-0.01
-0.01
-0.03
-0.03
-0.05
-0.01
-0.00
-0.01
-0.01
-0.01
-0.02
-0.01
-0.01
-0.01
-0.02
-0.10
-0.10
-0.61
-0.02
-0.01
-0.09
-0.02
-0.05
-0.07
-0.12
-0.06
-0.02
-0.01
-0.02
-0.03
0.05
-0.04
-0.02
-0.16
-0.04
-0.07
-0.04
-0.03
-0.09
-0.63
-0.02
-0.09
-0.03
-0.01
-0.03
-0.01
-0.04
0.07
-0.01
-0.05
-0.06
-0.06
-0.16
-0.01
-0.07
-0.09
-0.01
-0.02
-0.06
-0.06
-0.07
-0.01
-0.00
-0.09
-0.01
-0.02
-0.04
-0.01
-0.05
-0.09
-0.12
-0.12
-0.12
-0.63
-0.08
-0.09
-0.18
-0.08
-0.07
-0.08
-0.17
-0.10
-0.09
-0.03
-0.02
-0.07
-0.06
-0.06
-0.03
-0.20
-0.07
-0.09
-0.04
-0.08
-0.10
-0.66
-0.05
-0.18
-0.07
-0.04
-0.06
-0.01
-0.08
-0.09
-0.05
-0.07
-0.10
-0.10
-0.20
-0.03
-0.08
-0.18
-0.04
-0.03
-0.07
-0.07
-0.09
-0.03
-0.06
-0.18
-0.04
-0.03
-0.08
-0.03
-0.11
-0.18
-0.23
-0.15
-0.15
-0.66
-0.02
-0.02
-0.06
-0.03
-0.12
-0.16
-0.11
-0.06
-0.03
-0.02
-0.02
-0.04
-0.07
-0.08
-0.03
-0.19
-0.08
-0.05
-0.06
-0.04
-0.14
-0.62
-0.03
-0.06
-0.04
-0.03
-0.04
-0.02
-0.12
-0.05
-0.02
-0.12
-0.06
-0.06
-0.19
-0.03
-0.11
-0.06
-0.03
-0.03
-0.09
-0.09
-0.05
-0.03
-0.00
-0.06
-0.03
-0.03
-0.12
-0.03
-0.03
-0.06
-0.05
-0.14
-0.14
-0.62
-0.05
-0.04
-0.15
-0.06
-0.16
-0.20
-0.17
-0.09
-0.06
-0.04
-0.05
0.09
-0.14
-0.12
-0.06
-0.23
-0.12
-0.10
-0.12
-0.08
-0.28
-0.65
0.05
-0.15
-0.09
-0.06
-0.07
-0.03
-0.17
-0.10
-0.04
-0.16
-0.09
-0.09
-0.23
-0.05
-0.22
-0.15
-0.06
-0.07
-0.18
-0.18
-0.10
-0.05
-0.01
-0.15
-0.06
-0.06
-0.17
-0.05
-0.14
-0.15
-0.34
-0.18
-0.18
-0.65
-0.23
-0.26
-0.26
0.25
-0.20
0.24
-0.28
-0.17
-0.25
-0.10
-0.05
-0.21
-0.17
-0.16
-0.09
-0.31
-0.22
-0.15
-0.13
-0.22
-0.30
-0.68
-0.14
-0.26
-0.21
-0.14
-0.11
-0.04
-0.28
-0.15
-0.14
-0.20
-0.17
-0.17
-0.31
-0.09
-0.24
-0.26
-0.14
-0.10
-0.21
-0.21
-0.15
-0.09
-0.17
-0.26
-0.14
-0.09
-0.28
-0.09
-0.29
-0.26
-0.63
-0.24
-0.24
-0.68
-0.06
-0.05
-0.14
-0.07
-0.30
-0.39
-0.17
-0.10
-0.08
-0.05
-0.06
-0.10
-0.18
-0.21
-0.07
-0.21
-0.20
-0.10
-0.16
-0.10
-0.36
-0.65
0.07
-0.14
-0.10
-0.08
-0.09
-0.05
-0.23
-0.10
-0.05
-0.30
-0.10
-0.10
-0.21
-0.06
-0.28
-0.14
-0.08
-0.09
-0.23
-0.23
-0.10
-0.06
-0.01
-0.14
-0.08
-0.07
-0.23
-0.06
-0.10
-0.14
-0.18
-0.20
-0.20
-0.65
-0.12
-0.11
-0.24
0.15
-0.40
-0.49
-0.25
-0.14
-0.14
-0.10
-0.12
0.19
-0.36
-0.30
-0.12
-0.26
-0.29
-0.20
-0.32
-0.17
-0.72
-0.69
-0.11
-0.24
-0.19
-0.17
-0.16
-0.07
-0.30
-0.20
-0.08
-0.40
-0.14
-0.14
-0.26
-0.10
-0.56
-0.24
-0.17
-0.17
-0.47
-0.47
-0.20
-0.10
-0.02
-0.24
-0.17
-0.12
-0.30
-0.10
-0.25
-0.24
-0.52
-0.26
-0.26
-0.69
-0.60
-0.66
-0.38
-0.64
-0.50
-0.59
-0.50
-0.31
0.61
-0.26
-0.12
-0.46
-0.45
-0.38
-0.20
-0.41
-0.54
-0.31
-0.34
-0.54
-0.76
-0.74
-0.33
-0.38
-0.46
-0.40
-0.22
-0.10
-0.53
-0.31
-0.32
-0.50
-0.31
-0.31
-0.41
-0.19
-0.62
-0.38
-0.40
-0.26
-0.53
-0.53
-0.31
-0.19
-0.44
-0.38
-0.40
-0.20
-0.53
-0.19
-0.47
-0.38
-0.85
-0.37
-0.37
-0.74
ST AT -WASTE
STAT -WASTE
STAT-WASTE
STAT
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT -WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
TOT-AVG
TOT-AVG
STAT-WASTE
17
-------
SIC P WASTE TONS LB 89 MB 89 HB 89 LB 95 MB 95 HB 95 LB 09 MB 09 HB 09 SOUR
4101
4111
4111
4111
4111
4111
4111
4172
4172
4172
4172
4172
4172
4213
4213
4213
4213
4213
4213
4213
4213
4213
4213
4213
4213
4213
4214
4214
4225
4225
4225
4225
4225
4225
4225
4225
4226
4226
4226
4226
4226
4226
4226
4231
4231
4231
4231
4231
4231
4231
4231
4231
4231
4231
4231
4311
UT02
0001
0006
0007
0008
F002
UT02
0001
F001
F002
F003
F005
UT02
0001
0002
0006
0007
0008
F001
F002
F005
F006
U001
UP01
UP02
WT02
U001
UP01
0001
0002
U070
U080
U220
U226
WC02
UT02
0001
0008
0009
0010
F002
F003
WT02
0001
0006
0007
0008
F003
F005
U080
U158
WC01
UP01
WT01
WT02
0001
0.73
2.44
2.87
2.87
2.87
0.13
41.28
16.18
0.39
1.53
0.07
0.07
775.83
1.86
703.94
0.67
270.46
20.25
18.61
18.70
0.66
4289.4
25.58
18.61
0.08
7996.8
288.90
21.22
0.63
0.00
0.05
0.01
0.06
0.02
0.00
0.16
2.89
120.74
0.32
0.24
0.24
8.01
0.72
0.13
0.30
0.30
0.30
0.02
0.02
0.03
0.02
0.02
0.02
0.08
0.42
1.05
-0.01
-0.01
-0.09
-0.05
-0.01
0.01
-0.01
-0.00
-0.01
-0.00
-0.01
-0.01
-0.01
-0.01
-0.04
-0.09
-0.00
-0.01
-0.01
0.01
0.01
-0.14
0.05
-0.02
-0.04
-0.01
0.05
-0.02
-0.01
-0.61
-0.10
-0.10
0.10
-0.00
-0.04
-0.01
-0.01
-0.01
-0.02
-0.01
-0.01
0.01
-0.01
-0.00
-0.09
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.04
-0.02
-0.05
-0.01
-0.01
-0.01
-0.05
-0.12
-0.06
-0.03
-0.03
-0.01
-0.01
-0.09
0.01
-0.01
-0.02
-0.02
-0.05
-0.05
-0.12
-0.01
-0.03
-0.09
-0.03
-0.02
-0.16
-0.08
-0.04
-0.08
-0.01
-0.08
-0.04
-0.05
-0.63
-0.12
-0.12
-0.12
-0.00
-0.05
-0.01
-0.05
-0.03
-0.03
-0.01
-0.03
-0.01
-0.01
-0.01
-0.12
-0.06
-0.03
-0.01
-0.02
-0.01
-0.01
-0.05
-0.04
-0.07
-0.02
-0.01
-0.03
-0.11
-0.17
-0.10
-0.08
-0.07
-0.03
-0.09
-0.18
-0.07
-0.04
-0.03
-0.06
-0.11
0.07
-0.17
-0.05
-0.08
-0.18
-0.07
-0.03
-0.20
-0.12
-0.08
-0.11
-0.05
-0.12
-0.08
-0.11
-0.66
-0.15
-0.15
-0.15
-0.05
-0.06
-0.03
-0.11
-0.08
-0.09
-0.03
0.07
-0.04
-0.03
-0.08
-0.17
-0.10
-0.08
-0.04
-0.03
-0.09
-0.09
-0.06
-0.08
-0.09
-0.09
-0.03
-0.03
-0.03
-0.11
-0.06
-0.04
-0.04
-0.03
-0.01
-0.06
-0.01
-0.03
-0.03
-0.02
-0.03
0.12
-0.11
-0.01
-0.04
-0.06
-0.04
-0.03
-0.19
-0.31
-0.12
-0.21
-0.02
-0.31
-0.12
-0.03
-0.62
-0.14
-0.14
-0.14
-0.01
-0.12
-0.03
-0.03
-0.04
0.05
-0.02
0.04
-0.03
0.03
-0.01
-0.11
-0.06
-0.04
-0.03
-0.03
-0.02
-0.02
-0.11
0.12
-0.05
-0.02
-0.02
-0.05
-0.14
-0.17
-0.09
-0.08
-0.09
-0.05
-0.02
-0.15
-0.02
-0.06
-0.06
-0.05
-0.14
-0.16
-0.17
-0.02
-0.08
-0.15
-0.09
-0.06
-0.23
-0.39
-0.17
-0.30
-0.04
-0.39
-0.17
-0.14
-0.65
-0.18
-0.18
-0.18
-0.02
-0.16
-0.05
-0.14
-0.08
-0.10
-0.04
-0.09
-0.06
-0.05
-0.02
-0.17
-0.09
-0.08
-0.06
-0.06
-0.04
-0.04
-0.15
-0.17
-0.10
-0.05
-0.03
-0.09
-0.29
-0.28
-0.17
-0.22
-0.21
-0.09
-0.26
-0.26
-0.20
-0.14
-0.09
-0.19
-0.29
-0.20
-0.28
-0.16
-0.22
-0.26
-0.21
-0.09
-0.31
-0.47
-0.28
-0.39
-0.14
0.47
-0.28
-0.29
-0.68
-0.24
-0.24
-0.24
-0.17
-0.20
-0.09
-0.29
-0.22
-0.28
-0.10
-0.21
-0.14
-0.09
-0.23
-0.28
-0.17
-0.22
-0.14
-0.09
-0.26
-0.26
-0.19
-0.28
-0.15
-0.28
-0.09
-0.06
-0.10
-0.17
-0.10
-0.10
-0.10
-0.06
-0.02
0.14
-0.02
-0.08
-0.07
-0.06
-0.10
-0.30
-0.17
-0.03
-0.10
-0.14
-0.10
-0.07
-0.21
-0.67
0.23
-0.41
-0.05
-0.67
-0.23
0.10
-0.65
-0.20
-0.20
-0.20
-0.03
-0.30
-0.06
-0.10
-0.10
-0.12
-0.05
-0.10
-0.08
-0.06
-0.02
-0.17
-0.10
-0.10
-0.08
-0.07
-0.05
-0.05
-0.29
-0.23
-0.10
-0.06
-0.04
-0.10
-0.25
-0.25
-0.14
-0.17
-0.19
0.10
-0.04
0.24
-0.04
-0.17
-0.12
0.12
-0.25
0.40
-0.25
0.05
0.17
-0.24
0.19
0.12
0.26
0.74
-0.30
-0.57
0.08
-0.74
-0.30
0.25
-0.69
-0.26
-0.26
-0.26
-0.04
-0.40
-0.10
-0.25
-0.17
-0.25
-0.10
-0.19
-0.17
-0.10
-0.04
-0.25
-0.14
0.17
-0.17
-0.12
-0.10
-0.10
-0.38
-0.30
-0.20
-0.12
-0.09
-0.19
-0.47
-0.50
0.31
-0.54
0.46
0.19
-0.67
-0.38
-0.52
-0.40
0.20
0.49
-0.47
-0.50
-0.50
-0.41
-0.54
-0.38
-0.46
-0.20
-0.41
-0.80
-0.53
-0.72
0.32
-0.80
-0.53
0.47
-0.74
-0.37
0.37
-0.37
-0.44
-0.50
-0.19
-0.47
-0.54
-0.72
-0.26
-0.46
-0.40
-0.19
0.58
0.50
-0.31
-0.54
-0.40
-0.20
-0.68
-0.68
-0.47
-0.53
-0.31
-0.70
-0.22
STAT -WASTE
STAT-WASTE
STAT -WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
TOT-AVG
TOT-AVG
TOT-AVG
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT -SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
18
-------
SIC_P WASTE TONS LB_89 MB_89 HB_89 LB_95 HB_95 HB_95 LB_09 MB_09 HB_09 SOUR
4311
4311
4311
4311
4425
4452
4452
4452
4452
4452
4452
4454
4454
4454
4463
4463
4463
4469
4511
4511
4511
4511
4582
4582
4582
4582
4582
4582
4582
4723
4723
4723
4723
4723
4723
4723
4723
4723
4723
4811
4811
4811
4811
4825
4910
4910
4910
4911
4911
4911
4911
4911
4911
4911
4911
4911
D002
F005
U001
UT02
F005
0001
0002
0008
F003
W001
UT02
0007
0008
U051
0001
W001
WT02
0001
0001
0008
0009
WT02
0001
0002
F001
F002
F005
WP01
WT02
0001
0002
0003
0007
0008
P029
P030
P098
P106
WT02
0001
0002
F001
U159
0002
0001
W001
WP01
0001
0002
0003
0005
0007
0008
0009
D011
0016
2.10
0.44
0.09
0.00
0.81
0.58
0.01
2.70
0.58
9.36
2.70
0.58
0.58
0.81
2.23
4.80
0.22
0.44
6.70
0.44
0.09
0.44
5.45
0.16
3.58
30.89
8.39
0.52
4.65
0.05
0.12
0.00
0.01
0.05
0.00
0.00
0.00
0.00
0.17
0.23
15.87
3.40
0.23
0.70
0.36
163.26
5.82
15.31
0.64
0.01
0.12
0.08
7.84
1.05
0.10
0.03
-0.04
-0.01
-0.05
-0.01
-0.01
-0.01
-0.61
-0.01
-0.01
-0.05
-0.01
-0.05
-0.01
-0.00
-0.01
-0.05
-0.01
-0.01
-0.01
-0.01
-0.02
-0.01
0.00
-0.61
-0.01
-0.01
-0.01
-0.02
-0.01
-0.01
-0.61
-0.05
-0.05
-0.01
-0.10
-0.10
-0.10
-0.10
-0.01
-0.01
-0.04
-0.01
-0.10
-0.61
-0.01
-0.05
-0.02
-0.05
-0.71
-0.05
-0.05
-0.06
-0.08
-0.05
-0.05
-0.05
-0.05
-0.02
-0.08
-0.01
-0.02
-0.05
-0.63
-0.03
-0.01
-0.08
-0.01
-0.06
-0.03
-0.01
-0.05
-0.08
-0.01
-0.05
-0.05
-0.03
-0.03
-0.01
-0.00
-0.63
-0.09
-0.03
-0.02
-0.04
-0.01
-0.05
-0.63
-0.07
-0.06
-0.03
-0.12
-0.12
-0.12
-0.12
-0.01
-0.05
-0.05
-0.09
-0.12
-0.63
-0.05
-0.08
-0.04
-0.10
-0.73
-0.10
-0.10
-0.08
-0.12
-0.10
-0.10
-0.10
-0.07
-0.03
-0.12
-0.03
-0.03
-0.11
-0.66
-0.08
-0.04
-0.12
-0.03
-0.10
-0.08
-0.02
-0.11
-0.12
-0.03
-0.11
0.11
-0.08
-0.09
-0.03
-0.03
-0.66
-0.18
-0.07
-0.03
-0.08
-0.03
-0.11
-0.66
-0.08
-0.10
-0.08
-0.15
-0.15
-0.15
-0.15
-0.03
0.11
-0.07
-0.18
-0.15
-0.66
-0.11
-0.12
-0.08
-0.15
-0.75
-0.15
-0.15
-0.10
-0.16
-0.15
-0.15
-0.15
-0.12
-0.03
0.31
0.03
-0.03
0.03
0.62
0.04
-0.03
0.31
-0.03
-0.06
-0.04
-0.01
-0.03
0.31
-0.03
0.03
0.03
-0.04
-0.05
-0.03
-0.01
0.62
-0.06
0.04
0.03
-0.12
-0.03
-0.03
-0.62
-0.16
-0.06
0.04
-0.14
-0.14
-0.14
-0.14
-0.03
0.03
-0.12
-0.06
-0.14
0.62
-0.03
-0.31
0.12
-0.40
-0.71
-0.39
0.39
-0.07
-0.70
0.45
-0.39
-0.39
0.16
-0.06
-0.39
-0.05
0.06
0.14
-0.65
-0.08
-0.06
0.39
-0.05
0.09
-0.08
-0.03
-0.14
-0.39
-0.05
-0.14
-0.14
-0.08
-0.10
-0.05
-0.01
-0.65
-0.15
-0.09
0.06
-0.17
-0.05
-0.14
0.65
0.20
-0.09
-0.08
-0.18
-0.18
-0.18
-0.18
-0.05
-0.14
0.16
-0.15
-0.18
0.65
-0.14
-0.39
-0.17
-0.50
-0.74
-0.49
-0.49
-0.10
-0.75
-0.50
-0.49
-0.49
-0.20
-0.09
-0.47
-0.09
-0.09
-0.29
-0.68
0.22
0.14
0.47
-0.09
-0.17
-0.22
0.07
-0.29
-0.47
0.09
-0.29
-0.29
-0.22
-0.28
-0.09
-0.09
0.68
0.26
-0.21
-0.09
-0.28
0.09
-0.29
-0.68
-0.24
-0.17
0.22
-0.24
-0.24
-0.24
-0.24
-0.09
0.29
-0.20
-0.26
-0.24
-0.68
-0.29
-0.47
-0.28
-0.60
-0.76
-0.59
0.59
-0.13
-0.80
-0.55
-0.59
-0.59
-0.30
-0.07
-0.67
0.06
-0.07
-0.10
0.65
0.10
-0.08
-0.67
-0.06
-0.10
0.10
-0.03
-0.10
-0.67
-0.06
-0.10
0.10
-0.10
-0.12
-0.06
0.02
0.65
-0.14
-0.10
-0.07
-0.23
0.06
-0.10
-0.65
-0.39
-0.10
-0.10
-0.20
-0.20
-0.20
0.20
-0.06
0.10
-0.30
-0.14
-0.20
-0.65
-0.10
0.67
-0.23
-0.50
-0.72
-0.83
-0.83
-0.10
-0.90
-0.60
-0.83
-0.83
-0.40
-0.12
-0.74
-0.10
0.12
-0.25
0.69
-0.17
-0.17
0.74
-0.10
-0.14
-0.17
-0.07
-0.25
-0.74
-0.10
-0.25
-0.25
-0.17
-0.25
-0.10
-0.04
0.69
-0.24
0.19
-0.12
-0.30
-0.10
-0.25
-0.69
0.49
-0.14
-0.17
-0.26
-0.26
-0.26
-0.26
-0.10
-0.25
-0.40
-0.24
-0.26
-0.69
-0.25
-0.74
-0.30
-0.60
-0.74
-0.88
-0.88
-0.14
-0.95
-0.70
-0.88
-0.88
-0.50
-0.20
-0.80
0.19
-0.20
-0.47
-0.74
-0.54
-0.40
-0.80
-0.19
-0.31
-0.54
-0.19
-0.47
-0.80
0.19
-0.47
-0.47
-0.54
-0.72
-0.19
-0.23
0.74
-0.38
-0.46
0.20
-0.53
-0.19
-0.47
-0.74
-0.59
-0.31
-0.54
-0.37
-0.37
0.37
0.37
-0.19
-0.47
-0.50
-0.38
-0.37
-0.74
-0.47
-0.80
-0.53
-0.70
-0.77
-0.93
-0.93
-0.18
-1.00
-0.80
-0.93
-0.93
ENG-ANAL
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-UASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
TOT-AVG
TOT-AVG
TOT-AVG
TOT-AVG
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
TOT-AVG
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
GROUND
GT -WASTE
GT-SIC
GT-SIC
GT-WASTE
GROUND
GROUND
GT-SIC
GT-SIC
19
-------
SIC_P HASTE TOMS LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 HB_09 HB_09 SOUR
4911
4911
4911
4911
4911
4911
4911
4911
4911
4911
4911
4911
4911
4911
4922
4941
4941
4941
4951
4951
4951
4952
4952
4952
4952
4952
4953
4953
5012
5012
5012
5013
5013
5013
5013
5013
5013
5013
5013
5031
5031
5062
5062
5078
5078
5081
5082
5082
5082
5082
5082
5082
5082
5083
5083
5084
F001
F002
F003
F005
U211
U242
W001
WC01
UL02
WP01
UP02
UP03
WT01
WT02
UT02
D016
U001
WT02
D008
F001
F002
D006
D007
UP02
UT01
HT02
F001
F002
D001
F003
UT02
0001
0002
0006
0007
D008
F001
UT01
UT02
0001
WT02
0001
F002
F003
F005
0001
0001
D007
0008
F002
F003
WT01
UT02
D001
F002
D001
20.08
2.08
0.26
1.34
0.08
0.01
1216.7
0.22
0.17
3.34
2.31
0.01
4.19
2.29
3.28
0.02
0.03
0.01
2.24
9.94
9.94
0.69
0.69
0.69
0.69
1.00
0.86
0.86
0.31
0.31
1.54
0.02
0.22
2.12
0.62
1.32
3.35
0.62
0.70
0.55
0.55
3.20
0.09
0.20
0.20
0.25
3.91
1.38
1.38
0.09
2.87
0.40
1.38
0.81
0.31
3.75
-0.04
-0.03
-0.00
-0.01
0.05 *
-0.05
-0.05
-0.05
0.00
-0.05
-0.05
-0.05
-0.05
-0.05
-0.01
-0.10
0.05
-0.01
-0.01
-0.01
-0.01
0.09
0.05
-0.04
-0.05
-0.01
-0.01
-0.01
0.01
-0.01
0.01
-0.01
-0.61
0.01
-0.05
-0.01
-0.01
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
-0.01
-0.01
-0.05
-0.01
-0.01
-0.01
-0.01
-0.07
-0.07
-0.01
-0.02
-0.10
-0.10
0.10
-0.10
0.00
-0.10
0.10
-0.10
-0.07
0.07
0.01
0.12
0.08
0.01
-0.03
-0.09
-0.03
-0.12
-0.06
0.08
-0.07
-0.01
-0.09
0.03
0.05
0.01
0.01
-0.05
-0.63
-0.02
-0.06
0.03
-0.09
-0.07
-0.01
-0.05
-0.01
-0.05
-0.03
-0.01
-0.02
-0.05
-0.02
-0.06
-0.03
-0.03
-0.01
-0.07
-0.01
-0.05
-0.03
-0.05
-0.10
-0.11
-0.02
-0.03
-0.15
-0.15
-0.15
-0.15
0.00
-0.15
-0.15
-0.15
-0.09
-0.09
-0.03
-0.15
-0.12
-0.03
-0.08
-0.18
0.07
-0.17
-0.10
-0.11
-0.09
-0.03
-0.18
-0.07
-0.11
-0.04
-0.03
-0.11
-0.66
-0.02
-0.10
-0.08
-0.18
-0.09
-0.03
-0.11
-0.03
-0.11
-0.07
-0.04
-0.03
-0.11
-0.02
-0.10
-0.08
-0.07
-0.04
-0.09
-0.03
-0.11
-0.07
-0.11
-0.05
-0.05
-0.05
-0.03
-0.39
0.39
-0.40
0.39
0.00
-0.40
-0.40
-0.39
-0.05
-0.05
-0.03
-0.14
-0.31
-0.03
-0.04
-0.06
-0.04
-0.11
-0.06
-0.21
-0.05
-0.03
-0.06
-0.04
-0.03
-0.03
-0.03
-0.03
-0.62
-0.03
-0.06
-0.04
-0.06
0.05
-0.03
-0.03
-0.03
-0.03
-0.04
-0.03
-0.03
-0.03
-0.03
-0.06
-0.04
-0.04
-0.03
-0.05
-0.03
-0.03
-0.04
-0.03
-0.10
-0.10
-0.08
0.05
-0.49
0.49
0.50
-0.49
0.00
-0.50
0.50
-0.49
0.10
-0.10
-0.05
-0.18
-0.39
-0.05
-0.08
0.15
0.09
-0.17
-0.09
-0.30
-0.10
-0.05
0.15
-0.09
-0.14
-0.06
-0.05
0.14
-0.65
-0.05
-0.09
-0.08
-0.15
-0.10
-0.05
-0.14
-0.05
-0.14
-0.09
-0.06
-0.06
-0.14
-0.06
-0.09
-0.08
-0.09
-0.06
-0.10
-0.05
-0.14
-0.09
-0.14
-0.15
-0.15
0.12
-0.07
-0.59
-0.59
0.60
-0.59
0.00
-0.60
-0.60
-0.59
-0.15
-0.15
-0.09
-0.24
-0.47
-0.09
-0.22
-0.26
0.21
-0.28
-0.17
-0.39
-0.15
-0.09
0.26
-0.21
-0.29
-0.14
0.09
-0.29
-0.68
-0.07
-0.17
-0.22
-0.26
-0.15
-0.09
-0.29
-0.09
-0.29
-0.21
-0.14
-0.09
-0.29
-0.06
-0.17
-0.22
-0.21
-0.14
-0.15
-0.09
-0.29
-0.21
-0.29
-0.10
-0.10
-0.10
-0.06
0.83
0.83
-0.85
-0.83
0.00
-0.70
-0.70
-0.83
-0.10
0.10
-0.06
0.20
0.67
0.06
-0.10
0.14
-0.10
0.17
-0.10
-0.41
0.10
-0.06
-0.14
-0.10
-0.10
-0.08
0.06
-0.10
-0.65
0.07
-0.10
-0.10
-0.14
-0.10
-0.06
-0.10
-0.06
-0.10
-0.10
-0.08
0.07
-0.10
-0.08
-0.10
-0.10
-0.10
-0.08
-0.10
-0.06
-0.10
-0.10
-0.10
-0.20
-0.20
-0.24
-0.11
-0.88
-0.88
-0.90
-0.88
0.00
-0.75
0.75
-0.88
-0.20
-0.20
-0.10
-0.26
-0.74
0.10
-0.17
-0.24
-0.19
-0.25
-0.14
-0.57
-0.20
-0.10
-0.24
-0.19
-0.25
-0.17
-0.10
-0.25
-0.69
-0.13
-0.14
-0.17
-0.24
0.20
-0.10
-0.25
-0.10
-0.25
-0.19
-0.17
-0.12
-0.25
-0.16
0.14
-0.17
-0.19
-0.17
-0.20
-0.10
-0.25
-0.19
-0.25
-0.30
-0.30
0.37
0.15
-0.93
0.93
-0.95
-0.93
0.00
0.80
0.80
-0.93
-0.30
0.30
-0.19
-0.37
-0.80
0.19
-0.54
-0.38
-0.46
-0.50
0.31
0.72
-0.31
-0.19
-0.38
-0.46
-0.47
-0.40
-0.19
-0.47
-0.74
-0.18
-0.31
-0.54
-0.38
0.31
-0.19
-0.47
-0.19
-0.47
-0.46
-0.40
-0.20
-0.47
-0.16
-0.31
-0.54
-0.46
0.40
-0.31
-0.19
-0.47
-0.46
-0.47
GROUND
GROUND
GT -WASTE
GT -WASTE
GT-SIC
GT-SIC
GROUND
GT-SIC
GT -WASTE
GROUND
GROUND
GT-SIC
GROUND
GROUND
ST AT -WASTE
TOT-AVG
ST AT -WASTE
STAT-WASTE
ST AT -WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
20
-------
SIC_P WASTE TONS LB_89 HB_89 HB_89 LB_95 HB_95 HB_95 LB_09 MB_09 HB_09 SOUR
5084
5084
5085
5085
5085
5085
5085
5085
5085
5086
5088
5089
5089
5089
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5093
5141
5141
5161
5161
5161
5161
5161
D002
F002
0001
0006
0007
0008
F003
F005
UT02
F003
F001
0001
F003
F005
0001
0002
0004
0005
0006
0007
0008
0009
0010
0011
0014
0016
F001
F002
F003
F004
F005
F006
F007
F008
F009
K001
K009
K050
K052
U051
U158
U211
U240
W001
UP01
UP02
WP03
UT01
UT02
0001
0002
0001
0002
0004
0007
0008
1.54
0.02
1.69
16.74
16.74
16.74
1.69
1.69
1.69
0.68
3.90
0.34
0.34
0.34
267.27
360.38
13.22
4.46
219.61
261.25
488.39
5.42
0.86
0.56
4.62
2.52
22.51
28.73
169.17
3.15
14.08
616.30
1.25
0.04
1.71
141.69
4.90
2.61
6.71
12.56
1.22
0.37
0.20
23.45
88.11
2.73
15.06
42.56
756.60
1.44
0.34
2.31
18.99
0.01
0.00
18.80
-0.04
-0.01
-0.01
-0.09
-0.05
-0.01
0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
0.01
-0.01
-0.01
-0.00
-0.00
0.01
0.01
-0.01
0.01
0.00
0.01
-0.03
0.03
0.01
-0.03
0.00
-0.03
0.01
-0.14
-0.07
0.22
-0.18
-0.01
-0.03
-0.03
-0.03
-0.00
-0.03
-0.03
-0.03
-0.01
-0.01
-0.04
-0.01
-0.01
0.01
-0.01
0.61
-0.01
-0.04
-0.01
-0.05
-0.01
-0.05
-0.03
-0.05
-0.12
-0.06
-0.03
-0.01
-0.02
0.01
0.01
-0.09
-0.05
-0.01
-0.02
-0.05
-0.01
-0.01
-0.01
-0.02
-0.02
-0.02
-0.02
-0.01
-0.02
-0.04
-0.04
-0.02
-0.06
-0.00
-0.04
-0.02
-0.16
-0.10
-0.24
-0.20
-0.02
-0.04
-0.04
-0.04
-0.01
-0.04
-0.04
0.04
0.01
-0.02
-0.08
-0.02
-0.02
-0.01
-0.05
-0.63
-0.01
-0.05
-0.03
-0.06
-0.03
-0.07
-0.07
-0.11
-0.17
-0.10
-0.08
-0.04
-0.03
-0.03
0.04
0.18
-0.11
-0.04
-0.03
-0.11
-0.09
-0.10
0.10
-0.09
-0.07
-0.08
-0.08
-0.03
-0.05
-0.10
-0.10
-0.04
-0.06
-0.06
-0.06
-0.03
-0.21
-0.13
-0.26
-0.22
0.02
-0.10
0.10
0.10
-0.02
-0.10
0.10
-0.10
-0.06
-0.05
-0.11
-0.02
-0.09
-0.04
-0.11
-0.66
-0.04
-0.07
-0.06
-0.10
-0.08
-0.12
-0.04
-0.03
-0.11
-0.06
-0.04
-0.03
-0.03
-0.03
0.03
-0.06
-0.03
-0.03
0.03
-0.03
-0.02
-0.01
-0.01
-0.03
-0.03
-0.02
-0.02
-0.01
0.03
-0.05
-0.05
0.02
-0.08
-0.01
-0.08
-0.03
-0.18
-0.22
-0.25
-0.20
-0.02
-0.05
0.05
-0.05
-0.01
-0.05
-0.05
-0.05
-0.02
-0.03
-0.21
-0.02
0.03
-0.02
0.03
-0.62
-0.02
-0.12
-0.04
-0.06
-0.04
-0.16
-0.09
-0.14
-0.17
-0.09
-0.08
-0.06
-0.06
-0.05
-0.06
-0.15
-0.14
-0.06
-0.06
-0.13
-0.04
-0.03
-0.02
-0.07
-0.07
-0.05
-0.05
-0.02
0.05
-0.08
-0.08
-0.05
-0.17
0.01
0.12
-0.06
-0.21
0.26
0.28
-0.25
-0.05
-0.08
-0.08
-0.08
-0.03
-0.08
-0.08
-0.08
-0.04
-0.05
-0.30
-0.04
0.05
-0.04
0.14
-0.65
-0.04
-0.16
-0.08
-0.09
-0.08
-0.20
-0.21
-0.29
-0.28
-0.17
-0.22
0.14
-0.09
-0.09
-0.14
-0.26
-0.29
0.14
-0.09
-0.29
-0.28
-0.30
0.30
0.28
-0.22
-0.25
-0.24
-0.08
-0.14
-0.23
-0.23
-0.12
-0.17
0.17
-0.16
-0.09
-0.35
-0.30
-0.31
-0.29
-0.07
-0.23
-0.23
-0.23
-0.07
-0.23
-0.23
0.23
-0.19
-0.14
-0.39
-0.06
0.27
-0.14
-0.29
-0.68
-0.12
-0.20
-0.16
-0.17
-0.22
-0.30
-0.10
-0.10
-0.17
-0.10
-0.10
-0.08
-0.07
-0.06
-0.08
-0.14
0.10
0.08
-0.07
-0.10
-0.05
0.03
-0.03
-0.09
-0.08
-0.06
0.06
-0.03
0.07
-0.09
-0.09
-0.06
-0.21
-0.02
-0.21
-0.07
-0.20
-0.48
-0.28
0.27
0.06
-0.09
0.09
0.09
-0.03
-0.09
0.09
-0.09
-0.05
-0.07
-0.41
-0.05
0.07
-0.05
-0.10
-0.65
-0.05
-0.30
-0.11
-0.10
-0.10
-0.40
-0.19
-0.25
-0.25
-0.14
-0.17
-0.17
-0.12
-0.10
-0.17
-0.24
-0.25
-0.17
-0.12
-0.23
-0.09
-0.07
-0.05
-0.17
-0.17
-0.12
-0.13
-0.06
-0.11
-0.14
-0.14
-0.12
-0.42
-0.03
-0.30
-0.12
-0.24
-0.53
-0.32
-0.34
-0.13
-0.14
-0.14
-0.14
-0.07
-0.14
-0.14
-0.14
-0.11
-0.14
-0.57
-0.10
-0.14
-0.08
-0.25
-0.69
-0.11
-0.40
-0.21
-0.14
-0.17
-0.50
-0.46
-0.47
-0.50
-0.31
-0.54
-0.40
-0.20
-0.19
-0.40
-0.38
-0.47
-0.40
-0.20
-0.49
-0.71
-0.75
-0.76
-0.70
-0.56
-0.65
-0.60
-0.20
-0.33
-0.51
-0.51
-0.31
-0.44
-0.44
-0.38
-0.20
-0.55
-0.58
-0.37
-0.40
-0.18
-0.51
-0.51
-0.51
-0.19
-0.51
-0.51
-0.51
-0.49
-0.36
-0.72
-0.15
-0.68
-0.32
-0.47
-0.74
-0.31
-0.50
-0.41
-0.31
-0.54
ENG-ANAL
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT -WASTE
STAT-WASTE
STAT -WASTE
STAT-SIC
STAT
STAT-WASTE
STAT
STAT
STAT
STAT
STAT
STAT-WASTE
STAT-SIC
STAT-SIC
STAT
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-A
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-SIC
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-A
STAT -WASTE
STAT-WASTE
STAT
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
21
-------
SIC_P WASTE TOWS LB_B9 HB_89 HB_89 LB_95 MB_95 HB_95 LB_09 HB_09 HB_09 SOUR
5161
5161
5161
5161
5161
5161
5161
5161
5161
5161
5161
5161
5161
5161
5161
5171
5171
5171
5171
5171
5191
5191
5198
5198
5198
5198
5198
5198
5198
5198
5198
5209
5209
5209
5209
5209
5221
5231
5231
5231
5231
5231
5231
5231
5261
5261
5511
5511
5511
5511
5511
5511
5511
5511
5511
5511
0009
F001
F002
F003
F005
P030
U112
U117
U122
U154
U196
WP01
UP02
UT01
WT02
D001
DOM
D008
K052
UT02
D016
UT02
D001
D002
D006
0007
D008
F003
F005
UT01
UT02
D001
0006
F001
F003
F005
WL01
D001
0006
0007
0008
0009
F003
F005
U083
U084
0001
D002
D008
F001
F002
F003
F004
F005
UT01
UT02
0.00
38.15
39.55
2.31
2.23
0.01
0.01
0.00
0.11
0.01
0.00
16.26
2.23
1.21
0.96
62.57
1.20
49.80
6.20
4.26
0.21
47.20
1.81
1.55
0.92
1.12
1.38
0.19
0.19
0.46
1.65
0.25
1.86
1.86
1.86
1.86
8.35
3.91
0.06
0.06
0.06
25.41
3.89
3.89
0.08
0.08
83.61
1.70
0.04
0.26
6.92
15.34
0.44
16.15
0.04
0.95
-0.02
-0.01
-0.01
-0.01
-0.01
-0.01
-0.02
-0.01
-0.01
-0.01
-0.01
-0.02
-0.04
-0.05
-0.01
-0.04
-0.01
-0.01
-0.04
-0.01
-0.10
-0.01
-0.01
-0.04
-0.09
-0.05
-0.01
-0.01
-0.01
-0.05
-0.01
-0.01
-0.09
-0.01
-0.01
-0.01
-0.01
-0.01
-0.09
-0.05
-0.01
-0.02
-0.01
-0.01
-0.10
-0.10
-0.01
-0.02
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.05
-0.00
-0.03
-0.09
-0.03
-0.01
-0.02
-0.01
-0.12
-0.01
-0.01
-0.01
-0.01
-0.04
-0.08
-0.07
-0.01
-0.08
-0.03
-0.03
-0.08
-0.01
-0.12
-0.01
-0.05
-0.05
-0.12
-0.06
-0.03
0.01
-0.02
-0.07
-0.01
-0.05
-0.12
-0.09
-0.01
-0.02
-0.03
-0.05
-0.12
-0.06
-0.03
-0.03
-0.01
-0.02
-0.12
-0.12
-0.01
-0.04
-0.03
-0.09
-0.02
-0.02
-0.03
-0.02
-0.07
-0.00
-0.09
-0.18
-0.07
-0.04
-0.03
-0.04
-0.23
-0.04
-0.04
0.04
-0.04
0.08
-0.11
-0.09
-0.03
0.10
-0.06
-0.08
-0.10
-0.03
-0.15
-0.03
-0.11
-0.07
-0.17
0.10
0.08
-0.04
-0.03
-0.09
-0.03
0.11
-0.17
-0.18
-0.04
-0.03
-0.06
-0.11
0.17
-0.10
-0.08
-0.09
-0.04
-0.03
-0.15
-0.15
-0.10
-0.05
0.08
-0.18
-0.06
-0.06
-0.06
-0.06
-0.09
-0.03
-0.05
-0.06
-0.04
-0.03
-0.03
-0.02
-0.05
-0.02
-0.02
0.02
-0.02
0.12
-0.21
-0.05
-0.03
-0.13
-0.04
-0.04
-0.13
-0.03
-0.14
-0.03
-0.03
-0.12
-0.11
0.06
0.04
-0.03
-0.03
-0.05
-0.03
-0.03
-0.11
-0.06
-0.03
-0.03
-0.04
-0.03
-0.11
-0.06
-0.04
-0.05
-0.03
-0.03
-0.14
-0.14
-0.02
-0.05
0.04
-0.06
-0.03
-0.03
0.04
-0.03
-0.05
-0.01
-0.10
-0.15
-0.09
0.06
-0.06
-0.04
-0.34
-0.04
-0.04
-0.04
-0.04
-0.17
0.30
-0.10
0.05
-0.25
-0.08
-0.08
-0.25
-0.05
-0.18
-0.05
0.14
-0.16
-0.17
-0.09
-0.08
-0.06
-0.06
-0.10
-0.05
-0.14
-0.17
-0.15
-0.06
-0.06
-0.07
-0.14
-0.17
0.09
-0.08
0.10
-0.06
-0.06
-0.18
-0.18
-0.03
-0.11
-0.08
-0.15
-0.05
-0.06
-0.08
-0.06
-0.10
-0.01
-0.28
-0.26
-0.21
-0.14
-0.09
-0.12
0.63
-0.12
-0.12
-0.12
-0.12
0.28
-0.39
-0.15
-0.09
-0.31
-0.16
-0.22
-0.31
-0.09
0.24
-0.09
0.29
-0.20
-0.28
-0.17
-0.22
0.14
0.09
-0.15
-0.09
-0.29
-0.28
-0.26
-0.14
-0.09
-0.11
0.29
-0.28
-0.17
-0.22
-0.28
-0.14
0.09
-0.24
-0.24
-0.22
-0.15
-0.22
-0.26
-0.18
0.17
-0.18
-0.18
-0.15
-0.10
-0.12
0.14
-0.10
-0.08
-0.07
-0.05
-0.18
-0.05
-0.05
-0.05
-0.05
-0.23
-0.41
-0.10
-0.06
-0.32
-0.11
-0.10
-0.32
-0.06
-0.20
-0.06
-0.10
-0.30
-0.17
-0.10
0.10
-0.08
-0.07
-0.10
-0.06
-0.10
-0.17
-0.14
-0.08
-0.07
-0.09
-0.10
-0.17
0.10
-0.10
-0.12
-0.08
-0.07
-0.20
-0.20
-0.04
-0.13
-0.10
-0.14
-0.07
-0.07
-0.11
-0.07
-0.10
-0.02
-0.25
-0.24
-0.19
-0.17
-0.12
-0.11
-0.52
-0.11
-0.11
-0.11
-0.11
-0.30
-0.57
-0.20
-0.10
-0.64
-0.21
-0.17
-0.64
-0.10
-0.26
-0.10
-0.25
-0.40
-0.25
-0.14
-0.17
-0.17
0.12
-0.20
-0.10
-0.25
-0.25
-0.24
-0.17
-0.12
-0.16
-0.25
-0.25
-0.14
-0.17
-0.25
-0.17
-0.12
-0.26
-0.26
-0.08
-0.27
-0.17
-0.24
-0.13
-0.15
-0.22
-0.15
-0.20
-0.03
-0.72
-0.38
-0.46
-0.40
-0.20
-0.31
0.85
-0.31
-0.31
-0.31
-0.31
-0.53
-0.72
-0.31
-0.19
-0.79
-0.41
-0.54
-0.79
-0.19
-0.37
-0.19
-0.47
-0.50
-0.50
-0.31
-0.54
-0.40
-0.20
-0.31
-0.19
-0.47
-0.50
-0.38
-0.40
-0.20
-0.22
-0.47
-0.50
-0.31
-0.54
-0.72
-0.40
-0.20
-0.37
-0.37
-0.51
-0.39
-0.54
-0.38
-0.45
-0.43
-0.47
-0.46
-0.31
-0.26
STAT -WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT -WASTE
STAT-SIC
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-WASTE
TOT-AVG
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
TOT-AVG
TOT-AVG
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT
STAT
STAT-WASTE
STAT-WASTE
22
-------
SIC_P UASTE TONS LB_89 HB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
5531
5531
5531
5531
5541
5733
5733
5733
5733
5733
5931
5931
5931
5931
5931
5931
5931
5931
5931
5931
5931
5931
5931
5931
5931
5931
5931
5941
5941
5941
5941
5941
5999
5999
5999
5999
5999
5999
5999
5999
6103
6103
6103
6103
6103
6109
6109
6309
6409
6409
6511
6511
6511
6511
6531
6792
0004
0006
0007
0008
0001
D002
D006
D007
F007
FOOB
0001
0002
0004
0006
0007
0008
0009
0011
F001
F002
F003
F005
F006
UL02
UP01
UT01
UT02
0002
0007
0008
F006
UT02
0001
0002
0006
0007
0008
F002
F004
UT02
0001
0002
U211
UL01
UT01
0001
F003
D002
0001
0008
0006
0007
0008
UT02
0008
0001
5.41
5.41
5.41
7.17
807.99
0.14
0.05
0.09
0.05
0.05
72.62
12.70
0.04
0.09
0.25
0.09
5.16
1.02
0.84
1.97
0.35
5.34
0.35
0.03
0.72
2.24
57.28
0.91
3.81
0.33
0.49
3.15
6.03
1.36
0.76
0.76
1.36
0.11
0.11
0.60
0.00
0.03
0.00
0.03
0.00
0.69
0.69
0.79
0.28
0.28
0.82
0.82
0.82
0.82
10.33
0.80
-0.01
0.09
-0.05
-0.01
-0.01
-0.61
-0.09
0.05
-0.07
-0.22
-0.01
-0.04
-0.01
-0.09
-0.05
-0.01
-0.02
-0.01
-0.01
-0.01
-0.01
-0.01
-0.14
-0.01
-0.02
-0.05
-0.01
0.61
0.01
-0.01
-0.14
-0.00
0.00
-0.04
-0.09
0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.61
-0.10
-0.01
-0.05
0.01
-0.01
-0.61
-0.01
-0.01
-0.09
-0.05
-0.01
-0.01
-0.01
-0.01
-0.03
-0.12
0.06
-0.03
0.05
-0.63
-0.12
-0.06
-0.10
0.24
-0.05
-0.05
-0.03
0.12
0.06
-0.03
0.03
0.02
-0.09
-0.03
-0.01
-0.02
0.16
-0.01
-0.04
-0.07
-0.01
0.63
-0.01
-0.03
-0.16
0.00
-0.00
-0.05
-0.12
-0.06
-0.03
-0.02
-0.02
-0.01
-0.05
-0.63
-0.12
-0.03
0.07
0.05
-0.01
-0.63
-0.05
-0.03
-0.12
-0.06
-0.03
-0.01
-0.03
-0.05
-0.06
-0.17
-0.10
-0.08
-0.11
-0.66
-0.17
-0.10
-0.13
-0.26
-0.11
-0.07
-0.06
0.17
-0.10
-0.08
-0.09
0.05
-0.18
-0.07
-0.04
-0.03
0.20
0.01
-0.08
0.09
-0.03
0.66
-0.07
0.08
-0.20
-0.04
-0.00
-0.07
-0.17
-0.10
-0.08
-0.02
-0.02
-0.03
-0.11
-0.66
-0.15
-0.06
-0.09
-0.11
-0.04
-0.66
-0.11
-0.08
-0.17
-0.10
-0.08
-0.03
-0.08
0.11
-0.04
0.11
-0.06
-0.04
0.03
-0.62
0.11
0.06
-0.22
0.25
-0.03
-0.12
-0.04
-0.11
-0.06
-0.04
0.05
0.03
-0.06
-0.04
-0.03
-0.03
-0.19
0.02
0.12
0.05
-0.03
-0.62
0.02
-0.04
0.19
0.00
0.01
-0.12
-0.11
-0.06
0.04
0.03
-0.03
-0.03
-0.03
0.62
-0.14
-0.04
0.05
-0.03
-0.03
-0.62
0.03
-0.04
-0.11
-0.06
-0.04
-0.03
-0.04
-0.03
-0.08
-0.17
-0.09
-0.08
-0.14
-0.65
0.17
-0.09
-0.26
-0.28
-0.14
-0.16
-0.08
-0.17
-0.09
-0.08
-0.10
-0.05
0.15
-0.09
-0.06
-0.06
-0.23
0.03
0.17
-0.10
-0.05
-0.65
0.04
-0.08
0.23
-0.01
0.01
-0.16
-0.17
-0.09
0.08
-0.05
-0.05
-0.05
-0.14
0.65
-0.18
-0.07
0.10
-0.14
-0.06
-0.65
-0.14
-0.08
-0.17
-0.09
-0.08
-0.05
-0.08
-0.14
-0.16
-0.28
0.17
-0.22
0.29
-0.68
-0.28
-0.17
-0.30
-0.31
-0.29
-0.20
-0.16
-0.28
-0.17
-0.22
-0.28
0.14
0.26
-0.21
-0.14
-0.09
-0.31
-0.04
-0.28
-0.15
-0.09
-0.68
-0.22
0.22
-0.31
-0.13
-0.01
-0.20
-0.28
-0.17
-0.22
-0.06
-0.06
-0.09
-0.29
-0.68
-0.24
-0.11
0.15
0.29
-0.14
-0.68
-0.29
-0.22
-0.28
-0.17
-0.22
-0.09
-0.22
-0.29
-0.11
-0.17
-0.10
-0.10
-0.10
-0.65
-0.17
-0.10
-0.48
-0.28
-0.10
-0.30
-0.11
-0.17
-0.10
-0.10
-0.12
0.07
-0.14
-0.10
-0.08
-0.07
-0.21
0.05
0.23
-0.10
-0.06
-0.65
-0.05
0.10
-0.21
-0.01
-0.01
-0.30
-0.17
-0.10
-0.10
0.07
-0.07
-0.06
-0.10
-0.65
-0.20
-0.09
-0.10
-0.10
-0.08
-0.65
-0.10
-0.10
-0.17
-0.10
-0.10
-0.06
-0.10
-0.10
-0.21
-0.25
-0.14
-0.17
-0.25
-0.69
-0.25
-0.14
-0.53
-0.32
-0.25
-0.40
-0.21
-0.25
0.14
0.17
0.25
-0.11
-0.24
-0.19
-0.17
-0.12
-0.26
-0.07
0.30
-0.20
-0.10
-0.69
-0.10
0.17
-0.26
-0.02
-0.03
-0.40
-0.25
-0.14
-0.17
-0.14
-0.14
-0.10
-0.25
-0.69
-0.26
-0.16
-0.20
-0.25
-0.17
-0.69
-0.25
-0.17
-0.25
-0.14
-0.17
-0.10
-0.17
-0.25
-0.41
0.50
-0.31
0.54
-0.47
-0.74
-0.50
-0.31
-0.58
-0.37
-0.47
-0.50
-0.41
-0.50
0.31
-0.54
-0.72
-0.33
-0.38
-0.46
-0.40
-0.20
-0.41
-0.10
-0.53
-0.31
-0.19
-0.74
0.55
-0.54
-0.41
-0.33
-0.03
-0.50
-0.50
-0.31
-0.54
-0.16
-0.16
-0.19
-0.47
-0.74
-0.37
-0.22
0.31
-0.47
-0.40
-0.74
-0.47
-0.54
-0.50
-0.31
-0.54
-0.19
-0.54
-0.47
STAT-UASTE
STAT -WASTE
STAT-UASTE
STAT-WASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
ENG-ANAL
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
ENG-ANAL
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT
STAT
STAT-UASTE
STAT-UASTE
STAT-UASTE
TOT-AVG
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
STAT-UASTE
23
-------
SIC_P WASTE TONS LB_89 HB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
7216
7216
7216
7218
7218
7218
7219
7299
7299
7330
7330
7340
7340
7340
7340
7340
7340
7340
7390
7390
7390
7390
7391
7391
7391
7391
7391
7391
7391
7391
7391
7391
7391
7391
7391
7391
7391
7397
7397
7397
7397
7397
7397
7397
7397
7397
7397
7397
7399
7399
7399
7399
7399
7531
7531
7531
0001
F001
F002
WP01
UP02
WT01
F002
F001
F002
D001
F001
D002
D004
D005
D006
D007
0008
UT02
0002
F002
WL01
WT01
D001
0002
F001
F002
F003
F005
U031
U044
U122
U188
U220
WL01
UL02
UP02
UT01
D001
0002
F001
F002
F003
F005
W001
UL01
WL02
UT01
WT02
D001
F001
F002
F003
F004
0001
0005
F001
0.85
7.05
146.57
14.88
0.44
1652.6
0.32
1.34
19.50
0.78
0.78
9.90
8.58
8.58
8.58
9.25
10.57
2.48
0.05
0.43
0.02
0.02
1.55
0.50
0.33
3.92
4.00
0.66
0.01
0.05
0.00
0.04
0.00
2.42
0.04
0.01
0.10
0.20
0.09
0.83
0.13
0.19
0.18
0.38
0.05
0.55
0.08
0.05
1833.0
2.10
50.42
1.01
48.23
43.31
0.31
0.31
-0.01
-0.01
-0.02
-0.02
-0.04
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.04
-0.01
-0.00
-0.09
-0.05
-0.01
0.01
-0.61
-0.01
-0.01
-0.05
-0.01
-0.61
-0.01
-0.01
-0.01
-0.01
-0.10
-0.10
-0.10
-0.01
-0.10
-0.01
-0.01
-0.04
-0.05
-0.01
-0.61
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
0.00
-0.05
-0.01
-0.01
-0.01
-0.02
-0.01
-0.01
-0.01
-0.00
-0.01
-0.05
-0.09
-0.04
-0.04
-0.08
-0.07
-0.03
-0.09
-0.03
-0.05
-0.09
-0.05
-0.03
-0.01
-0.12
-0.06
-0.03
-0.01
-0.63
-0.03
-0.03
-0.07
-0.05
-0.63
-0.09
-0.03
-0.01
-0.02
-0.12
-0.12
-0.12
-0.02
-0.12
-0.03
-0.01
-0.08
-0.07
-0.01
-0.63
-0.09
-0.03
-0.01
-0.02
-0.08
-0.03
0.00
-0.07
-0.01
-0.02
-0.09
-0.03
-0.01
-0.01
-0.01
-0.01
-0.09
-0.11
-0.18
-0.10
-0.08
-0.11
-0.09
0.07
0.18
0.07
-0.11
-0.18
0.07
0.06
-0.10
-0.17
-0.10
-0.08
-0.03
-0.66
-0.07
-0.06
-0.09
0.11
-0.66
-0.18
-0.07
-0.04
-0.03
-0.15
-0.15
0.15
-0.03
0.15
-0.06
-0.01
-0.11
0.09
-0.03
-0.66
-0.18
-0.07
-0.04
-0.03
-0.12
-0.06
-0.04
-0.09
-0.03
-0.03
-0.18
-0.07
-0.04
0.05
-0.08
-0.10
-0.18
-0.03
-0.06
0.06
-0.12
-0.21
-0.05
0.04
0.06
-0.04
-0.03
-0.06
0.12
0.04
-0.01
0.11
-0.06
-0.04
-0.03
-0.62
-0.04
0.04
-0.05
-0.03
-0.62
-0.06
-0.04
-0.03
-0.03
0.14
-0.14
-0.14
-0.02
-0.14
-0.04
-0.02
-0.21
0.05
-0.02
-0.62
-0.06
-0.04
-0.03
-0.03
-0.31
-0.04
0.00
-0.05
-0.03
-0.02
-0.06
-0.05
-0.03
0.02
-0.02
0.01
-0.06
-0.14
-0.15
-0.13
-0.17
-0.30
-0.10
-0.09
-0.15
-0.09
-0.14
-0.15
-0.16
-0.08
-0.02
-0.17
-0.09
-0.08
-0.05
-0.65
-0.09
-0.07
-0.10
-0.14
-0.65
-0.15
-0.09
-0.06
-0.06
-0.18
-0.18
-0.18
-0.04
-0.18
-0.07
-0.03
-0.30
-0.10
-0.04
-0.65
-0.15
-0.09
-0.06
-0.06
-0.39
-0.07
0.00
-0.10
-0.05
-0.05
-0.15
-0.10
-0.06
-0.04
-0.03
-0.02
-0.15
-0.29
-0.26
-0.28
-0.28
-0.39
-0.15
-0.21
-0.26
-0.21
-0.29
-0.26
-0.20
-0.16
-0.30
-0.28
-0.17
-0.22
-0.09
-0.68
-0.21
0.11
-0.15
-0.29
-0.68
-0.26
-0.21
-0.14
-0.09
-0.24
-0.24
-0.24
-0.06
-0.24
-0.11
-0.04
-0.39
-0.15
-0.10
-0.68
-0.26
-0.21
-0.14
-0.09
'-0.47
-0.11
-0.12
-0.15
-0.09
-0.10
-0.26
-0.14
-0.14
-0.08
-0.22
-0.30
-0.26
-0.10
-0.14
-0.16
-0.23
-0.41
-0.10
-0.10
-0.14
-0.10
-0.10
-0.14
-0.30
0.11
-0.03
0.17
-0.10
-0.10
-0.06
0.65
-0.10
-0.09
-0.10
-0.10
-0.65
-0.14
-0.10
-0.08
-0.07
-0.20
-0.20
-0.20
-0.07
-0.20
-0.09
-0.05
-0.41
-0.10
-0.05
-0.65
-0.14
-0.10
-0.08
-0.07
-0.67
-0.09
0.00
-0.10
-0.06
-0.06
-0.14
-0.12
-0.08
-0.05
-0.04
-0.03
-0.14
-0.25
-0.24
-0.33
-0.30
-0.57
-0.20
-0.19
-0.24
-0.19
-0.25
-0.24
-0.40
-0.21
-0.05
0.25
-0.14
0.17
-0.10
-0.69
-0.19
-0.16
-0.20
-0.25
-0.69
-0.24
-0.19
0.17
-0.12
0.26
-0.26
-0.26
-0.09
-0.26
-0.16
0.07
-0.57
0.20
-0.11
0.69
-0.24
-0.19
-0.17
-0.12
-0.74
-0.16
0.00
0.20
-0.10
-0.12
-0.24
-0.25
-0.17
-0.10
-0.08
-0.05
-0.24
-0.47
0.38
-0.70
-0.53
-0.72
-0.31
-0.46
-0.38
-0.46
-0.47
-0.38
-0.50
-0.41
-0.76
-0.50
-0.31
-0.54
-0.19
-0.74
-0.46
-0.22
-0.31
-0.47
-0.74
-0.38
-0.46
-0.40
-0.20
-0.37
-0.37
-0.37
-0.11
-0.37
-0.22
-0.10
-0.72
-0.31
-0.25
-0.74
-0.38
-0.46
-0.40
-0.20
-0.80
-0.22
-0.30
-0.31
-0.19
-0.26
-0.38
-0.31
-0.40
-0.15
-0.54
-0.76
-0.38
STAT -WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
TOT-AVG
TOT-AVG
TOT-AVG
STAT-WASTE
TOT-AVG
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-UASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT-WASTE
24
-------
SIC_P WASTE TONS LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
7531
7531
7531
7531
7532
7532
7532
7535
7535
7535
7535
7538
7538
7538
7538
7538
7538
7538
7538
7538
7538
7538
7539
7539
7539
7539
7539
7539
7539
7539
7539
7539
7539
7600
7600
7600
7600
7629
7629
7641
7641
7641
7641
7641
7641
7641
7694
7694
7694
7694
7694
7694
7694
7699
7699
7699
F003
F005
WT01
UT02
0001
F003
F005
0001
F003
F005
UT02
D001
D002
D006
D007
D008
F001
F002
F004
K051
UT01
UT02
0001
D002
D006
D007
0008
F002
F003
F004
F005
UT01
UT02
D001
D008
F003
UT02
0001
F001
0001
0002
D003
F001
F003
F005
WP01
0002
0004
0005
0008
0009
0010
W001
0001
0002
0003
34.89
32.68
0.12
6.21
0.13
0.13
0.13
3.06
2.58
2.58
0.32
4.41
2.30
2.45
2.45
3.13
0.24
0.53
0.15
0.17
2.45
4.20
5.67
0.06
1.05
1.05
3.70
0.46
0.70
0.06
0.70
0.82
0.47
0.27
0.27
0.27
0.27
0.57
0.91
0.72
0.70
0.70
1.00
0.72
0.72
0.60
0.40
1.31
0.91
0.91
1.31
0.40
18.29
140.59
69.66
76.60
0.01
-0.01
-0.05
0.00
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.04
-0.09
-0.05
-0.02
-0.01
-0.03
-0.03
-0.02
-0.05
-0.01
-0.01
-0.61
-0.02
-0.02
-0.02
-0.01
-0.01
-0.03
-0.01
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.61
-0.05
-0.01
-0.01
-0.01
-0.02
-0.61
-0.01
-0.00
-0.01
-0.02
-0.01
-0.05
-0.01
-0.01
-0.05
-0.02
-0.02
-0.07
-0.01
-0.05
-0.01
-0.02
-0.01
-0.01
-0.01
-0.01
-0.03
-0.05
-0.12
-0.06
-0.03
-0.09
-0.07
-0.04
-0.03
-0.07
-0.01
-0.01
-0.63
-0.04
-0.04
-0.04
-0.03
-0.01
-0.04
-0.02
0.07
-0.01
-0.05
-0.03
-0.01
-0.01
-0.05
-0.09
-0.05
-0.63
-0.07
-0.09
0.01
-0.02
0.04
-0.63
-0.03
-0.01
-0.03
-0.03
-0.01
-0.08
0.05
-0.02
-0.07
-0.05
-0.07
-0.09
-0.03
0.11
0.04
-0.03
0.06
-0.04
-0.04
-0.03
-0.14
-0.07
-0.17
-0.10
-0.03
-0.18
-0.09
-0.06
-0.03
-0.09
-0.03
-0.19
-0.66
-0.04
-0.04
-0.04
0.07
-0.04
0.06
-0.03
-0.09
-0.03
-0.11
-0.08
-0.04
-0.03
-0.11
-0.18
-0.11
-0.66
-0.08
-0.18
-0.04
-0.03
-0.08
-0.66
-0.06
-0.10
-0.08
-0.09
-0.03
-0.12
-0.11
-0.12
-0.08
-0.02
0.02
-0.05
-0.01
-0.03
-0.03
0.03
-0.02
-0.02
-0.02
-0.03
-0.04
-0.12
-0.11
0.06
-0.05
0.06
-0.10
-0.08
0.05
-0.05
-0.03
-0.02
-0.62
-0.07
-0.07
0.06
-0.04
-0.03
-0.08
-0.03
-0.05
-0.03
-0.03
0.04
-0.03
-0.03
-0.03
-0.06
-0.03
-0.62
0.16
-0.06
-0.03
-0.03
-0.12
-0.62
-0.04
-0.01
-0.04
-0.05
-0.02
-0.31
-0.03
-0.04
-0.16
-0.05
-0.05
-0.10
-0.02
-0.14
-0.06
-0.06
-0.03
-0.04
-0.04
-0.05
-0.08
-0.16
-0.17
-0.09
-0.09
-0.15
-0.20
-0.12
-0.09
-0.10
-0.05
-0.04
-0.65
-0.13
-0.13
-0.13
-0.09
-0.06
-0.12
-0.06
-0.10
-0.05
-0.14
-0.08
-0.06
-0.05
-0.14
-0.15
-0.14
-0.65
-0.20
-0.15
-0.06
-0.06
-0.17
-0.65
-0.08
-0.02
-0.08
-0.10
-0.04
-0.39
-0.13
-0.07
-0.20
-0.15
-0.17
-0.15
-0.10
-0.29
-0.14
-0.09
-0.17
-0.12
-0.12
-0.09
-0.20
-0.20
-0.28
-0.17
-0.09
-0.26
-0.26
-0.16
-0.10
-0.15
-0.09
-0.26
-0.68
-0.13
-0.13
-0.13
-0.21
-0.14
-0.16
-0.09
-0.15
-0.09
-0.29
-0.22
-0.14
-0.09
-0.29
-0.26
-0.29
-0.68
-0.24
-0.26
-0.14
-0.09
-0.28
-0.68
-0.16
-0.30
-0.22
-0.28
-0.10
-0.47
-0.29
-0.35
-0.24
-0.06
-0.06
-0.10
0.02
-0.10
-0.08
-0.07
-0.04
-0.05
-0.05
-0.06
-0.11
-0.30
-0.17
-0.10
-0.12
-0.14
-0.25
-0.21
-0.12
-0.10
-0.06
-0.05
-0.65
-0.17
-0.17
-0.17
-0.10
-0.08
-0.21
-0.07
-0.10
-0.06
-0.10
-0.10
-0.08
-0.06
-0.10
-0.14
-0.10
-0.65
-0.39
-0.14
-0.08
-0.07
-0.23
-0.65
-0.11
-0.03
-0.10
-0.12
-0.05
-0.67
-0.10
-0.09
-0.39
-0.12
0.12
0.20
0.04
-0.25
-0.17
-0.12
-0.08
0.09
-0.09
-0.10
0.22
-0.40
-0.25
-0.14
-0.23
-0.24
-0.50
-0.30
-0.24
-0.20
-0.10
-0.10
-0.69
-0.34
-0.34
-0.33
-0.19
-0.17
-0.30
-0.12
-0.20
-0.10
-0.25
-0.17
-0.17
-0.10
-0.25
-0.24
-0.25
-0.69
-0.49
-0.24
-0.17
-0.12
-0.30
-0.69
-0.21
-0.05
-0.17
-0.25
-0.10
-0.74
-0.23
-0.18
-0.49
-0.38
-0.39
-0.31
0.24
-0.47
-0.40
-0.20
-0.43
-0.30
-0.30
-0.19
-0.35
-0.50
-0.50
-0.31
-0.24
-0.38
-0.66
-0.38
-0.26
-0.31
-0.19
-0.43
-0.74
-0.34
-0.34
0.34
-0.46
0.40
-0.38
0.20
0.31
0.19
0.47
-0.54
0.40
0.19
-0.47
-0.38
-0.47
-0.74
0.59
0.38
-0.40
0.20
-0.53
-0.74
-0.41
-0.76
-0.54
-0.72
-0.26
-0.80
-0.49
-0.88
-0.59
STAT
STAT
STAT -WASTE
STAT -WASTE
STAT-WASTE
STAT -WASTE
STAT-WASTE
STAT
STAT
STAT
STAT-WASTE
STAT
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT-WASTE
25
-------
SIC P WASTE TONS LB 89 MB 89 HB 89 LB 95 MB 95 HB 95 LB 09 MB 09 HB 09 SOUR
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7699
7814
8002
8002
8002
8061
8061
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8062
8069
8069
8069
8069
8069
0005
D006
D007
0008
0009
F001
F002
F003
F004
F005
U002
U036
U052
U117
U151
U159
W001
won
UP01
WP02
UP03
WT02
F001
0001
F003
F005
0001
F005
0001
0002
D003
0007
D009
F003
P003
P011
P022
P030
P098
U002
U012
U019
U044
U080
U108
U211
UC02
UL01
UL02
WT01
UT02
0001
D002
D003
0007
0009
2.84
470.81
497.19
408.47
336.84
3.98
16.65
3.62
t.11
3.62
0.21
0.08
2.00
0.12
6.56
1.99
19.31
1.49
5.44
1.06
103.66
122.19
0.60
1.35
0.36
0.36
0.20
0.20
1.25
0.06
0.03
0.01
0.00
0.84
0.02
0.00
0.02
0.00
0.00
0.03
0.02
0.03
0.02
0.02
0.03
0.02
0.73
0.10
0.04
0.04
0.17
2.10
0.01
0.00
0.09
0.08
-0.00
-0.01
-0.01
-0.01
-0.02
-0.01
-0.01
-0.01
-0.03
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.05
-0.04
-0.02
-0.04
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.02
-0.01
-0.05
-0.05
-0.02
-0.01
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.04
-0.01
-0.01
-0.05
-0.01
-0.02
-0.61
-0.05
-0.01
-0.00
-0.01
-0.01
-0.01
-0.02
-0.03
-0.09
-0.02
-0.03
-0.04
-0.01
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.08
-0.05
-0.04
-0.08
-0.02
-0.01
-0.09
-0.05
-0.01
-0.02
-0.05
-0.02
-0.03
-0.02
-0.07
-0.06
-0.03
-0.01
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.05
-0.02
-0.02
-0.07
-0.01
-0.04
-0.63
-0.07
-0.01
-0.01
-0.10
-0.10
-0.10
-0.09
-0.09
-0.18
-0.08
-0.06
-0.06
-0.02
-0.09
-0.09
-0.09
-0.09
-0.09
-0.09
-0.12
-0.06
-0.05
-0.11
-0.02
-O.OS
-0.18
-0.11
-0.04
-0.03
-0.11
-0.03
-0.09
-0.05
-0.08
-0.10
-0.09
-0.04
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.06
-0.04
-0.03
-0.09
-0.03
-0.06
-0.66
-0.08
-0.03
-0.01
-0.01
-0.02
-0.02
-0.03
-0.05
-0.06
-0.03
-0.04
-0.08
-0.02
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.31
-0.11
-0.06
-0.21
-0.02
-0.02
-0.06
-0.03
-0.03
-0.03
-0.03
-0.03
-0.05
-0.04
-0.16
-0.06
-0.05
-0.03
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.12
-0.02
-0.03
-0.05
-0.03
-0.07
-0.62
-0.16
-0.02
-0.01
-0.02
-0.04
-0.04
-0.06
-0.09
-0.15
-0.07
-0.09
-0.12
-0.04
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.39
-0.15
-0.12
-0.30
-0.04
-0.04
-0.15
-0.14
-0.06
-0.06
-0.14
-0.06
-0.10
0.07
-0.20
-0.09
-0.10
-0.06
-0.09
-0.09
-0.09
-0.09
-0.09
-0.09
-0.09
-0.09
-0.09
-0.09
-0.09
-0.09
-0.16
-0.05
-0.06
-0.10
-0.05
-0.13
-0.65
-0.20
-0.03
-0.02
-0.30
-0.31
-0.31
-0.25
-0.28
-0.26
-0.25
-0.17
-0.16
-0.05
-0.28
-0.28
-0.28
0.28
-0.28
-0.28
-0.47
-0.19
-0.16
-0.39
0.06
-0.14
-0.26
-0.29
-0.14
-0.09
-0.29
-0.09
-0.26
-0.16
-0.24
0.17
-0.28
-0.14
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
0.20
-0.11
-0.10
-0.15
-0.09
0.17
-0.68
-0.24
-0.08
-0.03
-0.03
-0.05
-O.OS
0.08
-0.12
-0.14
-0.08
-0.11
-0.21
-0.05
-0.07
-0.07
-0.07
-0.07
-0.07
-0.07
-0.67
-0.29
-0.15
-0.41
-0.05
-0.05
-0.14
-0.10
-0.08
-0.07
-0.10
-0.07
-0.13
-0.09
-0.39
-0.10
-0.12
-0.08
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
0.12
-0.30
-0.06
-0.08
-0.10
-0.06
-0.17
-0.65
-0.39
-0.04
-0.02
-0.05
-0.10
0.09
-0.14
-0.23
-0.24
-0.14
-0.22
-0.30
-0.10
-0.14
-0.14
-0.14
0.14
-0.14
-0.14
-0.74
-0.38
-0.31
-0.57
-0.10
-0.08
-0.24
-0.25
-0.17
-0.12
-0.25
-0.12
-0.26
-0.18
-0.49
-0.14
-0.25
-0.17
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.24
-0.40
-0.12
-0.16
-0.20
-0.10
-0.33
-0.69
-0.49
-0.08
-0.05
-0.76
-0.79
0.78
-0.61
-0.72
-0.38
-0.57
-0.43
-0.38
-0.14
-0.69
-0.69
-0.69
-0.69
-0.69
-0.69
-0.80
-0.47
-0.40
-0.72
-0.15
-0.32
-0.38
-0.47
-0.40
-0.20
-0.47
-0.20
-0.66
-0.42
-0.59
0.31
-0.72
-0.40
-0.61
-0.61
-0.61
-0.61
-0.61
-0.61
-0.61
-0.61
-0.61
-0.61
-0.61
-0.61
-0.50
-0.28
-0.24
-0.31
-0.19
-0.43
-0.74
-0.59
-0.22
-0.08
STAT -WASTE
STAT
STAT
STAT -A
STAT
STAT -WASTE
STAT -A
STAT
STAT -WASTE
STAT
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT -WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-WASTE
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT
STAT
26
-------
SIC_P WASTE TOtIS LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
8069
8069
8069
8069
8069
8069
8069
8069
8069
8069
8069
8069
8069
8069
8069
8069
8071
8071
8071
8071
8071
8071
8071
8071
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
F002
F003
PI 05
P106
U003
U044
U058
U122
U151
U188
U220
U239
UC01
UL01
WT01
UT02
0001
0007
0008
F002
F003
U003
U151
WL01
D001
0002
D006
D007
D008
F001
F002
F003
F005
P010
P011
P012
P022
P098
P108
U001
U002
U012
U019
U031
UOS2
UOS6
U122
U144
UU7
U148
U154
U159
U16S
U182
U188
U190
0.83
0.65
0.00
0.00
0.25
0.08
0.11
0.90
0.02
0.08
0.24
0.24
0.11
0.48
0.29
0.01
0.60
0.40
0.40
0.01
0.41
0.20
0.00
0.38
1.34
0.00
1.16
1.40
1.16
0.02
0.02
2.02
2.02
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.02
0.00
0.00
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
-0.01
-0.01
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.01
-0.02
-0.02
-0.04
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
-0.01
-0.01
-0.10
-0.10
-0.01
-0.02
-0.61
-0.09
-0.05
-0.01
-0.01
0.01
-0.01
-0.01
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.01
-0.02
-0.03
-0.01
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.02
-0.04
-0.04
-0.05
-0.02
-0.02
-0.01
-0.05
-0.06
-0.03
-0.03
-0.01
-0.10
-0.12
-0.03
-0.05
-0.63
-0.12
-0.06
-0.03
-0.09
-0.03
-0.01
-0.02
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.02
-0.04
-0.07
-0.04
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.03
-0.06
-0.06
-0.06
-0.09
-0.06
-0.03
-0.11
-0.10
-0.08
-0.07
-0.04
-0.12
-0.15
-0.06
-0.06
-0.66
-0.17
-0.10
-0.08
-0.18
-0.07
-0.04
-0.03
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.03
-0.06
-0.04
-0.03
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.02
-0.05
-0.05
-0.11
-0.03
-0.03
-0.03
-0.03
-0.06
-0.04
-0.04
-0.03
-0.15
-0.14
-0.04
-0.07
-0.62
-0.11
-0.06
-0.04
-0.06
-0.04
-0.03
-0.03
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.02
-0.06
-0.09
-0.06
-0.11
-0.11
0.11
-0.11
-0.11
0.11
0.11
-0.04
-0.11
0.11
0.15
-0.05
-0.06
-0.05
-0.14
-0.09
-0.08
-0.09
-0.06
-0.14
-0.18
-0.07
-0.14
-0.65
0.17
-0.09
0.08
-0.15
-0.09
-0.06
0.06
-0.13
-0.13
-0.13
-0.13
-0.13
-0.13
0.13
-0.13
-0.13
-0.13
-0.13
-0.13
-0.13
-0.13
-0.13
-0.13
0.13
0.13
0.13
0.13
0.13
0.04
-0.13
0.21
-0.14
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.06
-0.18
-0.18
-0.19
-0.26
-0.19
-0.09
-0.29
-0.17
-0.22
-0.21
-0.14
-0.18
-0.24
-0.11
-0.17
-0.68
-0.28
-0.17
-0.22
-0.26
-0.21
-0.14
-0.09
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
0.18
-0.18
0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.06
-0.18
-0.10
-0.08
-0.13
-0.13
0.13
-0.13
-0.13
-0.13
-0.13
-0.07
-0.13
-0.13
-0.29
-0.06
-0.07
-0.06
-0.10
-0.10
-0.10
-0.10
-0.08
-0.24
-0.20
-0.09
-0.17
-0.65
-0.17
-0.10
-0.10
-0.14
-0.10
-0.08
-0.07
0.16
-0.16
-0.16
-0.16
-0.16
-0.16
-0.16
-0.16
0.16
-0.16
-0.16
-0.16
0.16
0.16
-0.16
-0.16
0.16
-0.16
-0.16
-0.16
-0.16
0.07
-0.16
0.19
-0.17
-0.27
-0.27
-0.27
-0.27
-0.27
-0.27
-0.27
-0.09
-0.27
-0.27
-0.38
-0.13
-0.14
0.10
-0.25
-0.14
-0.17
-0.19
0.17
-0.26
-0.26
-0.16
-0.35
-0.69
-0.25
-0.14
0.17
-0.24
-0.19
-0.17
-0.12
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.32
-0.09
-0.32
-0.46
-0.40
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.11
-0.46
-0.46
-0.47
-0.67
-0.50
-0.19
-0.47
-0.31
-0.54
-0.46
-0.40
-0.37
-0.37
-0.22
-0.42
-0.74
-0.50
-0.31
-0.54
-0.38
-0.46
-0.40
-0.20
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.46
-0.11
-0.46
ST AT -WASTE
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
TOT-AVG
TOT-AVG
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-SIC
27
-------
APPENDIX C
Results of Statistical Analysis for Washington and Oregon
-------
SIC_P WASTE TONS LB_89 HB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
8211
8211
8211
8211
8211
8211
8211
8211
8211
8211
8220
8220
8220
8220
8220
8220
8220
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8221
8222
8222
8222
8222
8249
8249
8249
8321
8321
8911
8911
8911
8911
8911
8922
8922
8922
8922
8922
U201
U211
U219
U220
U239
W001
WL01
WL02
WP01
WT01
D001
U019
U122
U1S1
U211
U001
WL01
0001
D002
0003
0007
D008
F001
F002
F003
F005
F027
U048
U081
U188
W001
WC02
WL01
WL02
WP01
WT01
WT02
D001
F003
F005
WT02
D001
F002
F004
D001
U160
D001
0002
0008
U001
WT02
0001
0002
D003
0004
0005
0.00
0.01
0.00
0.00
0.00
3.70
0.17
0.52
0.02
0.69
0.50
0.02
0.02
0.00
0.02
1.05
0.04
7.20
4.03
0.11
0.15
1.72
0.00
0.96
3.09
3.08
0.02
0.30
0.27
0.27
1.18
1.62
10.01
0.39
0.94
0.00
0.87
0.41
0.92
0.47
0.41
1.65
0.11
0.11
0.92
0.92
2.06
3.50
0.79
0.02
4.29
88.69
223.58
1.21
0.58
1.19
-0.02
-0.02
-0.02
-0.02
-0.02
-0.05
-0.01
-0.02
-0.02
-0.05
-0.01
-0.10
-0.10
-0.10
-0.10
-0.05
-0.01
-0.02
-0.04
-0.02
-0.05
-0.01
-0.01
-0.01
-0.00
-0.00
-0.02
-0.02
-0.02
-0.01
-0.05
-0.04
-0.01
-0.01
-0.02
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.03
-0.01
-0.10
-0.01
-0.04
-0.01
-0.05
-0.01
-0.01
-0.04
-0.05
-0.01
-0.01
-0.04
-0.04
-0.04
-0.04
-0.04
-0.08
-0.03
-0.03
-0.04
-0.07
-0.05
-0.12
-0.12
-0.12
-0.12
-0.08
-0.03
-0.03
-0.08
-0.05
-0.06
-0.03
-0.09
0.03
-0.01
-0.00
-0.03
-0.03
-0.03
-0.02
-0.08
-0.05
-0.03
-0.01
0.04
-0.07
-0.01
-0.05
0.01
-0.02
-0.01
-0.05
-0.03
0.04
-0.05
0.12
0.05
-0.05
0.03
0.08
-0.01
-0.05
0.05
-0.07
-0.03
-0.02
-0.06
-0.06
-0.06
-0.06
-0.06
-0.12
-0.06
-0.07
-0.08
-0.09
-0.11
-0.15
-0.15
-0.15
-0.15
-0.12
-0.06
-0.07
-0.09
0.07
-0.10
-0.08
-0.18
-0.07
-0.04
-0.02
-0.06
-0.06
-0.06
-0.03
-0.12
-0.06
-0.06
-0.01
-0.08
-0.09
-0.03
0.11
-0.04
-0.03
-0.03
-0.11
-0.07
-0.06
-0.11
-0.15
-0.11
-0.07
-0.08
-0.12
-0.03
-0.11
-0.07
-0.08
-0.06
-0.08
-0.06
-0.06
-0.06
-0.06
-0.06
-0.31
-0.04
-0.05
-0.12
-0.05
-0.03
-0.14
-0.14
-0.14
-0.14
-0.31
-0.04
-0.05
0.13
-0.07
-0.06
-0.04
-0.06
-0.04
-0.01
-0.01
-0.05
-0.05
-0.05
-0.02
-0.31
-0.12
-0.04
-0.02
-0.12
-0.05
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.04
-0.08
-0.03
-0.14
-0.03
-0.12
-0.04
-0.31
-0.03
-0.03
-0.12
-0.16
-0.04
-0.03
-0.13
-0.13
-0.13
-0.13
-0.13
-0.39
-0.07
-0.10
0.17
-0.10
-0.14
-0.18
-0.18
-0.18
-0.18
-0.39
0.07
-0:10
-0.25
-0.14
-0.09
-0.08
-0.15
-0.09
0.02
0.01
-0.10
-0.10
0.10
-0.04
-0.39
0.16
0.07
-0.03
0.17
0.10
-0.05
-0.14
-0.06
-0.06
-0.05
-0.14
-0.09
-0.12
0.14
-0.18
-0.14
0.16
-0.08
-0.39
-0.05
-0.13
-0.16
-0.20
-0.08
-0.06
-0.18
-0.18
-0.18
-0.18
0.18
-0.47
-0.11
-0.22
-0.28
-0.15
-0.29
-0.24
-0.24
0.24
-0.24
-0.47
0.11
-0.21
-0.26
-0.22
-0.17
-0.22
-0.26
-0.21
0.13
-0.06
-0.18
-0.18
0.18
-0.06
-0.47
-0.20
-0.11
-0.04
-0.28
-0.15
-0.09
0.29
-0.14
-0.09
-0.09
-0.29
-0.21
0.16
-0.29
-0.24
-0.29
-0.20
-0.22
-0.47
-0.09
-0.29
-0.20
-0.24
-0.16
-0.25
-0.16
-0.16
-0.16
-0.16
-0.16
-0.67
-0.09
-0.13
-0.23
-0.10
-0.10
-0.20
-0.20
-0.20
-0.20
-0.67
-0.09
-0.13
-0.32
-0.18
-0.10
-0.10
-0.14
-0.10
-0.02
-0.01
-0.13
-0.13
0.13
-0.07
-0.67
-0.30
-0.09
-0.05
-0.23
-0.10
-0.06
-0.10
-0.08
-0.07
-0.06
-0.10
-0.10
-0.21
-0.10
-0.20
-0.10
-0.30
-0.10
-0.67
-0.06
-0.10
-0.30
-0.40
-0.11
-0.07
-0.32
-0.32
-0.32
-0.32
-0.32
-0.74
-0.16
-0.25
-0.30
-0.20
-0.25
-0.26
-0.26
-0.26
-0.26
-0.74
-0.16
-0.25
-0.64
0.37
-0.14
-0.17
-0.24
-0.19
-0.05
-0.03
-0.27
0.27
0.27
-0.09
-0.74
-0.40
-0.16
-0.07
-0.30
-0.20
-0.10
0.25
-0.17
-0.12
-0.10
-0.25
-0.19
-0.30
-0.25
-0.26
-0.25
-0.40
-0.17
-0.74
-0.10
-0.23
-0.40
-0.50
-0.21
-0.14
-0.46
-0.46
-0.46
-0.46
-0.46
-0.80
-0.22
-0.57
-0.53
-0.31
-0.47
-0.37
0.37
-0.37
-0.37
-0.80
-0.22
-0.55
-0.66
-0.56
-0.31
-0.54
-0.38
-0.46
-0.34
-0.15
0.47
0.47
0.47
-0.11
-0.80
-0.50
-0.22
-0.10
-0.53
-0.31
-0.19
-0.47
-0.40
-0.20
-0.19
-0.47
-0.46
-0.38
-0.47
-0.37
-0.47
-0.50
-0.54
-0.80
0.19
-0.49
-0.50
-0.60
-0.42
-0.65
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT -WASTE
STAT-A
STAT-SIC
STAT -WASTE
STAT -WASTE
STAT-WASTE
TOT-AVG
TOT-AVG
TOT-AVG
TOT-AVG
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT
STAT-SIC
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
TOT-AVG
STAT-WASTE
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-A
ENG-ANAL
ENG-ANAL
STAT-WASTE
STAT
28
-------
SIC_P WASTE TONS LB_89 HB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
0006
0007
0008
0009
0010
0011
F001
F002
F003
F004
FOOS
F027
P003
P010
P011
P012
P016
P022
P030
P064
P098
P102
P10S
P106
P107
P1 19
P120
U001
U002
U012
U019
U022
U031
U036
U044
U051
U052
U053
U055
U056
U057
U080
U091
U108
U117
U120
U122
U123
U133
U134
U151
U154
U159
U161
U162
U169
0.78
325.51
106.75
4.43
0.18
2.10
S.OO
1.40
6.38
0.33
7.04
0.18
0.00
0.00
o.oa
0.00
0.00
0.00
0.00
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.01
0.00
0.01
0.70
0.00
0.00
0.00
0.00
0.02
0.02
0.00
0.00
0.01
0.00
0.13
0.00
1.33
0.05
0.66
0.04
0.10
0.11
0.00
0.00
-0.01
-0.04
-0.01
-0.01
-0.02
-0.06
-0.01
-0.01
-0.01
-0.01
0.01
-0.01
-0.03
0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.01
-0.03
-0.03
0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.03
-0.01
-0.03
-0.03
-0.03
-0.03
-0.00
-0.03
-0.03
0.03
0.03
-0.03
-0.03
-0.03
0.03
-0.03
-0.03
-0.03
0.03
0.01
-0.03
-0.03
-0.02
-0.03
-0.03
-0.03
-0.03
-0.01
-0.06
-0.02
-0.03
-0.04
-0.12
-0.09
-0.02
-0.02
-0.02
-0.01
-0.01
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.02
-0.05
-0.05
0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.02
-0.05
-0.05
-0.05
-0.05
-0.01
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.01
-0.05
-0.05
-0.03
-0.05
-0.05
-0.05
-0.05
-0.10
-0.10
-0.09
-0.09
-0.08
-0.13
-0.18
-0.09
-0.07
-0.07
-0.08
-0.09
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.03
-0.08
-0.08
-0.08
-0.08
-0.08
0.08
-0.08
-0.08
-0.08
-0.04
-0.08
-0.08
-0.08
-0.08
-0.02
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.11
-0.08
-0.06
-0.09
-0.08
-0.08
-0.08
-0.08
-0.02
-0.05
-0.03
-0.05
0.06
-0.18
0.06
-0.02
-0.02
-0.03
-0.02
-0.02
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.03
-0.06
0.06
-0.06
-0.06
-0.06
0.06
-0.06
-0.06
0.06
-0.02
-0.06
-0.06
-0.06
-0.06
-0.01
-0.06
-0.06
0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.02
-0.06
-0.08
0.05
-0.06
-0.06
-0.06
-0.06
-0.03
-0.08
-0.06
-0.10
-0.13
-0.37
-0.15
-0.05
-0.05
-0.07
0.04
0.04
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.07
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.05
-0.10
-0.10
-0.10
-0.10
-0.03
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.04
-0.10
-0.16
-0.10
-0.10
-0.10
-0.10
-0.10
-0.29
-0.19
-0.25
0.28
-0.23
-0.38
-0.26
0.26
-0.21
-0.21
-0.24
-0.27
-0.19
-0.19
-0.19
-0.19
0.19
-0.19
-0.19
0.19
-0.09
-0.19
-0.19
-0.19
-0.19
-0.19
-0.19
-0.19
-0.19
0.19
-0.11
-0.19
-0.19
0.19
-0.19
-0.07
-0.19
0.19
-0.19
-0.19
-0.19
-0.19
-0.19
-0.19
-0.19
-0.19
-0.19
-0.19
-0.34
-0.19
-0.18
0.27
-0.19
-0.19
-0.19
-0.19
-0.04
-0.09
-0.08
-0.12
-0.16
-0.47
-0.14
-0.06
-0.06
-0.09
-0.05
-0.05
-0.15
0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.08
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.06
-0.15
-0.15
-0.15
-0.15
-0.03
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.15
-0.06
-0.15
-0.20
-0.13
-0.15
-0.15
-0.15
-0.15
-0.08
-0.13
-0.14
-0.25
-0.32
-0.95
-0.24
-0.12
-0.12
-0.18
-0.10
-0.11
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.17
-0.22
-0.22
-0.22
-0.22
-0.22
0.22
-0.22
-0.22
-0.22
-0.12
-0.22
-0.22
-0.22
-0.22
-0.07
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.11
-0.22
-0.40
-0.25
-0.22
-0.22
-0.22
-0.22
-0.73
-0.37
-0.61
-0.72
-0.59
-0.98
-0.39
-0.66
-0.55
-0.53
-0.60
-0.69
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.24
-0.42
-0.42
0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.27
-0.42
-0.42
-0.42
-0.42
-0.19
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.42
-0.86
-0.42
-0.47
-0.70
-0.42
-0.42
-0.42
-0.42
STAT
STAT
STAT -A
STAT -WASTE
STAT
STAT -A
STAT -A
STAT
STAT
STAT
STAT
STAT
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT -WASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT -WASTE
STAT-SIC
STAT
STAT
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
29
-------
SIC_P WASTE TONS LB_89 HB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09 SOUR
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922
8922,
8999
8999
8999
9111
9111
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
9199
U177
U188
U190
U196
U197
U210
U211
U216
U218
U220
U225
U226
U228
U238
U239
U240
W001
WC01
UC02
UL01
UL02
WP01
WP02
WP03
UT01
WT02
0001
K052
WT02
F002
F004
D001
0002
0007
0008
0009
0011
F001
F002
F003
F004
F005
K001
PI 08
U002
U012
U019
U037
U080
U154
U1S9
U220
U223
U240
U24Z
U001
0.01
0.00
0.00
0.01
0.00
0.32
0.14
0.00
0.00
0.04
0.01
0.10
0.12
0.00
0.02
0.00
0.17
10.28
336.11
5.13
3.45
39.68
2.60
0.87
483.06
361.58
36.36
28.66
18.06
0.01
0.01
11.69
0.51
0.14
0.40
0.00
0.00
3.97
0.11
1.11
3.45
1.27
0.28
0.00
0.22
0.09
0.15
0.02
0.91
0.07
0.63
0.92
0.13
0.07
0.28
684.46
-0.03
-0.01
-0.03
-0.01
-0.03
-0.01
-0.06
-0.03
-0.03
-0.03
-0.03
-0.00
-0.03
-0.03
-0.03
-0.03
-0.05
-0.10
-0.12
-0.10
-0.10
-0.02
-0.01
-0.01
-0.05
-0.01
-0.01
-0.10
-0.01
-0.01
-0.03
-0.01
-0.04
-0.00
-0.01
-0.02
-0.01
-0.00
-0.01
-0.01
-0.03
-0.02
-0.01
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.12
-0.05
-0.02
-0.05
-0.03
-0.05
-0.03
-0.12
-0.05
-0.05
-0.05
-0.05
-0.00
-0.05
-0.05
-0.05
-0.05
-0.08
-0.12
-0.13
-0.12
-0.12
-0.03
-0.01
-0.02
-0.06
-0.01
-0.05
-0.12
-0.01
-0.03
-0.04
-0.01
-0.05
-0.01
-0.02
-0.03
-0.02
-0.01
-0.03
-0.01
-0.04
-0.04
-0.02
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.13
-0.08
-0.03
-0.08
-0.04
-0.08
-0.08
-0.12
-0.08
-0.08
-0.08
-0.08
-0.05
-0.08
-0.08
-0.08
-0.08
-0.12
-0.15
-0.16
0.15
-0.15
-0.09
-0.08
-0.05
-0.09
-0.05
-0.11
-0.15
-0.03
-0.07
-0.06
-0.06
-0.07
-0.06
-0.04
-0.09
-0.05
-0.04
-0.07
-0.04
-0.06
-0.07
-0.03
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.06
-0.16
-0.06
-0.02
-0.06
-0.04
-0.06
-0.04
-0.17
-0.06
-0.06
-0.06
-0.06
-0.01
-0.06
-0.06
-0.06
-0.06
-0.31
-0.14
-0.14
-0.14
-0.14
-0.10
-0.02
-0.03
-0.05
-0.02
-0.03
-0.14
-0.03
-0.04
-0.08
-0.02
-0.12
-0.01
-0.02
-0.05
-0.03
-0.01
-0.04
-0.03
-0.08
-0.07
-0.02
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.12
-0.14
-0.10
-0.04
-0.10
-0.08
-0.10
-0.09
-0.35
-0.10
-0.10
-0.10
-0.10
-0.02
-0.10
0.10
-0.10
-0.10
-0.39
-0.18
-0.18
-0.18
-0.18
-0.14
-0.04
-0.07
-0.09
-0.04
-0.14
-0.18
-0.05
-0.09
-0.12
-0.04
-0.16
-0.02
-0.05
-0.10
-0.05
-0.03
-0.09
-0.06
-0.12
-0.13
-0.05
-0.16
-0.16
-0.16
-0.16
-0.16
-0.16
-0.16
-0.16
-0.16
-0.16
-0.16
-0.16
-0.18
-0.19
-0.06
-0.19
-0.11
-0.19
0.25
-0.35
-0.19
-0.19
-0.19
0.19
-0.17
-0.19
-0.19
-0.19
-0.19
-0.47
-0.24
-0.23
-0.24
-0.24
-0.29
-0.25
-0.14
0.17
-0.14
-0.29
-0.24
-0.09
-0.21
-0.16
-0.18
-0.20
-0.17
-0.12
0.28
-0.14
0.11
-0.21
-0.14
-0.16
-0.21
-0.09
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.20
-0.23
-0.15
-0.07
-0.15
-0.10
-0.15
-0.11
-0.44
0.15
-0.15
-0.15
-0.15
-0.03
-0.15
-0.15
-0.15
-0.15
-0.67
-0.20
-0.19
-0.20
-0.20
-0.19
-0.05
-0.09
-0.09
-0.05
0.10
0.20
0.06
-0.10
-0.21
-0.06
-0.30
-0.03
-0.06
-0.12
-0.07
-0.04
-0.10
-0.08
0.21
-0.17
-0.06
-0.29
-0.29
-0.29
-0.29
-0.29
-0.29
-0.29
-0.29
-0.29
-0.29
-0.29
-0.29
-0.19
-0.22
-0.09
0.22
-0.19
0.22
-0.23
-0.89
0.22
-0.22
-0.22
-0.22
0.04
-0.22
-0.22
-0.22
-0.22
-0.74
-0.26
-0.25
0.26
-0.26
0.26
0.10
0.18
-0.18
-0.08
-0.25
-0.26
0.10
-0.19
-0.30
0.11
-0.40
-0.05
0.12
-0.25
-0.11
-0.08
-0.19
-0.17
-0.30
0.34
-0.12
-0.39
-0.39
0.39
-0.39
0.39
-0.39
-0.39
-0.39
-0.39
-0.39
0.39
-0.39
-0.25
-0.42
-0.11
-0.42
-0.27
0.42
-0.64
-0.89
-0.42
-0.42
-0.42
-0.42
-0.44
-0.42
-0.42
-0.42
-0.42
-0.80
-0.37
-0.36
-0.37
-0.37
-0.60
-0.65
0.37
-0.35
-0.32
-0.47
-0.37
-0.19
-0.46
-0.38
0.45
-0.50
-0.42
-0.31
-0.72
-0.33
-0.27
-0.46
-0.40
-0.38
-0.52
-0.24
-0.50
-0.50
-0.50
-0.50
-0.50
-0.50
-0.50
-0.50
-0.50
-0.50
-0.50
-0.50
-0.36
STAT-SIC
STAT-UASTE
STAT-SIC
STAT
STAT-SIC
STAT
STAT
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-UASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT -WASTE
TOT-AVG
STAT -A
TOT-AVG
TOT-AVG
STAT-WASTE
STAT
STAT
STAT-A
STAT -A
STAT-WASTE
TOT-AVG
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
ENG-ANAL
STAT
STAT
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-A
30
-------
SIC_P WASTE TONS LB_89 MB_89 HB_89 LB_95 HB_95 HB_95 LB_09 MB_09 HB_09 SOUR
9199
9199
9199
9199
9223
9223
9223
9223
9223
9223
9223
9223
9233
9451
9451
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9511
9512
9512
9512
9512
9512
9512
9621
9621
9621
9621
9621
9621
9621
9621
9621
9621
9621
9621
9621
9621
9621
WL02
UP01
WT01
WT02
0001
0002
F001
F002
U080
U240
WT01
WT02
U001
0001
U220
0001
0002
0003
0008
0016
0017
F002
F003
F005
F027
P030
U044
U144
WC01
UC02
UP01
UP02
WP03
UT01
UT02
0001
0008
F002
W001
WC02
WT02
0001
0002
0006
0007
0008
0009
0010
F001
F002
F003
FOOS
U226
UP01
UT01
WT02
0.01
0.28
0.48
6.10
0.80
0.08
0.78
0.19
0.10
0.11
0.12
2.06
6.40
0.15
0.08
17.09
3.33
0.01
2.25
0.01
0.01
0.25
1.42
1.42
0.20
0.02
0.00
0.00
0.20
0.02
1.05
0.40
2.25
1.75
17.05
0.41
0.27
1.72
0.23
0.15
1.06
11.77
17.47
0.11
12.83
1.36
14.90
4.37
12.63
11.36
0.05
0.19
1.01
0.05
0.01
0.11
-0.01
-0.02
-0.02
-0.01
-0.01
-0.61
-0.01
-0.01
-0.01
-0.01
-0.05
-0.01
-0.05
-0.01
-0.10
-0.01
-0.04
-0.05
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.04
-0.04
-0.02
-0.04
-0.01
-0.05
-0.01
-0.01
-0.01
-0.01
-0.05
-0.04
-0.01
-0.01
-0.04
-0.09
-0.05
-0.01
-0.02
-0.01
-0.01
-0.01
-0.01
-0.02
-0.00
-0.02
-0.05
-0.01
-0.01
-0.04
-0.05
-0.01
-0.05
-0.63
-0.09
-0.03
-0.03
-0.03
-0.07
-0.03
-0.08
-0.05
-0.12
-0.05
-0.05
-0.07
-0.03
-0.05
-0.05
-0.03
-0.01
-0.02
-0.05
-0.05
-0.05
-0.05
-0.05
-0.05
-0.04
-0.08
-0.02
-0.07
-0.01
-0.05
-0.03
-0.03
-0.08
-0.05
-0.01
-0.05
-0.05
-0.12
-0.06
-0.03
-0.03
-0.01
-0.09
-0.02
-0.01
-0.03
-0.00
-0.04
-0.07
-0.01
-0.01
-0.08
-0.09
-0.05
0.11
-0.66
-0.18
-0.07
-0.06
-0.06
0.09
-0.06
0.12
-0.11
-0.15
-0.11
-0.07
-0.08
-0.08
0.11
0.11
-0.07
-0.04
-0.03
-0.11
0.11
-0.11
-0.11
-0.06
-0.06
-0.08
-0.11
-0.02
-0.09
-0.03
-0.11
-0.08
-0.07
-0.12
-0.06
-0.03
-0.11
-0.07
-0.17
-0.10
-0.08
-0.09
-0.03
-0.18
-0.08
-0.04
-0.04
-0.05
-0.08
-0.09
-0.03
-0.02
-0.12
-0.07
0.02
-0.03
-0.62
0.06
-0.04
-0.04
-0.04
0.05
-0.04
-0.31
-0.03
-0.14
-0.03
-0.12
-0.16
0.04
0.03
-0.03
0.04
0.03
-0.03
0.03
0.03
-0.03
-0.03
0.11
0.12
-0.12
-0.21
-0.02
-0.05
-0.03
-0.03
-0.04
-0.04
0.31
-0.12
0.03
0.03
-0.12
0.11
-0.06
-0.04
-0.05
-0.02
-0.06
-0.03
-0.03
-0.05
-0.01
-0.12
-0.05
-0.03
-0.03
-0.17
-0.15
-0.04
0.14
-0.65
-0.15
-0.09
-0.08
-0.08
-0.10
-0.08
-0.39
-0.14
-0.18
-0.13
-0.16
-0.20
0.08
0.13
-0.13
-0.09
0.06
-0.06
-0.13
-0.13
-0.13
-0.13
-0.15
-0.16
-0.17
-0.30
-0.04
-0.10
-0.05
-0.14
-0.08
-0.09
-0.39
-0.16
-0.05
-0.13
-0.16
-0.17
-0.09
-0.08
-0.10
-0.04
-0.15
-0.07
-0.06
-0.10
-0.02
-0.17
-0.10
-0.05
-0.04
-0.28
-0.28
-0.14
-0.29
-0.68
-0.26
-0.21
-0.18
-0.18
-0.15
-0.18
-0.47
-0.29
-0.24
-0.29
-0.20
-0.24
-0.22
-0.29
-0.29
-0.21
-0.14
-0.09
-0.29
0.29
0.29
-0.29
-0.19
-0.20
-0.28
-0.39
-0.06
-0.15
-0.09
-0.29
-0.22
-0.21
-0.47
-0.20
-0.09
-0.29
-0.20
-0.28
-0.17
-0.22
-0.28
-0.10
-0.26
-0.25
-0.14
-0.13
-0.17
-0.28
-0.15
-0.09
-0.05
-0.23
-0.19
-0.05
-0.10
-0.65
-0.14
-0.10
-0.11
0.11
-0.10
-0.11
-0.67
0.10
-0.20
-0.10
-0.30
-0.39
-0.10
-0.10
-0.10
-0.10
-0.08
-0.07
-0.10
-0.10
-0.10
-0.10
-0.29
-0.30
-0.23
-0.41
-0.05
-0.10
-0.06
-0.10
-0.10
-0.10
-0.67
-0.30
-0.06
-0.10
-0.30
0.17
-0.10
-0.10
0.12
-0.05
-0.14
-0.08
-0.08
-0.13
-0.03
-0.23
-0.10
-0.06
-0.07
-0.30
-0.38
-0.08
-0.25
-0.69
-0.24
-0.19
-0.21
0.21
-0.20
-0.21
0.74
-0.25
-0.26
-0.23
-0.40
-0.49
-0.17
-0.23
-0.23
-0.19
-0.17
-0.12
-0.23
-0.23
-0.23
-0.23
0.38
-0.40
-0.30
-0.57
-0.10
-0.20
-0.10
-0.25
-0.17
-0.19
-0.74
-0.40
-0.10
-0.23
-0.40
-0.25
-0.14
-0.17
-0.25
-0.10
-0.24
-0.14
-0.17
-0.26
-0.04
-0.30
-0.20
-0.10
-0.10
-0.53
-0.71
-0.32
-0.47
-0.74
-0.38
-0.46
-0.45
-0.45
-0.31
-0.45
-0.80
-0.47
-0.37
-0.49
-0.50
-0.59
-0.54
-0.49
-0.49
-0.46
-0.40
-0.20
-0.49
-0.49
-0.49
-0.49
-0.47
-0.50
-0.53
-0.72
-0.15
-0.31
-0.19
-0.47
-0.54
-0.46
-0.80
-0.50
-0.19
-0.49
-0.50
-0.50
-0.31
-0.54
-0.72
-0.26
-0.38
-0.57
-0.40
-0.34
-0.44
-0.53
-0.31
-0.19
ST AT -WASTE
STAT-WASTE
ST AT -WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
TOT-AVG
STAT
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
ENG-ANAL
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
31
-------
SIC_P WASTE TOMS LB_89 MB_89 HB_89 LB_95 HB_95 HB_95 LB_09 HB_09 HB_09 SOUR
9641
9641
9641
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9700
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
WL01
WP01
UT01
0001
0002
D003
D005
0006
0007
0008
0009
0010
F001
F002
F003
F004
FOOS
F006
F007
U158
U238
U001
WC01
WC02
VP01
VP03
UT01
WT02
0001
0002
0003
0004
DOOS
0006
0007
0008
0009
0010
0011
0013
F001
F002
F003
F004
FOOS
F006
F007
F027
P001
P030
P048
P098
PI 02
P106
PI 22
U051
0.10
0.03
0.06
34.40
12.26
249.92
6.77
25.72
279.39
12.52
0.35
3.30
1.54
257.99
2.71
0.27
5.29
5.92
0.42
0.40
0.05
0.52
0.42
0.10
5.14
0.04
175.12
341.06
240.40
449.38
104.66
4.11
23.07
359.49
725.96
886.80
15.31
0.08
16.95
0.01
33.21
95.69
0.81
89.95
7.77
25.75
0.18
0.03
0.00
0.20
0.00
0.03
0.07
0.00
0.01
0.19
-0.01
-0.02
-0.05
-0.03
-0.03
0.05
-0.00
-0.03
-0.04
-0.01
-0.02
-0.01
-0.00
-0.01
-0.01
-0.03
-0.02
-0.14
-0.07
-0.03
-0.03
-0.05
-0.04
-0.04
0.00
-0.01
0.05
-0.01
-0.02
-0.02
-0.05
-0.02
-0.00
-0.02
-0.01
-0.02
-0.02
-0.01
-0.00
0.01
-0.00
0.01
-0.01
-0.10
-0.01
-0.14
-0.07
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.00
-0.03
-0.04
0.07
-0.05
-0.06
-0.07
-0.01
0.06
0.06
0.01
-0.03
-0.01
-0.01
0.02
-0.01
0.04
-0.03
-0.16
0.10
-0.04
-0.04
-0.08
-0.05
-0.05
-0.01
-0.02
-0.06
-0.01
-0.03
-0.05
0.07
-0.03
-0.01
-0.05
-0.03
-0.04
-0.04
-0.01
-0.00
-0.02
-0.01
-0.02
-0.01
-0.12
-0.03
-0.16
-0.10
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.01
-0.06
-0.08
0.09
-0.09
-0.10
-0.08
0.10
-0.08
0.10
0.09
-0.09
-0.03
-0.03
0.08
0.10
-0.06
-0.07
-0.20
-0.13
-0.08
-0.08
-0.12
-0.06
-0.06
0.06
-0.02
-0.09
-0.05
0.11
-0.10
-0.08
-0.08
0.10
0.11
-0.12
-0.11
-0.09
0.03
0.05
0.07
-0.08
-0.08
-0.08
-0.15
-0.09
-0.20
-0.13
-0.07
-0.07
-0.07
-0.07
-0.07
-0.07
-0.07
-0.07
-0.02
-0.04
0.12
0.05
-0.08
-0.08
-0.16
-0.01
-0.09
0.05
0.02
-0.05
-0.02
-0.01
-0.03
0.02
-0.08
-0.05
0.19
0.22
-0.06
0.06
-0.31
-0.11
-0.12
0.01
0.02
-0.05
-0.02
0.05
0.07
0.16
-0.05
-0.01
-0.07
-0.04
-0.06
-0.05
-0.02
-0.00
-0.04
-0.01
-0.03
-0.02
-0.14
-0.04
-0.19
-0.22
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.01
-0.07
-0.17
0.10
-0.16
-0.17
-0.20
0.02
-0.18
0.08
-0.04
0.10
-0.04
-0.03
-0.07
0.04
-0.12
-0.10
-0.23
-0.26
-0.09
-0.09
-0.39
-0.15
-0.16
0.02
0.04
-0.09
-0.04
-0.10
0.15
0.20
-0.10
-0.02
-0.15
-0.08
-0.11
-0.11
-0.04
-0.01
-0.08
-0.02
-0.07
-0.03
-0.18
-0.09
-0.23
-0.26
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.03
-0.11
-0.28
-0.15
-0.27
-0.29
-0.24
-0.30
-0.25
0.19
0.27
0.28
-0.10
-0.08
-0.25
0.30
-0.16
-0.20
-0.31
-0.30
-0.20
-0.20
-0.47
-0.19
-0.20
0.19
-0.06
0.17
0.14
-0.33
0.29
0.24
-0.23
-0.30
-0.33
-0.35
-0.34
-0.26
-0.10
-0.16
-0.22
-0.23
-0.25
-0.25
-0.24
-0.28
-0.31
-0.30
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.07
-0.09
-0.23
-0.10
-0.20
-0.21
-0.40
-0.03
-0.23
-0.09
-0.06
0.12
-0.05
-0.04
-0.08
-0.05
-0.21
-0.12
-0.21
-0.48
-0.14
-0.14
-0.67
-0.29
-0.30
-0.02
-0.05
-0.09
-0.05
-0.12
-0.19
-0.40
-0.12
-0.02
-0.19
-0.10
-0.14
-0.14
-0.05
-0.01
-0.10
-0.02
-0.08
-0.04
-0.20
-0.11
-0.21
-0.48
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.03
-0.16
-0.30
-0.20
-0.41
-0.42
-0.50
-0.05
-0.45
-0.13
-0.11
-0.25
-0.10
-0.08
-0.14
0.11
-0.30
-0.24
-0.26
-0.53
-0.21
-0.21
-0.74
-0.38
-0.40
-0.05
-0.10
-0.18
-0.08
-0.24
0.37
-0.50
-0.24
-0.05
-0.38
-0.20
-0.29
-0.27
-0.10
-0.03
-0.18
-0.04
-0.14
-0.08
-0.26
-0.22
-0.26
-0.53
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.07
-0.22
-0.53
-0.31
-0.70
-0.73
-0.60
-0.76
-0.64
-0.37
-0.70
-0.72
-0.26
-0.20
-0.57
0.76
-0.38
-0.50
-0.41
-0.58
-0.46
-0.46
0.80
-0.47
-0.50
-0.48
-0.15
-0.35
0.32
-0.85
0.74
-0.60
-0.59
-0.76
-0.84
-0.89
-0.86
-0.67
-0.26
-0.41
-0.55
-0.60
-0.57
-0.64
-0.37
-0.72
-0.41
-0.58
-0.55
-0.55
-0.55
-0.55
-0.55
-0.55
-0.55
-0.55
-0.19
ST AT -WASTE
ST AT -WASTE
STAT-WASTE
STAT
STAT
ENG-ANAL
STAT-WASTE
STAT
STAT-WASTE
STAT
STAT-WASTE
STAT-WASTE
STAT
STAT-A
STAT
STAT-WASTE
STAT
STAT -WASTE
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT
STAT-WASTE
STAT-A
STAT-A
STAT
STAT
ENG-ANAL
STAT
STAT-WASTE
STAT
STAT
STAT
STAT
STAT-WASTE
STAT
STAT-SIC
STAT
STAT
STAT
TOT-AVG
STAT
STAT-WASTE
STAT-WASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-WASTE
32
-------
SIC P WASTE
TONS
LB_89 MB_89 HB_89 LB_95 HB_95 HB_95 LB_09 MB_09 HB_09 SOUR
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9711
9999
9999
9999
9999
9999
9999
9999
9999
9999
9999
U061
U075
U080
U121
U122
U129
U133
U134
U151
U158
U160
U179
U188
U210
U219
U220
U223
U226
U228
U239
U240
W001
WC01
WC02
WL01
UP01
UP02
WP03
WT01
WT02
D001
0005
0006
D007
0008
F003
F005
U001
WT01
WT02
0.01
0.13
0.24
0.22
0.07
0.01
0.08
0.00
0.02
0.00
0.01
0.00
0.00
0.02
2.74
0.00
0.00
0.95
0.02
0.67
0.01
6.96
17.13
1.24
0.44
41.94
91.35
0.19
49.38
3608.0
3.84
0.03
0.03
0.03
0.13
0.03
0.04
0.90
0.24
0.04
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.01
-0.00
-0.01
-0.01
-0.01
-0.01
-0.10
-0.02
-0.01
-0.02
-0.04
-0.02
-0.05
-0.01
-0.01
-0.00
-0.09
-0.05
-0.01
-0.01
-0.01
-0.05
-0.05
-0.01
-0.02
-0.02
-0.02
-0.02
-0.02
-0.02
-0.01
-0.02
0.02
-0.02
-0.02
0.02
-0.02
0.02
0.02
-0.02
-0.02
-0.00
-0.02
-0.02
-0.02
-0.01
-0.12
-0.05
-0.03
-0.03
-0.07
-0.05
-0.06
-0.01
-0.05
-0.01
-0.12
-0.06
-0.02
-0.01
-0.02
-0.08
-0.07
-0.01
-0.07
-0.07
-0.07
-0.07
-0.07
-0.07
-0.11
-0.07
-0.07
-0.07
-0.07
-0.07
-0.03
-0.07
-0.07
-0.07
-0.07
-0.07
-0.07
-0.07
-0.07
-0.06
-0.15
-0.06
-0.06
-0.09
-0.10
-0.06
-0.09
-0.05
-0.11
-0.10
-0.17
-0.10
-0.03
-0.04
-0.03
-0.12
-0.09
-0.03
-0.04
-0.04
-0.04
-0.04
-0.04
-0.04
-0.02
-0.04
-0.04
-0.04
-0.04
-0.04
-0.02
-0.04
-0.04
-0.04
-0.04
-0.00
-0.04
-0.04
-0.04
-0.02
-0.14
-0.07
-0.04
-0.10
-0.11
-0.07
-0.05
-0.02
-0.03
-0.01
-0.11
-0.06
-0.03
-0.03
-0.03
-0.31
-0.05
-0.03
-0.08
-0.08
-0.08
-0.08
-0.08
-0.08
-0.04
-0.08
-0.08
-0.08
-0.08
-0.08
-0.04
-0.08
-0.08
-0.08
-0.08
-0.00
-0.08
0.08
-0.08
-0.04
-0.18
-0.14
-0.07
-0.14
-0.21
-0.14
-0.09
-0.04
-0.14
-0.02
-0.17
-0.09
-0.05
-0.06
-0.06
-0.39
-0.10
-0.05
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.34
-0.22
-0.22
-0.22
-0.22
-0.22
-0.06
-0.22
0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.22
-0.19
-0.24
-0.17
-0.11
-0.29
-0.30
-0.18
-0.17
-0.14
-0.29
-0.30
-0.28
-0.17
-0.08
-0.14
-0.09
-0.47
-0.15
-0.09
-0.10
-0.10
-0.10
-0.10
-0.10
-0.10
-0.06
-0.10
0.10
-0.10
-0.10
-0.10
-0.07
-0.10
-0.10
-0.10
-0.10
-0.00
-0.10
0.10
-0.10
-0.05
-0.20
-0.18
-0.09
-0.19
-0.27
-0.18
-0.09
0.05
-0.10
-0.03
-0.17
-0.10
-0.07
-0.08
-0.07
-0.67
-0.10
-0.06
-0.18
-0.18
-0.18
-0.18
-0.18
-0.18
-0.11
-0.18
-0.18
-0.18
-0.18
-0.18
-0.09
-0.18
-0.18
0.18
-0.18
-0.00
-0.18
-0.18
-0.18
-0.10
-0.26
-0.37
-0.16
-0.26
-0.54
-0.35
-0.18
-0.08
-0.25
-0.05
-0.25
-0.14
-0.13
-0.17
-0.12
-0.74
-0.20
-0.10
0.55
0.55
-0.55
-0.55
-0.55
0.55
-0.86
-0.55
-0.55
-0.55
0.55
0.55
0.11
-0.55
-0.55
-0.55
-0.55
-0.57
-0.55
-0.55
-0.55
-0.48
-0.37
-0.43
-0.22
-0.60
0.77
-0.46
-0.35
0.32
0.47
-0.76
-0.50
-0.31
-0.21
-0.40
-0.20
-0.80
-0.31
-0.19
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-UASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT-UASTE
STAT-SIC
STAT-SIC
STAT-SIC
STAT-SIC
STAT
STAT-SIC
STAT-SIC
STAT-SIC
STAT
TOT-AVG
STAT
STAT -WASTE
STAT
STAT
STAT
STAT-WASTE
STAT -A
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-UASTE
STAT
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-WASTE
STAT-UASTE
185161
33
-------
Key to Appendix C
SIC_P - SIC code
Waste - EPA-RCRA waste type
Tons - Amount of Waste Generated in Washington in 1986 that formed the basis of the analysis
LB_89 - Low waste reduction scenario (net change in 1989 from base year)
M8_89 - Median waste reduction scenario (net change in 1989 from base year)
HB_89 - High waste reduction scenario (net change in 1989 from base year)
LB_95 - Low waste reduction scenario (net change in 1995 from base year)
MB_95 - Medium waste reduction scenario (net change in 1995 from base year)
HB_95 - High waste reduction scenario (net change in 1995 from base year)
LB_09 - Low waste reduction scenario (net change in 2009 from base year)
MB_09 - Medium waste reduction scenario (net change in 2009 from base year)
HB_09 - High waste reduction scenario (net change in 2009 from base year)
Sour is the source of the waste reduction factors.
GROUND - Direct results from groundtruthing conferences
GT-SIC - The Average of all SIC codes for industries involved in the groundtruthing conferences
GT-UASTE - The Average of all Waste codes for industries involved in the groundtruthing conferences
STAT - Direct results from the Statistical Analysis
STAT-A - Modified Results from the statistical analysis because of unrealistic results
STAT-SIC- Average of all SIC codes from statistical analysis
STAT-WASTE - Average of all waste codes from statistical analysis
ENG-ANAL - The engineering analysis
TOT-AVG - Average across entire state - used because of absence of data
34
-------
SIC P
WASTE
Washington
Summary of Waste Reduction Coefficients
LB 89 MB 89 HB 89 LB 95 HB 95 H8 95 LB 09 MB 09
KB 09
0726
1542
1542
1721
1721
1721
2434
2491
2491
2611
2621
2641
2651
2800
2812
2851
2851
2851
2851
2851
2851
2851
2869
2869
2869
2869
2869
2869
2869
2911
2911
3079
3079
3079
3079
3325
3334
3334
3334
3334
3334
3411
3411
3411
3471
3471
D001
D001
F003
D001
F003
F005
D001
D004
K001
D001
D001
D001
D001
F005
D002
0001
D002
D007
0008
F001
F003
F005
D001
D002
D007
D008
F002
F003
F005
D001
K051
0001
F002
F003
F005
D001
0001
F002
F003
F005
U226
0001
F001
F005
0001
0002
-.009
-.010
-.005
-.003
-.014
-.012
-.001
-.006
-.007
-.016
-.012
-.021
-.017
-.002
-.017
-.001
-.006
-.024
-.010
-.001
-.008
-.009
-.014
-.001
-.024
-.020
-.012
-.010
-.028
-.015
-.016
-.004
-.006
-.010
-.030
-.006
-.039
-.001
-.008
-.008
-.001
-.004
-.009
-.019
-.003
-.017
-.019
-.020
-.010
-.006
-.029
-.023
-.002
-.011
-.013
-.032
-.025
-.042
-.034
-.005
-.034
-.001
-.012
-.047
-.021
-.003
-.015
-.018
-.027
-.001
-.047
-.040
-.023
-.019
-.055
-.029
-.032
-.008
-.012
-.021
-.061
-.013
-.077
-.002
-.015
-.016
-.002
-.007
-.018
-.037
-.005
-.035
-.024
-.071
-.036
-.453
-.057
-.098
-.040
-.011
-.044
-.035
-.032
-.068
-.046
-.007
-.053
-.125
-.099
-.067
-.092
-.117
-.092
-.046
-.067
-.123
-.072
-.055
-.034
-.043
-.063
-.039
-.034
-.607
-.090
-.060
-.067
-.066
-.085
-.044
-.046
-.048
-.003
-.092
-.025
-.071
-.402
-.050
-.028
-.029
-.015
-.009
-.043
-.035
-.003
-.017
-.020
-.048
-.037
-.064
-.051
-.007
-.051
-.002
-.018
-.071
-.031
-.004
-.023
-.027
-.041
-.002
-.071
-.059
-.035
-.029
-.083
-.044
-.047
-.012
-.019
-.031
-.091
-.019
-.116
-.003
-.023
-.024
-.003
-.011
-.027
-.056
-.008
-.052
-.056
-.059
-.031
-.018
-.086
-.070
-.005
-.033
-.040
-.096
-.074
-.127
-.101
-.014
-.103
-.004
-.036
-.142
-.062
-.008
-.046
-.055
-.082
-.004
-.141
-.119
-.070
-.058
-.166
-.087
-.095
-.023
-.037
-.062
-.182
-.039
-.231
-.006
-.046
-.048
-.007
-.021
-.054
-.111
-.016
-.104
-.073
-.213
-.108
-.477
-.170
-.190
-.120
-.034
-.133
-.104
-.096
-.204
-.139
-.021
-.160
-.374
-.298
-.201
-.277
-.352
-.277
-.139
-.201
-.369
-.215
-.165
-.101
-.130
-.189
-.117
-.103
-.668
-.270
-.181
-.201
-.197
-.255
-.133
-.137
-.144
-.009
-.276
-.076
-.212
-.500
-.150
-.071
-.075
-.039
-.023
-.110
-.090
-.007
-.043
-.051
-.123
-.094
-.163
-.129
-.018
-.132
-.005
-.046
-.181
-.079
-.010
-.059
-.070
-.105
-.005
-.181
-.152
-.089
-.074
-.213
-.111
-.121
-.030
-.048
-.080
-.233
-.050
-.295
-.008
-.059
-.062
-.008
-.027
-.069
-.142
-.020
-.132
-.143
-.150
-.079
-.045
-.220
-.179
-.014
-.085
-.101
-.247
-.188
-.326
-.259
-.036
-.263
-.010
-.092
-.362
-.158
-.021
-.119
-.140
-.210
-.010
-.361
-.304
-.179
-.148
-.425
-.223
-.242
-.060
-.096
-.159
-.466
-.100
-.591
-.016
-.118
-.123
-.017
-.054
-.137
-.285
-.040
-.265
-.186
-.543
-.277
-.534
-.435
-.406
-.306
-.087
-.340
-.267
-.246
-.522
-.356
-.053
-.410
-.957
-.763
-.513
-.707
-.899
-.707
-.355
-.514
-.942
-.550
-.422
-.257
-.332
-.482
-.298
-.264
-.813
-.691
-.463
-.513
-.503
-.653
-.340
-.350
-.367
-.022
-.706
-.194
-.541
-.730
-.383
-------
SIC_P WASTE LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 HB_09 HB_09
3471
3471
3471
3471
3471
3471
3479
3479
3479
3479
3479
3499
3499
3536
3536
3573
3573
3599
3599
3662
3662
3674
3674
3674
3674
3674
3679
3679
3679
3679
3679
3679
3700
3715
3715
3721
3721
3721
3721
3721
3721
3721
3721
3721
3721
3724
0006
0007
0008
F001
F005
F006
0001
0002
0007
F003
F005
0001
F003
0001
F005
0001
0002
0002
F005
0001
F001
0001
0002
F002
F003
F005
0001
0002
0007
0008
F002
F006
0001
0001
F005
0001
0002
0006
0007
0008
F001
F002
F003
F005
F007
0001
-.011
-.013
-.006
-.018
-.008
-.016
-.002
-.030
-.001
-.004
-.008
-.012
-.012
-.010
-.015
-.008
-.029
-.011
-.005
-.004
-.002
-.020
-.017
-.029
-.007
-.017
-.031
-.003
-.009
-.011
-.008
-.029
-.003
-.004
-.010
-.003
-.004
-.009
-.004
-.007
-.011
-.007
-.020
-.006
-.035
-.006
-.022
-.027
-.012
-.036
-.016
-.032
-.005
-.060
-.002
-.007
-.017
-.024
-.024
-.019
-.030
-.016
-.057
-.022
-.011
-.008
-.005
-.041
-.034
-.058
-.013
-.034
-.062
-.006
-.018
-.023
-.017
-.057
-.005
-.009
-.019
-.006
-.007
-.017
-.009
-.014
-.021
-.014
-.040
-.013
-.071
-.013
-.069
-.057
-.051
-.048
-.461
-.052
-.043
-.072
-.114
-.016
-.019
-.040
-.040
-.032
-.039
-.080
-.061
-.084
-.013
-.195
-.275
-.070
-.080
-.075
-.034
-.039
-.074
-.104
-.032
-.056
-.048
-.065
-.059
-.014
-.026
-.145
-.136
-.064
-.139
-.083
-.106
-.219
-.053
-.127
-.072
-.022
-.033
-.040
-.018
-.053
-.024
-.047
-.007
-.090
-.003
-.011
-.025
-.036
-.036
-.029
-.045
-.025
-.086
-.033
-.016
-.012
-.007
-.061
-.051
-.087
-.020
-.051
-.093
-.009
-.027
-.034
-.025
-.086
-.008
-.013
-.029
-.009
-.011
-.026
-.013
-.021
-.032
-.021
-.060
-.019
-.106
-.019
-.066
-.080
-.036
-.107
-.049
-.095
-.014
-.180
-.006
-.022
-.050
-.072
-.072
-.057
-.089
-.049
-.171
-.066
-.033
-.025
-.014
-.122
-.103
-.175
-.040
-.102
-.186
-.018
-.055
-.069
-.050
-.171
-.016
-.026
-.058
-.019
-.022
-.052
-.026
-.042
-.064
-.042
-.120
-.039
-.212
-.038
-.207
-.170
-.153
-.144
-.525
-.156
-.129
-.217
-.343
-.047
-.056
-.121
-.121
-.095
-.117
-.241
-.183
-.253
-.040
-.241
-.340
-.209
-.241
-.225
-.103
-.118
-.222
-.313
-.097
-.167
-.143
-.195
-.177
-.042
-.077
-.358
-.344
-.192
-.316
-.249
-.288
-.312
-.158
-.279
-.216
-.065
-.084
-.102
-.046
-.136
-.062
-.121
-.018
-.230
-.008
-.029
-.064
-.092
-.092
-.073
-.114
-.063
-.219
-.085
-.042
-.032
-.017
-.155
-.131
-.223
-.052
-.130
-.238
-.024
-.070
-.088
-.063
-.219
-.020
-.033
-.074
-.024
-.028
-.066
-.034
-.054
-.082
-.054
-.154
-.050
-.271
-.049
-.168
-.205
-.092
-.272
-.124
-.242
-.036
-.460
-.015
-.057
-.128
-.184
-.184
-.147
-.228
-.126
-.437
-.170
-.084
-.064
-.035
-.311
-.263
-.447
-.103
-.260
-.476
-.047
-.140
-.175
-.127
-.438
-.040
-.067
-.149
-.048
-.057
-.133
-.067
-.109
-.164
-.108
-.307
-.099
-.543
-.097
-.529
-.434
-.392
-.369
-.673
-.398
-.329
-.554
-.876
-.119
-.144
-.308
-.308
-.244
-.300
-.615
-.467
-.646
-.101
-.347
-.493
-.534
-.615
-.575
-.263
-.301
-.568
-.801
-.249
-.427
-.366
-.499
-.452
-.108
-.196
-.852
-.830
-.491
-.728
-.636
-.713
-.529
-.404
-.634
-.552
-.166
-------
SIC P WASTE LB 89 MB 89 KB 89 LB 95 MB 95 HB 95 LB 09 MB 09 H8 09
3724
3728
3728
3728
3728
3728
3731
3731
3731
3731
3731
3731
3731
3731
3732
3760
3760
3811
3811
3825
3825
3825
3825
3825
3841
3949
3949
3999
4231
4311
4582
4911
4911
5093
5093
5093
5093
5093
5093
5093
5093
5093
5171
5511
5511
5511
0002
0001
D002
F001
F003
F005
0001
0002
0004
D006
D007
0008
F003
F005
F003
D002
0008
0001
0002
0001
0002
0008
F001
F003
0001
0001
F005
0001
0001
0001
0001
0001
F005
0001
0002
0004
0006
0007
0008
0009
F001
K001
0001
0001
0002
F002
-.019
-.001
-.000
-.013
-.003
-.005
-.018
-.015
-.003
-.020
-.013
-.004
-.015
-.015
-.014
-.001
-.001
-.023
-.010
-.006
-.004
-.012
-.008
-.023
-.027
-.009
-.011
-.001
-.004
-.006
-.002
-.025
-.002
-.007
-.004
-.005
-.016
-.010
-.007
-.003
-.005
-.008
-.042
-.006
-.018
-.009
-.037
-.001
-.000
-.027
-.006
-.011
-.036
-.029
-.005
-.041
-.027
-.009
-.030
-.030
-.028
-.002
-.002
-.046
-.020
-.011
-.007
-.025
-.016
-.047
-.055
-.017
-.023
-.001
-.008
-.012
-.005
-.050
-.004
-.014
-.007
-.010
-.032
-.021
-.014
-.006
-.009
-.016
-.084
-.012
-.035
-.017
-.064
-.958
-.960
-.338
-.741
-.804
-.147
-.071
-.020
-.043
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-.013
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-.096
-.062
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-.964
-.971
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-.831
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-.155
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-.446
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-.232
-.699
-.394
-.831
-.817
-.445
-.610
-.537
-.724
-.370
-.208
-.180
-.789
-.514
-.389
-.453
-------
SIC_P UASTE LB_89 MB_89 HB_89 LB_95 HB_95 HB_95 LB_09 MB_09 HB_09
5511
5511
5511
5999
5999
5999
7216
7399
7399
7399
7531
7531
7531
7535
7538
7538
7539
7699
7699
7699
7699
7699
7699
7699
7699
7699
8062
8069
8221
8221
8221
8221
8221
8922
8922
8922
8922
8922
8922
8922
8922
9999
F003
F004
F005
D001
F002
F004
F002
0001
F002
F004
D001
F003
F005
D001
D001
F002
D008
D001
D002
D006
D007
D008
D009
F002
F003
F005
0001
0001
0001
0002
0003
F003
F005
0001
0002
0003
0007
0008
F002
F003
F005
0008
-.010
-.014
-.010
-.002
-.009
-.009
-.021
-.008
-.016
-.007
-.004
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-.009
-.003
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-.033
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-.006
-.006
-.002
-.007
-.002
-.015
-.003
-.015
-.007
-.008
-.010
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-.020
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-.003
-.004
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-.001
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-.172
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-.061
-.276
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-.092
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-.259
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-.371
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-.267
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-.364
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-.192
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-.083
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-.015
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-.069
-.163
-.061
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-.252
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-.046
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-.016
-.113
-.020
-.112
-.051
-.060
-.077
-.172
-.154
-.097
-.023
-.027
-.023
-.008
-.267
-.116
-.039
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-.069
-.036
-.067
-.147
-.216
-.152
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-.138
-.327
-.121
-.248
-.100
-.063
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-.135
-.043
-.217
-.505
-.098
-.088
-.092
-.037
-.104
-.033
-.226
-.039
-.224
-.103
-.120
-.154
-.345
-.307
-.195
-.046
-.054
-.046
-.016
-.535
-.231
-.078
-.147
-.138
-.071
-.135
-.439
-.473
-.462
-.032
-.157
-.157
-.696
-.264
-.311
-.145
-.572
-.384
-.392
-.236
-.346
-.662
-.126
-.828
-.438
-.803
-.793
-.865
-.719
-.949
-.429
-.139
-.587
-.204
-.684
-.437
-.292
-.343
-.176
-.930
-.912
-.582
-.313
-.393
-.490
-.429
-.555
-.212
-------
Oregon Waste Minimization Reduction Coefficents
June 13, 1989
REF- org.orgwm_5 Dsk Oregon 1 file orgwmfin.out
SIC UASTE LB_89 MB_89 HB_89 LB_95 MB_95 HB_95 LB_09 MB_09 HB_09
2431 0001 -.039 -.079 -.079 -.118 -.237 -.237 -.303 -.605 -.605
2436 0001 -.041 -.082 -.130 -.123 -.246 -.294 -.315 -.630 -.677
2491 0004 -.002 -.004 -.051 -.006 -.013 -.153 -.016 -.033 -.392
2491 K001 -.015 -.029 -.049 -.044 -.088 -.148 -.113 -.226 -.379
2851 F003 -.056 -.113 -.113 -.169 -.338 -.338 -.432 -.864 -.864
3324 F001 -.016 -.032 -.032 -.048 -.096 -.096 -.122 -.245 -.245
3469 F001 -.025 -.049 -.049 -.074 -.148 -.148 -.189 -.378 -.378
3471 F006 -.014 -.029 -.106 -.043 -.086 -.318 -.110 -.220 -.812
3600 D001 -.016 -.032 -.032 -.047 -.095 -.095 -.121 -.242 -.242
3600 F001 -.001 -.001 -.098 -.002 -.003 -.293 -.004 -.008 -.749
3679 0001 -.008 -.017 -.017 -.025 -.050 -.050 -.064 -.128 -.128
3679 0002 -.013 -.027 -.042 -.040 -.080 -.126 -.102 -.205 -.323
3679 F001 -.016 -.031 -.045 -.047 -.094 -.136 -.120 -.240 -.348
3679 F002 -.043 -.087 -.087 -.130 -.261 -.261 -.333 -.667 -.667
3679 F006 -.006 -.013 -.024 -.019 -.038 -.071 -.048 -.096 -.181
4210 0001 -.009 -.017 -.052 -.026 -.052 -.156 -.066 -.132 -.399
4231 0001 -.008 -.016 -.071 -.024 -.049 -.153 -.062 -.125 -.344
4231 0002 -.045 -.089 -.134 -.134 -.268 -.312 -.342 -.684 -.728
4231 F003 -.001 -.003 -.055 -.004 -.008 -.164 -.010 -.021 -.419
4712 0001 -.032 -.064 -.064 -.096 -.192 -.192 -.245 -.490 -.490
4911 0001 -.029 -.058 -.149 -.087 -.174 -.128 -.222 -.444 -.745
4911 0002 -.056 -.112 -.112 -.168 -.336 -.336 -.429 -.859 -.859
4911 F002 -.064 -.128 -.128 -.192 -.384 -.384 -.491 -.982 -.982
4950 F003 -.028 -.055 -.055 -.083 -.165 -.165 -.211 -.423 -.423
5010 0001 -.028 -.056 -.075 -.083 -.167 -.224 -.213 -.426 -.572
5080 0001 -.007 -.013 -.506 -.020 -.040 -.567 -.051 -.103 -.708
5510 0001 -.006 -.012 -.050 -.019 -.037 -.150 -.048 -.095 -.383
5511 0001 -.009 -.018 -.051 -.028 -.055 -.153 -.070 -.141 -.391
5990 0001 -.030 -.060 -.060 -.089 -.179 -.179 -.229 -.457 -.457
7530 0001 -.008 -.016 -.049 -.024 -.047 -.148 -.060 -.120 -.378
-------
APPENDIX D
Engineering Analysis Profiles
-------
OPPORTUNITIES FOR WASTE MINIMIZATION IN THE INDUSTRIAL
ORGANIC CHEMICALS, N.E.C. INDUSTRY (SIC 2869)
THETRICHLOROETHYLENE/PERCHLOROETHYLENE
MANUFACTURING PROCESS
DESCRIPTION OF THE PROCESS1
A variety of feedstocks and processes can be used to produce
trichloroethylene (TOE) and perchloroethylene (PCE). The process that will
be focused on here will be the coproduction of TCE and PCE from the
oxychlorination of EDO, or other C2-chlorinated hydrocarbons.
TCE and PCE are coproduced from the oxychlorination of EDO or
other C2-chlorinated hydrocarbons. The raw material ratios determine the
proportions of TCE and PCE that will be produced. Conversion of chlorinated
hydrocarbons to TCE and PCE was reported as 75-85 percent, with 10-15
percent chlorinated by-products, and 5-10 percent loss as CO and CO2.
Figure 1 represents the flow diagram for the production of TCE and PCE by
oxychlorinatrion. In this process, EDC, recycled chlorinated hydrocarbons,
chlorine, and oxygen are fed into a fluidized bed reactor. For this process,
C2-chlorinated hydrocarbon wastes from other processes can also be con-
sumed by introducing them into the organic recycle storage tank that feeds
the fluid bed reactor. The reactor operates at slightly above atmospheric
pressure and about 800° F. The most common catalyst used is CuCI2.
The reactor effluent gas, containing chlorinated organics, water, a
small amount of HCI, CO, CO2, and traces of other inert gases, is condensed
using water-cooled and refrigerated condensers. The condensed crude
product stream is drained through a decanter to remove entrained catalyst
fines. The non-condensed vent gas stream is sent through an HCI recovery
unit where the gas stream is water scrubbed to remove HCI as by-product.
The crude hydrocarbon stream is separated in the decanter. This
stream is then azeotropically distilled to remove water. Wastewater from the
azeotropic distillation is combined with the aqueous phase containing cata-
lyst fines from the decanter. The combined stream is sent to wastewater
treatment.
The crude chlorinated hydrocarbon mixture is further separated
intoTCE and PCE crude streams in a TCE/PCE column. The TCE crude is
I
-------
VENT IMS
oROAMcsnai
ono PROCESSES
PROCESS WSTECATESORB
0
0
0
0
0
HEAVY EWB
SOT CATALYSTS
SPEKT AUULK SOUmON
SPEKTORWiaiMTEIUU
WAITEWATEfl
Production ol TCE and PCE by Qxychfartuton
(U.S. EPA, Waste Minimization Issues and Potions Vol. 2:
Apnendicas A & B. EPA/S30-sw-86-042. Washington DC (1968))
-------
purified in a ICE column. Overhead from this distillation column is sent to an
organic recycle storage tank. The bottom stream is neutralized with dilute
caustic, ammonia or washed with water, and then dried to give the desired
TCE product. Wastes from the neutralization and drying operations are sent
to wastewater treatment or disposal.
The bottom stream from the TCE/PCE column is separated in a heavy-
ends column. The PCE-rich overhead stream from the heavy-ends column
is sent to the PCE column where final PCE purification takes place. The
overhead from the PCE column is recycled to the process and the purified
PCE is withdrawn as bottoms, then neutralized, washed and dried.
The bottom stream from the heavy-ends column is flashed to separate
the tars and carbon in the organic recycle system. The flash overhead stream
is recycled back to the process. The separated heavies, called "hex-waste,"
contain hexachlorobenzene, hexachlorobutachrene plus various chlorinated
C, compounds in addition to tars and carbon.
WASTE REDUCTION ALTERNATIVES
PROCESS MODIFICATIONS
The wastes produced from the production of TCE/PCE by oxychlori-
nation can be significantly reduced by adopting an alternative process. One
such alternative is a combination of direct chlorination and an HCI oxidation
unit. The product yields from this alternative process are approximately 95
percent compared to only 80 percent for oxychlorination. Thus, the use of this
alternative process would reduce the amount of waste byproducts formed.
Subsequent product purification operations, as well, would be simpler
because of the absence of water being formed as byproduct in an organic
environment in an oxychlorination step.2
Another process modification involves the use of an additional reac-
tion to break the heavy chlorinated hydrocarbon byproducts into lighter
products. This involves the use of hydrocracking which can be done using
catalytic hydrogenation processes. The light hydrocarbons generated from
this operation can then be combined with other light chlorinated organic
streams to be recycled to the reactor.3
Waste Reduction Potential4
Alternative Production Process: 15 percent to 25 percent reduction in
KO30 waste stream.
-------
Hydrocracking of Chlorinated Hydrocarbons: 12 percent to 25 percent
reduction in K030 waste stream.
Economics
N/A
Limitations/Constraints5
Alternative Production Process: One problem with the directchlorina-
tion process is the large amount of HCI that is formed as a byproduct.
Additionally, the subsequent use of an HCI oxidation unit is very costly
and, as of 1985, cannot compete with the conventional oxychlorina-
tion route.
Hydrocracking of Chlorinated Hydrocarbons: As of 1985, research
had shown that this method was technically infeasible due to severe
fouling of the catalyst. Further research is planned to explore the
effect of increasing H/feed ratio on reactor performance.
Applicability to Other Processes
The limited information available suggests that these techniques are
specific to this particular process.
PRODUCT/INPUT SUBSTITUTION
In metal degreasing operations, TCE can be replaced by other
solvents such as 1,1,1 -trichloroethane orchlorofluorocarbons (CFC). In dry-
cleaning applications, petroleum-based stoddard solvent is used as an
alternative to PCE. Chlorofluorocarbons.such as l.t^-trichloro-l^^-
trifluoroethane, which are both non-flammable and very low in toxicity, are
used widely mainly due to cost.6
Improvements in equipment and techniques that make emission
control more effective may contribute to an increased use of these solvents
to replace TCE or PCE in the future. In addition, changes in cleaning
techniques can be adopted to allow for the use of less powerful cleaning
substances in place of TCE and PCE. A combined ultrasonic-alkaline
cleaning step, for example, would greatly improve the ability of alkaline
cleaning solutions to remove oily residues, and would thus eliminate the need
for using organic solvent cleaners.7
-------
Waste Reduction Potential
Undetermined reduction in KO30 and D002 waste streams.
Economics
N/A
Limitations/Constraints8
-Since PCE is used as a raw material in the manufacture of
several CFC's, their substitution for TCE/PCE may have a
limited impact on TCE/PCE production.
-The dominant factor controlling the production demand for any
solvent (including TCE and PCE) is the extent of the recovery
and conservation effort by the users of the solvent.
Applicability to Other Processes
These techniques have applicability to reducing waste in industries
that make use of TCE and/or PCE, such as 3471,3674,3679,3721
and 3728. In addition, the general idea of substituting less- or non-
hazardous cleaning solutions for solvents might also be applicable to
the production of other solvents in this industry.
MATERIALS RECOVERY/RECYCLE
The recovery or recycling of waste products from TCE/PCE produc-
tion has shown promise in a couple of areas. The heavy endswaste stream
can be incinerated with recovery of both heat and HCI. The recovered
hydrochloric acid can either be sold or used to generate anhydrous HCI for
use in the oxychlorination process. Hazardous wastes are also produced
from the periodic disposal of spent catalyst, or from the loss of catalyst due
to entertainment. To reduce the waste load, high temperature ceramic fiber
or sintered metal can be used as filter elements to remove entrained catalyst
fines from the effluent gas. The catalyst can be partially recycled back to the
process or collected separately from other waste streams.9
Waste Reduction Potential10
Recovery from Heavy Ends: 50 percent to 75 percent reduction in
KO30 waste stream.
-------
REFERENCES
Catalyst Recovery: 20 percent reduction in D002 waste stream.
Economics
N/A
Limitations/Constraints11
Catalyst Recovery: There may be longer residence time of reactor
offgas in the stand-alone filter with the use of this technique as
opposed to currently used cyclones. This may increase the potential
for plugging.
Applicability to Other Processes
Incineration is a technique that can be applied to a number of waste
streams. Catalyst recovery might also have application to industry
2911 due to the use of catalyst in that industry.
Liepins, R., Mixon, F., Hudak, C., et al, Industrial Process Profiles for
Environmental Use: Chapter 9. "The Industrial Organic Chemicals Industry,
Research Triangle Institute," EPA-600-2-77-023f, U.S. EPA, Cincinnati, Ohio
(1977).
U.S. EPA, Waste Minimization Issues and Options Volume 2:Appendices A
&B. EPA/530-SW-86-042, Washington, DC (1986).
-------
ENDNOTES
'Information in this section is taken from, Liepins, R., Mixon, F., Hudak, C.,
et. al.f Industrial Process Profiles for Environmental Use: Chapter 9. The
Industrial Organic Chemicals Industry. Research Triangle Institute, EPA-
600-2-77-023f, U.S. Environmental Protection Agency, Cincinnati, Ohio
(1977).
^aste Minimization Issues and Options Volume 2: Appendices A & B. EPA/
530-SW-86-042, U.S. Environmental Protection Agency, Washington, DC
(1986).
3lbid.
"Ibid.
5lbid.
6lbid.
7lbid.
8lbid.
9lbid.
10lbid.
"Ibid.
-------
OPPORTUNITIES FOR WASTE MINIMIZATION IN THE
PETROLEUM REFINING INDUSTRY (SIC 2911)
LIGHT HYDROCARBON PROCESSING
DESCRIPTION OF THE PROCESS1
Refining oil involves a series of many processes. For the most part,
these processes are closed to the environment with the product outputs from
one process proceeding directly to the next process where additional refining
takes place. The total petroleum refining industry can be divided into five
major segments:
Crude Separation,
Light Hydrocarbon Processing,
Middle and Heavy Distillate Processing,
Residual Processing, and
Auxiliary Units.
The concern of this report is the industry segment dealing with light hydrocar-
bon processing.
In light hydrocarbon processing, outputs from the crude separation
processes go through additional hydrocarbon separation and molecular
rearrangement. The primary purpose of this major industry segment is to
upgrade the octane ratings of the napthas and light hydrocarbons. Most of
the improved products are used in gasoline blending. A flow diagram for this
segment of refinery processes is shown in Figure 1. There are six separate
unit processes that are performed in this area: Naptha Hydrodesulfurization
(HDS), Catalytic Reforming, Isomerization, Alkylation, Polymerization, and
Light Hydrocarbon Storage and Blending.
In the HDS process, sulfurand nitrogen are removed from the naptha
split that comes from the atmospheric distillation unit. Gaseous napthas are
mixed with a hydrogen-rich gas, heated and passed through a non-noble
metal catalyst. The hydrotreated naptha continues into isomerization or
reforming units.
In catalytic reforming, desulfurized naptha with a low octane under-
goes molecular rearrangement to become a high-octane gasoline blending
stock or to produce aromatics for petrochemical use. Multireactor, fixed-bed
8
-------
LIGHT HYDROCARBON PROCESSING
ude
ToallHydrodesuHurizatlon,
^ Hydrotreating, and Hydro-
cracking Processes
p-k Polymerization
Alkylation
Isomerizatlon
HDS
Light Hydrocarbon
Storage and Blending
Catalytic
Reforming
r
MIDDLE AND HEAVY DISTILLATE PROCESSING
General process Row diagram for the petroleum refining Industry.
(U.S. EPA, Office of Solid Waste Industrial Resource Recovery Practices:
Petroleum Refineries and Related Industries (SIC 29V Washington DC (1982))
-------
catalytic processes are used. This reaction which primarily uses a platinum-
rhenium catalyst produces more hydrogen than it consumes.
The isomerization process molecularly rearranges normal butane and
desulfurized light naptha fractions containing pentanes and hexanes by
utilizing a platinum-aluminum oxide catalyst to give their respective iso-
paraffins. The desired products are isobutane foralkylation and isopentane
and isohexane for gasoline blending. Hydrogen is added to the process to
hydrogenate unsaturated compounds to prevent polymerization of the light
hydrocarbons.
The alkylation process produces high octane gasoline components,
called alkalates, by reacting an isoparaffin such as isobutane and an olefin
such as propylene or butylene. The reaction takes place in the presence of
a sulfuric and/or hydrofluoric acid catalyst.
In the polymerization process, olefin gases such as propylene are
passed over a catalyst (i.e., phosphoric acid) yielding a higher molecular
weight polymer gasoline.
Finally, in light hydrocarbon storage and blending, all of the products
of light hydrocarbon processing are stored separately until they are blended
together along with tetraethyl lead and dye to produce a final gasoline
product.
WASTE REDUCTION ALTERNATIVES
MATERIALS RECOVERY/RECYCLE
There are a number of hazardous waste streams generated from light
hydrocarbon processing that can be recovered or recycled on-site. For
example, product tank bottoms contain sludge with high oil content. This oil
can be recovered from the sludge using a solvent extraction process. This
process, called a phase separation system, combines several conventional
processes, including centrifugation, drying, decantation, steam stripping,
and distillation. The phase separation system yields recovered oil, reusable
wastewater, and dried solids for landfill disposal. The solvent used in the
process is recovered and reused many times. The selected solvent for this
process is acetone; however, others have been mentioned as applicable,
such as ethyl and methyl alcohol, ethyl acetate, methyl ethyl ketone, and
triethyl amine.2
Refineries that have a coker can benefit from the petroleum coke
-------
exemption under 40 CFR 261.6(a)(3)(ix). This exemption allows for refinery
hazardous wastes that contain oil to be used as feedstock to a coker.3
Various acids, such as napthenic acid, are commonly found in the
spent caustics from the caustic treating of crude. A recovery process based
upon continuous acidification followed bysimultaneous centrifugal separa-
tion and washing can be used to recover the acids from spent caustic. Spent
caustic is heated to 170° F and contacted with sulfuric acid in a special alloy
mixer. Acidification occurs rapidly producing a dark emulsion which is
continuously fed to a centrifugal extractor. The centrifugal force separates
the salt liquor (caustic/sulfuric acid mixture) and the sprung napthenic acids.
Although the napthenic acids are recovered on-site, these products are not
used on-site. They are generally sold to various industries for use in many
products including paint driers, wood preservatives, and mildew inhibitors.4
Waste Reduction Potential5
Oil Recovery: 80 percent reduction in D001 waste stream.
Oily Wastes as Feedstock for Coker: 100 percent reduction in D001
waste stream.
Recovery of Napthenic Acid from Spent Caustic: 9-17 percent recov-
ery of D002 waste stream.
Economics6
Oil Recovery: (*)
Costs (1976$)
Capital: $1,512,000
Annual O&M: $ 232,000
PAYBACK PERIOD 6.9 yrs.
Recovery of Napthenic Acid from Spent Caustic: (**)
Costs M967S1
Capital: $100,000
Annual O&M: $ 58,200
PAYBACK PERIOD 3 mo. (approximately)
-------
OThese numbers are representative of a plant designed to handle up to
6820 Ibs/hr. of waste.
(**)These numbers are representative of a plant designed for continuous re-
covery of crude napthenic acid from the processing of 100,000 pounds of
spent caustic per day, operating for 300 days per year.
Limitations/Constraints7
Oil Recovery:
The preferred solvent should be completely soluble in oil and
water at ambient temperatures in order to save energy that
would otherwise be required in order to maintain a lower or
highertemperature. It must also have a lower boil ing point than
water and oil and it must not be reactive with either water or oil.
Pollution control equipment will be needed in order to make
use of this technique.
Further research is needed on the feasibility of using this
technique in this situation.
Storage of the solvent poses a potential hazard and precau-
tions should be taken for safety reasons.
Oily Wastes as Feedstock to Coker:
This technique can be used as long as the wastes are
generated at the same facility at which the coker is located and
the resulting coke does not exhibit a hazardous characteristic.
Recovery of Napthenic Acid from Spent Caustic:
Recovery of the napthenic acids will be feasible as long as the
relative concentrations of the napthenic acids to cresylic acids
in the spent caustic is high enough.
Applicability to Other Processes
This oil recovery process could prove useful for recovering wastewa-
12
-------
ters containing oil that are produced in other industries. Industries
such as 3721 and 3728, where metalworking fluids containing oil are
often used, might benefit from this technology.
Off-Site Recycle
The technique of off-site recovery or recycling for some of the
hazardous waste streams produced in light hydrocarbonprocessing is
also promising. First, substantial quantities of spent caustic are
generated in the naptha hydrodesulfurization (HDS) process, but a
technique to recover this spent caustic has been utilized by an inde-
pendent waste processing company. This recovery technique con-
sists of four filtration stages and chemical processing. The recovered
caustic can be reused in the HDS process or in scrubbing hydrogen
sulfide from oil-fired steam generators used in enhanced oil recovery.8
Second, large quantities of spent sulfuric acid sludge is generated
from the alkylation units used to produce higher octane products.
Several large spent acid processors exist in the U.S. Similar process-
ing is common for all facilities that recover fresh sulfuric acid from
sludge that is typically contaminated by water (about 3 percent) and
hydrocarbons (about 10 percent). In the process, acid sludge is
burned at 2,000 to 2,300° F depending on the hydrocarbon content of
the sludge. This recovery process is essentially a variation of H2SO4
production from molten sulfur.9
Third, cresylic acid and sodium hydrosulfide from spent caustic has
been recovered by independent waste processing facilities. The
process uses standard industrial technology to recover materials from
spent caustic. The process begins with purification. Mercaptans are
converted to disulfides by air oxidation and the disulfides gravity
separate along with hydrocarbons. These selected sulfurcompounds
and hydrocarbons are sold back to the refineries and can also be
considered as recycled products. The purified caustic is neutralized
with hydrogen sulfide (a refinery waste product) which causes the
organic cresylate (phenolic compounds) layer to phase separate and
float to the surface. The cresylic acid layer is purified and separated
in a fractionation unit into its components: phenol, cresol, xylenols,
and alklated phenols for sale as raw materials to chemical and plastic
manufacturers. The aqueous bottom layer produced by the hydrogen
sulfide neutralization step is a dilute solution of sodium hydrosulfide.
This by-product is solvent extracted and concentrated in an evapora-
tor before it is sold to the paper industry.10
-------
Fourth, spent catalyst, and in particular cat poly catalyst, which is used
in a refinery's catalytic polymerization unit, is a high volume waste that
shows promise as an effective substitute for other commercially
available chemicals. FCC equilibrium catalyst also exhibits possibili-
ties as an effective alumina source and admixture in the cement
manufacturing industry."
Waste Reduction Potential12
Recovery of Spent Caustic: 99 percent reduction in D002 waste
stream.
Recovery of Sulfuric Acid: overall efficiency of the process from spent
acid to new acid is approximately 94 percent.
Recovery of Cresylic Acid and Sodium Hydrosulfide: 10-32 percent
reduction in D002 waste stream.
Reuse of Spent Catalyst: 100 percent reduction in D002 waste
stream.
Economics13
Recovery of Spent Caustic: it is estimated that oil companies can save
about 20-30 percent in costs by recycling caustic rat her than dumping
it, as well as having the caustic available for reuse.
Recovery of Sulfuric Acid:Capital costs of $5 million (1960$) for a 715
ton/day facility.
Limitations/Constraints14
Recovery of Spent Caustic:
The availability of this technique is limited.
Recovery of Cresylic Acid and Sodium Hydrosulfide:
Pollution control equipment will be needed in order to make
use of this technology.
The availability of this technique is limited.
-------
Applicability to Other Processes
Not much information is available, but it would seem possible to apply
these same techniques to the recovery of other waste chemicals that
are produced in numerous industrial processes.
REFERENCES
Dickerman, J. C., Raye, T. D., Colley, J. D., and Parsons, R. H., "Industrial
Process Profiles for Environmental Use: Chapter 3. Petroleum Refining
Industry," prepared for the U.S. EPA by RadianCorporation (January 1977).
Krishnan, K. R., "Alternatives for Hazardous Waste Management in the
Petroleum Refining Industry," preparedforthe U.S. EPAby Jacobs Engineer-
ing Company (March 1978).
Labine, R. A., "Converting Waste Sludge Acid to H2SO4," Chemical Engineer-
ing, January 11,1960.
Leemann, James E, "Waste Minimization in the Petroleum Industry," JAPCA,
vol.38, No. 6, June 1988.
"New Acid From Refinery Sludge." Chemical Engineering. January 1954.
"Recycled Caustic Soda Will be Used in Enhanced Oil Recovery." Chemical
Engineering. January 11,1982.
"Reducing RCRA Impact Thru Waste Minimization," Workshop Proceedings
prepared by M. B. Van Hook, American Petroleum Institute and National
Petroleum Refiners Association, Arlington, VA (1987).
Todd, D. B., and F. C. Rac, "Recover Napthenic Acids Continuously,"
Hydrocarbon Processing, vol. 46, No.8, pp. 115-118 (August 1967).
U.S. EPA, Office of Solid Waste, Industrial Resource Recovery Practices:
Petroleum Refineries and Related Industries (SIC 29). prepared by Franklin
Associates, Contract No. 68-01-6000, Washington, DC (1982).
15
-------
ENDNOTES
'Information in this section is taken from, "Industrial Process Profiles for
Environmental Use: Chapter 3. Petroleum Refining Industry," prepared for
the U.S. Environmental Protection Agency by Radian Corporation (eds. J. C.
Dickerman, T. D. Raye, J. D. Colley and R. H. Parsons), (January 1977).
2K. R. Krishnan, "Alternatives for Hazardous Waste Management in the Pe-
troleum Refining Industry," prepared for the U.S. Environmental Protection
Agency by Jacobs Engineering Company (March 1978).
3"Reducing RCRA Impact Thru Waste Minimization," Workshop Proceedings
prepared by M.B. Van Hook, American Petroleum Institute and National
Petroleum Refiners Association, Arlington, VA (1987).
industrial Resource Recovery Practices: Petroleum Refineries and Related
Industries fSIC 291. Franklin Associates, Contract No 68-01 -6000, prepared
for the U.S. Environmental Protection Agency, Office of Solid Waste, Wash-
ington, DC (1982).
5D. B. Todd, and F. C. Rac, "Recover Napthenic Acids Continuously,"
Hydrocarbon Processing. Volume 46, No. 8, August 1967, pp 115-118.
Cf. Alternatives. 1978; Waste Minimization. 1988; Resource Recovery.
1982.
6Napthenic Acids. Cf. Alternatives. 1978.
7James E. Leemann, "Waste Minimization in the Petroleum Industry," JAPCA,
vol. 38, No. 6, pp. 814-823 (June 1988). Cf. Alternatives. 1978; Waste
Minimization. 1988: Resource Recovery. 1982.
8RCRA Impact.
"Ibid.
"Ibid.
"James E. Leemann, "Waste Minimization in the Petroleum Industry,"
JAPCA, vol. 38, No. 6, pp. 814-823 (June 1988).
12"New Acid From Refinery Sludge," Chemical Engineering, pp. 114-116
(January 1954). Cf. Waste Minimization. 1988: Resource Recovery. 1982.
13R. A. Labine, "Converting Waste Sludge Acid to H2S04," Chemical Engi-
neering, pp. 80-83 (January 11,1960). Cf. "Recycled Caustic Soda Will be
Used in Enhanced Oil Recovery." Chemical Engineering (January 11,1982).
"RCRA Impact.
16
-------
OPPORTUNITIES FOR WASTE MINIMIZATION IN THE
PETROLEUM REFINING INDUSTRY (SIC 2911)
THE WASTEWATER TREATMENT PROCESS
DESCRIPTION OF THE PROCESS1
Refining oil typically involves a series of many processes. For the
most part these processes are closed to the environment, and the product
outputs from one process proceed directly to the next process where
additional refining takes place. The total petroleum refining industry can be
divided into five major segments:
Crude Separation,
Light Hydrocarbon Processing,
Middle and Heavy Distillate Processing,
Residual Processing, and
Auxiliary Units.
The focus of this report is the treatment of the wastewater that results from
the various refinement processes. This industry segment is categorized
under auxiliary units.
The processing operations related to wastewater treatment are not
directly involved in the production of refined petroleum products. Since many
of the direct processes are closed in nature, the auxiliary processes, namely
wastewater treatment, are responsible for the majority of the waste streams
generated in refineries.
Wastewater produced in petroleum refineries is high in oil, phenols,
sulfides, ammonia, and dissolved and suspended solids. These water
streams must be treated before being returned to the environment or reused.
Several levels of treatment have been identified within refineries. Some
process waste streams must be pretreated prior to combining in primary
treatment facilities. Examples of pretreatment processes include sour water
stripping, spent caustic oxidation or neutralization, acidic/alkaline waste
neutralization, and cooling tower and boiler blowdown treatment. Primary
treatment facilities usually utilize gravity separation techniques to remove oil
and grit. Intermediate treatment provides longer holding time to allow
17
-------
leveling of concentration surges and consists of dissolved air flotation/
sedimentation units to remove suspended matter from the water. Secondary
treatment processes usually utilize biological oxidation processes to degrade
soluble organics. Solid wastes, including dirt, grit, oily sludge, clarifier sludge,
and bacterial sludge,are produced in wastewater treatment processes.
WASTE REDUCTION ALTERNATIVES
MATERIALS RECOVERY/RECYCLE
Every refinery generates contaminated oil which can be reprocessed.
The API separator, which is basically a primary wastewater treatment
process within a refinery, employs a gravity separation principle to recover
waste oil from various aqueous waste streams contaminated with oil. The
recovered oil, referred to as "slop oil," is skimmed from the top of the
separator tank and sent to storage or treatment.
If oil recovery is selected rather than land disposal, subsequent
processing requirements will be dictated by the characteristics of the slop oil.
Some recovered oils are treated in only the recovered oil tank. They are
heated, then a demulsifier is added, and when the water content is less than
0.5 percent, the recovered oils are reprocessed in the refinery. Other
recovered oils, because they are solids-stabilized, do not adequately sepa-
rate into oil and water fractions. A substantial middle layer emulsion is formed
which requires additional treatment to successfully recover the oil fraction.
Four methods of recovering oil from a solids-stabilized slop oil emulsion have
been identified:
Chemical stabilization
Centrifugation
Rotary vacuum filtration
Solvent extraction
The first method involves treatment of the emulsion with chemicals
which react with the stabilizing particles. Following chemical addition in batch
tanks, the slop oil is heated to 180° F for 12 to 14 hours. This treatment breaks
the emulsion down into layers consisting of oil, water, settling solids, and a
small remaining "rag layer" which does not separate. The oil is returned to
the front end of the refinery for re-refining.
A second method of oil recovery from slop oil emulsion is centrifuga-
tion. Chemical treatment of the emulsion followed by centrifugation can yield
18
-------
additional oil while minimizing the residual sludge which requires landfill
disposal or incineration.
A third method for recovering oil from slop oil emulsions is rotary
vacuum filtration. With rotary vacuum filters, refineries heat the recovered oil
and pass it through a filter to remove the solids and thus break down the
emulsion. The hot oil/water mixture is then gravity separated in a common
settling tank.
The fourth method of oil separation is a solvent extractionprocess.
This process has been proposed and designed to recover oil not only from
slop oil emulsion, but also from other wastewater treatment waste streams
such as API separator sludge and DAF skimmings. The process, called a
phase separation system, combines several conventional processes includ-
ing centrifugation, drying, decantation, steam stripping, and distillation. The
phase separation system yields recovered oil, reusable wastewater, and
dried solids for landfill disposal. The solvent used in the process is recovered
and reused many times. The selected solvent for this process is acetone;
however, others have been mentioned as applicable such as ethyl and
methyl alcohol, ethyl acetate, methyl ethyl ketone, and triethyl amine.2
A final identified method involves the on-site reuse of various waste
streams containing oil. Refineries that have a coker can benefit from the
petroleum coke exemption under 40 CFR 261.6(a)(3)(ix). This exemption
allows for refinery hazardous wastes that contain oil to be used as feedstock
to a coker. The oily wastes that a coker can normally receive includes DAF
float (KO48), slop oil emulsion solids (KO49), and API separator sludge
(KO51).3
Waste Reduction Potential4
Oil Recovery from Slop Oil Emulsions: from 36-38 percent reduction
in KO49 waste stream.
Oil Recovery from Oily Sludge: significant reductions in KO48, KO49,
and K051 waste streams.
Oily Wastes used as Feedstock for Coker: 100 percent reduction in
KO48, KO49, and KO51 waste streams.
19
-------
REFERENCES
Economics5
Oil Recovery from Slop Oil Emulsions: (1979$)
Annual costs of $260,200 and total savings of $611,000 in
recovered oil and reduced disposal costs.
Limitations/Constraints6
Oil Recovery from Slop Oil Emulsions: to implement any of these
techniques may require extensive equipment modifications depend-
ingupon the recovered material and the particular recovery process
employed.
Oil Recovery from Oily Sludge: the preferred solvent should be
completely soluble in oil and water at ambient temperatures in order
to save energy that would otherwise be required to maintain a lower
or higher temperature. It must also have a lower boiling point than
water and oil and it must not be reactive with either water or oil.
Oily wastes use as Feedstock for Coker: this method can be used as
long as the wastes are generated at the same facility at which the
coker is located and the resulting coke does not exhibit a hazardous
characteristic.
Applicability to Other Processes
These oil recovery processes could prove useful for recovering
wastewaters containing oil that are produced in other industries.
Industries such as 3721 and 3728, where metalworking fluids contain-
ing oil are often used, might benefit from this technology.
Dickerman, J. C., Raye, T. D., Colley, J. D., and Parsons, R. H., "Industrial
Process Profiles for Environmental Use: Chapter 3. Petroleum Refining
Industry," prepared forthe U.S. EPA by Radian Corporation (January 1977).
Franklin Associates, Industrial Resource Recovery Practices: Petroleum
Refineries and Related Industries (SIC 291. Contract No. 68-01-6000,
prepared forthe U.S. EPA, Office of Solid Waste, Washington, DC (1982).
20
-------
Gruette, J. L, "Chemical Treatment Helps Refinery Recover Oil from Waste,"
Pollution Engineering. October 1979, pp 44-45.
Krishnan, K. R., "Alternatives for Hazardous Waste Management in the
Petroleum Refining Industry," prepared forthe U.S. EPA by Jacobs Engineer-
ing Company (March 1978).
"Reducing RCRA IMpact Through Waste Minimization," Workshop Proceed-
ings prepared by M. B. Van Hook, American Petroleum Institute and National
Petroleum Refiners Association, Arlington, VA (1987).
21
-------
ENDNOTES
'Information in this section is taken from: J. C. Dickerman, T. D. Raye, J. D.
Colley, and R. H. Parsons, "Industrial Process Profiles for Environmental
Use: Chapter 3. Petroleum Refining Industry," prepared for the U.S.
Environmental Protection Agency by Radian Corporation (January 1977).
2K. R. Krishnan,"Alternatives for Hazardous Waste Management in the
Petroleum Refining Industry," prepared for the U.S. Environmental Protec-
tion Agency by Jacobs Engineering Company (March 1978).
3"Reducing RCRA Impact Through Waste Minimization," Workshop Pro-
ceedings prepared by M.B. Van Hook, American Petroleum Institute and
National Petroleum Refiners Association, Arlington, VA (1987).
"Industrial Resource Recovery Practices: Petroleum Refineries and Related
Industries (SIC 291. Franklin Associates, Contract No 68-01 -6000, prepared
for the U.S. Environmental Protection Agency, Office of Solid Waste, Wash-
ington, DC (1982). Cf. Waste Management. 1978 and RCRA Impact. 1987.
6J. L Gruette, "Chemical Treatment Helps Refinery Recover Oil from Waste,"
Pollution Engineering. October 1979, pp 44-45.
6Cf. Waste Management. 1978; RCRA Impact. 1987; Recovery Practices.
1982.
22
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OPPORTUNITIES FOR WASTE MINIMIZATION IN THE PRIMARY
ALUMINUM PRODUCTION INDUSTRY (SIC 3334)
THE ALUMINUM SMELTING PROCESS
DESCRIPTION OF THE PROCESS
The basic process for reducing alumina to aluminum is depicted in the
flow diagram in Figure 1. The raw materials used in aluminum production
include alumina, cryolite (a double fluoride of Na and Al), pitch, petroleum
coke, and aluminum fluoride. The heart of the process is the electrolytic cell,
which consists of a steel container lined with refractor brick, with a bottom
inner lining of carbon. The cells are arranged in rows in an operating unit
(potline) and as many as 100 to 250 cells are electrically connected in series.
The electrical supply is direct current, and is on the order of several hundred
volts and 60,000-100,000 amperes. The carbon lining at the bottom of the
cell acts as a cathode when covered with molten alumina. The anode of the
cell is baked carbon. The electrolyte consists of a mixture of cryolite (80-85
percent by wt), calcium fluoride (5-7 percent), and alumina (2-8 percent).
During the reduction process, the carbon anode is consumed and combines
with oxygen to form CO and CO2. The reduced heavier aluminum sinks to the
bottom of the cell and is periodically tapped and sent to be degassed and cast
into a salable product. Fresh alumina and cryolite are added periodically to
the top of the melt. The individual cells operate between 950 and 1000° C.1
The result of this smelting process is aluminum metal, which is an
intermediate product used in the manufacturing of yet other products.
Aluminum metal is usually supplied in a variety of rough shapes such as
ingots, sheets, billets, and rods.2
WASTE REDUCTION ALTERNATIVES
The largest source of waste resulting from the primary aluminum
smelting process is the spent potliners. These potliners have an average life
of 2-3 years. Over a period of time, the cathode potliners become partially
saturated with cryolite. After continued use, they crack and the molten
aluminum becomes contaminated with iron from the outer shelf of the
cathode. Whenthis occurs the cathodes must be replaced.3
23
-------
PETROLEUMCOKE
CRUSHING
AND
CLASSIFYING
PITCH
ANODE PASTE
HOT BLENDING
I
COOLING
PRESSING
SOLDERBERG
ANODE
BRIQUETTES
BAKING
ELECTRICAL POWER
SUPPLY
(DC.)
ANODES
ALUMINA
CRYOLITE
CALCIUM aOURIDE
ALUMINIUM ROURIDE
FUSED SALT
ELECTROLYTIC
CELL
CATHODES
BLENDING
I
MOLTEN A1.
TO DEGASSING
AND CASTING
Arrthraoto
DRY PROCESS
SOLIDS TO
CELL
WET
SCRUBBER
LIQUOR
TO
TREATMENT
Aluminum
(pg,bM. ingot.
rod)
Spent Potfnara
Pnmaiy Aluminium Producton
(LL Tavlarides, Process Modifications for Industiral Pollution
Source Reduction. Lewis Publishers. Chelsea, Ml. 1985)
24
-------
The spent cathode potliners are removed by drilling and/or soaking in
water. They consist largely of carbon (the cathode), but also contain cryolite,
aluminum carbide, and aluminum nitride. NaOH and sodium cyanide also
appear in waters as a result of leaching of the potliners. The carbides react
with water vapor in the air to produce methane (CH4), hydrogen, C2H2 and
other hydrocarbons, and the nitride yields ammonia.4
In the past these spent potliners have been dumped or used as landfill.
In recent years, however, a number of alternative methods have been
devised by which to recover or recycle the potliners themselves and/or some
of the hazardous constituents present in the potliner. These methods
primarily involve either on- or off-site chemical recovery or off-site energy
recovery.
MATERIALS RECOVERY/RECYCLE5
The examples of on-site chemical recovery include cryolite recovery,
recycling to anodes, and pyrohydrolysis. In Cryolite recovery, significant
portions of spent potliner is reclaimed in cryolite recovery operations which
produce synthetic cryolite. These recovery operations are closely inter-
twined with the primary aluminum reduction process. The reclaimed cryolite
is recycled back to the primary process, and is also marketed at free-market
prices. Recycling to anodes involves the direct reuse of potliner as a raw
material substitute in the solderberg anode of an aluminum reduction cell. Up
to 50 percent of the coke aggregate can be replaced by spent potliner in the
production of anodes. In pyrohydrolysis the carbon portion of the potliner is
burned and the fluoride reacts with steam to produce hydrogen fluoride.
Fluoride is recovered as commercial-grade aluminum fluoride.
Waste Reduction Potential
Cryolite recovery: at least 82,000 tons of K088 waste stream.
Recycling to anodes: an amount equal to between 22 and 25 percent of total
aluminum production (by weight).
Economics
N/A
Limitations/Constraints
Recycling to Anodes:
25~~
-------
-the use of spent potliner in the anodes is estimated to increase
anode carbon consumption slightly.
-the presence of spent potliner in the anodes is estimated to
degrade metal quality to as low as g or h grade.
Applicability to Other Processes
N/A
OFF-SITE RECOVERY/RECYCLE6
The examples of off-site recovery include centralized aluminum
fluoride recovery, and combustion processes such as cement kilns, basic
oxygen furnace steelmaking, mineral wool production, iron making foundry
cupolas, power plants, and rotary kilns. The centralized recovery of alumi-
num fluoride recycles potliners to produce aluminum fluoride, caustic, and
graphic products. More than 95 percent of the fluoride is recovered as useful
aluminum fluoride; cyanide is destroyed by incineration. In the case of the
combustion processes, spent potliners are used as partial fuel substitutes for
coal, carbon and fluorspar, or coke. Typically, the cyanide Is burned off in the
process of incineration, and the fluoride is either used for its value or enters
the process slag or resulting ash.
Waste Reduction Potential
Aluminum fluoride recovery: at least 90 percent of K088 waste stream.
Cement kilns: it is estimated that only 20 percent of the U.S. cement kiln
capacity would be required to burn the annual production of K088 waste.
Basic oxygen furnace (BOF) steelmaking: it is estimated that only 1/3 of the
U.S. BOF capacity would be required to burn the annual production of K088
waste.
Mineral wool production: spent potliners can replace up to 60 percent of coke
feed in theproduction of mineral wool.
Iron making foundry cupolas: spent potliners can replace up to 20 percent
of coke feed in this process.
Power plants: a small 100-megawatt coal-fired power generating unit could
burn the entire annual generation of spent potliner at a medium to large-sized
aluminum reduction plant.
26~
-------
Economics
Mineral wool production:
Coke costs are in the $120-140/ton range, while spent potliner can
be supplied at considerably lower costs, even including transportation
and material preparation charges.
Power plants:
Fuel savings could be $450,000 per year, assuming coal costs of $30
per ton and operation 250 days per year.
Li mitatio ns/Co nstrai nts
Aluminum fluoride recovery:
On a large scale (greater than 150,000 tons/year), the process has
favorable economics, but it has yet to be tested in pilot or full plant
scale.
Cement kilns:
Attention must be paid to how the spent potliner is handled and stored
prior to being burned in the kiln.
Mineral wool production:
« Corrosion due to hydrofluoric acid may be a potential problem in
some plants, but can be avoided with dry, hot removal systems.
Power plants:
No full-scale studies of spent potliner as a fuel supplement in a power
plant have been documented to date.
Solid waste and water quality would need to be considered, because
it is believed that virtually all of the excess fluorides would be removed
from the system as a constituent of the solid waste.
Applicability to Other Processes
N/A
27
-------
REFERENCES
Parsons, Terry, "Primary Aluminum Industry." Industrial Process Profiles for
Environmental Use (U.S. EPA, Environmental Research
Laboratory, 1977), PB-281 491.
Tavlarides, Lawrence L, Process Modifications for Industrial Pollution Source
Reduction. Lewis Publishers, Chelsea, Ml, 1985.
U.S. EPA, "Primary and Secondary Non-Ferrous Smelting and Refining,"
Assessment of Industrial Hazardous Waste Practices in the Metal Smelting
and Refining Industry, vol. II, Report No. ND-5520-M-1 (April 15, 1977).
28
-------
ENDNOTES
1l_Hwrence L. Tavlardies, Process Modifications for Industrial Pollution Source
Reduction. Lewis Publishers, Chelsea, Ml (1985).
2 Terry Parsons, "Primary Aluminum Industry," in Industrial Process Profiles
for Environmental Use, U.S. EPA, Environmental Research Labortory, PB-
281 491 (1977).
3 "Primary and Secondary Non-Ferrous Smelting and Refining." Assessment
of Industrial Hazardous Waste Practices in the Metal Smelting and Refining
Industry, vol. II, U.S. EPA, Environmental Research Laboratory, PB-281 491
(1977).
4Process Modifications. 1985.
The information in this section is adapted from "Comments of the Aluminum
Industry," Incorporated on the Proposed Reinterpretation of the Bevill
Amendment and the Proposal to List Spent Potliners as a Hazardous Waste,
50 Federal Register 40292 (1985).
elbid.. 1985.
29
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OPPORTUNITIES FOR WASTE MINIMIZATION IN THE PLATING
AND POLISHING INDUSTRY (SIC 3471)
THE ELECTROPLATING PROCESS
DESCRIPTION OF THE PROCESS
The electroplating process involves the application of a thin metal
coating of one metal upon another by electrodeposition. Electroplating is
used to enhance the corrosion resistance of a metal, to improve or alter the
appearance of a metal, or to impart improved mechanical properties (hard-
ness, lubricity) to the metal.1 The plating process is achieved by passing an
electric current through a solution containing dissolved metal ions as well as
the metal object to be plated. The metal object becomes a cathode in an
electrochemical cell, resulting in the deposition if the dissolved metal ions
onto the surface if the metal object. Metal objects are commonly electro-
plated with brass, bronze, cadmium, chromium, copper, iron, lead, nickel, tin
and zinc. Precious metals such as gold, silver and platinum are also widely
used.2
The electroplating process generally calls for moving the object to be
plated through a series of process tanks. Each process bath is usually
followed by a rinse tank in order to remove residual process solution from the
part and prevent cross contamination. The object can be carried either on
racks or in barrels.3 The specific focus of this report is chromium plating
operations, for which a flow chart is shown in Figure 1.
Electroplating is one of many processes that is typically used in the
manufacturing of a final product. Some of the many product areas in which
electroplating processes are involved include:4
automotive exterior/interior parts
plumbing fixtures
bearings
kitchen appliances
tools
computer chassis
30
-------
Work (low
W (600 fl 2/h)
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360 gal/h
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*
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*
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v
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rinse ©
|
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Y
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^
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1
360
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+
Nickel-Chrome Wastewater Flow Rates. Original System
m S EPA Reducmo Water Pollution Control Costs in the Elactroolatma Indus ti
EPA/625/5-85/016. Cincinnati, OH (May 16, 1985).)
-------
WASTE REDUCTION ALTERNATIVES
PROCESS MODIFICATIONS
Several process modifications have been shown to reduce, at their
source, hazardous waste generation from electroplating. These modifica-
tions can be grouped into the following categories:
improving housekeeping practices
reducing drag-out
water conservation
Improving Housekeeping Practices
Changes in housekeeping practices can be made rapidly with little capital
investment. Successfully implemented, these changes can result in in-
creased production rates, improved product quality, and improved workplace
safety, as well as reduction of hazardous waste generation. The following is
a list of possible housekeeping improvements:5
Repair all leaking tanks, pumps, valves, and similar items.
Inspect tanks and tank liners periodically to avoid failures that may
result in bath dumps.
Maintain plating racks and anodes to prevent contamination of baths.
Minimize the volume of water used during cleanup operations.
Train plating personnel so that they understand the importance of
minimizing bath contamination and wastewater discharge.
Waste Reduction Potential6
Significant reductions of D002, D003, and D007 waste streams.
Economics
N/A
Limitations/Constraints7
These kinds of changes are often people-based, rather than technology-
based, and can be more difficult to maintain long-term.
32
-------
Applicability to Other Processes
These kinds of modifications apply to other industries which employ plating
within the overall process. These industries include 3679 and 3721.
Drag-out Reduction
By reducing the quantity of solution dragged out of the process tanks in an
electroplating operation, the amount of waste that must be treated and
disposed of can be significantly reduced. There are a number of simple
operational and process changes that can significantly reduce drag-out as
shown in Table 1. One of the simplest methods of drag-out reduction is to
provide sufficient drain-time over the process tank. It has been shown that
this can reduce drag-out by at least 70 percent. Another effective technique
for the control of drag-out is drag-out recovery. This is a technique in which
a series of one or more air-agitated non-flowing rinses is placed between the
process tank and the running rinse. These tanks capture most of the drag-
out and thus reduce the contaminant load to the running rinse. Typically,
each drag-out tank reduces the concentration in the running rinse by 50
percent leading to a much lower concentration of plating chemicals in the
wastewater.8
Table I. Drag-out reduction techniques
Increase part drain time
Use low pressure air to blow solution off parts (air knife)
Use fog or spray rinsing over the process tank
Minimize concentrations of metal in plating bath
Rack parts to maximize drainage
Design racks to maximize drainage
Maintain racks/barrels and coating
Use drip bars to hold racked parts over plating tank
Use drain boards between tanks
Maximum hole size on barrels
Rotate barrels above tank
(G E Hunt, "Waste Reduction in the Metal Finishing Industry.' JAPCA. vol. 38. No. 5 (May 1988))
33
-------
Waste Reduction Potential9
From 50 percent to more than 90 percent of D002 waste stream
Economics10 (*)
Capital costs of less than $900 and monthly savings of $784 for a payback
period of 1.1 months.
Othese numbers correspond to the addition of one drag-out board.
Li m itatio ns/Co nstrai nts11
Success is dependent upon the shape and design of the parts, racks,
and barrels used in the process
Level of drag-out achievable depends on the level of drag-out prior
to implementation of one of the alternatives
Applicability to Other Processes
these alternatives are applicable to processes in industries 3673,
3674, 3721, and 3728
Water Conservation
Techniques for water conservation are simple, inexpensive, and well known,
and will save money through reduced flow water and sewer costs. More
importantly, however, water conservation techniques increase potential for
water recovery. The most common techniques include the use of mechanical
water flow control valves, reactive rinsing systems, and countercurrent
rinsing systems.12
Waste Reduction Potential13
90 to 99 percent of D006 and D007 waste streams
34
-------
Economics14
Costs
PAYBACK
Capital O&M PERIOD
Flow Control Valve $ 10 NA 1 mo
Reactive Rinsing $ 250 NA 2 mo
Countercurrent Rinsing $1000-
$10000 NA <1 yr
Limitations/Constraints15
Flow Control: limiting flow to a rinse tank must be balanced to ensure
adequate agitation for effective rinsing.
Reactive Rinsing: Careful evaluation must be made of each potential
use in order to avoid contamination of process baths and reduction in
plating quality through pitting and passivation.
Countercurrent Rinsing: Use of this technique can be limited due
to a number of factors including the cost of purchasing the system,
the extra floor space needed for the additional rinse tanks, the
additional production timerequired, and the difficulty in providing
adequate mixing in the additional tanks.
Applicability to Other Processes
These techniques are applicable to processes in industries 3673,
3674, 3721, and 3728.
Product/Input Substitution
In addition to changes and refinements to the electroplating process,
substitution of inputs and/or products within the process can serve to lessen
both the volume and toxicity of the waste produced. There are a number of
electroplating processes, including chromium, that can make use of this
strategy. For chromium electroplating, low concentration trivalent chromium
35
-------
baths can be used in place of conventional solutions of hexavalent chromium.
Because of the lower chrome concentration, trivalent baths can reduce drag-
out concentration of chromium by more than 80 percent. Consequently, the
sludge that is produced from trivalent baths has about one-seventh of the
volume of sludge that results from hexavalent baths, and is much less toxic.16
Waste Reduction Potential17
70 percent or more reduction of D007 waste stream
Economics18
The raw material cost is two to three times higher, but there are significant
savings related to wastewater treatment and sludge disposal needs.
Limitations/Constraints
N/A
Applicability to Other Processes
This technique is applicable only to processes employing
chromium electroplating
Materials Recovery/Recycle
Another area of possible waste reduction in the electroplatingprocess is ma-
terials recovery prior to treatment. Heavy metals are the predominant
material recovered from a plating operation. There are a number of proven
technologies which can remove some of the water from drag-out or contami-
nated rinse water, so that a concentrated plating solution can be returned to
the process bath. These technologies include: ion-exchange, reverse
osmosis, evaporation, and electrodialysis. These processes reconcentrate
plating solutions from rinsewater, producing a relatively pure water, which is
reused for rinsing. They have been shown to have the potential to recover
between 90 and 100 percent of the desired material.19
The two techniques that are most applicable to recovery from chromium
electroplating are evaporation and ion exchange. Evaporation reclaims the
material by heating the process waste rinse water. Ion exchange involves the
passing of a chemical solution through a resin bed which selectively removes
36
-------
particles (ions). Ion exchange is typically used to recover trace pollutants
from wastewater, or too recover plating solution drag-out from rinse water
and to return the purified water for reuse. Ion exchange is ideally suited for
dilute solutions and can achieve high levels of recovery.20
Waste Reduction Potential21
Evaporation: 90 to 99 percent of D007 waste stream
Ion Exchange: 90 to 99 percent of D007 waste stream
Economics22 (*)
Evaporation Ion Exchange
Capital Costs $47,000 $38,000
Annual Operating Costs $20,100 $12,500
PAYBACK PERIOD 3.3 yr. 3.6 yr.
OThese numbers are representative of systems designed to treat up to 20-
gal/h of waste for up to 5000 h/yr.
Limitations/Constraints23
General: these techniques should only be considered after low-cost plating
line modifications or rinse-and-recycle modifications have been examined.
Evaporation: the success of this technique depends on havingan
adequate quantity of plating chemicals available for recovery.
Ion Exchange: this technique is better suited to recovery from
dilute solutions. In addition, a major drawback of this technique is
that the resin must be regenerated after it has exhausted its
exchange capacity. This complicates the operation of the system
and adds significant volumes of regenerant and wash solutions to
the wastewater treatment loading.
Applicability to Other Processes
These techniques are broadly applicable to processes that require
separation and purification of process rinse waters for reuse. These
37
-------
processes could include plating operations employing other plating
bath formulations as well as processes in industries 3673,3674,3721,
and 3728.
OFF-SITE RECYCLE
Off-site recycling, in terms of a plating operation, refers to the shipping
of wastes to a centralized treatment facility. These centralized facilities can
either be operated independently for a specific geographic region or they can
be owned and operated by a relatively small number of platers in close
proximity. The technologies used at a centralized facility are similar to
existing process technologies for primary metals. The major advantage of a
centralized facility would be the resulting economies of scale leading to lower
costs to individual platers. The regional approach to centralized treatment of
electroplating wastes has been shown to be of great economic benefit in re-
gions as diverse as Cleveland and Atlanta where participating plating shops
are close to the central facility. For smaller group-owned treatment facilities,
it is unclear whetherthe cost savings are sufficient to cover the capital costs
for a facility that will allow recovery of material.84
Waste Reduction Potential25
Significant reduction of D001 and D002 waste streams (up to the capacity of
the plant)
Economics26 (*)
Capital Costs: $2.8 million
Annual Operating Costs: $705,000
PAYBACK PERIOD: 3.4 yrs
(*)These figures are representative of a plant large enough to handle the pro-
jected waste stream from 76 plating shops <(approximately 42,000 gpd)>.
Limitations/Constraints27
The feasibility of this technique depends to a great extent on the level
of participation on the part of the individual plating shops. This has
been shown too be an effective alternative in highly industrialized
areas where participants are in close proximity to each other and the
centralized facility.
38
-------
Applicability to Other Processes
Off-site recycling can be practiced with respect to many types of
wastes. The key issues which will affect the viability of off-site
recycling are economics and liability. In industries such as 3674,
3979,3721, and 3728, this technique would be directly applicable to
recycling the spent process baths used in the plating lines.
REFERENCES
Cushnie, George, et al, Design and Costs for Cleveland Resource Recovery
Park. Contract No. 68-03-2907, Task 12, U.S. EPA, Cincinnati, OH (1981).
Higgins, Thomas, Hfl^flPfous Waste Minimization Handbook. Lewis Publish-
ers, Inc., Chelsea, Michigan, 1989.
Hunt, Gary E., "Waste Reduction inthe Metal Finishing Industry," JAPCA, vol.
38, No. 5, pp. 672-680 (May 1988).
U.S. EPA, Waste Minimization Issues and Options Volume 2: Appendices A
&B. EPA/530-SW-86-042, Washington, D.C. (1986).
U.S. EPA, Reducing Water Pollution Control Costs in the Electroplating
Industry. EPA/625/5-85/016, Cincinnati, OH (May 16, 1985).
U.S. EPA, Centralized Waste Treatment Alternatives for the Electroplating
Industry. EPA 625/5-81-017, Cincinnati, OH (May 17, 1981).
39
-------
ENDNOTES
1Thomas Higgins, Hfl7flrd9us Waste Minimization Handbook. Lewis Publish-
ers, Inc., Chelsea, Michigan, 1989.
^ary E. Hunt, "Waste Reduction in the Metal Finishing Industry," JAPCA, vol.
38, No. 5, pp. 672-680 (May 1988).
3Waste Minimization Issues and Options Volume 2: Appendices A & B. EPA/
530-SW-86-042, U.S. Environmental Protection Agency, Washington, D.C.
(1986).
4lbid. 1986.
Minimization Handbook. 1989.
6lbid.
7lbid.
'Metal Finishing. 1988.
"Cf. Minimization Handbook. 1989; Metal Finishing. 1988.
10U.S. EPA, Reducing Water Pollution Control Costs in the Electroplating
Industry. EPA/625/5-85/016, Cincinnati, OH (May 16,1985).
11Cf. Minimization Handbook. 1989: Metal Finishing. 1988.
12Metal Finishing.
13lbid.
14Cf. Minimization Handbook. 1989: Metal Finishing. 1988.
15lbid.
16lbid.
17Metal Finishing.
^Minimization Handbook.
19Cf. Minimization Handbook. 1989; Metal Finishing. 1988; and Minimization
Issues. 1986.
'"Reducing Water Pollution Control Costs in the Electroplating Industry. EPA/
625/5-85/016, U.S. Environmental Protection Agency, Cincinnati, OH (May
16, 1985).
40
-------
21Cf. Minimization Handbook. 1989; Metal Finishing. 1988; Minimization
Issues. 1986; and Pollution Control. 1985.
"Pollution Control.
f. Metal Finishing. 1988; Minimization Issues. 1986; Pollution Control.
1985.
"U.S. EPA, Centralized Waste Treatment Alternatives for the Electroplating
Industry. EPA 625/5-81-017, Cincinnati, OH (May 17, 1981).
^George Cushnie, et al, Design and Costs for Cleveland Resource Recovery
Park. Contract No. 68-03-2907, Task 12, U.S. Environmental Protection
Agency, Cincinnati, OH (1981).
41
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OPPORTUNITIES FOR WASTE MINIMIZATION IN THE PLATING
AND POLISHING INDUSTRY (SIC 3471)
THE SOLVENT CLEANING AND DECREASING PROCESS
DESCRIPTION OF THE PROCESS
The solvent cleaning and degreasing process involves the removal of
oil, grease and dirt from metal parts. 1 In almost all cases, solvent cleaning
and degreasing is also used to prepare surfaces for painting. The selection
of a specific cleaner will depend on the nature of the base metal, the type of
soil which has to be removed, and how much soil there is to remove. There
are three distinct types of operations that fit into the category of solvent
cleaning and degreasing: cold cleaning, vapor degreasing, and precision
cleaning.2
The first operation, cold cleaning, is the simplest, least costly, and
most common type of solvent cleaning. The solvent is usually applied at
ambient temperature or is heated slightly. It is applied either by brush or by
dipping the items to be cleaned in a solvent dip tank.3
The second operation, vapor degreasing, uses nonflammable, chlo-
rinated hydrocarbons in a vapor phase to clean metallic and other suitable
surfaces. The special apparatus that provides solvent vapor consists of a
tank that is one-tenth full of solvent (Figure 1). The solvent is heated, usually
by steam coils, to its boiling point, in orderto produce solvent-saturated vapor
in the upper portion of the tank. The item to be cleaned is then either inserted
manually or automatically into the vapor region, where hot solvent vapor
immediately condenses onto the surface of the item. The condensed solvent
then drips back into the liquid bath and takes with it the removed dirt and
grease. The solvent vapor is usually prevented from escaping to the atmos-
phere by use of a refrigerated section on the upper part of the tank. The
solvent condenses on the walls of this section and returns to the liquid sump.4
The most common solvents used in vapor degreasing aretrichloroeth-
ylene; perchloroethylene; 1,1,1-trichlorethane; and methylene chloride.
Trichlorethylene is the most popular vapor degreasing solvent due to its
relatively low boiling point (190°F) which allows the use of low-pressure
steam for heating and permits the handling of parts immediately after
cleaning. The second most popular solvent is 1,1,1 -trichlorethane, which has
42
-------
an even lower boiling point than trichloroethylene but reacts with zinc and
aluminum. Approximately 15 percent of vapor degreasing applications use
perchloroethylene, because it is stable, has a high boiling point, and is the
least aggressive solvent on the market. Other solvents used in vapor
degreasing include fluorocarbons (freon) and carbon tetrachloride.
The third operation, precision cleaning, requires solvents of high
purity, high solvency, and rapid evaporation rates. Precision cleaning is
usually used in applications involving instruments and electronic parts.
Freon compounds are customarily used for these applications.
WASTE REDUCTION ALTERNATIVES
PROCESS MODIFICATIONS
There are a number of process modifications that can reduce the level
of waste from solvent cleaning and degreasing operations. Solvent losses
due to drag-out can be reduced by regimenting good operating procedures.
With open-tank systems, even though covers are part of the original equip-
ment design, it is common for operators to leave the covers off when the
system is at rest or is shut-down. The use of a tank cover during shut down
periods can reduce solvent loss significantly.7
Equipment modifications such as increasing the height of the de-
greaser freeboard and making use of refrigerated chillers can also signifi-
cantly reduce solvent loss. The freeboard height of a degreaser is the height
of the tank above the vapor level. Increasing this height from 50 percent to
75 percent of the tank width will significantly reduce solvent losses. The
refrigerated chillers create a cold blanket above the vapor zone in the de-
greaser and prevent the escape of vapors?
Waste Reduction Potential9
Tank Covers: 25 percent to 59 percent reduction in F001, F002, F003,
and F005 waste streams.
Increased Freeboard Height: 25 percent to 55 percent reduction in
F001, F002, F003, and F005 waste streams.
Refrigerated Chillers: 40 percent to 60 percent reduction in F001,
F002, F003, and F005 waste streams.
43
-------
Economics10
Tank Covers and Increased Freeboard Height: savings of $6,600 in
solvent purchases lead to a payback of 6 months on the installed
equipment.
Refrigerated Chillers: chillers installed on two degreasers saved
$17,688 in solvent purchases in the first year of operation.
Limitations/Constraints
None Identified
Applicability to Other Processes
These modifications are broadly applicable to those processes which
make use of solvent vapor degreasing. These processes are used in
industries such as 3674,3679,3721, and 3728.
PRODUCT/INPUT SUBSTITUTION
In applications such as cleaning oil and grease from metal parts, high
pressure hot water washers can be used without solvents or detergents.
These units supply a stream of hot water j'ets to a handheld wand that cuts
the grease and oil from the metal part without the need for detergents or sol-
vents.11
Waste Reduction Potential12
100 percent reduction in FOOL F002, F003, F005, and D002 waste
streams
Economics13 (1987$)
Capital Costs: $7,062
Annual O&M:$1,597
PAYBACK PERIOD: 6 mo.
Limitations/Constraints14
Because water is heated to above 120° F, it is necessary to allow parts
time to cool off, especially prior to assembly.
44
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Applicability to Other Processes
Depending on the particular wastes involved and the level of cleanli-
ness desired, this technique may be applicable to processes in
industries such as 3674, 3679, 3721, and 3728.
MATERIALS RECOVERY/RECYCLE
There are a number of methods that can be used to recycle solvents.
These include cascade reuse, distillation, carbon adsorption, and nitrogen-
based solvent recovery. Cascade reuse involves the use of an untreated
waste solvent, recuperated from an operation with high purity standards, for
a less demanding function. Solvent recovery using distillation involves
heating a solvent until it vaporizes, and then condensing the vapor. The
condensed vapor is reused. If the boiling point of the solvent is high (over 200°
F), the distillation usually takes place under a vacuum to minimize the thermal
decomposition of the solvent.15 In carbon adsorption, solvent-laden air is
forced through a bed of activated carbon were the solvent molecules adhere
to the porous surface area of the activated carbon. The trapped solvent mole-
cules remain in high concentration until forced out by some means of carbon-
bed regeneration: water purge regeneration or steam sweep regeneration.16
Nitrogen-based solvent recovery involves the use of an inert nitrogen atmos-
phere. With an inert nitrogen atmosphere, solvent vapor can be safely con-
centrated to well above traditional oven levels, at which levels the solvent is
recoverable by condensation. The oven exhaust is cooled with multiple heat-
exchange stages.17
Waste Reduction Potential1fl
Cascade Reuse: N/A
Distillation: 75 percent to 94 percent reduction in F001, F002, F003,
and F005 waste streams
Nitrogen-Based Solvent Recovery: 99 percent reduction in F001,
F002, F003, and F005 waste streams.
Carbon Adsorption: 80 percent to 100 percent reduction in F001,
F002, F003, and F005 waste streams.
45
-------
Economics10
Costs (1985$)
PAYBACK
Capital O&M PERIOD
Distillation "cost savings: $3.39/gal." 15 mo.
Carbon Adsorption $800,000 $327,000 24 mo.
Limitations/Constraints20
Cascade Reuse: none Identified
Distillation: only 65 percent (by concentration) of the inhibitors added
to many brands of solvents is reclaimed by the distillation process.
This may affect the performance of some reclaimed solvents. In
addition, for recycling by distillation to be effective, solvents should be
segregated.
Nitrogen-Based Solvent Recovery: this technology is relatively new.
At present, nitrogen-based solvent recovery is primarily applicable to
larger businesses because of the significant capital costs.
Cannon Adsorption: the materials of construction must be carefully se-
lected for the type of solvents to be recovered and to protect against
any acidity which may be present in the inlet airstream. In addition, the
quantity of airflow to be handled by a solvent recovery plant is a critical
factor in the size and cost of the plant.
Applicability to Other Processes
These methods of recycling are broadly applicable in other industries,
depending upon the extent that solvents are used in those industries.
And in other studies, distillation and carbon adsorption have been
shown to be effective in the recovery of other aqueous waste streams.
46
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OFF-SITE RECYCLE
There are two techniques that have shown promise for reducing the
amount of waste from solvent cleaning and degreasing operations. The first
technique involves the use of some of the technologies described in the
previous section at a centralized location. Primarily, distillation can be used
on a large scale to recover solvent from a number of cleaning and degreasing
operations.21 The second technique involves the use of waste solvent
residue as a substitute low-grade fuel. As discussed above, recovery
efficiencies range between 75 percent and 100 percent. For anything less
than 100 percent efficiency, a residue of waste solvent is left over. In recent
years, use of this waste solvent as a low-grade fuel has shown promise.22
Waste Reduction Potential23
Off-Site Recycling: same as for distillation above
Use as Fuel Substitute: 100 percent reduction in F001, F002, F003,
and F005, waste streams.
Economics24
Off-Site Recycling: capital costs of $48,000 yielded annual savings of
$81,000 for a payback of less than 6 months. (1983$)
Use as Fuel Substitute: (*) (1981 $)
Cost of Present Revenue
Burying Residue From Fuel Sales
$696,000/year $90,000/year
OThese numbers are based on the assumption that 20 percent of 3
million gallons of solvent handled annually results in residue.
Limitations/Constraints25
Off-Site Recycling: because many different types of solvents are re-
cycled, great care must be taken with waste segregation and sample
analysis. In addition, the solvents must be transported to and from the
point of use.
47
-------
Use as a Fuel Substitute: none identified
Applicability to Other Processes
Off-site recycling can be practiced with respect to many types of
wastes. The key issues which will affect the viability of off-site
recycling are economics and liability. In industries such as 3674,
3979,3721, and 3728, this technique would be directly applicable to
recycling the solvents used in the cleaning and degreasing operation
undertaken in the processes.
REFERENCES
Campbell, M. and Glenn, W., Profit from Pollution Prevention: A Guide to
Industrial Waste Reduction and Recycling. Pollution Probe Foundation,
Toronto, Canada, 1982.
Cheremisinoff, Paul N., "Special Report: Volatile Organic Compounds," Pol-
lution Engineering, vol. 17, No. 3, pp. 30-38, (March 1985).
Durr, Larry J. and Rawlins, Ellen, "Solvent Recovery for Compliance with
Federal Regulations," Plating & Surface Finishing, (October 1981).
Higgins, Thomas. Hazardous Waste Minimization Handbook. Lewis Publish-
ers, Inc., Chelsea, Michigan, 1989.
Hunt, Gary E., "Waste Reduction in the Metal Finishing Industry," J ARC A, vol.
38, No. 5, pp. 672-680 (May 1988).
48
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Minnesota Technical Assistance Program, 1.1.1 -Trichloroethane Reduction
Alternatives. Minneapolis, MM, 1987.
ENDNOTES
1Gary E. Hunt, "Waste Reduction in the Metal Finishing Industry," J ARC A, vol.
38, No. 5, pp. 672-680 (May 1988).
Thomas Higgins, Hazardous Waste Minimization Handbook. Lewis Publish-
ers, Inc., Chelsea, Michigan, 1989.
3lbid..1989.
"Ibid.. 1989.
5JJ2id.,1989.
6lbid..1989.
7M. Campbell and W. Glenn, Profit from Pollution Prevention: A Guide to
Industrial Waste Reduction and Recycling. Pollution Probe Foundation,
Toronto, Canada, 1982.
8lbid.. 1982.
9lbid.. 1982.
"Ibid.. 1982.
"Minimization Handbook. 1989.
121.1.1 -Trichloroethane Reduction Alternatives. Minnesota Technical Assis-
tance Program, Minneapolis, MN, 1987.
13lbid.. 1987.
14lbid..1987.
^Minimization Handbook.. 1989.
"Larry J. Durr and Ellen Rawlins, "Solvent Recovery for Compliance with
Federal Regulations," Plating & Surface Finishing, (October 1981).
17Pollution Prevention.. 1982.
18Cf. Waste Minimization. 1989; Pollution Prevention. 1982; Solvent Recov-
fiiy., 1981.
19Cf. Pollution Prevention, 1982; and Paul N. Cheremisinoff, "Special Report:
49
-------
Volatile Organic Compounds." Pollution Engineering, vol. 17, No. 3, pp. 30-
38 (March 1985).
"Cf. Minimization Handbook. 1989; Pollution Prevention. 1982; Solvent
Recovery. 1981.
^Minimization Handbook. 1989.
^Profit from Pollution. 1982.
"Of. Minimization Handbook 1989.-Pollution Prevention 1982.
24lbid.
^Minimization Handbook 1989.
50
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OPPORTUNITIES FOR THE MINIMIZATION OF WASTE IN THE
SEMICONDUCTORS AND RELATED DEVICES INDUSTRY (SIC 3674)
THE SEMICONDUCTOR MANUFACTURING PROCESS
THE PROCESS AND PRODUCTS
As indicated in Figure 1 (p. 52), there are a series of steps required to
manufacture semiconductor devices. In the first step of the process, ingots
of either silicon or gallium arsenide are cut into wafers, which are then
smoothed and polished. The second step involves chemically cleaning and
polishing the wafers in order to produce surfaces free of imperfections,
because surface imperfections might interfere with circuit or device fabrica-
tion. In the third step, the wafers are inserted into an epitaxial growth furnace
(oven) where they receive a polishing etch. A very thin layer of doped
semiconductor is then grown on top of the polished wafer surface. In the
fourth step the wafers are further cleaned, and then thickly coated with a pho-
tosensitive emulsion called photoresist, or simply resist, that hardens and
clings to the wafer surface when exposed to light. Next, a photographic
reproduction of the circuit pattern ("photomask") is aligned with the wafer.
The resist is exposed for five seconds to ultraviolet light through transparent
areas of the photomask. The fifth step involves the use of diffusion which is
an evaporative process in which the dopant-impurities such as boron, phos-
phorus, and other specific metals-is heated in a furnace, causing it to be
transformed into a gaseous state. The atoms of the dopant bombard the
wafer and enter the semiconductor substrate to form the lattice of devices
within the wafer. In the sixth and final step a thin metal film is deposited onto
the wafer surface to provide contact points for final product assembly and to
electrically connect two or more doped semiconductor layers that make up
a circuit. Once again, thorough cleaning is done prior to this final step.1
The term semiconductor actually refers to a wide range of devices
whose main functioning parts are composed of a semiconductor material;
these include transistors, diodes, thyristors, and integrated circuits. These
solid state devices have no moving parts and are used for information
processing, display purposes, power handling, and conversion of light to
energy.2
51
-------
WAFER cuTTwa,
SUOOTMNQ.AND
("GUSHING
CHEMICAL
CLEANING AND
POLBHINQ
CIRCUIT
FABRICATION
DIFFUSION
BUNTED
WAFER
EPITAXIAL
GROWTH
1
METAL
INTERCONNECTION
6
X\. WATER
CD «R
O SOUD
Transistor and diode production flowsheet
52
-------
WASTE REDUCTION ALTERNATIVES
PROCESS MODIFICATIONS
In the manufacturing of semiconductor devices there are a
number of modifications to the process that can achieve high levels
of waste reduction. A first group of modifications is linked to
housekeeping refinements. Waste stream segregation as applied
to solvents, for example, has historically shown good results.
Separation of halogenated and non-halogenated solvents, acid/
solvent mixtures, and chelated and nonchelated chemicals can
make the difference between reclamation and incineration.3 This
method, together with improving training and supervision programs
for employees and supervisors (through periodic training classes,
for instance) and the addition of signs with operating directions on
specific pieces of equipment, has generally met with good results.4
Another area where waste reduction has proven to be suc-
cessful is in the modifications to procedures and equipment em-
ployed in the manufacturing process. In particular, there has been
success in modifying the dispensing of photoresist which, although
representing only a small percentage of the hazardous waste
generated in semiconductor manufacturing, is extremely expensive
to purchase and dispose of. Typically, the manual dispensing of
photoresist leaves a residual amount which is collected and man-
aged as a waste, and this waste can total four gallons per week or
more. The use of an automated dispensing system could reduce
this residual to zero.5
Waste Reduction Potential6
Waste Segregation: N/A
Improved Training: 40 percent of D002 waste stream
Automated Dispensing of Photoresist: 50 percent of D003 waste
stream
Economics7
Waste Segregation: N/A
Improved Training: N/A
53
-------
Automated Dispensing of Photoresist: Capital Costs: $3,750 (for
each system serving 4 bottles of virgin photoresist) Annual Operating
Costs: minimal
PAYBACK PERIOD: 7 mo.
Limitations/Constraints8
Waste Segregation:
There must be sufficient room for locating necessary pipes,
pumps, tanks, and other equipment. In addition, once located,
segregation equipment may restrict the plant's flexibility for
changing or putting in new process equipment.
Installation of equipment could interrupt or otherwise ad-
versely affect ongoing production.
Safety considerations: solvents present hazards of fires.
Could lead to higher transportation costs due to fewer smaller
volume loads.
Improved Training: N/A
Automated Dispensing of Photoresist: None reported
Applicability to Other Processes
Segregation of solvent cleaning wastes is applicable to any industry
that uses solvents within the process. These industries include 3471,
3674,3979,3721, and 3728. Improved training is gene rally applicable
across all industries as a way of reducing the generation of waste. The
automated dispensing system for photoresist can also be applied to
the process of fabricating printed circuit boards (SIC 3679).
PRODUCT/INPUT SUBSTITUTION
Efforts to reduce waste in semiconductor manufacturing by means of
product/input substitution have been complicated by the dominance of
54
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applicability over availability as a criteria for considering changes. This
means that a process chemical that works to produce the widest variety of
products will often be chosen over one with more limited uses that also
happens to be recyclable or easier to manage as a waste. Nevertheless,
there are some examples of effective measures. One such measure in-
volves the substitutionof dry film resist for photoresist in the creation of the
circuit pattern on the wafer. Photoresist requires the use of chlorinated
solvents to first develop and then to strip the coating. Dry film resist is
mechanically laminated to the wafer and can be stripped using a variety of
semi-aqueous solutions.9
Waste Reduction Potential10
100 percent of F001 and F002 waste streams
Economics11
Operating costs are twice as much, but are offset to some extent by
savings on disposal or recycling of solvents.
Limitations/Constraints
None Reported
Applicability to Other Processes
This modification is also specifically applicable to the process for
fabricating printed circuit boards (SIC 3679).
MATERIALS RECOVERY/RECYCLE
Efforts to reuse process materials in semiconductor manufacturing
have been complicated by the high level of purity that is often required. There
are, however, three areas of waste generation where recovery/recycle
techniques have shown promise. The first area involves the generation of
solvent wastes. Acommonly used solvent in the fabrication of semiconductor
wafers is N-methyl pyrrolidone (NMP). In this application it is used to strip
polyamide which has been used as a passivator between layers on the wafer.
The stream of waste solvent consists of NMP with small amounts of
polyamide and water. Water from the waste stream is evaporated under
vacuum and discharged for on-site treatment. The NMP/polyamide mixture
55
-------
is boiled, allowing the NMP to be separated by flash distillation at 245° F.12
The second area in which recovery/recycle techniques have shown
promise is in the generation of waste hydrofluoric acid. In the manufacturing
of semiconductor devices, hydrofluoric acid is used in the etching of wafers.
Normally, the waste hydrofluoric acid is treated by neutralization with lime,
which process yieldsa calcium fluoride sludge that is typically landfilled. It has
been shown, however, that calcium fluoride sludge can be recovered and
used to make useable hydrofluoric acid, resulting in reuse of the original
Input.13
In the case where gallium arsenide is used as the raw material for the
wafers, significant levels of arsenic are also present in the sludge. A system
has been developed to remove arsenic from the process waste to a level that
allows the sludge to be reclassified as hazardous, due to its fluoride content,
and recovered gallium arsenide to be sold for reclaim.14
The third area in which recycling methods have had good results is in
the generation of waste oil from the furnaces used to dope the wafer surface.
The oil typically contains trace contaminants such as arsine and phosphine.
A reported alternative to offsite management of the waste oil is onsite
reclamation using a system that provides for pH adjustment, distillation, and
filtration. The system draws oil, by vacuum, from a waste oil tank through a
pre-filter, an adjustable flow control valve, and an electric heater into a
vaporizer. The resulting vapor is condensed and collected for disposal and
the purified oil is then pumped through a polishing filter and collected in a
clean oil tank for reuse.15
Waste Reduction Potential16
Solvent Recycling: 90 to 100 percent of F003 waste stream
Reclaiming arsenic wastes: significant reduction in D004 waste
stream
Recovery of Calcium Fluoride Sludge: 99 percent of Hydrofluoric Acid
waste stream
Waste Oil Reclamation: 90 percent of D001 waste stream
56
-------
Economics17
(a) (b) (c) (d)
Solvent Reclaiming Recovery Waste Oil
Recycling Arsenic of Sludge Reclamation
Capital Costs $630,000 N/A $4.3 MM $20,500
Annual O&M $21,000 $100,000 N/A N/A
PAYBACK PERIOD 1.5yr. N/A 4.5 yr. 1.1 yr.
(a)These numbers are representative of a facility designedto recycle
up to 10,000 gal of a waste over 2 to 3 weeks.
(b)These numbers are representative of a facility designed to treat up
to 5,000 gal of waste over 1 to 2 weeks.
(c)These numbers are representative of a facility designed to treat up
to 8,000 tons of waste per year.
(d)These numbers are representative of a facility designed to reclaim
20-gal/h operating once per month.
Limitations/Constraints16
Solvent Recycling:
The recycled chemicals must meet stringent purity require-
ments.
By storing used solvents on the premises, there is the risk of
having someone mistakenly reuse the dirty solvents. This
could potentially ruin a batch of wafers, which would cost
between forty and fifty thousand dollars to replace.
Reclaiming of Arsenic Wastes:None identified
Recovery of Calcium Fluoride Sludge: None identified
Waste Oil Reclamation: None identified
57
-------
Applicability to Other Processes
N/A
REFERENCES
Burckle, T. Coven, The Electronic Component Manufacturing Industry," in
Industrial Process Profiles for Environmental Use. U.S. EPA, Environmental
Research Laboratory, PB 83-299-190 (1983).
Foecke, Terry L, "Waste Minimization in the Electronics Products Indus-
tries," JAPCA, vol. 38, No. 3, pp. 283-291 (March 1988).
Johnnie, S. T., "Waste Reduction in the Hewlett-Packard, ColoradoSprings
Division, Printed Circuit Board Manufacturing Shop,"
Hazardous Waste Hazardous Materials, vol 4, No. 9 (1987).
Ryan, C. W., Hazardous Waste Source Reduction Potential in the Semicon-
ductor Manufacturing Industry. Boston Regional Source Reduction Task
Force (undated).
Pollution to Profit: Reducing Industrial Waste in Illinois. Proceedings of the
Waste Reduction Conference. Chicago, III., Document No. HW 84.02 (April
16-17,1984).
"Waste Generation and Disposition Practices and Currently Applied Waste
Minimization Techniques Within the Semiconductor Industry," Kennedy/
Jenks/Chilton, Prepared forthe Semiconductor Industry Association, State of
California Department of Health Services Waste Reduction, Grant No. 85-
00181 (1987).
58
-------
ENDNOTES
1J. Burckle, T. Coven, The Electronic Component Manufacturing Industry,"
In Industrial Process Profiles for Environmental Use. U.S. EPA, Environ-
mental Research Laboratory, PB 83-299-190 (1983).
2lbid.
9 Terry L Foecke, "Waste Minimization in the Electronics Products Indus-
tries," JAPCA, vol. 38, No. 3, pp. 283-291 (March 1988).
'"Waste Generation and Disposition Practices and Currently Applied Waste
Minimization Techniques within the Semiconductor Industry," Kennedy/
Jenks/Chilton, Prepared for the Semiconductor Industry Association, State of
California Department of Health Services Waste Reduction Grant No. 85-
00181 (1987).
5Waste Minimization.
^f. Waste Minimization. 1 988; Waste Generation. 1 987.
7Cf . Waste Generation.
8C. W. Ryan, Hazardous Waste Source Reduction Potential in the Semicon-
ductor Manufacturing Industry. Boston Regional Source Reduction Task
Force, (undated). Cf. Waste Generation.
Minimization.
"S. T. Johnnie, "Waste Reduction in the Hewlett-Packard, Colorado Springs
Division, printed circuit board manufacturing shop," Haz. Waste Haz. Mate-
rials, vol. 4, No. 9 (1987).
11 Ibid.
12Cf. Waste Minimization. 1 988; Waste Generation. 1 987.
13Pollution To Profit: Reducing Industrial Waste in Illinois. Proceedings of the
Waste Reduction Conference, Chicago, Illinois, Document No. HW 84/02
(April 16-17, 1984).
14Cf. Waste Minimization. 1 988; Waste Generation. 1 987.
15Waste Generation.
16Waste Minimization. 1988; Waste Generation. 1987; Reducing Industry.
1984.
59
-------
"Ibid.
18Waste Minimization. 1988: Waste Generation. 1987: Hazardous Waste:
Reducing Industry. 1984.
60
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OPPORTUNITIES FOR WASTE MINIMIZATION IN THE AIRCRAFT
MANUFACTURING INDUSTRY (SIC 3721 & 3728)
THE METALWORKING PROCESS
DESCRIPTION OF THE PROCESS
Metalworking involves a group of operations by which stock is re-
moved from a metal workplace by a cutting tool or abrasive material in order
to produce a desired shape and dimension. Metalworking operations include
machining, sawing, milling, grinding, drilling, turning, stamping, forging,
shaping, and heat treating.1
Most metalworking operations involve high pressure, metal-on-metal
moving contacts between tools and workplaces. These contacts result in
high friction and generation of heat. If left uncontrolled, this heat and friction
can cause excessive wear on tools and undesirable metallurgical transfor-
mations in the workplaces. To reduce these effects, metalworking fluids are
circulated over working surfaces, reducing friction, cooling the tool and the
workpiece, and removing metal chips from the work face. A variety of cutting
oils and coolants have been developed to perform these functions. These
metalworking fluids are typically stored in open reservoirs, located in either
the individual machine or in a central reservoir serving a number of similar
machines.2
Metalworking fluids are available in a range of formulations and can
be broken down into four basic categories. Straight oils are blends of
petroleum, vegetable, or animal products. Soluble oil-based fluids are a
stable emulsion of water and oil; their formulations will contain 2-12 percent
oil and use a variety of chemical additives. Synthetic fluids contain no oil and
instead use a wide range of water-soluble chemicals which provide the
needed lubrication properties. Semisynthetic products contain less oil than
soluble oil, but use a wider range of additives.3
Numerous products are manufactured through metalworking opera-
tions. These are products that are primarily composed of metal, including
such things as aircraft body parts, propellers, and fuel tanks.
61
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WASTE REDUCTION ALTERNATIVES
The primary source of waste from a metal working operation is spent
metalworking fluids. The degradation of the fluids is caused by a number of
factors: metal particles or shavings (swarf), grease, tramp oil, and dirt
accumulate in the coolants or contact oils. In addition to heat, which can
cause loss of water and depletion or breakdown of additives, bacteria, as
well, can grow in the fluid and cause it to degrade. Leaks in hydraulic seals
can result in contamination of the metalworking fluids with incompatible hy-
draulic and/or lubricating oils. When metalworking fluids no longer meet
performance requirements, they are removed from their reservoirs and must
be managed. There are a number of ways of managing these fluids that will
reduce the amount which must ultimately be disposed of.4
PROCESS MODIFICATIONS
In metalworking operations, modifications to the process will involve
improvements to the inventory of materials and procedures, fluids selection,
training of personnel, maintenance, and establishing fluid removal criteria.5
Preparing a current inventory of the metalworking, hydraulic, and lubricating
fluids used is the first step in a waste reduction program. An inventory of
waste oils generated from each operation should also be prepared. After
preparing an inventory of existing metalworking fluids and waste production,
an evaluation is needed to determine if the number and volume of different
fluids being used can be reduced. The combination of these three steps can
lead to the consolidation of fluids used in the operations and result in a
significant reduction of waste produced.6
In addition to the above three steps, training and maintenance must
also be considered. Machine operators should be educated and trained as
to proper fluid management procedures. Steps should be taken to correct
any machine-caused failure in the fluids with the goal of extending their useful
lives and reducing the amount of waste generated.7
Waste Reduction Potential6
Maintenance: up to between 66 percent and 90 percent reduction in
D001 waste stream
Economics9
Consolidation of product saves $12,000 per year
62~
-------
Limitations/Constraints10
These kinds of changes are often people-based rather than technol-
ogy-based, and can be more difficult to maintain long-term.
Applicability to Other Processes
Improved training and maintenance is broadly applicable as a first
step in any waste reduction program.
MATERIALS RECOVERY/RECYCLE
Many metalworking fluids can be reclaimed for reuse for months or
years before they are spent. There are a number of techniques that can be
used on-site for this purpose. These include settling, filtration, centrifuge,
distillation, and ultrafiltration. Typically, a combination of these processes is
used in order to achieve the desired level of removal.
Waste Reduction Potential11
From 50 percent to 98 percent of D001 waste stream
Economics12 (*)
Costs (Current $)
Filtration
Settling
Centrifuge
Distillation
Ultrafiltration
Capital
$ 300-
$1,000
$ 2,000-
$ 5,000
$10,000-
$20,000
$10,000-
$10,000-
$20,000
O&M
($/gal)
03-.08
.04-. 10
.05-.15
.05-. 15
.15-.30
PAYBACK
PERIOD
<6mo.
<6 mo.
<24 mo.
<24 mo.
<24- 36 mo.
63
-------
'These numbers are representative of a system designed to reclaim
up to 25,000 gal/yr of metalworking fluids.
Limitations/Constraints13
Settling: long holding times may be necessary to allow for fine
particles to be effectively removed and all of the tramp oil may
not be removed.
Filtration: the cost of a filtration system can vary widely de-
pending on its type and capacity. In addition, some types of
filters will not remove tramp oil from the fluid.
Centrifuge: to operate successfully, centrifuges usually re-
quire that the two materials to be separated have differences
in specific gravity of at least 2 to 3 percent.
Distillation: distillation is usually employed for oil/water mix-
tures and the temperature must be carefully regulated to avoid
degradation of the fluid.
Ultrafiltration: wastes containing from 0.1 to 10 percent oil,
with temperatures upto 150° F and havingawidepH range, are
suited to Ultrafiltration. Pretreatment by filtration is recom-
mended to keep the membranes from becoming plugged or
fouled with dirt and bacteria.
Applicability to Other Processes
These techniques are useful for any application where the removal of
solids from an aqueous solution will facilitate recovery of useable
material. Particular application, however, will require careful matching
of the technique with the waste to be recovered. Industries such as
3471,3674,3679,3721, and 3728, could probably make use of some
of these technologies in their waste reduction efforts.
Off-Site Recycle14
Not only can waste metalworking fluids be recovered on-site using one
of the technologies described in the last section, but they can also be
recovered by an off-site facility using the same technologies. The
objective of such a facility would be to reduce the cost which the
64
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individual operator must bear for proper management of spent metal-
working fluids through economies of scale. The feasibility of operating
this type of a facility was conducted in the state of Vermont employing
chemical phase separation as the recovery method.
Waste Reduction Potential
N/A
Economics?*)
Capital Costs:$140,550
Annual O&M:$127,490
PAYBACK PERIOD: <11 mo.
(*)These numbers are representative of a facility operating at 600 hrs./
yr. to treat up to 300 gal. of waste.
Limitations/Constraints
None Identified
Applicability to Other Processes
The general concept of off-site treatment has been applied in other
industries with success. The key deciding factor will be the economic
feasibility of the facility, since many of the same technologies are
employed whether on- or off-site.
REFERENCES
Gordian Associates, Inc., Technical and Economic Analysis of Waste Cool-
ant Oil Management Options in Vermont. Agency for Environmental Conser-
vation, Montpelier, VT (1980).
Higgins, Thomas. Hazardous Waste Minimization Handbook. Lewis Publish-
ers, Inc., Chelsea, Michigan, 1989.
Hunt, Gary E., 'Waste Reduction in the Metal Finishing Industry," JAPCA, vol.
38, No. 5, pp. 672-680 (May 1988).
Kohl, J. and Currier, J., Managing Waste Oils. North Carolina Pollution
Prevention Pays Program, Raleigh, NC (1987).
65
-------
ENDNOTES
Thomas Higgins. Hazardous Waste Minimization Handbook. Lewis Publish-
ers, Inc., Chelsea, Michigan, 1989.
2lbid.
3Jbjd,
4lbid.
5Gary E. Hunt, "Waste Reduction in the Metal Finishing Industry," JAPCA,
vol.38, No. 5, pp. 672-680 (May 1988).
"Minimization Handbook.
7lbid.
"Ibid.
9J. Kohl and J. Currier, Managing Waste Oils. North Carolina Pollution
Prevention Pays Program, Raleigh, NC, 1987.
"Minimization Handbook.
"Ibid.
12M1.
13Cf. Minimization Handbook. 1989; Waste Reduction. 1988.
14Gordian Associates, Inc., Technical and Economic Analysis of Waste
Coolant Oil Management Options in Vermont. Agency for Environmental
Conservation, Montpelier, VT, 1980.
66
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OPPORTUNITIES FOR WASTE MINIMIZATION IN THE AIRCRAFT
MANUFACTURING INDUSTRY (SIC 3721 & 3728)
THE PAINTING PROCESS
DESCRIPTION OF THE PROCESS
The painting process is the process of applying an organic coating to
a workplace. Paints that are applied to the surface of parts, components, and
assembled products forpurposes of corrosion protection, surface protection,
identification, and aesthetic appeal, are usually solvent-based. Most painting
is performed by conventional liquid spray technology, although application by
dipping, brushing, powder and roll coating is also used. In spray painting, the
paint is mixed with a carrier, usually an organic solvent, and is applied to the
surface with an air-pressurized sprayer. Spray painting is usually done in a
horizontal or downdraft paint spray booth. The paint can be sprayed
manually or automatically, hot or cold. During typical spray painting, 50
percent of the paint is deposited on the surface being painted; the other 50
percent, called overspray, is sprayed into the air. After use, the painting
equipment is cleaned using solvents.1
WASTE REDUCTION ALTERNATIVES
Painting processes generate two significant sources of hazardous
wastes: paint sludge and waste solvents. The first and largest volume of
hazardous waste generated in painting involves air emissions that create
paint sludge. The air from a paint booth is often exhausted through a water
scrubber that separates the paint from the air. The scrubber water is normally
recycled, and paint solids are concentrated as sludge in the scrubber sump.
The second significant source of hazardous waste is the use of solvents to
clean painting equipment. Most paints are solvent-based, so they require
solvents for cleanup. The type of solvent used varies with the paint. Some
of the more common solvents are methyl ethyl ketone (MEK), xylene, 1,1,1-
trichloroethane, and toluene.2
Alternatives to conventional solvent-based spray painting are avail-
able and can reduce hazardous pollutants. These alternatives require an
integrated approach in which painting technologies are improved and proc-
67
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esses are used to reduce or eliminate hazardousmaterials. The more
promising developments in the area of painting modifications and substitu-
tions are discussed below.3
PROCESS MODIFICATIONS
There are a number of modifications to the conventional painting
process that can lead to the reduction or elimination of hazardous wastes.
These alternative techniques include powder coating technologies such as
electrostatic dry powder painting, fluidized bed powder coating, and plasma
spray powder coating. The powder coating technologies involve depositing
specially formulated thermoplastic, or thermosetting, heat-fusible powders
on metallic substrata. Productivity is increased because, with these tech-
niques, the coating can be cured immediately after application and in a
shorter period of time. These techniquesare also readily adaptable to current
production methods and are easily learned by painting personnel.4
Electrostatic painting, electrocoating, and pressure atomized air-
assisted spray painting, as well, have been shown to be an improvement over
conventional spray painting. In the electrostatic painting method, paint is
sprayed onto the surface, where it is electrostatically deposited. While some
solvent is used as a thinner in this process, the content is lower than in
conventional spray painting. Overspray is minimized, if not entirely elimi-
nated, thus resulting in hazardous waste reduction.8
In the electrocoating process, metallic parts or other electrically
conductive parts are dipped into a solution that contains specially formulated
ionized paint. The action of an electric current induces the paint ions to
deposit on the part. The paint formulations are a special class of waterborne
nonvolatile organic compounds. Hazardous waste production is minimal,
and VOC air emissions are almost eliminated.6
For the pressure atomized air-assisted spray painting technique, an
airless fluid spray tip is used to atomize the coating into a fan pattern at
moderate pressures; a second low-pressure air stream is injected just after
the nozzle to improve atomization and spray pattern. This system is reported
to provide the finer control of air spraying, with less overspray, and a higher
transfer efficiency than airless spray.7
68
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Waste Reduction Potential8
Powder Coating Techniques:
80 percent to 99 percent reduction in D001 waste stream.
Undetermined reduction in F002, F003, and F005 waste
stream.
Electrostatic Painting:
30 percent to 99 percent reduction in D001 waste stream.
Undetermined reduction in F002, F003, and F005 waste
stream.
Pressure Atomized Air-assisted Spray Painting:
30 percent to 40 percent reduction in D001 waste stream.
Undetermined reduction in F002, F003, and F005 waste
stream.
Economics9/*)
Percent Transfer Efficiency
(a) (b)
40 60 80 100
Total Annual O&M $257,520 $166,120 $120,390 $93,000
(1985$)
OThese costs are based on annual costs for a typical small shop
within a representative segment of the spray coating industry.
(a)This column is representative of costs forthe average conventional
paint spray technology.
(b)These three columns are representative of the average ranges in
cost forthe alternative painting technologies described above. Pres-
sure atomized air-assisted spray painting would be at the lower end
of the range, powder coating would be at the higher end, with
electrostatic painting typically in the middle.
69
-------
Limitations/Constraints10
Powder Coating Techniques: the items to be painted must be
able to withstand the typical curing temperatures of 350° F for
30 minutes. Aluminum alloys cannot be subjected to these
conditions without significant loss of strength.
Electrostatic Painting: one of these techniques, electrocoat-
ing, requires the use of dip tanks. This necessarily limits the
size of items that can be painted. More importantly, this
technique can be used to apply only one coat because the
electrocoated surface prevents further electrodeposition.
Pressure Atomized Air-assisted Spray Painting: none Iden-
tified
Applicability to Other Processes
These techniques are broadly applicable to processes that involve
applying paint to a surface. There are some variation depending on
the type of surface (I.e. plastic, wood, metal, or other), but these tech-
niques could be used in most instances.
PRODUCT/INPUT SUBSTITUTION
In addition to modifications to the painting process itself, waterborne
and high-solids coatings can be used as a substitute for organic solvent-
based coatings. In waterborne coatings, the carrier is a water solvent rather
than an organic solvent. Waterborne paints are normally used where
surfaces require only moderate protection and where decorative require-
ments are most important. Fewer hazardous pollutants are generated when
using waterborne paints because the volume of solvents used are reduced
and the solvents used comply with air pollution control regulations. In
addition, no solvents are needed for paint thinning, and the use of solvents
for cleanup is greatly reduced.11
High-solids solvent based coatings, which are similar in composition
to conventional solvent-based coatings, are becoming more widely used in
industrial applications. These coatings contain about 25 percent to 50
percent solids and, compared to solvent-based coatings, use lower molecu-
lar weight paint resins with highly reactive sites to aid in coating polymeriza-
70
-------
tion. High-solids coatings require special spray equipment for application
because of their high viscosity. This technology improves the efficiency of
paint application as well as reducing waste generation. Reduced use of paint
results in less solvent to evaporate in leaving the final paint film. Reducing
overspraymeans less paint sludge to be removed from a water-wall scrubber,
or less paint to be eventually stripped off the walls or floor of a paint booth.
The resulting finished coat is comparable to typical solvent-based coatings.12
Waste Reduction Potential13
Water-Borne Coatings:
70 percent to 85 percent reduction in D001 waste stream.
Undetermined reduction in F002, F003, and F005 waste
streams.
High Solids Coatings:
50 percent to 70 percent reduction in 0001 waste stream.
Undetermined reduction in F002, F003, and F005 waste
streams.
Economics14
Current costs for these alternative paint formulations are higher than
for conventional solvent-based paints, but this higher cost must be
balanced against the disposal cost savings.
Limitations/Constraints15
Waterborne Coatings: the surface to be painted must be
completely free of oil-type films or the paint will not adhere well.
Also, waterborne coatings require longer drying times or even
oven drying in cold or humid weather; this requirement may
result in significant expense to outfit a facility for waterborne
paints.
High-Solids Coatings: surface preparation to remove oils is
critical to the success of this technology. Also, spray applica-
tions can be wasteful because there is a tendency to apply too
much coating to achieve a "wet" appearance similar to that
obtained with normal solvent coatings.
71
-------
Applicability to Other Processes
These alternative paint formulations are applicable to all processes
involving the application of paints.
MATERIALS RECOVERY/RECYCLE
With paint sludge disposal costs in an upward spiral, and paint and
solvent costs following suit, some businesses are turning to recycling paint
overspray. Typically, the overspray is in the from of sludge. In the sludge
recovery process, the first step is to re-dissolve everything that is soluble in
the sludge. Some of the paint sludge will remain in its polymerized form as
lumps. The next step is to filter out or centrifuge the non-soluble lumps.
Essentially all the pigment is saved. Some binders, resins, solvents or other
ingredients are added to bring the paint back close to its original condition.16
Waste Reduction Potential17
80 percent to 99 percent reduction in D001 waste stream.
Economics1^*) (1981$)
Monthly savings of $20,000 in paint costs and $3,000 in sludge
disposal costs.
(*)These numbers are representative of a company generating 10055
gal. drums of sludge per month.
Limitations/Constraints
None Identified
Applicability to Other Processes
Recycling of paint overspray sludge is broadly applicable to all
processes that make use of paint.
72
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REFERENCES
Campbell, M. and Glenn, W., Profit from Pollution Prevention: A Guide to
Industrial Waste Reduction and Recycling. Pollution ProbeFoundation, Toronto,
Canada, 1982.
Duletsky, B. W. and Newton, D. L, The Use of Process Modifications in
Reducing Industrial Wastes from Spray Coating Operations." 1985 Triangle
Conference on Environmental Technology. Raleigh, NC.
Higgins, Thomas, Hazardous Waste Minimization Handbook. Lewis Publish-
ers, Inc., Chelsea, Michigan, 1989.
73
-------
ENDNOTES
1Thomas Higgins, Hflgfifdpus Waste Minimization Handbook. Lewis Publish-
ers, Inc., Chelsea, Michigan, 1989.
2lbid.
3lbid.
4lbid.
5lbid.
6Mi.
7lbid.
8M. Campbell and W. Glenn, Profit from Pollution Prevention: A Guide to
Industrial Waste Reduction and Recycling. Pollution Probe Foundation,
Toronto, Canada, 1982.
9B. W. Duletsky and D. L. Newton, The Use of Process Modifications in Re-
ducing Industrial Wastes from Spray Coating Operations," 1985 Triangle
Conference on Environmental Technology. Raleigh, NC.
10Cf. Minimization Handbook. 1989: Pollution Prevention. 1982.
"Minimization Handbook.
"Ibid.
13PollutiQn Prevention.
14Jbid.
15Cf. Minimization Handbook. 1 989; Pollution Prevention. 1 982.
16Pollution Prevention.
"Ibid.
74
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OPPORTUNITIES FOR WASTE MINIMIZATION IN THE
ELECTRIC SERVICES INDUSTRY (SIC 4911)
THE FOSSIL-FUELED STEAM ELECTRIC POWER
PRODUCTION PROCESS
DESCRIPTION OF THE PROCESS1
There are five major unit processes involved in the generation of
electric power from fossil fuel: the storage and handling of fuel related
materials both before and after usage, the production of high-pressure
steam, the expansion of the steam in a turbine which drives the generator, the
condensation of the steam leaving the turbine and its return to the boiler, and
the generation of electric energy from the rotating mechanical energy. In
addition to these major processes, maintenance, repair, cleaning of the
generation, transmission, and/or distribution equipment is routinely per-
formed. Figure 1 shows a schematic flow diagram of a typical steam electric
powerplant.
All fuels must be delivered to the plant site, stored until usage, and the
spent fuel materials stored on the premises or removed. The combustion of
fossil fuels results in gaseous products of combustion and non-gaseous non-
combustible residues called ash. A portion of the ash, which is referred to as
fly ask, is carried along with the hot gases. The remainder of the ash settles
to the bottom of the furnace in the combustion zone and is called bottom ash.
Coal produces a relatively large amount of bottom ash and fly ash. Oil
produces little bottom ash but substantial fly ash. Gas produces little ash of
any type.
The production of high-pressure steam from water involves the
combustion of fuel with air and the transfer of the heat of combustion from the
hot gases produced by the combustion to the water and steam by radiation
and convection. In order to obtain the highest thermal efficiency, as much of
the heat of combustion as possible must be transferred from the gases to the
steam and the gases discharged at the lowest possible temperature. This
requires the transfer to be accomplished in a series of steps, each designed
for optimum efficiency of the overall process.
75
-------
Stock LJSJ
Arm
(U S. EPA, Development Document tor Effluent Limitations Guidelines and
Standards for the Steam Electric Power Generation Point Source Category
EPA-440/1-74/029-a, Washington DC (1974))
Net Pow Loss
Net Power
L/L/L/
Hl^i Pressure BaedHeaas
T7T7
Lov Prassun fltood HosiBfi
Boflsr Food Rxnp
-------
The conversion of the pressure energy of the steam into mechanical
energy occurs in the steam turbine. In the turbine the steam flows through
a succession of passages made up of bladesmounted on alternately moving
and stationary discs. As the steam passes from disc to disc, it gives up its
energy to the rotating blades and in the process loses pressure and increases
in volume.
Steam electric powerplants use a condenser to maintain a low turbine
exhaust pressure by condensing the steam leaving the turbine at a tempera-
ture corresponding to vacuum conditions, thus providing a high cycle
efficiency and recovering the condensate for return to the cycle. The
condenser consists of a shell with a chamber at each end, connected by
banks of tubes. They can be either single-pass or two-pass, depending on
whether steam passes through the tubes in one or two directions. Steam
passed into the shell condenses on the outer surface of the cooled tubes.
The actual generation of electric energy is accomplished in a genera-
tor, usually directly connected to the turbine. The generator consists of a
rotating element called a rotor revolving in a stationary frame called a stator.
The process converts mechanical energy into electric energy at almost 100
percent of theoretical efficiency and therefore produces little waste heat.
WASTE REDUCTION ALTERNATIVES
The hazardous wastes generated from the production of electricity
come from the indirect activities-maintenance, repair, and cleaning-rather
than the direct process of generating electricity. The maintenance and repair
of process equipment typically requires the use of machining tools which
make use of various lubricating oils and coolants. In addition, repair practices
often yield waste transformer oil that contains PCB's. Much of the process
equipment is routinely cleaned using either solvents or alkaline cleaners.
Cleaning descale from the inside of the boilers is contaminated with various
levels of heavy metals. Also, painting and other activities produce hazardous
waste. Much of the techniques that can be used to minimize the amounts of
these wastes that must be disposed of are those which are used in other
industries such as metalworking, solvent cleaning, and electroplating.
Product/Input Substitution
Often basic cleaning solutions and other chemicals which may test
hazardous for disposal purposes can be substituted forwith solutions
that may not be hazardous. For example, one power station has
77
-------
substituted a nonhazardous water-based citric acidparts washing
solvent for a chlorinated solvent (1,1,1 Trichloroethane) in much of
their routine cleaning activities.
Waste Reduction Potential2
75 percent reduction in F002 waste stream
Economics3
Realized annual savings of $7,200 in avoided disposal costs
Limitations/Constraints
None identified
Applicability to Other Processes
This technique can be broadly applied to all equipment and parts
cleaning operations depending on the desired level of removal. These
types of operations would be found in such industries as 3471,3674,
3679, 3721, and 3728.
Materials Recovery/Recycle
Much of the waste oils and painting wastes produced as a result of
powerplant maintenance can be effectively managed on-site using
proven techniques. In particular, powerplants have been able to
manage waste transformer and lubricating oil as well as paint wastes
using various technologies. One plant has used the waste trans-
former oil containing PCB's as a fuel supplement in its coal-fired
boilers. In addition to recovering the BTU value of the oil, this practice
has been shown by extensive stack emission testing to achieve
greater than 99.9999 percent destruction efficiency for PCB's. An-
other production facility has had good results with burning waste
lubricating oil in its boilers. Spent clean up thinners are being
segregated from other thinners and paints at a production facility in
order to facilitate on-site recovery by distillation.4
78
-------
Waste Reduction Potential5
Waste Oils as Fuel Supplements:
One plant burned 250,000 gallons of transformer oil.
One plant burned 138,000 gallons of lubricating oil.
Distillation of Paint Wastes: 80 percent to 90 percent reduction in F005
waste stream.
Economics6 (1988$)
Transformer Oil: produced annual savings of $916,400 in avoided
disposal cost and $62,000 in fuel costs.
Lubricating Oil: need to getl
Distillation of Painting Wastes: (*)
Annual Operating Costs $ 8,542
Avoided Disposal Costs $14,900
NET COST SAVINGS $6,358
OThese costs are based on six hours recycling time every two months
and an 80 percent recovery rate.
Limitations/Constraints
None identified
Applicability to Other Processes
On-site burning of waste oils would be difficult to apply because of the
need for bringing an incineration unit on-site. In most other cases
where waste oils are produced, off-site management would probably
be more feasible. On-site recovery of painting wastes, however, can
be applied to other processes that apply paints and other coatings.
Such industries as 3721 and 3728 would be included in this group.
79
-------
Off-Site Recycle
Sending wastes off-site for recovery and reuse is another viable option
for many of the hazardous wastes produced at a power plant.
Specifically, spent solvents and cleaners have been sent off-site by
power plants for either recovery orto be used as a fuel substitute. Also
lead and mercury wastes have been sent off-site for recovery. One
plant has used a recycling service for dirty parts washer solvent and
methylene chloride/cresylic acid carburetor cleaner fluid. Another
sends spent solvents and solvent-contaminated waste oil to a fuel
blenderto be used as afuel substitute. Other facilities collect lead-acid
batteries, scrap lead, and liquid mercury from power plant instrumen-
tation and sell them to a recycler.7
Waste Reduction Potential8
Solvent recovery: 100 percent reduction in F002, F003, F004, F005
waste streams.
Solvent as Fuel Substitute: 100 percent reduction in D001, F002,
F003, F004, F005 waste streams.
Lead and Mercury Recovery: 100 percent reduction in D008 and
D009 waste streams.
Economics2 (1988$)
Solvent Recovery: saved $2,548 in avoided disposal costs and
$8,060 in avoided product costs. (*)
Solvent as Fuel Substitute: cost savings of $23,000 overdisposal cost
as a hazardous waste.
Lead and Mercury Recovery: in addition to avoided cost of disposal,
lead recovery provided $500 of revenue. (**)
OThese numbers are based on recycling 27,000 pounds of spent
solvent.
("JThese numbers are based on the recovery of 109,000 pounds of
lead.
80
-------
Limitations/Constraints
None identified
Applicability to Other Processes
Off-site recovery of solvent and the use of solvent as a fuel substitute
can be applied to any process where solvent wastes are produced.
This would include such industries as 3471,3674,3679,3721,3728.
REFERENCES
Duke Power Company, 1988 entry for the Governor's Award of
Excellence for Outstanding Achievement in Waste Management.
U.S. EPA. Development Document for Effluent Limitations Guidelines
and Standards for the Steam Electric Power Generation Point Source
Category. EPA-440/1-74/029-a, Washington, DC (1974).
81
-------
ENDNOTES
development Document for Effluent Limitations Guidelines and Standards
for the Steam Electric Power Generation Point Source Category. EPA-440/
1-74/029-a, U.S. Environmental Protection Agency, WAshington, DC (1974).
2Duke Power Company, 1988 entry for the Governor's Award of Excellence
for Outstanding Achievement in Waste Management.
3lbid.
4lbid.
5lbid.
6jbjd,
7lbid.
"Ibid.
82
-------
Appendix E
Results of WM-form Analysis
-------
8/18/89
WASTE MINIMIZATION
Page 1
ID#
AK1570028695
AK3570028677
AK5570028618
AK5570028691
AK6570028716
AK8690360492
AK8690360492
AK9570028697
AKD00924371B
AKD0354 17872
AKD041331067
AKD052581758
AKD980983001
IDD000602631
IOD067550103
ID0067979922
IDD980978183
ID0980985808
1DD990727471
OR621 382091 7
OR6213820917
OR0000403485
ORD000602490
ORD000604652
ORD000773937
ORD000813071
ORD007908304
ORD007908304
ORD007908304
ORD007908304
ORD007908304
ORD009020470
ORD009020603
ORD009024613
ORD009024613
ORD009024613
ORD009029893
ORD009038761
ORD009040973
ORD009049198
ORD009101965
ORD0094 12370
ORD0094 12602
ORD009623729
ORDOS4263S9S
ORD057070948
ORD081 182180
ORD084426089
OTY GEN
1986
1,700
366
1.700
366
294
84,000
70,000
366
500
490
6,307
4,070
495
31
37
600
4,235
600
573,200
305
1,765
98,775
4,016
9,240
660
28,277
26,452
11,757
30,660
400
200
1,980
7,000
15,920
0
475
1,233
130
1.485
55
1,300
25,200
103
23,518
510
1.155
1.895
2,800
OTY GEN PROD WASTE MIN
1987 RATIO PERCENTAGE
1,700
366
1.700
366
294
70.000
45,600
366
50
230
3,290
350
495
32
20
600
1,897
600
484,340
280
440
97.400
3.828
2,640
330
21,878
32,120
5,280
38,095
600
920
1,320
4,000
10,560
935
275
550
120
220
0
400
8,250
92
2,558
135
495
1,526
800
.00
.00
.00
.00
.00
.00
.00
.00
.00
.47
.52
.00
.00
1.19
.97
1.01
1.00
1.01
1.42
.93
.25
1.18
.84
1.68
.10
.31
.20
.45
.20
.50
4.60
1.45
1.00
1.23
1.23
1.23
.99
1.04
.91
1.00
1.00
1.00
1.14
.11
1.14
.97
1.18
1.00
0.00
0.00
0.00
0.00
0.00
-16.67
-34.86
0.00
-90.00
-.13
.32
-91.40
0.00
-13.26
-44.27
-.99
-55.21
-.99
-40.49
-1.29
-.28
-16.43
13.47
-82.99
-54.55
-40.94
1.19
-.20
3.54
0.00
.00
-54.02
-42.86
-46.07
0.00
-52.93
-54.94
-11.24
-83.72
-100.00
-69.23
-67.26
-21.65
-1.12
-76.78
-55.82
-31.76
-71.43
QUANTITY QUANTITY
RECYCLED PREVENTED
1,700
366
1.700
366
294
70,000
45,600
366
0
710
495
50
280
440
97,400
2,255
200
21 ,878
1,320
1,500
0
935
275
120
220
8,250
92
2,300
1,526
0
0
0
0
0
14,000
24.400
0
450
200
3.720
495
5
16
0
2,338
0
329,604
4
12.880
396
15.165
1.551
3,000
9,021
309
671
15
1.131
900
16,950
25
29
446
625
710
2.000
SOURCE
DIESEL POWER GENERATION
DIESEL POWER GENERATION
DIESEL POWER GENERATION
DIESEL POWER GENERATION
SPENT BATTERIES (LEAD ACID
WASTE PRODUCTS FROM INDUSTRIAL SANDBLASTING SHED CONTAINS PAINT C
DIESEL POWER GENERATION
COMPRESSOR BLOW DOWN AND MAINTENANCE
SOLVENT FILTERS & STILL BOTTOMS
PCS OIL FROM TRANSFORMERS
USED OIL FROM VEHICLE MAINTENANCE WHICH MAY HAVE BEEN MIXED WITH
SOLVENT USED FOR CLEANING EQUIPMENT PARTS
FILTERING CONTAMINATED GROUNDWATER THROUGH ABSORBING AND ADSORBIN
THERMAL PROCESS
DISTILLATION & FILTRATION OF DRY CLEANING SOLVENT
WASTE EVOLVED AS A RESULT OF LABORATORY
DISTILLATION & FILTRATION OF DRY CLEANING SOLVENT
WASTE PRETREATMENT SYSTEM
VEHICLE ENGINE REPAIRS OR CARRIAGE MAINTENANCE ACTIVITIES
SMALL ARMS AMMUNITION DESTRUCTION BY INCINERATION
PANEL COATING LINE
SOLVENT WASH CLEANING
INGOT AND SLUG ETCHING PROCESS
SOLVENT CLEANING
PAINT MIX TANK CLEANING
PCB CONTAMINATED DISTRIBUTION TRANSFORMERS REMOVED FROM THE ELECT
PCB CONTAMINATED DISTRIBUTION TRANSFORMERS REMOVED FROM THE ELECT
PCB CONTAMINATED DISTRIBUTION TRANSFORMERS REMOVED FROM THE ELECT
PCB CONTAMINATED DISTRIBUTION TRANSFORMERS REMOVED FROM THE ELECT
PCB CONTAMINATED DISTRIBUTION TRANSFORMERS REMOVED FROM THE ELECT
TANK & CONTAINER WASH.
WASTEWATER EVAPORATOR
COATING OF PLATE FOR THE MANUFACTURE OF METAL CONTAINERS
MACHINE WASH UPS
DECREASING REPAIR PARTS
PRINTING PRESS CLEAN-UP
ELECTROLYTIC MAGNESIUM
OIL FROM MACHINES AND SOLVENTS FROM PARTS CLEANING TANKS.
CHEMICAL REMOVAL OF PAINT
ROUTINE PAINTING RESIDUALS
ROUTINE PRODUCTION OPERATIONS
MANUFACTURING TANK & EQUIPMENT CLEANING
SOLVENT BATH
LIQUID SCINTILLATION COUNTING
HOLLIS WAVE SOLDERING MACHINE
CALCULATOR SERVICE CENTER/BATTERIES FROM REPAIR OF CALCULATORS/CO
PLATING (DRYING PROCESS)
SIC
9711
9711
9711
9711
9711
3449
9711
2813
7216
4911
4612
4612
9511
2491
7216
8221
7216
3577
9711
9711
2493
2851
3679
3324
5198
4911
4911
4911
4911
4911
2851
2491
3411
3411
3411
2711
3339
3411
3499
2611
2434
2851
3699
8733
3679
3433
RCRA WASTE CODES
D001
D001
D001
D001
0001
D002
D004
D001
F001
F002
H71
D008
F001
U051
F001
?
F001
F006
D002
D003
F003
F003
U032
F002
F005
7
?
?
?
?
F003
K001
F003
P001
F001
D001
0003
D001
F002
D001
D001
F003
F003
U019
D008
D008
D001
D008
D005
D001
H72
D008
D008
F005
F005
U134
F003
U080
F003
F003
F005
D009
D009 0010
D006 D007
N44 N72
D006
D001
F005
F004 F005
D006
-------
8/18/89
WASTE MINIMIZATION
Page
I0#
ORD084426089
ORD084426089
ORD084426089
ORD084426089
ORD084426089
ORD084426089
OR0088597992
OR0096249081
OR0096253737
ORD096253737
ORD096253737
OR0980665350
OR0980837322
OR0980837322
ORD980837322
OR0980975320
ORD980985550
ORD980985550
OR098098SSSO
OR098098SS50
ORD98098SS50
ORD980985550
ORD990659492
ORD991281619
WA2 1700234 18
WA2 1700234 18
WA9571 924647
WAD000065508
UAD000065508
WA0000065508
WAD000602813
WA0000617902
WA0000618140
WA0000618140
WAD000711598
WAD000711846
WA0000814004
UAD000814004
UA00049086S3
WA0009051871
WAD009052978
WAD0090S8S04
UAD009062332
WAD009063S46
WAD009063546
WAD009065145
UAD009238668
WAD009241621
WAD009241621
QTY GEN
1986
4,400
69,420
2.610
2.000
2,800
11,400
450
1,045
76,000
610,000
180,000
162,840
5,500
19,106
8.799
330
1,625
36
2,947
660
1,364
8.005
385,100
34,530
62.727
13,275
1.435
1.195
25,050
20
117
1,000
731
144
126,440
30,390
0
164,000
63,800
62,060
8,500
16,560
6,500
26,373
20.873
2,310
900
50.738
0
OTY GEN
1987
1.600
27.145
890
400
400
2.550
450
715
47.000
490,000
38,000
76,644
2,959
35.213
6,707
660
2,350
24
2,934
660
900
5,415
278,870
20,945
24.400
5,796
1,355
1,219
35,980
0
79
1,000
1,660
1,645
174.750
24,538
25,400
103,000
56,216
28,958
4,800
4.840
6,000
20,090
5,225
1,700
1.452
42.350
156,213
PROD WASTE MIN
RATIO PERCENTAGE
1.00
1.00
1.00
1.00
1.00
1.00
1.25
.68
1.11
1.11
1.11
.91
.54
1.84
.76
2.00
1.32
1.32
1.32
1.32
1.32
1.32
1.05
1.24
1.23
.44
1.00
1.47
1.47
1.47
.84
1.00
.96
.96
1.47
1.20
.47
.47
1.22
.99
.98
.98
.92
1.22
1.22
.85
1.06
1.05
1.05
-63.64
-60.90
-65.90
-80.00
-85.71
-77.63
-20.00
.62
-44.29
-27.63
-80.98
48.28
-.37
.16
.30
0.00
9.56
-49.49
-24.58
-24.24
-50.01
-48.75
-31.03
51.08
-68.38
-.77
-5.57
-30.61
-2.29
-100.00
-19.62
0.00
136.55
1,089.96
-5.98
-32.71
0.00
33.63
27.78
52.87
-42.38
70.18
.33
-37.56
-79.48
-13.42
52.20
-20.51
0.00
QUANTITY QUANTITY
RECYCLED PREVENTED
323,000
0
0
0
2,350
2.851
163
3,139
278,870
24,400
5,346
1,000
1,219
75
900
935
1,380
0
9.800
25,400
103.000
56,216
0
3,600
4,840
5,640
13,688
5,225
1.700
1,452
0
156,213
2,800
42,275
1.720
1,600
2,400
8,850
113
37,000
190,000
160,000
71,540
11
58
20
800
24
956
211
900
5,152
106,230
21,874
52,754
45
538
844
29
0
760
11,290
11,930
32,481
11,389
12,085
20,240
264
12
10,925
SOURCE
SPRAY PAINTING
ELECTROPLATING WASTE TREATMENT SLUDGE
ELECTROPLATING (FILTERS)
PAINTING & DRYING PROCESS
SILVER SOLDERING (COOLING WATER)
DECREASING ft DIP PAINT
BATCH TANK STRIPPING OF NICKEL PLATE OF HAND TOOLS PRIOR TO REWOR
SOLVENT CLEANING OF APPLICATION ROLLS.
CLEANING OPERATIONS
CLEANING OPERATIONS
ETCHING PROCESS
ZINC COATINGS STRIPPED FROM PARTS TO BE RE-WORKED AND FROM RACKS
TRANSFORMER MAINTENANCE AND REBUILD
TRANSFORMER MAINTENANCE
TRANSFORMER MAINTENANCE
SLUDGE
SOLDERING
DIELECTRIC HEAT TRANSFER
SOLVENT VAPOR DECREASING
SOLVENT BATH DECREASING
DIELECTRIC HEAT TRANSFER
SOLVENT VAPOR DECREASING
GROUNDWATER AND RAINWATER TREATMENT
PROCESS CLEANING SOLUTION
PARTS CLEANING
PARTS CLEANING
SOLVENT BATH DECREASING
PARTS CLEANING
ELECTRIC ARC FURNACE DUST
DECREASING OF ELECTRICAL PARTS
RE METING STEEL SCRAP IN ELECTRIC ARC FURNACE TO PRODUCE INGOTS F
SOLVENT WASHINGS OF PAINT MIXING TANKS
DECREASING PROCESSES
DECREASING PROCESSES
TANK WASHINGS CONTAINING PHOSPHATE
ELECTRONIC COMPONANT CLEANING
SHIP CONSTRUCTION- FLUSHING ft DECREASING OF PIPE SYSTEMS
PAINTING OF SHIP UNDER CONSTRUCTION AND REPAIR
THE MANUFACTURE OF POLYESTER AND EPOXY COATINGS FOR THE FIBERGLAS
PRINTING INK
STILL BOTTOMS FROM THE RECOVERY OF PAINT MANUFACTURING CLEAN-UP 0
CLEAN-UP OF TOOLS AND EQUIPMENT
COLD CLEANING PRIOR TO ASSEMBLY
TANK CLEANING AND SPRAYING OPERATIONS FROM PAINT AND COATINGS HAN
TANK CLEANING AND SPRAYING OPERATIONS FROM PAINT AND COATINGS MAN
PAINTING CLEANUP
PAINTING AUTOMOBILES
LATEX PAINT CANNING WASH CHEMICALLY SETTLED AND SOLIDIFIED
LATEX PAINT CANNING WASH
SIC
3433
3433
3433
3433
3433
3433
3423
2493
3333
3333
3333
3479
4911
4911
4911
2491
3669
3669
3669
3669
3669
3669
2818
5085
3731
3731
9711
3334
3334
3334
3462
2851
3672
3672
2899
3577
3731
3731
2821
2656
2851
3732
3714
2851
2851
3559
7532
2851
2851
RCRA WASTE COOES
F005
F006
D002
F003
D006
F001
D001
F005
F001
F001
D007
D002
D004
D008
F001
F001
F001
D002
F002
D001
D001
D001
D008
F001
D007
0001
D001
D001
D007
F001
F001
F003
D001
D001
F003
F001
F003
D009
F005
D001
0009
D009
F003
D002
D008
0007
D007
D008
0007
F001
F003
D008
D001
FOOS
0008
FOOS
0001
0001
D008
D008
F002
D006 D007
F003
F003 FOOS
F002
F003
-------
8/18/89
WASTE MINIHIZATION
Page 3
I0#
WAD009241621
WAD009248287
UAD009249509
UAD009249509
WAD009249509
WAD009249863
WAD009249863
WAD009249863
WAD009251042
WAD009252719
WAD009255548
WAD009255548
WAD009255548
WAD009255647
WAD00925B468
WAD009262171
WAD009262171
WAD009262171
WA0009262171
WAD009262171
WAD009264730
WAD009270794
WA0009274234
WAD009274234
UAD009422411
WAD0094 23682
WAD012425385
UA0019419928
WAD027438910
WAD027543032
UAD029131125
WAD04 13335 19
WAD04 1585464
WA004 1585464
UA004 1585464
UAD04 1585464
WAD04 1585464
UAD04 1585464
WAD041920554
UAD044599645
WAD04459964S
UAD047494331
WAD048440424
UAD053814091
WAD053814091
WAD05 7068561
UAD057068561
WAD057068561
WA005 7068561
WAD057068561
OTY GEN
1986
23.338
25.000
63,500
1.300
28.308
8,512
48,825
53,980
84,240
11
10,500
10,500
10,500
117.000
234,611
10,500,000
88
31
119
1,098,100
224
2,000
703
1,434
5,867
8,867
7,645
3,915
6,825
3.000
4,840
800
9,590,942
661
2.544
205
597
21,752
39,735
23,632
1,466
1,040
2,310
110,840
58,500
8,365
6,500
240
36
8,500
OTY GEN PROD WASTE NIN
1987 RATIO PERCENTAGE
36,225
6,600
77,000
13.600
32,205
3,317
42,424
54,648
57,870
A
6,850
6,850
6,850
88.200
498,312
2,000,000
1
32
185
1,330,600
109
1,400
2,998
605
15,867
550
6,145
.10
.05
.27
.27
.27
.14
.14
.14
.20
.00
.53
.53
.53
.29
.85
.20
.20
.20
.20
.20
.03
.10
.93
.93
.26
.21
.01
4,000 1.15
2,240 1.25
2,000 2.00
3.440 1.55
0 1.10
10,022,901 .85
230 .85
5.950 .85
913 .85
4,822 .85
23,926 .85
35.000 1.15
22,555 1.08
11.118 1.08
1,040 1.22
9,940 .91
46,550 .53
81,250 .19
5.630 .03
5.480 .03
240 .03
36 .09
118,124 .03
41.11
-74.86
4.52
723.74
-10.42
-65.82
-23.78
-11.20
-42.75
-18.18
-57.36
-57.36
57.36
-41.56
149.88
-84.13
-99.05
13.98
29.55
.98
-52.76
-36.36
120.96
-78.14
114.64
-94.87
-20.42
-11.16
-73.74
-66.67
-54.15
-100.00
22.95
-59.06
175.16
423.96
850.24
29.41
-23.41
-11.63
602.21
-18.03
372.86
-20.76
16.71
-34.66
-18.15
-2.91
-8.26
1,249.22
QUANTITY
RECYCLED
36,225
6,000
23.400
13.600
0
3,317
29,480
54,648
18.000
48.923
52,000
104
1,330,600
1,400
1,581
605
550
4,096
2,860
2,240
10,022,901
230
5.950
913
4,822
23.926
5,906
2.746
1,040
466
81,250
5,630
5,480
240
36
118,124
QUANTITY
PREVENTED
19.650
3,746
6,387
13,237
6.889
43,218
2
9,215
9,215
9,215
62.730
10,600,000
104
1
122
800
2.162
11.369
10,179
1,500
502
4.000
4,000
4.062
800
0
0
0
0
0
0
10,695
0
12.195
2.986
1.215
7
3
0
SOURCE
ACKYD PAINT CANNING WASH
PRESSURE TREATMENT OF WOOD PRODUCTS
PAINT SPRAY GUN CLEANING
MACHINE TOOL COOLANT
WASTE PAINT FROM TRUCK PAINTING OPERATIONS
SOLVENT CLEANING OF MACHINE PARTS
SOLVENT CLEANING OF MACHINE PARTS
SOLVENT CLEANING OF MACHINE PARTS
METALS BATH PLATING AND DECREASING
SOIL
MACHINING CUTTING FLUIDS
MACHINING CUTTING FLUIDS
MACHINING CUTTING FLUIDS
PRINTING PRESS CLEAN UP AND WASTE INKS.
PAINTING IN PROCESSES RELATED TO SB/SR
RINSES OF DRAGOUT FROM CONVERSION COATING
PHOTO LAB
SURFACE PREPARATION OF PARTS BY DIP RINSING
PAINT WASTES - PAINTING
PAINT BOOTH RINSEWATERS
SULPHURIC ACID PICKLING BATH
SOLVENT CLEANING
VAPOR & BATH DECREASING USING 1.1.1-TRICHLOROETHANE
MAT'L & PART CLEANING USING (1986) MEK
PROCESS WASTE WATER EVAPORATION (RESIDUE)
SOLVENT USED TO CLEAN OUT PAINT LINES FOR COLOR CHANGES
STILL BOTTOMS
MANUFACTURING
STEAM CLEANER SETTLING TANK SLUDGE & PARTS CLEANERS SOLVENTS.
PURGING HOSES
CAUSTIC HOT DIP TANK BATH
FUEL TRUCKS
SURFACE PREPARATION & METAL FINISHING
BATTERIES
COLD TANK DEGREASER
COLD TANK DEGREASER
DECREASING
HYDRAULIC UNITS
WASTEWATER TREATMENT
ANILINE INK PRINTING
WASHING OUT PRINTING PLATES
CLEANING OF SCREENS USED TO APPLY SOLDER MASK PRIOR TO SOLDERING.
LEAD GLASS MANUFACTURE
LEAD REMOVAL FROM WATER PRIOR TO RELEASE FROM PLANT.
PAINT AND LABORATORY SOLVENTS
PARTS DECREASING
DUST FROM STEEL SHOT BLAST UNIT
WET SCRUBBER FOR MIXERS
SURPLUS TRANSFORMER OILS
SIC
2851
2491
3711
3711
3711
3411
3411
3411
3672
2911
3532
3532
3532
3070
3731
3721
3721
3721
3721
3721
3479
3334
3728
3728
2491
3646
2851
2831
3531
2869
3519
4581
3721
3721
3721
3721
3721
3721
3471
2677
2677
3672
3999
3999
3334
3334
3334
3624
3334
RCRA WASTE COOES
F003
K001
D001
D006
D001
F003
F005
F001
D002
K051
D001
D001
0001
D001
D001
D002
D011
D002
D001
D001
D002
F001
Fd01
0001
K001
F003
D001
D001
F002
D001
D008
D001
0006
D002
D001
F002
F001
F006
D001
F002
F003
D008
D008
0001
D001
F005
F005
D007
F003
K048
D005
D005
D005
D006
D007
D007
F002
F002
F003
F003
F004
U002
D007
0008
F004
F002
D007
F003
K050
0008 D007
D008 D007
0008 D007
F007 F008
D008
F005
F005
D007 D008
U031 U080
F005 F003
0006 D008
-------
8/18/89
WASTE MINIMIZATION
Page 4
ID*
UA00581 39304
WAD058367152
WAD059315069
WAD059317933
WA0061670766
WAD069548154
WAD070054309
WAD075204164
UAD089343354
WAD 11 7350033
WAD980383376
WA0980383376
WAD980509947
WA09805 10069
WAD9805 10069
WAD980723449
WAD980724371
WA0980737977
UAD980738488
UA0980738868
UAD980738868
WAD980738926
WA0980833099
WA0980833099
UA0980833099
WAD980833099
WAD980833099
WA0980833099
WA0980833099
WA0980833099
WAD980833099
WAD980833099
WAD980835680
UAD98083S680
WA0980835680
UAD980835680
WAD980974984
WA0980975361
WA0980975759
WA0980975759
WA098097879S
WAD980978795
WAD980980015
WA0980980577
WA0981 760556
OTY GEN
1986
17.385
3.060.000
9,420
90.720
17.130
7.944
10,560
14,103
3,080
12,000
110
40
5,060
10
10
76,706
5,447
100
550
6,370
34,200
5.478
964,166
459
54.067
35,903
825
86,162
203,128
885
26,719
113,150
59
6
3,518
2.092
2.600
66,000
33
338,494
660
110
55,250
12,012
4,000
OTY GEN
1987
41.662
2.500,000
4.785
47.310
7,200
7,944
8.120
12,898
645
5,200
55
20
0
18
7
20,651
4,518
400
250
3.900
28
10.043
620.701
282
0
0
0
44,421
232.848
1,225
0
117.135
0
0
620
1,668
8.600
15,275
29
623,957
660
110
43,550
12,000
1,815
PROD V.
RATIO F
2.00
1.50
.96
.03
.25
.02
.60
.33
.00
.50
.05
.05
.10
.10
.10
.01
.83
6.40
1.67
.78
.78
1.83
.93
.93
.34
.34
.34
.34
.34
.34
.38
.38
.77
.77
.77
.77
4.10
1.30
.91
.91
.10
.00
.45
.32
.80
MSTE MIN
ERCENTAGE
19.82
-45.53
47.09
49.37
66.37
-1.96
28.16
31.24
-79.06
71.11
-52.38
-52.38
-100.00
63.64
-36.36
-73.34
-.07
37.50
72.78
21.51
-99.90
.18
-30.78
-33.94
-100.00
-100.00
-100.00
-61.53
-14.45
3.30
-100.00
-24.98
-100.00
-100.00
-90.04
-54.95
19.32
82.20
3.43
102.56
9.09
0.00
45.64
-24.32
-74.79
QUANTITY
RECYCLED
26.400
26.796
3,310
0
0
55
20
18
15,000
4,518
120
1,600
0
44,421
232,848
1,061
117,135
620
8.500
98,782
660
600
43,550
1,648
16,800
QUANTITY
PREVENTED SOURCE
ACETONE RECYCLING STILL BOTTOMS
2.090.000 OEUATERING OF HAZARDOUS UASTE
4,258 STILL RECYCLING THINNERS
46,132 MIXED SOLVENT UASTE FROM LITHOGRAPHIC PRINTING.
14.225 PAINTING PARTS AND ASSEMBLIES
SOLVENT BATH DECREASING
-8 ACETONE - WASH TOOLS
5,859 MACHINE PARTS DECREASING
2,435 SULFURIC ACID HYDROGEN PEROXIDE SOLUTION USED FOR ETCHING COPPER
12.800 COATING GLASS ft INSULATING GLASS
0 RESIDUALS LEFT IN BARRELS
0 RESIDUALS LEFT IN BARRELS
5,566 UASTE PAINT STRIP
11 ELECTROLESS DEPOSITION OF COPPER ONTO PRINTED CIRCUIT BOARD SURFA
4 UASTEUATER TREATMENT PRODUCING METAL HYDROXIDE SLUDGE
56,822 (1) STILL BOTTOMS (2) PAINT STRIPPING
ASPHALT EXTRACTION TEST
240 POPTIOE ft DNA SYNTHESIS SOLVENT
670 STILL BOTTOMS AND FILTERS FROM DRY CLEANING OPERATION
1,069 RAGS AND DEBRIS CONTAMINATED UITH SOLVENTS-ACETONE
26,648 SOLVENTS USED IN CLEANING OF PRODUCT UAFERS DURING MANUFACTURING
1,600 ALODINE DIP PROCESS
279.452 QUALITY CONTROL ETCHING
145 INGOT PULLER MACHINE CLEANING
72.673 SILICON UAFER POLISHING/CLEANING
48.110 UAFER CLEANING
1,106 UAFER CLEANING/INSPECTION
71,036 SILICON UAFER POLISHING/EQUIPMENT DECREASING
39.345 VAPOR PHASE SOLVENT RECOVERY
UAFER CLEANING
36,997 CLEANING OF AIR POLLUTION CONTROL EQUIPMENT
39,012 SILICON INGOT & UAFER ETCHING
104 LABORATORY UASTE FROM ANALYTICAL PROCEDURE
11 LABORATORY UASTE FROM ANALYTICAL PROCEDURE
5.607 EQUIPMENT/PARTS CLEANING AND DECREASING
2,035 PAINTING EQUIPMENT CLEANING
2.060 RESIN CLEAN UP FROM MANUFACTURING OF FIBERGLASS BOATS
70,525 PARTS CLEANING AIRCRAFT MAINTENANCE
13 INSPECTION OF DEFECTIVE BATTERIES
UASH/RINSE WATER AFTER BATTERY FORMATION PROCESS.
655 UASTE FROM CLEANING UNFINISHED ALUM ft METAL PARTS.
490 SOLVENT FOR CLEANING SPRAY PAINTING EQUIPMENT
36.563 ETCHANT USED IN CHEMICAL MACHINING
3,856 PARTS DECREASING
THE HAZARDOUS UASTE IS CREATED BY THE USE OF MEK
SIC RCRA WASTE COG
3083 D001 F003
4953 F006
2851 0001 F003 FOOS
2752 D001 D008 F003
3721
2911 D001
2821 F003
3069 D001
3672 D002 0008
3211 D001 D006 D008
2436
2436 0001
3470 F002 D002
3672 D002 U122
3672 F006
3728 0001 F001 D002
9621 F002
8069 D001 F003 F002
7219 F002
3674 F002 F003 FOOS
3674 F003 0001
2899 D007
3674 D002 D007
3674
3674 F002
3674 F001
3674 F001
3674 F002
3674 F001 F002
3674 F002
3674 D002
3674 D002
2800 D009 001 1
2800 D001
2800 U226
2800 F003 FOOS 0007
3732 F003
4512 D001
5063 D002
5063 0002
3479 U226
3479 U159 D007
3479 D002
3728 F002
1721 0001 FOOS F003
ES
FOOS
F002
F002
U003
0008
-------
APPENDIX F
Groundtruthing Results
-------
GROUNDTRUTHING MEETING
JUNE 19, 1989
8-12 AM
US ENVIRONMENTAL PROTECTION AGENCY
REGION X
-------
APOGEE
RESEARCH
INC.
June 12, 1989
Dear participant,
Thank you for agreeing to participate in this Groundtruthing Meeting in which
specialists in industry; public agency staff; EPA officials; and other interested parties
will come together to review and provide your views on EPA Region X's hazardous
waste minimization analysis. The Groundtruthing Meeting will take place between 8-
12 AM on June 19,1989, at the following address:
U.S. Environmental Protection Agency - Region X
Park Place Building
Floor 12, Conference Room 12 A (look for sign:.)
1200 61& Avenue (Comer of University and 6%
Seattle, Washington 98101
You will be asked to consider and comment on EPA's preliminary' estimates of
hazardous waste reduction potential specific to facilities in Alaska, Idaho, Oregon, and
Washington. Your comments will be incorporated into the analysis to refine the
approach and to identify reasonable rates of waste reduction that may be expected over
the next 20 years for specific hazardous waste streams.
So that we may be as productive as possible in the short time that we have available, we
have provided some general guidelines that will help facilitate the discussions. The
guidelines arc the following:
Waste reduction for this exercise is defined as those in-plant
practices that reduce, avoid, or eliminate the generation of
hazardous waste so as to reduce the risks to human health and
the environment. The objective is to prevent the generation of
hazardous waste at its source, not to treat, manage, or control a
hazardous waste after its generation. It is assumed that such
reductions will lower the demand for commercial waste
management capacity.
-------
EPA and its consultants, Apogee Research, Inc., are mainly here
to listen. We will present our preliminary findings briefly and
ask that industry do most of the talking.
The value of this exercise requires that you be candid with your
views. We all recognize the limitations of long-term forecasts
and imperfect data, but we ask that you contribute your
opinions, uncertain as they may be.
We are interested in industry's perception of their own "waste
reduction frontier." As such, we will focus on industry's
views, specific to unique combinations of their industry and the
wastes they generate. Others with insights relevant specifically
to industrial processes are welcome to comment as well.
Enclosed is an explanation of the purpose of the analysis, a brief discussion of
methodology, example graphics of the waste reduction analysis, and preliminary
figures showing reasonable rates of reduction in future hazardous waste generation for
specific waste streams. Also enclosed is an agenda for the meeting, a list of
participants identified by industry group affiliation, and an example Participant
Comment Sheet that we will ask you to fill out with your views on waste reduction
potential.
We are optimistic that the role that you are to play in this effort will contribute
significantly to understanding future reductions in hazardous waste generation. Thank
you for your participation.
Yours Sincerely,
Kenneth Rubin, Ph.D. William M. Jones, Ph
President Director
enclosures
-------
GROUNDTRUTHING MEETING
Monday. June 19. 8-12 AM
AGENDA
I. Introduction: Charles F. Findley (Division Director, Hazardous
Waste Division, USEPA Region X)
A. Welcome participants
B. Explain purpose of meeting and why participants invited
C. What is expected of Participants
D. Structure of die sessions
II. Apogee Research Overview of Waste Reduction Methodology
A. Explanation of die approach
B. Sources of data and information
C. How die information from participants will be incorporated into the analysis
III. Break-up into Industrial Groupings
A. Participants will be grouped according to the industries that they represent (based
on responses to the biennial and annual hazardous waste report forms)
Group I: Plating and Polishing (SIC 3471) 1
Aircraft (SIC 3721) [
Aircraft Parts and Equipment (SIC 3728) s
Group H: Primary Aluminum Industry (SIC 3334) ^ ^\M
IV. Apogee Presentation
A. Findings
B. Estimated reasonable hazardous waste reduction rates
C. Supporting evidence for reduction rates
V. Participant Discussion
A. Open session to participant discussion
VI. Fill-Out Participant Comment Sheets
VII. Reconvene Participants and Close Groundtruthing Meeting
-------
PRIVATE SECTOR GROUNTRUTHING PARTICIPANTS
June 19, 1989 Morning Meeting
Group I: Aircraft and Aircraft Pans, Electroplating and Polishing
Elliott Berkihiser
Boeing Company
Manager, Environmental Compliance
600 Naches Avenue SW
Renton, WA 98005
David Caldwell
Korry Electronics Company
801 Dexter Avenue N
Seattle, WA 98109
Chuck Christiansen
Tri-Coatings
1104 10th Street
Everett, WA 98201
Danny Devaney
Protective Coating, Inc.
1215 North Second Avenue
Kent, WA 98032
Melt Haworth
Northwest Plating Company
825 South Oakota Street
Seattle, WA 98108-5290
Randy Haworth
Surftech Finishes, Inc.
22436 72nd Avenue S
Kent, WA 98031
Group II.
Aluminium
Thomas D. Dickey
Reynolds Metal Company
4029 Industrial Way
Longview, WA 98362
David M. Lishe
Intalco
4050 Mount View Road
Ferndale, WA 98248-0937
Brian Jespersen
Health Tecna Aerospace Company
19819 84th Avenue S
Kent,WA 98032
Clifton A. Johnson
Hytek Finishes Company
8202 South 200th
Kent, WA 98032
Mike Palmer
Seatle Technical Finishing
1005 S. King Street
Seattle. WA 98114
Gilbert Pigotti
Industrial Plating Corp
2411 6th Avenue S
Seattle, WA 98134
Jay Ramaswami
Evergreen Industries
10924 Chennault Beach Road
Everett, WA 98204
Bob Williams
Blue Streak Finishers LTD.
10425 33rd Avenue W
Everett, WA 98204
James A. Thompson
Wenatchee Works of Alcoa
Malaga Road
Wenatchee, WA 98801
-------
Example Participant Comment Sheet
OREGON
SIC 3471
ELECTROPLATING INDUSTRY
Respondent Name*:
Company Name/Address:
Telephone:
Quantity Estimated Estimated Estimated
EPA Generated Reduction Reduction Reduction
Waste Waste Tons" t989*** 1995*** 2009*«*
Type Description 1987 ( % ) ( % ) { % )
D001
D002
D006
D007
D008
F001
F002
F006
K062
f
Ignitable Waste
Corrosive Waste
Cadmium
Chromium
Lead
Spent halogenated solvents from degreasing:
tetrachlorethylene. trichlorethylene.
methylene chloride; 1,1.1-trichloroethane.
carbon tetrachloride. chlorinated fluro-
carbons
Still bottoms - recovery of above spent solvents
Spent halogentaed solvents: tetrachloroethylene,
trichlorethylene. 1.1 ,1-techloroethane.
Chlorobenzene, 1,1,2, trichloro-1 ,2,2-tri-
fluoroethane, ortho-dichlorobenzene. tri-
chlorofluoromethane, 1.1,2, trichloroethane.
Still bottoms - recovery of above spent solvents
Wastewater treatment sludges from electo-
plating operations
Spent pickle liquor from steel finishing oper-
ations of plants that produce steel or iron
9.79
4.84
3.19
20.79
0.99
24.97
0.11
325.6
15.95
"While this is optional, we would like to be able to contact you with follow-up at a future date.
Even if you do not to fill in your name, we encourage you to fill out the comment sheet.
"Data from Oregon annual waste generation reports.
"When possible, please indicate reduction activities that will achieve your estimates (e.g., technology
change, product substitution, housekeeping activites, process change, etc.).
-------
The Purpose of EPA Region X's Waste Minimization Analysis
The waste minimization analysis that you are being asked to comment on is part of a
Superfund requirement Under the 1986 Superfund Amendments and Reauthorization Act
(SARA) each state is required to prepare a Capacity Assurance Plan (CAP). Specifically,
Section 104(k) of SARA requires that each state provide a report to the U.S. Environmental
Protection Agency with specific information on hazardous waste generation and disposal
for 1987 (baseline data). The report must also forecast hazardous waste generation and
available disposal capacity for the years 1989,1995, and 2009.
The baseline data for these CAPs come from biennial or annual reports that all qualified
hazardous waste generators and facilities must submit either to the Department of Ecology
if in Washington, Department of Environmental Quality if in Oregon, or EPA Region X if
in Alaska or Idaho. Many of you who are attending these meetings have probably filled out
these reports and understand the level of detail on waste generation and disposal practices
facilities are required to report.
One variable that will surely affect future hazardous waste generation and disposal capacity
is waste reduction activity by industry. Reductions in a particular hazardous waste stream
could reduce a facility's overall hazardous waste stream and the total quantity of hazardous
waste that is generated in a given state. Reductions could also decrease the capacity needs
for the management practice that is used to treat and dispose of the hazardous waste. Thus,
EPA is encouraging states to incorporate a waste reduction assessment in their CAPs.
Several sources of information have been combined into an analysis that sheds light on
future waste reduction potential for specific hazardous waste streams. The sources of
information include the following:
Hazardous waste generation data from the biennial and annual
reports mentioned above,
Economic data,
Process engineering information for selected industrial processes,
Waste minimization information from the EPA Biennial Reports,
Review of engineering literature, and
Industry opinion on waste reduction potential.
The last information source represents the meeting that you have been invited to attend and
participate.
-------
Explanation of Waste Minimisation Methodology
Waste Reduction Methodology
You will be seeing the preliminary results of EPA Region X's analysis. Figures that will
be presented we believe represent reasonable rates of hazardous waste reduction based on
our analysis to date and are to be considered a take-off point to stimulate discussion among
the participants. As industry representatives you will be asked to assess your current
hazardous waste generation and then estimate the quantity and time period over which your
hazardous waste may be reduced.
During the course of the meeting we will be handing out information and displaying
graphics and tables on overhead projectors. Since the information and graphics will
probably be unfamiliar to you, we have provided a short introduction to the waste reduction
methodology and several examples of the types of information that will be presented during
the meeting.
Statistical Analysis of Waste Generation
The first step in the waste reduction analysis has been to get a fix on the types and
quantities of hazardous wastes generated by each industry in the base year (1987). The
analysis is performed at the facility level in order to assess the range of processes that are
used to produce similar products. This allows us to identify the statistically significant
range of hazardous waste generation for each facility producing the same product
The distribution of hazardous waste generated for each facility is critical to our analysis.
Exhibit A in this package is an example which graphically displays the distribution of spent
chromium plating bath by the electroplating industry. What it indicates is the amount of
hazardous waste per employee that is generated by each facility (R Factor is the term we
have used to describe the relationship between hazardous waste generation and number of
employees). Facilities with high R Factors (i.e., generate large amounts of hazardous
waste per employee) are located toward the right hand side, while those with low R Factors
(i.e., small amounts of hazardous waste per employee) are toward the left side of the
graph. The curve represents the frequency of facilities. That is, the higher the curve the
greater the frequency of facilities.
Significance of the R Factors
-------
Explanation or Waste Minimization Methodology
The significance of the R Factors is to show the range of hazardous waste generation for an
industry/hazardous waste combination and the potential that may exist for waste reduction.
We consider the middle two quartiles or intervals in the curve in Exhibit A to be the most
important for our analysis. These intervals represent the range over which we believe we
might observe movement or migration toward a reduction in hazardous waste generation.
Since there are uncertainties about the future, we think it is necessary to base our reduction
rates on several key assumptions. We believe assumptions should be made about, (1) the
technical means that facilities will use to achieve waste reduction, (2) the total quantity of
waste reduction, and (3) the period of time over which waste reduction could reasonably be
expected to occur.
In order to make these assumptions and use the information we have gleaned from the
curves we need to apply other analyses. Two sources of information have been used to
identify potential changes in R Factors - process engineering analysis and analysis of
waste minimization data from 1987 EPA Biennial Report Forms.
Engineering Waste Reduction Analysis
Information from the engineering analysis is designed to identify the processes that account
for hazardous waste generation in the statistical analysis. Engineering analysis provides, in
part, an explanation as to why there is a range of waste generation (i.e., R Factors) for a
particular hazardous waste stream within an industry. For example, there may be different
R Factors in the electroplating industry for chromium based on the type of rinse processes
or drag-out controls used by a facility. In addition, the engineering analysis identifies
waste reduction techniques (e.g., equipment or technology modification/substitution;
process or procedure modification/substitution; reformulation or redesign of product;
modification/substitution of input or raw material; better housekeeping/operating practices;
and waste stream segregation) that can reduce the R Factor. The procedures we have used
to accomplish this analysis include the following:
Analysis of the processes responsible for generating the identified
hazardous waste in each selected industry. The analysis includes
review of existing engineering and waste reduction literature,
studies, and reports; waste reduction databases; expert opinion; and
engineering and waste reduction audits;
Identification of typical hazardous waste generation processes which
account for the range of R Factors for each selected industry; and
-------
Explanation of Waste Minimization Methodology
Identification of hazardous waste reduction activities that could
result in a decline in the R Factor for the selected industry.
Turning to Exhibit A, the legend has information on the type of options available for
reducing the R Factor for spent chromium plating bath in the electroplating industry. These
options have been identified by the engineering analysis. If not already incorporated into
the production process, we believe each might contribute to a reduction in hazardous waste
generation.
Engineering analysis will be completed for each industry. Through this analysis we will
identify hazardous waste reduction options that could result in a reduction in R Factor.
However, we will use another source of information that links the engineering analysis
with the statistical analysis. We have some knowledge of the range of R Factors and the
types of hazardous waste reduction options that are available for each industry. What we
need to identify, however, are the facilities that have already incorporated the waste
reduction options identified in the engineering analysis. We have used data from EPA's
1987 Waste Minimization Data Biennial Reports to help make this link.
Analysis of Waste Minimization Data from Biennial Report Forms
The purpose of this information source is to identify the degree of waste reduction activities
that have actually occurred in EPA Region X states for the hazardous wastes in selected
industries. The information on waste minimization activities come from the 1987 EPA
Biennial Reports.
The value of this information is two-fold. First, we can assess whether R Factor
differences are due to waste reduction efforts that have already been incorporated into the
production process. Second, the Waste Minimization Biennial report forms can provide
information on additional waste reduction options.
Reasonable Rates of Waste Reduction
By combining the statistical, engineering, and waste minimization analysis we have
assessed the potential for hazardous waste reduction for a selected set of hazardous waste
streams. Assigning an actual reduction rate for a specific waste, though, is difficult
because it relies on a number of additional factors (e.g., incentives, existing information,
inenia, and existing inplant restrictions). We have made what we believe are some
reasonable rates of reduction for each hazardous waste stream. For the spent chromium
-------
Explanation of Waste Minimization Methodology
plating bath in Exhibit A we have assigned a total rate of reduction of about 20.5% by the
year 2009 AD. That is, by that date it is conceivable that, given what we currently
understand about future waste reduction activities, 20.5% less hazardous waste may be
generated.
"Groundtruthing"
The statistical, engineering, and waste minimization analysis have been combined to
forecast reasonable waste reduction for the three projection years (1989,1995, and 2009).
We are looking for a critical evaluation of this approach from the panel of experts to help
EPA Region X, (1) refine the methodology, (2) make recommendations as to which waste
reduction activities will most likely be adopted, and (3) determine a reasonable rate of
reduction in hazardous waste generation for each of the projection periods based on
adoption of the waste reduction activities. Their opinions will be combined to estimate
reasonable reductions in hazardous waste generation by waste stream for selected industries
in EPA Region X states.
We are asking you to assist us in developing reasonable rates of reduction. We will present
our findings and discuss with you any changes or recommendations in the waste reduction
estimates you may have to the same projection periods. Based on these discussions we
will calculate ranges of hazardous waste reduction for each industry.
-------
Log Normal Distribuiton
SIC 3471 (Electroplating), D007 (Spent Chromium Plating Bath)
e
o
«
(0
>
In
V
tn
.0
O
t
o
.0
a
Minimum 1st
Quartile
No. of Observations = 15
Minimum = .0009
1st Quartile = 0131
2nd Quartile = .0566
3rd Quartile .1652
Maximum = .2860
Most likely
scenario
= 20.45% Reduction
by 2009
Options
- Counter current rinsing
- Drag-out recovery
- Reverse osmosis
- Multi-stage filtration
2nd 3rd
Quartile Quartile
R FACTOR (unit waste per unit output)
Maximum
APOGEE RESEARCH
-------
PRIVATE SECTOR GROUNDTRUTHING PARTICIPANTS
June 19, 1989 Morning Meeting
Group I: Aircraft and Aircraft Pans, Electroplating and Polishing
Elliott Berkihiser
Boeing Company
Manager, Environmental Compliance
600 Naches Avenue SW
Renton, WA 98005
David Caldweli
Korry Electronics Company
801 Dexter Avenue N
Seattle, WA 98109
Chuck Christiansen
Tri-Coatings
1104 10th Street
Everett, WA 98201
Danny Devaney
Protective Coating, Inc.
1215 North Second Avenue
Kent, WA 98032
Melt Haworth
Northwest Plating Company
825 South Dakota Street
Seattle, WA 98108-5290
Randy Haworth
Surftech Finishes, Inc.
22436 72nd Avenue S
Kent, WA 98031
Charlie Simpson
Boeing Company
600 Naches Avenue SW
Renton, WA 98005
Brian Jespersen
Health Tecna Aerospace Company
19819 84th Avenue S
Kent, WA 98032
Clifton A. Johnson
Hytek Finishes Company
8202 South 200th
Kent, WA 98032
Mike Palmer
Seattle Technical Finishing
1005 S. King Street
Seattle, WA 98114
Gilbert Pigotti
Industrial Plating Corp
2411 6th Avenue S
Seattle, WA 98134
Jay Ramaswami
Evergreen Industries
10924 Chennault Beach Road
Everett, WA 98204
Bob Williams
Blue Streak Finishers LTD.
10425 33rd Avenue W
Everett, WA 98204
Roy Chandler
Health Tecna Areospace
19819 84th Avenue S
Kent, WA 98032
Group II. Aluminum
Thomas D. Dickey
Reynolds Metal Company
4029 Industrial Way
Longview, WA 98362
James A. Thompson
Wenatchee Works of Alcoa
Malaga Road
Wenatchee, WA 98801
-------
Group II. continued.
David M. Lishe
IntaJco
4050 Mount View Road
Femdale, WA 98248-0937
-------
PRIVATE SECTOR GROUNDTRUTHING PARTICIPANTS
June 19, 1989 Afternoon Meeting
Group I. Paints, Industrial Organic Chemicals
Frank Debiase
Universal Paint Products Inc.
2442 First Avenue S
Seattle, WA 98134
Kevin Hudson
Preservative Paint Company
5410 Airport Way South
Seattle, WA 98107
Laurel Jamison
Rudd Company, Inc.
1630 15th Avenue W
Seattle, WA 98119
Roger Nelson, Vice President
Chemical Processors, Inc.
Sales & Marketing
734 S. Lucile Street
Seattle, WA 98108
Gary L. Podrabsky
Rhone-Poulenc Inc.
9229 E Marginal Way S
Seanle, WA 98108
Curtis P. Bailey
Jarves Paint Company
760 Aloha Street
Seattle, WA 98109
Group II.
Electronics
Daniel Bolser
Pacific Circuits, Inc.
17550 NE 67th Court
Redmond, WA 98052
Jerry Mathieson
Westak North
14815 NE 40th Street
Redmond, WA 98052
Walter Sadowski
Daniel Boone Paint Company, Inc.
103 Nelson Place
Renton, WA 98055
William Shackelford
Gaco Western Inc.
18700 South Center Parkway
Seattle, WA 98188
Paul Sheehan
Farwest Paint Manufacturing Company
4522 S 133rd Street
Tukwila,WA 98188
Paul Urban1
Betz Laboratories, Inc.
818 S 32nd Street
Washougal, WA 98671
Richard Tahell
Cowan Cambell Paints
5221 Ballard Avenue NW
Seattle, WA 98107-0328
Mark Benjamin
Professor of Civil Engineering
University of Washington
Seattle, WA 98195
Geoff Short
PUD #1 of Snohomish County
2320 California Avenue
Everett, WA 98108
Dan White
Universal MFG
14410 NE 190th
Woodinville, WA 98072
mail.
Mr. Urban will not be coming to the meeting but would like to participate through the
-------
Group II continued
Russel Post Debby Dole
City of Tacoma Seattle City Light
Department of Public Utilities Envommental Affairs
3628 35th Street S 1015 3rd Avenue, Room 922
Tacoma, WA 98411 Seattle, WA 98104
-------
PRIVATE SECTOR GROUNDTRUTHING PARTICIPANTS
June 20, 1989
Group I. Aircraft and Aircraft Parts, Electroplating and Polishing
Larry Ansen
Columbia American Plating Company
3003 NW 35th Street
Portland, OR 97210
C. Todd Ball
Luhr Jensen & Sons
P.O. Box 297
Hood River, OR 97301
Ron Graham
Superior Metal Finishing, Inc.
18240 SW 100th Court
Tualatin, OR 97062
Jim Kerbs
Anodizing, Inc.
P.O. Box 11263
Portland, OR 97211
Richard McCullah
PSI Manufacturing
514 Milton Way
St. Helens, OR 97051
Mike Pessl
Aeroscientific Corporation
1270 NW 167th Place
Beaverton, OR 97005
Dave Pofsahl
Beaverton Parts Manufacturing
1800 NW 216th
Hillboro, OR 97123
David Sicilia
Russ Leninger Polish & Plating
627 SE Division Place
Portland, OR 97202
Dave Standley
Excello Products
8710 SE 76th Drive
Portland, OR 97206
Diane Stockton
Omark Industries
P.O. Box 22127
Milwaukie, OR 97222
Jim Thibodeau
East Side Plating
310 SE Stephens
Portland, OR 97214
Group II.
Electronic
Mike Gotterba
Siltec Corporation
P.O. Box 7748
Salem, OR 97301
Ron Graham
Superior Metal Finishing, Inc.
18240 SW 100th Court
Tualatin, OR 97062
-------
Group II. Continue
Jim King Nina Poppelsdorf
Facilities Manager Union Carbide
Sentrol, Inc. 3333 Index Street
10831 SW Cascade Blvd. Washougal, WA 98671
Portland, OR 97201
Kyle Ritchey-Noll Chet Schink
American Electronics Association 3943 SB Cooper Street
707 13th Street SE, Suite 118 Portland, OR 97204
Salem, OR 97331
Diane Lefevre
SEH American, Inc.
4111 Northeast 112th Avenue
Vancouver, WA 98662
Jim McDaniel
Hewlett Packward
1020 NE Circle Blvd
Corvallis, OR 97330
Ted Molinari
Praegitzer Industries
1270 Monmouth Cutoff
Dallas, OR 97338
Oiher
Ken Williamson
Civil Engineering Department
Oregon State University
Corvallis, OR 97331
-------
GROUNDTRUTHING NOTES
WASHINGTON
C022-002
PAINTS AND ALLIED PRODUCTS (SIC 2851)
INDUSTRIAL ORGANIC CHEMICALS (SIC 2869)
Gary Podrabsky
Rhone Poulenc
Seattle, Washington
(206) 764-4450
Kevin Hudson
Preservative Paint Company
5410 Airport WayS.
Seattle, Washington 98108
(206) 763-0300
Walt Sadowski
15701 Nelsen Place South
Tukwila, Washington 98020
(206) 228-7767
Industry Attendance
Hal Williams
chemical Processors
2203 Airport Way S.
Seattle, Washington
(206) 223-0500
Gerald Johnson
Formulating Technician
Rudd Company, Inc.
1630 SUiAve. West
Seattle, Washington 98119
(206) 284-5400
CJP. Bailey
Martec Industries
760 Aloha Street
Seattle Washington 98109
(206)284-1040
Ken Wilson
Preservative Paint Company
5410 Airport WayS.
Seattle, Washington 98108
(206)763-0300
Paul Sheehan
Farwest Paint Manufacturers
4522 South 133Q1 St
Tukwila, Washington 98168
(206)244-8844
-------
Comments on SIC 2851 - Paint & Allied Products & SIC 2869 - Industrial Organic Chemicals
EPA
Waste
Code1
Waste
Description
Total Quantity Waste Generated
General Comments:
Regulation or the threat of
regulation was considered by the
participants to be one of the
major incentives for waste
reduction activities. The threat of
"California-like" regulations on
VOC emissions being
implemented in Wa. was reason
why many paint companies have
begun to convert from liquid to
dry paint formulations.
However, there are limits
according to industry on the
extent of waste reduction in the
industry. For example, the
relatively moist climate in the
Northwest makes it more difficult
to convert from solvent to latex
based paints.
At the same time participants
indicated substantial waste
reductions, they also admitted
that most companies knowledge
about their waste streams. Few
companies had implemented
waste tracking or conducted
analysis of their streams. This
suggested a greater potential for
waste reduction as more facilities
monitor waste generation and
begin reduction programs.
One company, Preservative Paint
Co. introduced an incentive
program that encouraged
Quant
Gen
Tons
19862
2,243
Estimated
Reduction
1989
(%)3
General Process Changes:
Change intake valves for removing
paint from mixing tanks to remove
more paint before cleaning. Drain
rack redesign to remove more paint
before sending to off-site waste
management facility.
General Housekeeping: Improve
scheduling of paint formulation to
reduce frequency of cleaning tanks.
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
-------
Comments on SIC 2851 & 2869
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
Estimated
Reduction
1995
Estimated
Reduction
2009
Cont.
employee suggestions for waste
reduction providing a monetary
reward for suggestions
implemented. The program was
so successful that in 1987 the
Company reduce by 50% the
quantity waste shipped off-site in
1985.
Finally, specialty coating paint
formulators had fewer waste
reduction options available than
did paint large companies that
produce paints for retail.
D001
Ignitable Waste
1.742
1% (Sheehan, Johnson); 25%
(Hudson)
Substitution: Increase use of
water as a substitute for solvent
cleaners.
Housekeeping: Keep solvent used
for cleaning batch tanks separate.
Once it is off-spec for cleaning,
solvent can often be used in paint
formulation.
5% (Johnson); 10% (SadowsM); 15%
(Sheehan); 25% (Hudson); 73%
(Bailey)
20% (Johnson); 25% (Hudson); 45%
(Sheehan); 50% (Sadowski); 95%
(Bailey)
D002
Corrosive Waste
38
2% (Johnson)
Substitution
10% (Johnson)
20% (Johnson)
D003
Reactive Waste
25% (Wilson)
-------
Comments on SIC 2851 & 2869
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
D007
D008
D009
F001
F002
Chromium
Lead
Mercury
Spent halogenated solvents from
degreasing: tetrachloroethylene,
trichloroethylene, methylene
chloride, 1,1,1-trichloroethane,
carbon tetrachloride, chlorinated
flurocarbons; still bottoms -
recovery of above spent solvents
Spend halogenated solvents:
tetrachloroethylene,
trichloroethylene, 1,1,1-
techloroethylene, chlorobenzene;
1,1,2 trichloro-l,2,2-trifluo-
roethane, otho-dichlorobenzene,
trichlorofluoromethane; 1,1,2
trichloroethane; still bottoms
from recovery of above spent
solvents
10
17
14
40
1
25% (Hudson)
General Comments: most
chromium based paints are specified
formulation for federal govt contracts
as trafficAoad paint There exists
substitute paint with the same
reflective properties, but govt
specifications have yet to change.
Therefore companies will continue to
formulate chromium based paints and
generate chromium waste
Housekeeping: Segregating metal
waste from other waste streams.
3% (Johnson); 25% (Hudson)
General Comments: Like D007,
lead wastes are from specified
formulation. Waste reduction
potential will change as specified
formulations change.
3% (Johnson)
25% (Hudson, Wilson)
Substitution: Expect government
to begin changing chromium content
specifications^ubstitute non-
chromium based paints.
2% (Johnson);5% (Sadowski); 25%
(Hudson, Wilson)
20% (Johnson)
25% (Hudson)
10% (Sadowski); 25% (Hudson); 50%
(Johnson)
50% (Johnson
10% (Johnson)
10% (Johnson)
-------
Comments on SIC 2851 & 2869
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
F003
Spent nonhalogenated solvents:
xylene, acetone ethyl acetate,
ethyl benzene, ethyl ether,
methyl isobutyl ketone, n-butyl
alcohol, cyclohexanone,
methanol; still bottoms from
recovery of above spent solvents
138
1% (Sheehan, Johnson); 25%
(Hudson)
General Comments: There was
some concern that waste reduction
activities was on the frontier and there
would be little change in waste
generation in the near future unless
there was a significant change in
technology.
Preservative Paint Co. claimed that
the had actually increased men* waste
stream btw. 1986-89 by 50% because
of business expansion, but were
expecting decreases by a similar amt
Process Changes: Closed loop
processes will become increasingly
common in paint formulation. For
instances, acetone, a cleaner, will be
used in paint formulation after it is no
longer useful as a cleaner. There will
also be limited use of sludge in paint
formulation.
6% (Johnson); 10% (Wilson); 15%
(Sheehan); 25% (Hudson)
25% (Hudson); 40% (Sheehan)
F004
Spend nonhalogenated solvents:
cresols, cresylic acid,
notrobenzene; still bottoms from
recovery of above spent
solvents.; still bottoms from the
recovery of the above spent
solvent mixtures
-------
Comments on SIC 2851 & 2869
^^^^^M^BBB
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
F005
F006
F007
U031
U112
U117
U228
won
WC02
WP01
WP02
WT01
WT02
Spent nonhalogenated solvents:
methyl ethyl ketone, carbon
disulfide, isobutanol, pyridine,
benzene, 2-eihoxyethanol, 2-
nitropane; still bottom from
recovery of above spent solvents
and spent solvent mixtures
Waste Water Treatment sludges
from electroplating operations
Spent cyanide plating bath
solutions from electroplating
1-Butanol (i)
Ethyl acetate (i)
Ethyl ether (1), ethane, 1,1',-
oxybis-(i)
Trichloroethylene
EHW (Carcinogenic Dangerous
Wastes)
DW (Carcinogenic Dangerous
Wastes)
EHW (Halogenated
Hydrocarbons)
DW (Halogenated Hydrocarbons)
EHW (Toxic Dangerous Wastes)
DW (Toxic Dangerous Wastes)
45
3
.07
.22
2
.22
1
.21
.64
15
79
4
88
1% (Sheehan, Johnson); 5%
(Sadowski)
General Comments: Participants
were concerned that Wa. would follow
recent changes in California's VOC
regulations. Paint companies were
beginning to consider changes in
production that would meet the Ca.
regulations. Dry or powder paints
was considered one method to reduce
solvent emissions. Such changes
would also reduce solvent use.
Housekeeping: toluene skimmed
to reuse from top of drums holding
sludges previously removed from
toluene cleaner. This process would
ensure that paint company used as
much of the solvent as possible
before it was completely off-spec.
5% (Bailey)
25% (Hudson)
3% (Johnson);5% (Sadowski); 15%
(Sheehan)
9% (Bailey)
25% (Hudson)
5% (Sadowsky); 10% (Johnson); 40%
(Sheehan)
20% (Bailey)
10% (Johnson)
25% (Hudson)
-------
Comments on SIC 2851 & 2869
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
1 Wastes in Bold identify hazardous wastes that qualified for reduction analysis by EPA Region X.
2Hazardous waste stream data from 1986 Washington Generator Annual Dangerous Waste Reports.
3Medium estimate represents EPA Region X estimate of reasonable waste reduction based on statistical analysis prior to "Groundtruthing" Meetings.
-------
GROUNDTRUTHING NOTES
C022-002
PRIMARY ALUMINUM (SIC 3334)
Industry Attendance
A. John Michaelson E. James A. Thompson
Chief Chemist & Environmental Aluminum Co. of America
Engineer (509) 663-9273
Intalco Aluminum Corp.
P.O. Box 937
Femdale, Wa. 98248
(206) 384-7584
C. Fred A. Rufher D. Tom Dickey
Environmental Manager Reynolds Metals Co.
Columbia Aluminum Corp. (206) 636-8203
85 John Day Dam Rd
Goldendale, Wa, 98620
(509) 773-7302
-------
Comments on SIC 3334 - Primary Aluminum
EPA
Waste
Code1
D001
D007
D008
F001
F002
F003
Waste
Description
Total Quantity Waste Generated
Ignitable Waste
Chromium
Lead
Spent halogentated solvents from
degreasing: tetrachlorethylene,
trichlorethylene, methylene
chloride, 1,1,1-trichlorethane,
carbon tetrachloride, chlorinated
flurocarbons; still bottoms -
recovery of above spent solvents
Spend halogenated solvents:
tetrachloroethylene,
trichloreihylene, 1,1,1-
techloroethylene, chlorobenzene;
1,1,2 trichloro-l,2,2-trifluo-
roethane, otho-dichlorobenzene,
trichlorofluoromethane; 1,1,2
trichloroethane; still bottoms
from recovery of above spent
solvents
Spend nonhalogenated solvents:
xylene; acetone; ethyl acetate;
ethyl benzene; ethyl ether;
methyl isobutyl ketone; n-butyl
alcohol; cyclohexanone;
methanol; still bottoms -
recovery of above spent solvents
Quant
Gen
Tons
19862
37,890
18.83
.18
12.7
.16
.49
.94
Estimated
Redaction
1989
(%)3
Apogee median estimate all waste
types = 6.9%
Medium estimate = 7.7%
75% reduction expected this year
according to John Michaelson
(Intalco)
Medium estimate = .2%
All industry representatives recycle
nearly 100% of F001-S and therefore
do not see need for reductions in these
very small waste streams in the near
future. Also feel that they are
currently on die frontier of waste
reduction, there are no incentives for
further waste reduction at this time.
Medium estimate = 1.5%
ditto industry comment above
Estimated
Reduction
1995
(%)
Apogee median estimate all waste
types = 7.4%
Medium estimate = 23.1%
Medium estimate = .6%
Medium estimate = .4.6%
Estimated
Reduction
2009
(%)
Apogee median estimate all waste
types = 18.9%
Medium estimate = 59%
Medium estimate = 1.6%
Medium estimate = .11.8%
-------
Comments on SIC 3334 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
F004
F005
F006
U080
U210
U226
U239
WP01
WP03
WT01
Spend nonhalogenated solvents:
cresols; cresylic acid,
nitrobenzene; still bottoms from
recovery of above spent solvents;
still bottoms from recovery of
above spend solvent mixtures.
Spent nonhalogenated solvents:
methyl ethyl ketone; carbon
disulfide; isobutanol; pyridine;
benzene, 2-ethoxyethanol; 2-
nitropropane; still bottoms from
recovery of above spent solvents
and spent solvent mixtures
Wastewater treatment sludges
from electroplating
Methylene chloride; methane,
dichloro-
Tetrachloroethylene; ethene;
1,1,2,2-trachloro
1,1,1-Trichloroethane;
methylchlorofoim
Xvlene(i)
EHWW(Halogenated
Hydrocarbons)
Polycyclic Aromatic
Hydrocarbons EHW
EHW (Toxic Daneerous Wastes)
.12
.84
3.00
.02
.001
.42
.03
1.13
8.282
ditto industry comment above
Medium estimate = 1.6%
ditto industry comment above
Medium estimate = .2%
Medium estimate = 4.8%
Medium estimate = .7%
Medium estimate = .12.3%
Medium estimate = 1.7%
10
-------
Comments on SIC 3334 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
{%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
WT02
DW (Dangerous Wastes) Potliner
Tom Dickey, Reynolds
Aluminum believed that the
designation for potliners were
wrong. He believed that WTO 1
was Potliner and kiln dust
wastes, while WT02 was Black
mud (residue of cyanide & carbon
from cryolyte operations). Based
this on fact that they reported
26.000 tons WT02 as black mud
leaving only a balance of 3,500
for potliners. Further, of the 7
aluminum companies that
generate potliner wastes, 3 didn't
designate/report their wastes (did
not meet Washington has. waste
characteristic for reporting, 3 did
designate but as WT01, and
Reynold Al. recycled potliner so
it was exempt from reporting.
If Tom Dickey is correct and
WT02 is black mud, it will be
completely eliminated within 6
months as they close cryolyte
plants, black mud is a residue of
cyanide and carbon from cryolyte
operations (spent potliner is
ground up and mixed with
sodium aluminum floride. the
precipitate is cyanide and carbon).
The spent potliner will still have
to be managed - probably ship
out of state.
29,529
Concern of all industry representatives
that potliner regulation as a RCRA
hazardous waste (KO88) will limit
reduction alternatives. Production
technology is over 100 years old -
hasn't changed much. Extensive
R&D, according to Reynolds
Aluminum & Alcoa ($100 million),
has not significantly improved
production aluminum or extended life
of potliner. Not optimistic that new
technologies exist to reduce potliner
waste.
Some recycling alternatives industry
investigating include - cement kiln
fuel substitute (60+% energy re-
covery) and also a feed stock. Intalco
claims that cement kilns will not
want to risk accepting spent potliners
since they are designated hazardous.
Intalco subsidiary no longer accepts
their spent potliner. However, this
may not be policy of other cement
kirn operations since potliner is
usually free and contains carbon and
aluminum (feedstocks used in cement
process). Other uses include
carbonation (only completed trial
bums to date). Finally, Columbia
Aluminum is investigating a mineral
wool process with an adjacent facility
to the aluminum smelter that would
use all spent potliners. Mineral wool
is an insulating product made from
5-15% reduction in potliner waste
(Tom Dickey, Reynolds Metal and
John Michaelson, Intalco) Primarily
from technology changes that
improve potliner life: this has been
verified by Ted Mix of DOE who has
studied potliner waste generation.
Michaelson's 15% figure is based on
modifications in potliners that Intalco
is making. Anticipate potliner life
extension from 4 to 5 years.
11
-------
Comments on SIC 3334 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
WT02
W001
PCB
41.27
molten coke and slag metal which is
spun into rock wool insulation. The
potliner would be a feedstock
substitute for the metal slag.
Residues from the process would be
recycled through the mineral wool
process again.
Pastes in Bold identify hazardous wastes that qualified for reduction analysis by EPA Region X.
^Hazardous waste stream data from 1986 Washington Generator Annual Dangerous Waste Reports.
3Medium estimate represents EPA Region X estimate of reasonable waste reduction based on statistical analysis prior to "Groundtruthing" Meetings.
12
-------
SOG HAZARDOUS WASTE OUTPUT 198/ IDAHO
Industry Group
Shops
wholesale and
Retail Sales
Relevant SICs
at the
2-digit level
82
83
Total
51
52
53
1987
Employment
Estimate
695.9
0.0
1182.5
2426.6
40(4.3
Waste
Quantity
(Tons/yr/emp)
(National)
1985
Based on
Industrial
Group
0.000552
Hazardous
Waste Generated
For SQGs
By Industry
In Idaho
1987
-------
SOG HAZARDOUS WASTE OUTPUT 1989 IDAHO
Industry Group
Metal Manufacturing
Construction
Motor Freight Terminals
Furniture/Wood
Manufacturing and
Ref inishing
Printing/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Relevant SICs
at the
2-digit level
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
1989
Employment
Estimate
2140.8
10428.7
37.1
181.1
96.9
2994.5
2035.6
2453.4
983.6
4071.2
1173.0
1544.7
4441.7
347.6
376.7
366.7
212.5
222.4
200.0
161.4
475.3
695.1
6134.8
763.7
2536.4
Waste
Quantity
(Tons/yr/emp) V
(National)
1985
Based on
Industrial
Group
0.007695
0.001760
0.000119
0.001213
0.004170
0.001630
0.003179
0.000894
0.000553
Hazardous
laste Generated
For SOGs
By Industry
In Idaho
1989
(Tons/yr)
-
.
16.474
80.253
-
0.285
1.394
0.745
5.269
3.582
4.317
0.117
4.939
1.423
6.441
18.521
1.449
1.571
0.598
0.675
0.707
0.636
0.513
1.511
0.384
3.391
0.422
1.402
Sara Sara
1 2
-
.
1.647
8.025
-
0.029
0.139
0.075
0.878
0.597
0.720
0.023
1.235
-
0.356
0.644
1.852
0.145
0.157
0.100
0.096
0.101
0.091
0.073
0.378
0.064
0.565
0.070
0.234
Sara
3
-
.
0.659
3.210
.
0.011
0.056
0.030
0.351
0.239
0.288
0.005
0.494
-
0.142
0.258
0.741
0.058
0.063
0.020
0.019
0.020
0.018
0.015
0.076
0.026
0.226
0.028
0.093
Sara Sara Sara
456
-
.
1.647
8.025
-
0.029
0.139
0.075
0.878
0.597
0.720
0.012
1.235
.
0.356
0.644
1.852
0.145
0.157
0.050
0.048
0.051
0.045
0.037
0.189
0.064
0.565
0.070
0.234
Sara
7
.
.
0.494
2.408
.
0.009
0.042
0.022
0.263
0.179
0.216
0.004
0.370
.
0.107
0.193
0.556
0.043
0.047
0.015
0.014
0.015
0.014
0.011
0.057
0.019
0.170
0.021
0.070
Sara Sara
8 9
.
.
6.672
32.503
0.116
0.565
0.302
1.756
1.194
1.439
0.051
2.576
7.408
0.580
0.628
0.100
0.096
0.101
0.091
0.073
0.378
0.077
0.678
0.084
0.280
Sara
10
0.644
1.852
O.KS
0.157
Educational & Vocational
Total
0.000871
-------
SOG HAZARDOUS WASTE OUTPUT
Relevant SICs
Industry Group at the
2-diglt level
Metal Manufacturing
Construction
Motor Freight Terminals
Furniture/Wood
Manufacturing and
Ref imshing
Pr i nt i ng/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
Waste
Quant ( ty Hazardous
(Tons/yr/emp) Waste Generated
(national) For SQGs
1985 By Industry
1987 Based on In Idaho
Employment Industrial 1987 Sara Sara
Estimate Group (Tons/yr) 1 2
0.007695
1957.3
8576. 2
33.7
148.6
90.9
0.001760
2826.3
1945.3
2563.9
0.000119
930.7
0.001213
3890.6
1075.5
0.004170
1429.2
4141.3
318.7
353.4
0.001630
366.7
0.003179
194.2
202.0
200.0
151.5
0.000894
439.8
0.000553
637.3
5684.3
695.9
2323.6
15.062
65.998
0.259
1.144
0.699
4.973
3.423
4.512
0.110
4.720
1.305
5.960
17.268
1.329
1.474
0.598
0.617
0.642
0.636
0.482
1.398
0.352
3.142
0.385
1.284
1.506
6.600
0.026
0.114
0.070
0.829
0.571
0.752
0.022
1.180
0.326
0.596
1.727
0.133
0.147
0.100
0.088
0.092
0.091
0.069
0.350
0.059
0.524
0.064
0.214
Sara Sara Sara Sara Sara Sara Sara
3456789
0.602
2.640
0.010
0.046
0.028
0.332
0.228
0.301
0.004
0.472
0.130
0.238
0.691
0.053
0.059
0.020
0.018
0.018
0.018
0.014
0.070
0.023
0.209
0.026
0.086
1.506
6.600
0.026
0.114
0.070
0.829
0.571
0.752
0.011
1.180
0.326
0.596
1.727
0.133
0.147
0.050
0.044
0.046
0.045
0.034
0.175
0.059
0.524
0.064
0.214
0.452
1.980
u.008
0.034
0.021
0.249
0.171
0.226
0.003
0.354
0.098
0.179
0.518
0.040
0.044
0.015
0.013
0.014
0.014
0.010
0.052
0.018
0.157
0.019
0.064
6.100
26.729
0.105
0.463
0.283
1.658
1.141
1.504
0.049
2.384
6.907
0.532
0.589
0.100
0.088
0.092
0.091
0.069
0.350
0.070
0.628
0.077
0.257
Sara
10
0.596
1.737
0.133
O.U7
Educational & vocational
Total
0.000871
-------
$00 HAZARDOUS WASTE OUTPUT 198? IDAHO
Industry Group
Pesticide End-Users
Pesticide Application
Services
Chemical Manufacturing
Wood Preserving
Formulators
laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Relevant SICs
at the
2-diglt level
Total
79
84
Total
07
49
73
Total
28
Total
24
Total
28
Total
72
Total
72
n
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
Waste
Quant I ty Hazardous
(Tons/yr/emp) Waste Generated
(National) For SOGs
1985 By Industry
1987 Based on In Idaho
Employment Industrial 1987 Sara Sara
Estimate Group (Tons/yr) 1 2
0.001350
269.4
0.002803
970.9
273.1
318.7
0.002465
513.3
0.001059
972.6
0.002424
1571.4
0.006960
1720.8
0.002777
573.6
318.7
0.009364
956.0
0.000955
46.7
0.046071
242.7
8007.8
2826.3
2792.1
15.4
2426.6
148.6
2589.5
8427.8 0.000150
5455.1
551.5
2151.0
269.4
0.364
2.722
0.766
0.893
1.266
1.030
3.809
11.977 0.
1.593
0.885
8.952
0.045
11.183
368.926
130.209
128.634
0.709
111.795
6.846
119.302
-
0.820
0.083
0.323
0.040
0.158
1.030
0.317
599 5.390
0.398
0.221
1.279
0.022
1.864
61.488
21.702
21.439
0.118
18.633
1.141
19.884
-
0.164
0.017
0.065
0.008
Sara Sara Sara Sara Sara Sara Sara
3456789
0.032
0.063
0.080
0.044
0.512
-
0.746
24.595
8.681
8.576
0.047
7.453
0.456
7.953
-
0.066
0.007
0.026
0.003
0.079
0.159
0.199
0.111
1.279
-
1.864
61.488
21.702
21.439
0.118
18.633
1.141
19.884
.
0.164
0.017
0.065
0.008
0.024
0.048
0.599 4.
0.060
0.033
0.384
-
0.559
18.446
6.510
6.432
0.035
5.590
0.342
5.965
.
0.049
0.005
0.019
0.002
0.316
0.635
,192
0.398
0.221
2.814
-
4.100
135.273
47.743
47.166
0.260
40.992
2.510
43.744
.
0.328
0.033
0.129
0.016
Sara
10
0.398
O.Z21
1.279
-
-------
SOG HAZARDOUS WASTE OUTPUT 2009 - ALASKA
Sara
11
Sara
12
Sara
13
Sara
14
Sara
15
Sara
16
Sara
17
0.019 0.010 0.096
0.016 0.008 0.080
0.036 0.018 0.178
0.059 0.030 0.297
1.336 55.578 10.847 27.789 218.246 4.484 2.320
-------
SOG HAZARDOUS WASTE OUTPUT 2009 ALASKA
Sara Sara
11 12
0.066
0.031
0.002
0.000
0.009
0.275
0.023
0.012
0.002
0.047
0.073
0.051
0.322
0.030
0.013
0.002
0.018
0.001
0.000
0.003
0.01S
0.013
0.107
0.010
0.073
Sara
13
0.331
0.154
0.009
0.000
0.046
1.377
0.114
0.059
0.236
0.364
0.036
0.179
0.008
0.000
0.030
0.150
Sara
14
0.033
0.01S
0.001
0.000
0.005
0.138
0.011
0.006
0.001
0.024
0.036
0.026
0.161
0.015
0.006
0.001
0.009
0.000
0.000
0.002
0.007
0.007
0.053
0.005
0.036
Sara
15
0.315
0.146
0.008
0.000
0.044
0.012
0.018
0.359
0.015
0.000
0.061
0.052
0.427
0.041
0.290
Sara Sara
16 17
0.331
0.154
0.009
0.000
0.046
0.510
3.215
0.296
0.130
0.179
0.008
0.000
0.030
0.065
0.534
0.051
0.363
-------
SOG HAZARDOUS WASTE OUTPUT 2009 ALASKA
Sara Sara Sara Sara Sara Sara Sara
11 12 13 H 15 16 17
0.253
5.535
0.644
0.996
0.003 0.029 0.001 0.029 0.058
0.006 0.231 0.003 0.058 0.115 0.058
1.336
0.0(4 0.022
0.025 0.012
0.285 0.143 1.141
0.067
0.758 0.379 3.032
20.435 10.217 81.740
7.212 3.606 28.849
3.024 1.512 12.096
0.217 0.109 0.869
2.982 1.491 11.927
14.908 7.454 59.633
4.271 2.136 17.085
0.011 0.005
0.053 0.026
0.003 0.001
O.OU 0.007
0.001 0.001
-------
SQG HAZARDOUS WASTE OUTPUT 2009 ALASKA
Industry Group
Shops
Wholesale and
Retail Sales
Relevant SICs
at the
2-digit level
82
83
Total
51
52
53
2009
Employment
Estimate
553.0
865.4
1941.6
3236.0
Waste
Quant i ty
(Tons/yr/emp)
(National)
1985
Based on
Industrial
Group
0.000552
Hazardous
Waste Generated
For SOGs
By Industry
In Alaska
2009
(Tons/yr)
0.482
0.477
1.071
1.785
Sara
1
0.016
0.036
0.059
Sara
2
0.096
0.080
0.178
0.297
Sara
3
0.039
0.032
0.071
0.119
Sara Sara
4 5
0.096
0.084
0.187
0.312
Sara Sara
6 7
0.029
0.024
0.054
0.089
Sara
8
0.060
0.134
0.223
Sara
9
0.096
0.080
0.178
0.297
Sara
10
TOTALS
1701.106 0.779 284.761 111.156 0.000 277.917 0.000 84.035 5.091 612.574 4.192
-------
IIKU
Industry Croup
Metal Manufacturing
Construction
Motor Freight Terminals
Furniture/Wood
Manufacturing and
Refmishing
Printing/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Relevant SlCs
at the
2-digit level
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
2009
Employment
Estimate
.
430.6
200.0
11.1
0.0
,60.0
4696.5
388.2
200.0
656. 4
776.5
1199.3
611.8
3855.1
355.4
155.6
66.7
394.9
16.7
0.0
66.7
188.2
710.7
5793.2
553.0
3939.6
Waste
Quantity
(Tons/yr/emp) I
(National)
1985
Based on
Industrial
Group
0.007695
0.001760
0.000119
0.001213
0.004170
0.001630
0.003179
0.000894
0.000553
Hazardous
/aste Generated
For SOGs
By Industry
In Alaska
2009
(Tons/yr)
.
3.313
1.539
.
0.086
0.000
0.462
8.264
0.683
0.352
0.078
0.942
1.455
2.551
16.075
1.482
0.649
0.109
1.255
0.053
0.000
0.212
0.598
0.393
3.202
0.306
2.178
Sara Sara
1 2
.
0.331
0.154
.
0.009
0.000
0.046
1.377
0.114
0.059
0.016
0.236
0.364
0.255
1.608
0.148
0.065
0.018
0.179
0.008
0.000
0.030
0.150
0.065
0.534
0.051
0.363
Sara
3
.
.
0.133
0.062
.
0.003
0.000
0.018
0.551
0.046
0.023
0.003
0.094
0.146
0.102
0.643
0.059
0.026
0.004
0.036
0.002
0.000
0.006
0.030
0.026
0.213
0.020
0.145
Sara Sara
4 5
.
.
0.331
0.154
.
0.009
0.000
0.046
1.377
0.114
0.059
0.008
0.236
-
0.364
0.255
1.608
0.148
0.065
0.009
0.090
0.004
0.000
0.015
0.075
0.065
0.534
0.051
0.363
Sara Sara
6 7
.
.
0.099
0.046
.
0.003
0.000
0.014
0.413
0.034
0.018
0.002
0.071
-
0.109
0.077
0.482
0.044
0.019
0.003
0.027
0.001
0.000
0.005
0.022
0.020
0.160
0.015
0.109
Sara Sara
8 9
.
.
1.342
0.623
0.035
0.000
0.187
2.755
0.228
0.117
0.034
1.020
6.430
0.593
0.259
0.018
0.179
0.008
0.000
0.030
0.150
0.079
0.640
0.061
0.436
Sara
10
0.255
1.608
O.H8
0.065
Educational & Vocational
Total
0.000871
-------
SOG HAZARDOUS WASTE OUTPUT 2009 ALASKA
Industry Group
Pesticide End-Users
Pesticide Application
Services
Chemical Manufacturing
Wood Preserving
Formulators
Laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Waste
Quant 1 ty Hazardous
(Tons/yr/enp) Waste Generated
(National) For SOGs
1985 By Industry
R*l«vant SICa 2009 Baaed en In Alaska
at the Employment Industrial 2009 Sara Sara
2-dlglt level Estimate Group (Tons/yr) 1 2
Total
79
84
Total
07
49
73
Total
28
Total
24
Total
28
Total
72
Total
72
73
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
0.001350
187.6
0.002803
1974.5
229.8
355.4
0.002465
93.3
0.001059
194.1
0.002424
285.7
0.006960
1918.9
0.002777
639.6
355.4
0.009364
1066.1
0.000955
140.0
0.046071
493.6
13306.6
4696.5
1969.1
141.5
1941.6
9707.9
2781.3
0.000150
1777.3
8735.1
441.3
2398.6
187.6
0.253
5.535
0.644
0.996
0.230
0.206
0.692
13.356 0.
1.776
0.987
9.983
0.134
22.742
613.047
216.369
90.717
6.518
89.450
447.249
128.136
0.267
1.313
0.066
0.360
0.028
0.029
0.206
0.058
668 6.010
0.444
0.247
1.426
-
0.067
3.790
102.174
36.062
15.120
1.086
14.908
74.541
21.356
0.053
0.263
0.013
0.072
0.006
Sara Sara Sara Sara Sara Sara Sara
3456789
0.006
0.012
0.089
0.049
0.570
1.516
40.870
14.425
6.048
0.435
5.963
29.817
8.542
0.021
0.105
0.005
0.029
0.002
0.014
0.029
0.222
0.123
1.426
-
3.790
102.174
36.062
15.120
1.086
14.908
74.541
21.356
0.053
0.263
0.013
0.072
0.006
0.004
0.009
0.668 4,
0.067
0.037
0.428
-
1.137
30.652
10.818
4.536
0.326
4.472
22.362
6.407
0.016
0.079
0.004
0.022
0.002
0.058
0.115
.675
0.444
0.247
3.137
8.339
224.784
79.335
33.263
2.390
32.798
163.991
46.983
0.107
0.525
0.027
0.144
0.011
Sara
10
0.444
0.247
1.426
-------
SOC HAZARDOUS WASTE OUTPUT 1989 - ALASKA
Sara
11
Sara
12
Sara
13
Sara
14
Sara
15
Sara
16
Sara
17
0.011 0.005 0.055
0.010 0.005 0.048
0.021 0.011 0.107
0.036 0.018 0.179
0.785 37.098 7.164 18.549 145.657 2.936 1.417
-------
SOG HAZARDOUS WASTE OUTPUT 1989 - ALASKA
Sara Sara
11 12
0.051
0.015
0.001
0.000
0.006
0.204
0.018
0.012
0.001
0.038
0.043
0.051
0.189
0.017
0.010
0.002
0.011
0.001
0.000
0.002
0.015
0.008
0.055
0.006
0.041
Sara
13
0.254
0.077
0.004
0.000
0.028
1.021
0.092
0.059
0.190
0.214
0.036
0.111
0.008
0.000
0.024
0.150
Sara
14
0.025
0.008
0.000
0.000
0.003
0.102
0.009
0.006
0.000
0.019
0.021
0.026
0.094
0.009
0.005
0.001
0.006
0.000
0.000
0.001
0.007
0.004
0.028
0.003
0.021
Sara Sara
15 16
0.242
0.073
0.004
0.000
0.026
0.007
0.510
1.889
0.174
0.105
0.018
0.222 0.111
0.015 0.008
0.000 0.000
0.049 0.024
0.031
0.221
0.023
0.166
Sara
17
0.254
0.077
0.004
0.000
0.028
0.039
0.276
0.029
0.207
-------
SOG HAZARDOUS WASTE OUTPUT 1989 -- ALASKA
Sara Sara Sara Sara Sara Sara Sara
11 12 13 14 15 16 17
0.139
3.420
0.425
0.586
0.003 0.029 0.001 0.029 0.058
0.006 0.231 0.003 0.058 0.115 0.058
0.785
0.026 0.013
0.015 0.007
0.168 0.084 0.671
0.067
0.468 0.234 1.874
15.154 7.577 60.616
5.348 2.674 21.394
1.739 0.870 6.956
0.185 0.093 0.742
1.790 0.895 7.159
8.948 4.474 35.794
2.317 1.159 9.269
0.008 0.004
0.036 0.018
0.002 0.001
0.008 0.004
0.001 0.000
-------
SOG HAZARDOUS WASTE OUTPUT 1989 -- ALASKA
Industry Group
Shops
Wholesale and
Retail Sales
Relevant SICs
at the
2-digit level
82
83
Total
51
52
53
1989
Employment
Estimate
314.6
519.2
1165.4
1942.3
Waste
Quantity
(Tons/yr/emp) I
(National)
1985
Based on
Industrial
Group
0.000552
Hazardous
taste Generated
For SQGs
By Industry
In Alaska
1989
(Tons/yr)
0.274
0.286
0.643
1.071
Sara
1
0.010
0.021
0.036
Sara
2
0.055
"
0.048
0.107
0.179
Sara
3
0.022
0.019
0.043
0.071
Sara Sara
4 5
0.055
*
0.050
0.112
0.187
Sara Sara
6 7
0.016
"
0.014
0.032
0.054
Sara
a
0.036
0.080
0.134
Sara
9
0.055
*
0.048
0.107
0.179
Sara
10
TOTALS
1134.048 0.459 189.666 74.197 0.000 185.509 0.000 56.040 2.999 408.986
2.584
-------
SOG HAZARDOUS WASTE OUTPUT 1989 -- ALASKA
Industry Croup
Hetal Manufacturing
Construction
Motor Freight Terminals
Furniture/Wood
Manufacturing and
Ref inishing
Printing/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Relevant SlCs
at the
2-digit level
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
1989
Employment
Estimate
330.6
100.0
5.6
0.0
36.2
3482.8
314.0
200.0
377.5
627.9
705.3
611.8
2264.9
209.0
125.6
66.7
244.0
16.7
0.0
53.8
188.2
417.9
2992.9
314.6
2248.5
Waste
Quantity
(Tons/yr/emp) I
(National)
1985
Based on
Industrial
Group
0.007695
0.001760
0.000119
0.001213
0.004170
0.001630
0.003179
0.000894
0.000553
Hazardous
iaste Generated
For SOCs
By Industry
In Alaska
1989
(Tons/yr)
.
.
2.544
0.770
-
0.043
0.000
0.279
6.129
0.552
0.352
0.045
0.762
-
0.856
2.551
9.444
0.871
0.524
0.109
0.776
0.053
0.000
0.171
0.598
0.231
1.654
0.174
1.243
Sara Sara
1 2
.
.
0.254
0.077
-
0.004
0.000
0.028
1.021
0.092
0.059
0.009
0.190
-
0.214
0.255
0.944
0.087
0.052
0.018
0.111
0.008
0.000
0.024
0.150
0.039
0.276
0.029
0.207
Sara
3
.
.
0.102
0.031
.
0.002
0.000
0.011
0.409
0.037
0.023
0.002
0.076
.
0.086
0.102
0.378
0.035
0.021
0.004
0.022
0.002
0.000
0.005
0.030
0.015
0.110
0.012
0.083
Sara Sara
4 5
.
_
0.254
0.077
.
0.004
0.000
0.028
1.021
0.092
0.059
0.004
0.190
.
0.214
0.255
0.944
0.087
0.052
0.009
0.055
0.004
0.000
0.012
0.075
0.039
0.276
0.029
0.207
Sara Sara
6 7
.
.
0.076
0.023
.
0.001
0.000
0.008
0.306
0.028
0.016
0.001
0.057
0.064
0.077
0.283
0.026
0.016
0.003
0.017
0.001
0.000
0.004
0.022
0.012
0.083
0.009
0.062
Sara Sara
8 9
m
1.030
0.312
0.017
0.000
0.113
2.043
0.184
0.117
0.020
1.020
3.778
0.349
0.209
0.018
0.111
0.008
0.000
0.024
0.150
0.016
0.331
0.035
0.249
Sara
to
0.255
0.9U
0.087
0.052
Educational & Vocational
Total
0.000871
-------
SOG HAZARDOUS WASTE OUTPUT 1989 ALASKA
Industry Group
Pesticide End-Users
Pesticide Application
Services
Chemical Manufacturing
wood Preserving
Fornulators
Laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Relevant SICs
at the
2-digit level
Total
79
84
Total
07
49
73
Total
28
Total
24
Total
28
Total
72
Total
72
73
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
Waste
Quantity Hazardous
(Tons/yr/emp) Waste Generated
(National) For SQGs
1985 By Industry
1989 Based on In Alaska
Employment Industrial 1989 Sara Sara
Estimate Group (Tons/yr) 1 2
0.001350
102.8
0.002803
1220.1
151.5
209.0
0.002465
93.3
0.001059
157.0
0.002424
285.7
0.006960
1128.4
0.002777
376.1
209.0
0.009364
626.9
0.000955
140.0
0.046071
305.0
9867.9
3482.8
1132.5
120.8
1165.4
5827.0
1508.9
0.000150
1369.5
6041.8
264.9
1410.5
102.8
0.139
3.420
0.425
0.586
0.230
0.166
0.692
7.854 0.
1.044
0.580
5.870
-
0.134
14.052
454.620
160.454
52.174
5.563
53.691
268.453
69.516
0.206
0.908
0.040
0.212
0.015
0.029
0.166
0.058
393 3.534
0.261
0.145
0.839
-
0.067
2.342
75.770
26.742
8.696
0.927
8.948
44.742
11.586
0.041
0.182
0.008
0.042
0.003
Sara Sara Sara Sara Sara Sara Sara
3456789
0.006
0.012
0.052
0.029
0.335
-
0.937
30.308
10.697
3.478
0.371
3.579
17.897
4.634
0.016
0.073
0.003
0.017
0.001
0.014
0.029
0.131
0.073
0.839
-
2.342
75.770
26.742
o.oVo
0.927
8.948
44.742
11.586
0.041
0.182
0.008
0.042
0.003
0.004
0.009
0.393 2.
0.039
0.022
0.252
-
0.703
22.731
8.023
2.609
0.278
2.685
13.423
3.476
0.012
0.054
0.002
0.013
0.001
0.058
0.115
.749
0.261
0.145
1.845
-
5.153
166.694
58.833
19.130
2.040
19.687
98.433
25.489
0.082
0.363
0.016
0.085
0.006
Sara
10
0.261
O.K5
0.839
-------
SOG HAZARDOUS WASTE OUTPUT 19Bf
Sara Sara
11 12
0.04?
0.015
0.001
0.000
0.005
0.190
0.017
0.012
0.001
0.035
0.038
0.051
0.168
0.016
0.010
0.002
0.010
0.001
0.000
0.002
0.015
0.007
0.049
0.005
0.038
Sara
13
0.234
0.077
0.004
0.000
0.023
0.950
0.084
0.059
0.173
0.191
0.036
0.099
O.OOB
0.000
0.023
0.150
Sara
14
0.023
0.008
0.000
0.000
0.002
0.095
0.008
0.006
0.000
0.017
0.019
0.026
0.084
0.008
0.005
0.001
0.005
0.000
0.000
0.001
0.007
0.003
0.025
0.003
0.019
Sara
IS
0.223
0.073
0.004
0.000
0.022
0.006
0.018
0.199
0.015
0.000
0.046
0.028
0.196
0.021
0.152
Sara Sara
16 17
0.234
0.077
0.004
0.000
0.023
0.510
1.682
0.156
0.098
0.099
0.008
0.000
0.023
0.034
0.245
0.026
0.190
-------
SOC HAZARDOUS WASTE OUTPUT 1987 ALASKA
Industry Croup
Shops
Wholesale and
Retail Sales
Relevant SICs
at the
2-diglt level
82
83
Total
51
52
53
Waste
Ouant i ty
(Tons/yr/enp) I
(National)
1985
1987 Based on
Enptoyment Industrial
Estimate Group
280.2
0.000552
476.6
1072.2
1786.9
Hazardous
laste Generated
For SOGs
By Industry
In Alaska
1987
(Tons/yr)
0.244
0.263
0.591
0.986
Sara
1
0.009
0.020
0.033
Sara
2
0.049
0.044
0.099
0.164
Sara
3
0.020
0.018
0.039
0.066
Sara Sara
4 5
0.049
0.046
0.103
0.172
Sara Sara
6 7
0.01S
0.013
0.030
0.049
Sara
8
0.033
0.074
0.123
Sara
9
0.049
0.044
0.099
0.164
Sara
10
TOTALS
1047.163 0.412 175.092 68.535 0.000 171.352 0.000 51.752 2.688 377.796 2.336
-------
Relevant SICs
Industry Group at the
2-diglt level
Hetal Manufacturing
Construction
Motor Freight Terminals
Furni ture/Uood
Manufacturing and
Ref inishtng
Printing/Ceramics
Cleaning agents end
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic ft Clinical
Laboratories
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
20
Total
07
30
31
32
Total
26
Total
73
80
82
89
Waste
Quantity Hazardous
(Tons/yr/emp) Waste Generated
(National) For SOGs
1985 By Industry
1987 Based on In Alaska
Employment Industrial 1987 Sara Sara
Estimate Group (Tons/yr) 1 2
0.007695
304.5
100.0
5.6
0.0
29.7
0.001760
3238.4
285.2
200.0
0.000119
336.2
0.001213
570.4
630.6
0.004170
611.8
2017.2
186.8
117.8
0.001630
66.7
0.003179
218.6
16.7
0.0
50.5
0.000894°
188.2
0.000553
373.7
2662.3
280.2
2050.4
.
2.343
0.770
-
0.043
0.000
0.229
5.699
0.502
0.352
0.040
0.692
-
0.765
2.551
8.411
0.779
0.491
0.109
0.695
0.053
0.000
0.161
0.598
0.207
1.472
0.155
1.138
.
0.234
0.077
-
0.004
0.000
0.023
0.950
0.084
0.059
0.008
0.173
-
0.191
0.255
0.841
0.078
0.049
0.018
0.099
0.008
0.000
0.023
0.150
0.034
0.245
0.026
0.190
Sara Sara Sara Sara Sara Sara Sera
3456789
.
0.094
0.031
-
0.002
0.000
0.009
0.380
0.033
0.023
0.002
0.069
-
0.077
0.102
0.336
0.031
0.020
0.004
0.020
0.002
0.000
0.005
0.030
0.014
0.098
0.010
0.076
.
0.234
0.077
0.004
0.000
0.023
0.950
0.084
0.059
0.004
0.173
-
0.191
0.255
0.841
0.078
0.049
0.009
0.050
0.004
0.000
0.011
0.075
0.034
.0.245
0.026
0.190
.
0.070
0.023
.
0.001
0.000
0.007
0.285
0.025
0.018
0.001
0.052
-
0.057
0.077
0.252
0.023
0.015
0.003
0.015
0.001
0.000
0.003
0.022
0.010
0.074
0.008
0.057
.
0.949
0.312
.
0.017
0.000
0.093
1.900
0.167
0.117
0.018
1.020
3.365
0.312
0.196
0.018
0.099
0.008
0.000
0.023
0.150
0.041
0.294
0.031
0.228
Sara
10
0.255
0.841
0.078
0.049
Educational & Vocational
Total
0.000871
-------
SOG HAZARDOUS WASTE OUTPUT 1987 ALASKA
Industry Group
Pesticide End-Users
Pesticide Application
Services
Chemical Manufacturing
Wood Preserving
Formulators
Laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Relevant SICs
at the
2-diglt level
Total
79
84
Total
07
49
73
Total
28
Total
24
Total
28
Total
72
Total
72
73
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
1987
Employment
Estlmnte
92.5
1093.2
140.7
186.8
93.3
142.6
285.7
1009.0
336.3
186.8
560.5
140.0
273.3
9175.6
3238.4
1008.6
116.2
1072.2
5360.8
1384.9
1310.5
5556.6
243.7
1261.2
92.5
Waste
Quant < ty
(Tons/yr/emp) V
(National)
1985
Based on
Industrial
Croup
0.001350
0.002803
0.002465
0.001059
0.002424
0.006960
0.002777
0.009364
0.000955
0.046071
0.000150
Hazardous
taste Generated
For SOGs
By Industry
In Alaska
1987
(Tons/yr)
0.125
-
3.065
0.394
0.524
0.230
0.151
0.692
7.023
0.934
0.519
5.249
0.134
12.592
422.726
149.198
46.466
5.355
49.396
246.979
63.804
0.197
0.835
0.037
0.190
0.014
Sara Sara
1 2
0.029
0.151
0.058
0.351 3.160
0.233
0.130
0.750
0.067
2.099
70.454
24.866
7.744
0.892
8.233
41.163
10.634
0.039
0.167
0.007
0.038
0.003
Sara
3
0.006
0.012
0.047
0.026
0.300
-
0.839
28.182
9.947
3.098
0.3S7
3.293
16.465
4.254
0.016
0.067
0.003
0.015
0.001
Sara Sara
4 5
0.014
0.029
0.117
0.065
0.750
-
2.099
70.454
24.866
7.744
0.892
8.233
41.163
10.634
0.039
0.167
0.007
0.038
0.003
Sara Sara
6 7
0.004
0.009
0.351
0.035
0.019
0.225
-
0.630
21.136
7.460
2.323
0.268
2.470
12.349
3.190
0.012
0.050
0.002
0.011
0.001
Sara Sara
8 9
0.058
0.115
2.458
0.233
0.130
1.650
-
4.617
155.000
54.706
17.038
1.963
18.112
90.559
23.395
0.079
0.334
0.015
0.076
0.006
Sara
10
0.233
0.130
0.750
-------
APPENDIX H
Summary of Small Quantity Generator Analysis
-------
Figure 3
SUMMAR Y SHEET FOR ONE-TIME WASTES FROM STATE SUPERFUND SITES
STATE ALASKA
RIFS - Remedial Investigation/Feasibility Study
p=pre- c-complele
« Operable unit ROD - Record of Decision
ST ** State lead RD Remedial Design UK = unknown
EPA = EPA lead RA - Remedial Action
EM « Esssrfsscy Rscsoval
'where applicable, plage enter operable unit I
Pagel
*pleate enter wane quantities in lom/yeaf
Sll£
Name
ALASKA BATTERY
ENTERPRISES
ARTIC SURPLUS
USAF EIELSON AFB
Ludfill
USAF ELMENDORf AFB
USARMY FT WAJNWRJG
UADOT/FRA
STANDARD STEEL
EPA ID
Number
AKD0049042IS
AKD980988158
AK 1570028646
AKI570028649
AK62I0022426
AKO980975787
*
Lead
EPA
EPA
USA
USA
USA
USD
Site
Manager
KatbRoie
CwlKjB
CulKaz
MiluDTewea
Mike Drewca
Paul Sievke
UK
On
NPL
Y
N
N
N
N
N
Site
Status
pRIFS
EM
pPJFS
pRJFS
pRJFS
pRIFS
pRIFS
Off-Site
Treat
Y
Y
Y
Y
Y
Y
Waste
Description
eQw/lead
lead battery caiugi
Soil w/voc,pah,pcb.Pb.Zj>
Pol. peb, +
Pol. peb. +
Pol, peb, +
Pol. peb. +
KCRA
Code
DOOS
Destinauon
EPA ID*
UTD99130I74S
UK
UK
UK
Treat.
Code
Waste Quanoty (tons/year
1988
4500
1989
1990
1991
1992
1993"
1994
1995
1 2009
-------
Figure 4
SUMMAR Y SHEET FOR ONE-TIME WASTES FROM STA TE SUPERFUND SITES
STATE IDAHO
RTFS = Remedial Investigation/Feasibility Study
p=pre- c**complele
ROD - Record of Decision
Pagel
= Operable unit
ST » Stale lead
EPA - EPA lead
RD Remedial Design
RA Remedial Action
EM = Emergency Remcr-i!
UK = unknown
where applicable, pleuc enter operable unit t
Site
Name
ARRCOM CORP
BUNKER HULL MINING 4.
METALLURGICAL COMPL
PACIFIC HIDE &. FUR
RECYCLING CORP
UNION PACIFIC/
POCATELLO
EPA ID
Number
IDDOOOS0096I
IDD04834092I
EX
IDD098812S78
IDD0555030352
Lead
EPA
EPA
EPA
EPA
Site
Manager
L Marihall
I Meyer/
S Martyn
led \V«U
To) Wall
Ua
NPL
Y
Y
Y
>
Site
Status
pRIFS
R1FS
ROD.RD
RIFS
OfT-Sne
Trot
nuyfac
N
N
mavbe
\Vaste
Descnpuon
SeOw/lead
oil kludge 4. aoil
RCRA
Code
DOM
EPA ID 0
UK
UK
Treat.
Code
M72
M72
please enter wute quumoei u unu/vev
Waste Quantity (tons/year)
F585"
1989
1990
no
2700
1991
1992
1993
1994
1995
2009
-------
Figure B
SUM MAR Y SHEET FOR ONE- TIME H ASTES FROM STA TE SUPERFUND SITES
STATE OREGON
RIFS - Remedial Investigation/Feasibility Study
p^prc" c^complele
= Operable unit ROD Record of Decision
ST = Sute lead RD - Remedial Design UK » unknown
EPA = EPA lead RA - Remedial Acnon
EM Emergency Reisavs!
Page 1
where applicable, please enter oeenble unit i
SlU
Name
ALKAJLAKE
IBERGSOE METAL
CORPORATION
IBROADWAY CAB
CASCADE CORPORATION
DAMT A. RUSSELL
(MILL SFTE)
FORREST PAINT
EPA ID
Number
ORD9805 11497
ORD99128M60
ORD00903I37I
ORD9S0639629
ORD06M27306
OO
Lead
ST
ST
ST
ST
ST
ST
Site
Manager
M Rosen
Ann Levue
M Rosen
Paul Buroet
BillDuu
&andr> Anderco
On
NPL
N
N
N
N
N
N
Site
Status
pRTFS
pRIFS
pRIFS
RTFS
UFS.EM
RIFS
OfT-Sne
Treat
UK
Y
UK
N
Y
UK
Waste
Description
herbicides in aoO tt
J£l UundwBtCT
(OH
peotaeU dudge
ubesu»& muc
labehenieali
nD w/chenucali
ftuttwtaes
kCRA
Code
DOOB
FOZ1
DOOI
D001
D004
D007T
D008V
F003 ]
F005-'
Destination
EPA ID 17
UK
ORD0894523S3
WAD0008I2917
ORD089452353
ORD08M52353
*please enter waste quantities in tons/vear
Treat.
Code
waste (juanaty (tons/year)
1988
5
13
7
317
429
1989
1990
1991
1992
1993
1994
1995
2009
-------
Figure 5 (cont.)
SUMMAR Y SHEET FOR ONE-TIME WASTES FROM STATE SUPERFUND SITES
STATE OREGON
Page 2
where applicable, pleaate enter operable unit 1 *please enter waste quantities in tons/year
Site
Name
GOULD/NL
INDUSTRIES, INC
J H BAXTER & CO
EUGENE
{JOSEPH FOREST PRODUC
LAKE OSWEGO PUBLIC
WATER SUPPLY
it D McFARLAND
LAUREMCE DAVID. INC
IMALARKEY ROOFING CO
1 MARATHON PROPERTIES
1
IMARTIN -MARIETTA
EPA ID
Number
ORD095003687
ORD009032400
ORD06B782820
ORD009026600
ORD009023524
ORDOS222I02S
Lead
EPA
ST
ST
EPA
ST
ST
ST
ST
ST
ST
IEPA
ST
Site
Manager
David Tctu
Aon Levue
Bill Duu
KatbRote
E Eeelei
E Eccla
Paul Burnet
Aon Levine
Bill Rcnfrcc
S Andenon
lanet O'Han
Bill Renfroe
Oa
NPL
Y
N
Y
N
N
N
N
N
Y
Site
Status
ROD.RJD
pRIFS
pRIFS
pRJFS
pRJFS
pRJTS
pRIFS
RJFS
ROD.RD,
RA.EM
Off-Site
Trau
N
UK
UK
UK
UK
N
N
UK
N
Waste
Description
PCP «. PAHt in tod and
ground water
folvents in aoil &
ground water
incinerator alh v/lead li
other neuli
RCRA
Code
Destination
EPA ID «
Treat.
Code
Waste Quantity (tons/year)
1988
1989
1990
1991
1992
1993
1994
1995
2009
-------
Figure 5 (cont.)
SUMMARY SHEET FOR ONE-TIME WASTES FROM STATE SUPERFVND SITES
STATE OREGON
wbcrt policablc. pleuc enlcr operable unit If
Site
Name
MILWUKIE PUBLIC WATE
SUPPLY
MULLER MOBILE HOME
PROJECT
N1COLA1 CO
NORTHWEST PIPE i
CASING. PORTLAND
INU WAY on. COMPANY
OREGON CONVENTION
CENTER
P C DEVELOPMENT. INC
PENDELTON GRAIN
GROWERS -HERMJSTON
PORTABLE EQUIPMENT
SALVAGE
EPA ID
Number
t
ORD980988307
ORDO090555J4
ORD 144987039
ORD02761S186
Lead
ST
ST
ST
ST
ST
ST
ST
ST
ST
Site
Manager
E Eccl*
Bruce Cilia
BillDuu
Bill Dun
M Rosen
M Rosen
Ann Levioe
Bruce Gillu
BDl Duu
On
NPL
N
N
N
N
N
N
N
N
N
Site
Status
pRIFS
pRJFS
pRIFS
pRIFS
pRTFS
pRIFS
pRIFS
RffS. E
OfT-Sne
Treal
UK
UK
UK
UK
UK
Y
UK
Y
UK
Waste
Description
mercury conuuunifltcd raobil
home
soil w/metals
nlveou u proundwater
SoD w/P&U ILII pctucidei
RCRA
Code
F006
P' \
U- J
Destuulion
EPA ID IT
(oon-RCRA ludTdl)
ORDOS0973417
ORD0894S2353
Treat.
Code
M72
Page 3
please enter waste quantities m Ions/year
Waste Quantity (loos/year)
1988
1350
1989
380
1990
1991
1992
1993
1994
1995
2009
-------
Figure 5 (cont.)
SUMMARY SHEET FOR ONE-TIME WASTES FROM STATE SUPERFUND SITES
STATE OREGON
Page 4
please enter waste quantities in Ions/year
Site
Name
PORTLAND GENERAL
ELECTRIC-STATION L
RHONE-POULENC
ROSE CfTY PLATING
SCHNITER ZIDELL MOOD
STREET SITE
ISOUTII WATERFRONT
REDEVELOPMENT
TELEDYNE *AH CHANG
ALBANY
UMATD.LA ARMY DEPOT
ACTIVITY
UNION PACIFIC RAO.ROA
THE DALLES
lUNTTED CHRONfE
PRODUCTS
EPA ID
Number
ORD007909054
ORD990&S9492
ORD00040W35
f
ORD98 1769474
ORD050955M8
OR62I38209I7
ORD009049412
ORD009M300I
Lead
ST
ST
ST
ST
ST
EPA
ST
ST
ST
ST
EPA
Site
Manager
P Burno
Sandra Andeno
M Rotea
Bruce Cnllej
M Rottn
Ned Tbonpsoo
BOlDana
BdJDana
Sandra Anderto
Paul Bunet
L McPhillipi
OD
NPL
N
N
N
N
N
Y
Y
N
Y
Site
Status
RIFS
RIFS. RA
pRIFS
pRIFS
RIFS
RIFS
RIFS
RIFS
ROD.RA
Off-Site
Treat
-Y
UK
Y
UK
UK
UK
UK
UK
Y
Waste
Description
Soflw/pcb
pencidei & pbenobcl in
jtiouod water & aou
plauog aludge
SoO w/beavy nwlalt &
pemcidcs
eonuniniled groundwaler
and tod
Sludge w/hvdroude
RCRA
Code
F006
D- 1
U- J
D007
DestmaUon
EPA IDA
IDD073II46S4
UK
ORD0894S2353
ORDOS94523S3
Treat
Code
M72
M72
Waste Quantity (tons/year)
1988
2500 ey
35
1989
70
110
100
1990
130
1991
130
1992
35
1993
35
1994
35
1995
35
2009
-------
Figure 6
SUMMARY SHEET FOR ONE-TIME WASTES FROM STATE SUPERFUND SITES
STATE WASHINGTON
RIFS Remedial Investigation/Feasibility Study
p^-pie cBcomplete
" Operable unit ROD «= Record of Decision
ST > State le*d RD = Remedial Design
EPA «= EPA lead RA " Remedial Action
EM > Emergency Removal
P.gel
UK = unknown
where applicable, plow eater operable unn *
Site
Name
ALCOA -VANCOUVER
COLBERT LANDFILL
COMMENCEMENT BAY
-SEAJtSHORETIDEFLATS
ASARCO/RUSTON
NEARSHORE/TIDEFLAT
TACOMA TARPFTS
COMMENCEMENT BAY
SOUTH TACOMA CHANN
TACOMA LANDFILL
TACOMA LANDFILL
TACOM'^SWANfP
WELL I2:A
EPA ID
Number
WAD009W5279
V-AH9805I4MI
WADOIOI87896
WAD980726368
WAD9M72379S
L
WAD9S072630I
WAD0007L2265
WAD980986731
WAD98072423I
Lead
ST
EPA
ST
EPA
EPA
EPA
EPA
ST
ST
ST
Site
Manager
Ted Mu
N Thompson
Mike Blum
Keith Rose
Mike Stoner
L Mmhall
D Yunaraao
C CUTOSUIO
C Ctrrosuio
G Ctrrosino
On
NPL
Y
V
V
Y
Y
Y
Y
Y
Y
Sue
Sums
RIFS
ROD RD
RIFS.EM
RIFSc
ROD.RD.R
ROD
ROD.RD.E
pRIFS
ROD RDR
EM
Off-Site
Treat
UK
N
Y
N
N
UK
N
UK
N
waste
Description
demolition debtu
building debns
toD w/lead
sod w/orf anic« S. lead
RCRA
Code
DOOS
Destj nation
EPA TO*
ORD0894S2353
ORD0894S2353
Treat.
Code
M72
*plea3e enter qaanitia IB tons/year
^asie Quanuty (tons/year)
FI988
11000
110
1989
1990
1991
1992
1993
1994
1995
2009
-------
Fioure 6 (oont.)
SUMMARY SHEET FOR ONE-TIME WASTES FROM STATE SWERFUND SITES
STATE WASHINGTON
RIFS " Remedial Investigation/Feasibility Smdy
p=»pre- c*>complele
«= Openble unit ROD - Record of Decision
ST *> Slate lead RD » Remedial Design
EPA " EPA lead RA " Remedial Action
EM - Emergency Removal
Page 2
UK » unknown
where ip]
Site
Name
HARBOR ISLAND
NON-FERROUS METALS
SEATTLE IRON & METAL
SHELL. OLD TANK
HIDDEN VALLEY LANDFIL
THUN FIELD
IKMSER ALUMINUM
fMEAD WORKS)
LAKEWOOD
PONDERS CORNER
MICA LANDFILL
MIDWAY LANDFILL
NORTHS1DE LANDFILL
MOPTHWEST TRANSFOR
MISSION RD
EPA ID
Number
WAD9M772839
1
L
WAD980SIIS39
WAU00006S508
UADOS007S662
WAD9S051I66I
WAD9806389IO
WAD9805M778
WAD9S0833974
Lead
EPA
ST
ST
ST
ST
ST
EPA
ST
ST
EPA
EPA
pbeible. plaue enter operable unit t
Site
Manager
Keith Row
D Carpll
M Rosenberg
D Cu|3]
G Cftrrocino
Ted Mix
1 O'Hani
D Cunmiafs
R ICrunnilali
N Thoraown
Sallv Mamn
On
NPL
Y
Y
Y
N
Y
1
Y
Y
Y
^
1
Site
Status
RIFS. EM
RffS
RTFS
RD
RTFS
RIFS
ROD. RA
RIFS
RIFS. EM
RIF&c
ROD
Off-Site
Tre«l
Y
UK
UK
UK
UK
UK
N
UK
UK
UK
N
Waste
Description
tedunenu it/lead
RCRA
Code
DOOJ
EPA ID ff
ORD0894S23S3
Treat:
Code
M72
please enter quinine* in uneven
Waste Quantity (tons/year)
T9?8~
275
1989
1990
T991
1992
1993
1994
1995
2009
-------
Figure 6 (oont.)
SUMMARY SHEET FOR ONE-TIME WASTES FROM STATE SUPERFUND SITES
STATE WASHINGTON
RIFS Remedial Investigation/Fusibility Study
p=pre- c=complete
«= Operable unit' ROD - Record of Decision
ST State lead RD * Remedial Design
EPA - EPA lead RA > Remedial Acdon
EM Emergency Removal
Page 3
UK - unknown
oboe ippliublt. pleue eater openble ma t
Sit*
Name
QUEEN CfTY FARMS
ISEVTTLE MUNICIPAL
LANDFFLL K£NT HIGHLA*
SILVER MOUNTAIN MINE
ISIMPSON -TACOMA K.RAF
(PRP, cot Siiperfund')
ISTRANDLEY/MANNING
WYCKOFF co
WYCKOFF/EAGLE HARBO
YAKIMA PLATING
EPA ID
Number
WAD9 80S! 1745
W/VD9S0639462
DS
WAD9807I2789
WAD0825 10595
WA.D980976328
WAD009248295
WMXMOI87I90
01
02
Lead
FJ>A
ST
EPA
ST
EPA
tPA
EPA
EPA
Site
Manager
Ted Kill
R Kiuhoilih
I O'Hara/
K Rose
C Beu
Ted Wdl
Dtvid Tetu
Divid Tetu
Divid Tetu
On
NPL
\
V
Y
Y
V
Y
Site
Status
RIFS. EM
RTFS
RIFS
pRJFS
pRJFS
pRJFS
Off-Sne
Tre»
^
UK
UK
N
Y
Y
Waste
Description
lludge mix meuli. PCBi.
volmlei. PAH>. penieidM
io3 & dodge earae
creosote sludpe
iputoble wane
RCRA
Code
F003 1
D0071
D008-1
FOOST
D006T
D008 J
DOOI
D001
EPA \.D.f
(mcinemioB)
ORDOS94SUS3
ORD08945I333
ORD0894S23S3
Treat.
Code
MSO
M72
*pleaie enter quantity ID loaiiyear
nsr
SO
11000
I7SO
07
1989
1990
1991
1992
I99J
1994
1995
2009
-------
Figure 7
SUMMA K Y SHEET FOR RCRA CORRECTS/CLOSURE A CT1ONS WITH OFF-SITE TRCA TMENT
STATE ALASKA
GENERAL STATUS CLOSURE STATUS
I = Interim Sums PR = Plao Received
2 = Permit Issued CPA = Closure Plao Approved
4 = Closing pCPA - post-Closure Plan Approved
0 = Other (Closing) CR * Certificate Received
A > Permit Denied
Page 1
CORRECTIVE ACTION STATUS
RFA - RFA Onpouig/Complele UK = Unknown
RFI = RF1 Required
CMS < Corrective Measure Study Ongoing/Complete
where gpriicable pletue enter wine muafunaa unit *
*pleaie enter quantify in lent/year. if potnble
Site
Nine
NORTH POLE REFINERS
USDOT-FAA (MHM)
LAKE MINCHUNdNA
EPA ID
Number
AKD00085070I
AK 7690590012
Lad
EPA
EPA
Siu
Muuccr
B31 Adarai
Svivu Burpu
Site Sunit
Gen ICIot/Corr
0
0
RFA.RFI
RFA.RFI
CMSru)uircc
Of(-Slt£
Treat
UK
\Vuu
Dcscnpooo
cooUumiuifd loD
toil «/ dioun. 2.4D. oil.
DDT, PCBi. solvents
Type
Code
Deaimnaa
EPA Sue ID*
Treat
Code
Mane Ouuiurv (umi/veu)
1988
1989
1990
1991
1992
1993
1994
I99S
2009
-------
Figure 8
SUMMAR Y SHEET FOR RCRA CORRECTI\'E/CLOSURE ACTIONS WTTH OFF-SITE TREATMEffT
STATE IDAHO
GENERAL STATUS CLOSURE STATUS
1 = Interim Status PR = Plan Received
2 « Permit Issued CPA - Closure Plan Approved
4 » Closing pCPA *> post-Closure Plan Approved
0 = Other (Closing) CR = Certificate Received
A ° Permit Denied
Page I
CORRECTIVE ACTION STATUS
RFA » RFA Ongoing/Complete UK = Unknown
RFI = RFI Required
CMS = Corrective Measure Study Ongoing/Complete
where ipebcable please enter wane management unit t
Siu
Name
-IHVTROSAFE SERVICES
OF IDAHO -SITE A
MORRISON KNUDSON
BOISE COMPLEX
'RESSURE TREATED
TIMBER
JSDOE IDAHO NAT'L
ENGINEERING LAB
_TAH POWER «. LIGHT
POLE YARD
EPA ID
Number
IDDOOOT73952
IDD980976831
IDD0471MOI1
ID4890008952
IDD00060203I
.
Lead
EPA
EPA
EPA
EPA
EPA
Sac
Manager
Wallace Reid
Janet O'Hara
C Ahlnroro
» N Pierre
Margaret Small
Site Sunu
ICenlCloVCorr
4
1
2
1
RFA.RFI.
CMS
RFA.CPA
RFA.RFI
CR.pCPA
RFI.RFA
RFA.RFI.
CMS
arr-sne
Treat
Y
N
N
N
Y
Wane
Description
leachate from mutile tilo
spent carbon Iroro
croundwater cleanup
type
Code
many
U05I
Deatination
EPA Sne IDf
UK
ARD06974SI92
UTD99I30I748
Cixle
M50
M50
pleaae enter quantity in una/vear. if poaiible
V-.« Quarmty (tonayyeu)
1988
50
1919
3
50
1990
3
50
1991
50
1992
50
1993
50
1994
SO
1995
50
2009
-------
Fioure 9
SUMMARY SHEET FOR RCRA CORRECTS'CLOSURE ACTIONS WTTH OFF-SITE TREATMENT
STATE: OREGON
GENERAL STATUS CLOSURE STATUS
1 - Interim Status PR « Plan Received
2 - Permit Issued CPA - Closure Plan Approved
4 = Closing pCPA ~ poM-Clo"!ure Plan Approved
0 » Other (Closing) CR = Cemricaie Received
Pice I
CORRECTTVE ACTION STATUS
RFA » RFA Onpoinp/Cotnplele UK = Unknown
RFI = RFI Required
CMS *= Corrective Measure Stud; Ongoing/Complete
»here applicable ftt»te enter mult mmateraenl unit t
*ple«ie enter quantity la tom/ve«r. if pomble
Sue
Nine
ARNAV SYSTEMS INC
BOEING PORTLAND
CASCADE V.OOD PROD
COLUMBIA HELICOPTE
EVANFTE fFfBER-BATTE
SEP DIVISION)
JOHNSON CONTROLS IN
(GLOBE BATTERY DtV
IMADRASCm AIRPORT
IM^KIIN MAKJEI 1 A
IMEU. DATA APMS
EPA ID
Number
ORD 106072010
ORDOVI 96*481
ORD09289425I
ORD009613609
ORD00902 <466
ORDOI0746402
ORDOU9I9739
ORD0522ZI02S
ORD0345953S5
Lad
ST
EPA
ST
ST
EPA
ST
ST
ST
57
Sue
Muiifer
Rirtiin Puchi
W N Pient
Fred Bromfcld
fji Cbonf
C Ahlniora
Fied Bromfcld
Bnihora Pueh)
Fred Biomlcld
John hoi)
Sue Suuu>
IGenlCln
FOIO
Dcmnanon
EPA Sne \D>
UK
lupuvc nemmeni
hciliry)
UK
Treat
Cede
M72
M7:
Vriute Ouannrv (loni'veai)
IOSS
1919
22
1500
1990
1991
1992
1993
1994
I99S
2009
-------
Figure 9 (cont.)
RCRA REGION X OREGON
»here ippltuhle plejue enter wane rnuiitreinent unit f
SOJ
Hint
MONTEZUMA *-EST
NORTHWEST AVIATION
INDEPENDENCE AIRPC
NORTHWEST INDUSTR1
JMARK INDUSTRIES
MANUFACTURING
)R£CON REGIONAL
PRIMATE CENTER
ACIFIC FABRICATORS
ERMAPOST PRODUCTS
OTTER MANUFACTURI
£IDEL IXTERNATIOSA
ECHNICAL IMAGES
EKTRONDi INC
EKTRONIXfTANK CLO
HP EC M
EPA ID
Number
ORD(U4II3I27
ORD09500400I
RT
ORD009020S35
ORDOI0736262
ORDOJ4263S9S
ORDISI093267
ORD009041IS7
ORD009CM9MS
ORD0089V1473
ORD0094I4673
ORD00902023I
URE)
ORD98098550I
Ua4
EPA
ST
ST
ST
ST
ST
EPA
ST
ST
ST
EPA
ST
ST
Sue
Snr Sutiu
Mui>r« iGcnlClm/Con
V. N p.ctrc
Mike Rcu
MikeRciu
JohnBoDk
John Baik
Mike Renz
C Ahliuora
Mike heu
Ld Chonf
John Boil
C Muuinuin
Fied Bromleld
John Boil,
0
0
0
0
1
C
0
(1
1
0
RFA.RFI
RFARFI
CMS
RF1
RFI.PR
CMS
CPA.pCPA
IFA.RFI.CF
RFA RFI.
PR.CMS
PR.CPA
pCPACR
CPA.pCPA.
RFA RFI
CR CMS
PP
Off Sue
Treni
N
^
Y
N
N
V
^
V
V
Y
N
Y
UK
Description
rereneraicfl cjirhon
chfome
tcl-KlU
ml «/MEC
TCE
Punt ftludpe
srcm earboo Iron
FroumJwater clmnup
wlventl. toluene MEK
benrene
Soil w/pch
Sod w/pum winei
folwentx
Snil wiprrrnlrurn
Type
Cndr
D007
=002
F003
PW2
DOOI
FOI7
FOiK
XOK
F006
FOOS
D002
DOOI
EPA Site IDf
tnc
VfADOaM7;i7S
ORDOS
-------
figure 9 (cont.)
RCRA RECION X OREGON
Pipe 3
where applicable plcue enter wane rauupemem onit 0
Sue
Nlme
VALLEY PLATING
VAN WATERS *. ROGER
PORTLAND
VAN WATERS & ROGER!
VELCO EUGENE
VELCO
EPA ID
Number
ORD05i;27S68
ORD09922739S
ORD009JIUOO
Lad
ST
EPA
ST
EPA
ST
S.<
Mimrei
John Boik
V. N Pierre
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0
4
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N
\
Y
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EPA Site ID'
UK
UK
ORD080452353
Treat
Code
M72
*f4eaie enter quannrv ta lotu'veu. If possible
V.KIC OiVBOtv Itont'veu)
19(8
1989
1990
74
1991
1992
1993
1994
1995
2009
-------
Figure 10
SUMMARY SHEET FOR RCKA CORRECTfl'E.'CLOSURE ACTIONS WITH OFF-SITE TRFATMENT
STATE WASHINGTON
GENERAL STATUS CLOSURE STATUS
I = Interim Statin PR - Plan Received
2 Permit Issued CPA > Closure Plan Approved
4 " Closing pCPA « post-Closure Plan Approved
0 - Other (Closing) CR - Certificate Received
A = Permit Denied
Pipe I
CORRECTIVE ACTION STATUS
RFA - RFA Onpomp/Complete UK = Unknown
RFI = RFI Required
CMS = Corrective Measure Study Ongoing/Complete
where ipnliceble pleue emer wuw nunifcinc
Site
Nime
AMERICAN PLATING
(I* LEWIS R JONES)
JAKCO PETROLLEUM
CHERRY POINT
BPOILCOMPAM
FERNDALE
ICAMEPOI* YAKIMA
CHEMICAL PROCESSOR
s LUCO.EST
CROSBY L OVERTON
PLANT*!
IDEU1LS INDUSTRIES
iCREAT WESTERN
CHEMICAL
IHVTF.I
IPCO (INTERNATIONAL
PAPF.P -MOOD PPOD )
EPA ID
Number
WAOOE?350231
WAD069348IM
WAD0092S0366
WAD009477I7J
*AD0008i:90«
WAD99 i:S 1767
WADOOU^^S?:
V.AD0560S3S20
WAD0766JSIS2
WAU01074S9I7
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CPACR
RFA.RFI
RFA. RFI
CPA
RFA RFI
RFA.RFI
3013
RFI
3013
CPA.pCPA
RFA.RFI.
CR.CMS
CPA.pCPA
RFA.RFI
in anil H
Ofl-Snc
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UK
UK
UK
UK
Uk
til.
N
UK
V.HJU
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soil wrperchlorcellnlcnc
solvents in prnundwuter
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Type
Cnde
D007
DemaiuoD
EPA Site ID'
Tren.
Code
pieaiK enter quantny in umwear. if pouibie
1988
1980
1990
1991
1992
1993
1994
I99S
2009
-------
Figure 10 I cent.)
RCRA REGION X W ASHJNOTOH
Ptftl
where applicable pleaje cmn vuie nanitemem unit >
S,u
Name
MANCHESTER FUEL
DEPOT
MASCO PRODUCTS
McCLARI COLUMBIA
WASHOUGAL
NW PETROCHEMICAL
OCCIDENTAL CHEMJCA
PENDELTON WOOLEN
MILLS
IREICHOLD CHEMICAL
SEAFAfi METAL COW
SHELL OIL
ANACORTES
TEXACO REFINING
MARKETING
L'SDA SLA MAXIMA
AC P.ESEAJ>CH LAB
EPA ID
Number
VkA2l7PO:>426
WAD009^(M24
V. ADW: 300150
WAD009624M7
WAD0092423I'
WAD009C35502
WAD 009 152191
WADOJ86tI3l6
WAD009275082
WAD009276I97
WAD 1205 13957
LCM)
EPA
EPA
EPA
EPA
EPA
EPA
EPA
EPA
EPA
EPA
EPA
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Manlier (GenlCloi'Con
S Huriei
J Ballet
V. N Pierre
C MaMinuno
W. N Pierrt
Marcarel Small
Marcia Bailey
C SiVorik)
C Sikorikj
Bill Adann
4
1
0
2
0
2
1
2
2
0
RFA
FA.RFI.P
UFA RF1
RFA RFI
RFA.RFI
CMS
3008(h)
CPA.pCPA
RFA.RFI
CMS
CR
RFA RFI
RFA RFI
RFA RFI
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Irul
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UK
N
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1
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Wane Ouantirv |u»<'vut)
I9R8
1989
1990
1991
1992
1993
1994
1995
2009
-------
figure 10 Icont.)
RCRAREG10KX WASHINGTON
here tpolieiblc ple*M enter wuie mejiirement unit t
Site
NlRW
VANPORT INDUSTRIES
VAJ. WATCRS & POGER
EPA ID
Number
WAD065IS7875
WAEOW«!Mi<
U*d
EPA
E»*
Sue
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) Boiler
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V
ItK
Wide
DucrtptKm
drum* of ««
-------
Off-Site Management; This column indicates whether (Y) or not
(N) wastes will be shipped off site for management.
Waste description; This column describes the form or
characteristics of the hazardous waste to be managed.
RCRA (waste) Code: This column provides the RCRA hazardous
waste code associated with each waste type listed in the waste
description column. When the waste consisted of several
different types of wastes, the waste codes are connected by
a bracket. Site managers were not always able to identify
waste codes for each waste description.
Destination EPA ID #; This column provides the EPA
identification number of the RCRA facility to which the
hazardous waste will be sent.
Treatment Code; This column provides the off-site RCRA
hazardous waste management code for the type of treatment of
the waste (see Appendix I).
Waste volume: This column provides the estimated volume of
specific hazardous wastes to be managed off site for the years
1988 through 1995 and 2009. Capacity Assurance Plan only
requires projections for 1989, 1995 and 2009, the table
provides, where possible, waste to be shipped off site for
every year between 1989 and 1995. Site managers were rarely
able to project hazardous waste off site shipment for 1995.
No managers were able to determine waste quantities for 2009.
However, managers were able to provide estimates for the years
between 1989 and 1995. Waste quantities are estimated in
(short) tons. Most waste quantities were reported in either
cubic yards, gallons, or drums. These quantities were
converted into short tons (2000 Ib.) using the following
equations:
(1) 1 cubic yard =1.09 tons,
(2) 1 gallon = 8.25 pounds,
(3) 1 drum = 55 gallons = 0.22 tons.
-------
investigation, a "No" was interpreted as "Unknown". This
interpretation was usually not altered by the EPA or state
during review, and was considered to be correct.
Waste description; This column describes the form or
characteristics of the hazardous waste to be managed.
RCRA (waste) Code: This column provides the RCRA hazardous
waste code associated with each waste type listed in the waste
description column. When the waste consisted of a mixture of
several different types of wastes, the waste codes are
connected by a bracket. Site mangers were not always able to
identify waste codes for each waste description.
Destination EPA ID #; This column provides the EPA
identification number of the RCRA facility to which the
hazardous waste will be sent. UK indicates that the exact
destination was unknown at the time of the survey.
Treatment Code: This column provides the off-site RCRA
hazardous waste management code for the type of treatment of
the waste (see Appendix I).
Waste volume; This column provides the estimated volume of
specific hazardous wastes to be managed off site for the years
1988 through 1995 and 2009. While the Capacity Assurance Plan
only requires projections for 1989, 1995 and 2009, the table
provides, where possible, waste to be shipped off site for
every year between 1989 and 1995. Site managers were rarely
able to project hazardous waste off site shipment for 1995.
No managers were able to determine waste quantities for 2009.
However, managers were able to provide estimates for the years
between 1989 and 1995. Waste quantities are estimated in
(short) tons. Most waste quantities were reported in either
cubic yards, gallons, or drums. These quantities were
converted into short tons (2000 Ib.) using the following
equations:
(1) 1 cubic yard =1.09 tons,
(2) 1 gallon = 8.25 pounds,
(3) 1 drum = 55 gallons = 0.22 tons.
-------
Explanation of "Summary Sheets for One-Time Wastes from State
Superfund Sites"
The summary sheet is broken down into 13 columns of information;
a description of the information contained in each column is as
follows:
Site Name; This column provides the Superfund site name
and/or location.
EPA ID Number; This is the EPA identification number assigned
to the site by the EPA. Since these numbers were not
requested in the original matrix the contractor matched the
site name with those listed on CERCLIS List 8 for Region X.
Operable Unit Number: Certain sites have several individual
operating units, but the contractor was not able to accurately
assign operable unit numbers from CERCLIS List 8. Operable
unit numbers were requested when the summary sheets went to
the EPA and state for review, but unit numbers were provided
for only one site.
Lead; This column identifies the source of the information
as being from the State (ST) or from the EPA manager. Some
sites have both State and EPA staff overseeing operations.
Site Manager; This is the site managers name as provided on
the one-time waste information matrix.
On NPL: This column indicates whether (Y) or not (N) the site
is listed on the National Priorities List.
Site Status: This column provides the current stage of
Superfund activity occurring at the site as indicated by the
managers on the "One-Time Waste Matrix." The status codes
are as follows: RIFS (remedial investigation/feasibility
study); pRIFS (pre-RI/FS stage or preliminary investigation
started); RIFSc (RI/FS completed); ROD (record of decision);
RD (remedial "design); RA (remedial action); EM (emergency
removal).
Off-Site Management: This column indicates whether (Y) or not
(N) wastes will be shipped off site for management. A UK (for
"unknown") was used when the staff person did not yet know
whether off-site treatment would be necessary. In earlier
drafts of the matrix, question 14 asked, "Waste being managed
off-site?" If the site was in a preliminary stage of
-------
APPENDIX G
Summary of One-Time Waste Analysis
-------
GROUNDTRUTHING NOTES
OREGON
C022-002
PLATING AND POLISHING
SIC 3471
H. Michael Pessl. P.E.
Engineering Manager
Aero DDL
1270N.W. 167& Place
Beaverton, Oregon 97006
(503) 645-3807 fax: 629-8494
Ronald L. Graham
Independent Resource Service
Mailing Addr P.O. Box 14432
2625 S.E. Hawthorne
Portland, Oregon 97214
(503)231-7511
Dave Pofahl
Beaverton Parts MFG.
1800 N.W. 216&
Hills, Oregon 97124
(503) 645-1214
Industry Attendance
Cheryl J. Davis
Chemist
PSI Manufacturing Corp.
514 Milton Way
St Helens, Oregon 97051
(503) 397-4512; Fax: 397-5682
C. Ted Ball
Luhr Jensen & Sons
(503)386-3811
George Dalich
Praegitzer Industries, Inc.
(503) 623-9273
Jim Thipodeau
Vice President
East Side Plating, Inc.
310 S.E. Stephens
Portland, Oregon 97214
(503) 233-8554; Fax: 234-1952
Diane Stockton
Omart Industries
(503) 653-4269
13
-------
Comments on SIC 3471 - Polishing and Plating
EPA
Waste
Code1
Waste
Description
Quant
Gen
Tons
19862
Estimated
Reduction
1989
Estimated
Reduction
1995
Estimated
Reduction
2009
Total Quantity Waste Generated
General comments:
Participants represented diverse
group of electroplators. Circuit
board manufactures, in general,
were more likely to have
instituted or will institute waste
reduction activities. The nature
of their operations required greater
control over production and more
stringent quality controls. Other
participants (e.g., Luhr Jensen &
Sons who manufactures fishing
lures) were less optimistic about
waste reduction activities and the
means by which they were going
to meet waste reduction
percentages they specified.
participants raised the issue of
economic incentives and
regulation as major factors for
reducing waste generation.
407.55
Apogee median estimate for all waste
types = 2.9%
General comments: There is
increasing acceptance by electroplators
to conserve water. The rate of
acceptance of these technologies and
process changes is slow. The types
of process changes include closed-loop
cooling, counterflow rinsing, etc...
These processes affect the volume of
waste generated for each of the wastes
below. "Black hole" technology
instead of Electrolysis Copper is
another conservation measure.
Apogee median estimate all waste
types = 8.6
Apogee median estimate all waste
types = 22%
D001
Igni table Waste
9.79
20% (Dave Potahl - process changes
will reduce their waste stream);
increase of 5% (Diane Stockton - the
increase in waste generation will be
due to substitution toward an aqueous
based cleaner such as acetone)
5% (Ball),10% (Dave Pofahl - process
changes), -15% (Thibodeau and
Graham),, consensus that there would
be process changes leading to product
modifications (e.g.. from liquid to dry
or powder paints). However, concern
that the reduction could not go as
high technically conceivable because
of off-shore competitors who are not
regulated.
5% (Stockton)10% (Ball), 35%
(Graham),
14
-------
Comments on SIC 3471 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
D002 Corrosive Waste
4.84
2% (Dalich); 5% (Pessl, Davis), 10%
(Pofahl); increase of 5% (Stockton)
In circuit-board industry (Pessl) there
is move to reduce corrosive waste:
Technology changes: reduce foil
coating on circuit-boards from 1/2 oz.
to 1/4 oz. This process reduces by
50% copper etched as well as reduces
corrosive waste. Membrane and
electrowinning technology can be
used to produce pure metallic copper
for re-smelting. This concentrates
waste stream and eliminates other
treatment chemicals that electroplators
previously used
2% (Dalich); 5% (Ball, Davis); 20%
(Pofahl); 10% (Thibodeau); 15%
(Graham) 30% (Pessl); increase of 5%
(Stockton)
Housekeeping: carry forward the
activities in 1989. Believed that full-
impact of housekeeping will occur by
this time.
5% (Davis, Dalich); 10% (Stockton,
Ball); 35% (Graham) 90% (Pessl);
Consensus that by this time that
given waste reduction activities that
are occurring in 1989, ones that are
expected (in experimental stage), as
well as assumed there will be changes
in the economy and demand for
products, there will continue to be
reductions in the waste stream.
15
-------
Comments on SIC 3471 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
D002
(Com)
D006
Corrosive Waste (continued)
Cadmium
4.84
3.19
Technology/Process change
(Pessl)- totally reuse chemistry by
incorporating membrane unit to
concentrate metals that can be fed
back into bath (this process can lead
to nearly 10% reduction in waste
generated but this will occur over a
period of time in the industry); change
in drag-out controls (currently
occurring but will have increasing
impact over time); changed to
"additive vs. subtractive" technology
where processes are used recover
essential chemistry from the rinse
tanks and returned to the plating bath.
Use of "Black Hole* Technology vs.
Electrolysis Copper which reduces
rinse water generation, and amount of
waste copper.
Product Substitution:
concentrated sulfuric acid is replacing
chlorinated D Smear. Pessl's
company has changed from bar to
100% consumable anodes which
reduced copper feedstock, reduces
copper processing and recycling.
Housekeeping: increasing
frequency of analysis and control of
the bath concentration for copper.
ammonia etchant (Pessl indicated
concentration from 18oz/gallon to 21
oz/gal which reduced amount
generated as waste) , cupric etchant
(Pessl indicated cupric went from 21
oz/gal to 24/gal through this
housekeeping measure) insure that it
meets plating criteria. Recycling of
sheared flash router dust, etchant
(copper particulates)
increase of 5% (Stockton)
5% (Graham, Thibodeau); increase of
5% (Stockton)
10% (Stockton); 15% (Thibodeau)
16
-------
Comments on SIC 3471 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
D007 Chromium
20.79
increase of 5% (Pessl); increase of 5%
(Stockton)
The comments below and the largest
reduction estimates in these categories
come from the circuit-board industry
which makes computer boards and are
more likely to require higher plating
standards. They are also more likely
to make changes in the type of waste
Process change: Evaporation,
Drag-out controls; reduce chrome
sludge from new drill process which
affects chrome-bath dwell time which,
in turn, reduces rinse time and thus
chrome sludge.
Product Substitution: change
from chrome to permanganate
(eliminates waste stream)
Housekeeping: recycling of
chrome sludge _
5% (Graham); 15% (Thibodeau); 50%
(Pessl); increase of 5% (Stockton)
Product Substitution: chromate
conversion to phosphate or floride.
10% (Stockton)l; 20% (Thibodeau);
100% (Pessl)
D008
Lead
.99
5% (Dalich); increase of 5%
(Stockton)
Technology Changes:
Membrane and electrowinning
technology can be used to produce
pure metallic lead for re-smelting.
This concentrates waste stream and
eliminates other treatment chemicals
that electroplators previously used.
Substitution: use organic coating
which eliminates all subtractive lead
processes. Also reduces rinse water
requirements. In the printed circuit-
board industry move toward lead-free
alloy (e.g., tin) for final coating
(H.AX.) or non-metallic final coating
- the latter is in limited use now
("En-Tek")
5% (Graham); 10% (Dalich); 60%
(Pessl); increase of 5% (Stockton)
10% (Stockton); 50% (Dalich); 100%
(Pessl);
17
-------
Comments on SIC 3471 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
F001
F002
F006
K062
X004
Spent halogenatated solvents
from degreasing:
tetrachloroethylene,
trichloroethylene, methylene
chloride, 1,1,1-trichloroethane,
carbon tetrachloride, chlorinated
flurocarbons; still bottoms -
recovery of above spent solvents
Spend halogenated solvents:
tetrachloroethylene,
trichloroethylene, 1,1,1-
techloroethylene, chlorobenzene;
1.1.2 trichloro-1.2,2-trifluo-
roethane, otho-dichlorobenzene,
trichlorofluoroniethane; 1,1,2
trichloroethane; still bottoms
from recovery of above spent
solvents
Waste Water Treatment sludges
from electroplating operations
Spent pickle liquor from steel
finishing operations of plants
that produce iron or steel.
Oregon Non-hazardous waste
24.97
.11
325.6
15.95
1.1
15% (Thibodeau); 95% (Stockton)
General Comment: There may
actually be an increase of this waste
stream if regulations change that
prohibit use of other feedstocks or
require reduction of generation of
certain wastes and electroplators shift
toward aqueous solutions. Pessl
stated that his company would
eliminate two waste streams during
1989 - TCE (Trichloroethylene?), and
TCA(7).
Substitution: Methyl Ethyl
Chloride is substituted with
propycene carbon.
25% (Stockton)
5% (Davis); 5-8% (Pessl); increase of
10% (Thibodeau); increase of 5%
(Stockton)
General Comments: There will
probably be an increase of this waste
stream over the next 5 years because
of increasing market. It is still
cheaper to generate and manage this
waste than to initiate waste reduction.
Initial reductions will probably come
from such programs as evaporation.
increase of 10% (Stockton)
5% (Graham); 100% (Ball, Pofahl,
Stockton)
50% (Stockton)
5% (Ball. Davis);10% (Dalich); 15%
(Graham, Thibodeau); 50% (Pessl);
increase of 5% (Stockton)
General Comments: Plant
modernization will make
electroplating more efficient.
Between 1989-95 plant modernization
will account for 10-20% of the
reduction.
20% (Pofahl); increase of 20%
(Stockton)
15% (Thibodeau)
100% (Stockton)
5% (Davis); 10% (Ball, Stockton);
20% (Thibodeau, Dalich); 100%
(Pessl)
Technology Change: will see a
decrease of up to 100% in waste
stream by such techniques as
membrane - electrowinning out
metals which can be sold as a pure
metal (e.g., copper, lead, chrome).
There will also be plant
modernization that will
increase of 30% (Stockton)
18
-------
Comments on SIC 3471 Continued
EPA
Waste
Code
Waste
Description
X006
Lab Packs
General Comments: These
are testing packs from
laboratories. They may contain
any number of wastes - some
not related to the electroplating
industry. One participant
commented that they accepted lab
packs from labs as a courtesy and
a way to insure Subtitle C
disposal.
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
.22
5% (Stockton); 20% (Thibodeau);
100% (Pofahl)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
20% (Thibodeau; Stockton)
20% (Thibodeau; Stockton)
1 Wastes in Bold identify hazardous wastes that qualified for reduction analysis by EPA Region X.
2Hazardous waste stream data from 1986 Washington Generator Annual Dangerous Waste Reports.
3Medium estimate represents EPA Region X estimate of reasonable waste reduction based on statistical analysis prior to "Groundtruthing" Meetings.
19
-------
GROUNDTRUTHING NOTES
WASHINGTON
C022-002
AIRCRAFT (SIC 3721)
Roy Chandler
Heath-Techna Aerospace, Co.
19819 - 84tii Avenue South
Kent, Washington 98032
Industry Attendance
Charles Simpson
Environmental Administrator
Boeing Support Service
Seattle, Washington 98124
Elliott Berkihiser
Boeing Company
Manager
Environmental compliance
600 Naches Avenue SW
Renton, Washington 98005
20
-------
Comments on SIC 3721 - Aircraft
EPA
Waste
Code1
D001
D002
D003
D006
D007
D008
D009
D011
D016
F001
Waste
Description
Total
Ignitable Waste
Corrosive Waste
ReactiveWaste
Cadmium
Chromium
Lead
Mercury
Silver
2,3-D(2,4-dichlorophenoxyacetic
acid)
Spent halogenated solvents from
degieasing: tetrachloroethylene,
trichloroethylene, methylene
chloride, 1,1,1-trichloroethane,
carbon tetrachloride, chlorinated
flurocarbons; still bottoms -
recovery of above spent solvents
Quant
Gen
Tons
19862
24,861
1.265.4
4,075.1
4.4
490.1
3,636.5
419
2.2
12.9
.3
102.6
Estimated
Reduction
1989
<%)3
No Comment
No Comment
No Comment
No Comment
No Comment
No Comment
No Comment
Estimated
Reduction
1995
(%)
3%
3%
6%
3%
5%
45-55%
8%
Estimated
Reduction
2009
(%)
5%
Input Substitution: Attendees
believed that this figure could be
much higher due to input
substitution, but they were not able
to indicate the percent reduction.
6-20%
Technology Changes: Acid
recover may actually yield a 20%
reduction.
13%
7-80%
Technology/Process Changes:
Consensus that for certain types of
processes there could be a much
greater reductions (e.g., 80%).
11%
60-80%
16%
21
-------
Comments on SIC 3721 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
Estimated
Reduction
1995
Estimated
Reduction
2009
F002
F003
F004
F005
F006
F007
Spend halogenated solvents:
tetrachloroethylene,
trichloroethylene, 1,1,1-
techloroeihylene, chlorobenzene;
1,1,2 trichloro-l,2.2-trifluo-
roethane, otho-dichlorobenzene,
trichlorofluoromethane; 1,1,2
trichloroethane; still bottoms
from recovery of above spent
solvents
Spent nonhalogenated solvents:
xylene, acetone ethyl acetate,
ethyl benzene, ethyl ether,
methyl isobutyl ketone, n-butyl
alcohol, cyclohexanone,
methanol; still bottoms from
recovery of above spent solvents
Spent nonhalogenated solvents;
cresols & cresylic acid, &
nitrobenzene; & still bottoms
from recover of above solvents
and blends & mixtures
Spent nonhalogenated solvents:
methyl ethyl ketone, carbon
disulfide, isobutanol, pyridine,
benzene, 2-ethoxyethanol, 2-
nitropane; still bottom from
recovery of above spent solvents
and spent solvent mixtures
Waste Water Treatment sludges
from electroplating operations
Spent cyanide plating bath
solutions from electroplating
45.1
4.4
.1
311.7
30.7
13.8
No Comment
No Comment
No Comment
No Comment
5%
15%
5%
27%
11%
31%
10%
54%
Substitution: Consensus among
attendees that there will be good
opportunities for input substitution
that will reduce the amount of F007
generated.
22
-------
Comments on SIC 3721 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
Estimated
Reduction
1995
Estimated
Reduction
2009
F008
P030
P044
U188
W001
WL01
WL02
WC01
WP01
WP02
WP03
WT01
WTO2
Plating bath residues from
electro, w. cyanides
Cyanides (Soluble cyanide Salts)
Dimethoate (t);
Phosphorodithioic acid, 0,0-
dimethyl S-[2-(methylaminoO-2-
Oxethyl]-ester(t)
Phenol; Bezene, hydroxy-
PCB
Lab Packs EWH
Lab Packs DW
EHW (Carcinogenic Dangerous
Wastes)
EHW (Halogenated
Hydrocarbons)
DW (Halogenated Hydrocarbons)
Polycyhclic Aromatic
Hydrocarbons EHW
EHW (Toxic Dangerous Wastes)
DW (Toxic Dangerous Wastes)
7
.1
3.7
1.1
35.6
3.1
11
2.3
19.8
.7
3.7
15.8
14.343
No Comment
5%
10%
1 Wastes in Bold identify hazardous wastes that qualified for reduction analysis by EPA Region X.
2Hazardous waste stream data from 1986 Washington Generator Annual Dangerous Waste Reports.
3Estimate represents percentage waste reduction based on "Groundtruthing" Meeting.
23
-------
GROUNDTRUTHING NOTES
WASHINGTON
C022-002
AIRCRAFT PARTS (SIC 3728)
Roy Chandler
Heath-Techna Aerospace, Co.
19819 - 84& Avenue South
Kent, Washington 98032
Industry Attendance
Charles Simpson
Environmental Administrator
Boeing Support Service
Seattle, Washington 98124
Elliott Berldhiser
Boeing Company
Manager
Environmental compliance
600 Naches Avenue SW
Renton, Washington 98005
24
-------
Comments on SIC 3728 - Aircraft Parts
EPA
Waste
Code1
D001
D002
D003
0004
D006
D007
D008
D009
F001
F002
Waste
Description
Total
Ignitable Waste
Corrosive Waste
ReactiveWaste
Arsenic
Cadmium
Chromium
Lead
Mercury
Spent halogenated solvents from
degreasing: tetrachloroethylene,
trichloroethylene, methylene
chloride, 1,1,1-trichloroethane,
carbon tetrachloride, chlorinated
flurocarbons; still bottoms -
recovery of above spent solvents
Spend halogenated solvents:
tetrachloroethylene.
trichloroethylene, 1,1,1-
techloroethylene, chlorobenzene;
1,1,2 trichloro-l,2,2-trifluo-
roethane, otho-dichlorobenzene,
trichlorofluoromethane; 1,1,2
trichloroethane; still bottoms
from recovery of above spent
solvents
Quant
Gen
Tons
19862
6391.9
S36.8
475.4
4.4
.02
1.069.2
1.374.8
9
.38
25.1
20.9
Estimated
Reduction
1989
(%>3
No Comment
No Comment
25%
25%
25%
3%
Estimated
Reduction
1995
(%)
2-50%
Housekeeping: The higher figure
of 50% could be attained if the issue
of liability for onsite recovery could
be reduced or addressed
2%
5%
5%
5%
10%
Estimated
Reduction
2009
(%)
5%
6%
5%
5%
5%
2%
25
-------
Comments on SIC 3728 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
<%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
F003
F005
F006
F007
F008
F009
F019
P030
WL01
WL02
WP01
WP02
WP03
WT01
WT02
Spent nonhalogenated solvents:
xylene, acetone ethyl acetate,
ethyl benzene, ethyl ether,
methyl isobutyl ketone, n-butyl
alcohol, cyclohexanone,
methanol; still bottoms from
recovery of above spent solvents
Spent nonhalogenated solvents:
methyl ethyl ketone, carbon
disulfide, isobutanol, pyridine,
benzene, 2-ethoxyemanol, 2-
nitropane; still bottom from
recovery of above spent solvents
and spent solvent mixtures
Waste Water Treatment sludges
from electroplating operations
Spent cyanide plating bath
solutions from electroplating
Plating bath residues from
electro, w. cyanides
Spent Stripping & cleaning Bath
Solutions from electroplating
withcycanides
Wastewater treatment sludeges
from chemical conversion coating
of aluminum
Cyanides (Soluble cyanide Salts)
Lab Packs EWH
Lab Packs DW
EHW (Halogenated
Hydrocarbons)
DW (Halogenated Hydrocarbons)
Polycyhclic Aromatic
Hydrocarbons EHW
EHW (Toxic Dangerous Wastes)
DW (Toxic Dangerous Wastes)
56.2
125.6
1,241.6
13.5
4.2
3.9
1
.1
.6
2
2.5
.6
1.2
26.7
1,396.2
0%
0%
0%
0%
2%
2%
5%
25%
5-30%
4%
10%
25%
26
-------
Comments on SIC 3728 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
Estimated
Reduction
1995
Estimated
Reduction
2009
1 Wastes in Bold identify hazardous wastes that qualified for reduction analysis by EPA Region X.
^Hazardous waste stream data from 1986 Washington Generator Annual Dangerous Waste Reports.
3Estimate represents percentage waste reduction based on "Groundtruthing" Meeting.
27
-------
GROUNDTRUTHING NOTES
WASHINGTON
C022-002
ELECTRIC SERVICES (SIC 4911)
Daniel Bolser
Pacific Circuits, Inc.
17550 ME 67& Court
Redmond, Washington 98052
Shirli Axelrod
Seattle City Light
1015 3ri Avenue
Seattle, Washington 98104
Industry Attendance
Russell Post
QtyofTacoma
Department of Public Utilities
362835111 Streets.
Tacoma, Washington 98411
Terry Kakida
Seattle City Light
10153Q1 Avenue
Seattle, Washington 98104
Debbie Dole
Seattle Gty Light
1015 3Si Avenue
Seattle, Washington 98104
28
-------
Comments on SIC 4911 - Electric Services
EPA
Waste
Code1
D001
D002
D003
D005
D007
D008
D009
F001
F002
Waste
Description
Total
General Comment:
There was a general concern
expressed by the attendees fa-
increased regulation by the state
for some wastes (See comments
under WOOD.
Ignitable Waste
Corrosive Waste
ReactiveWaste
Barium
Chromium
Lead
Mercury
Spent halogenated solvents from
degreasing: tetrachloioethylene,
trichloroethylene, methylene
chloride, 1,1,1-trichloroethane,
carbon tetrachloride, chlorinated
flurocarbons; still bottoms -
recovery of above scent solvents
Spend halogenated solvents:
tetrachloroethylene,
trichloroethylene, 1,1,1-
techloroethylene, chlorobenzene;
1 , 1 ,2 trichloro- 1 ,2,2-trifluo-
roeihane, otho-dichlorobenzene,
trichlorofluoromethane; 1,1,2
trichloroethane; still bottoms
from recovery of above spent
solvents
Quant
Gen
Tons
19862
1,278.2
15.31
.64
.01
.12
.08
7.84
1.0S
20.08
2.08
Estimated
Redaction
1989
(%)3
No Comment
No Comment
No Comment
No Comment
No Comment
Estimated
Reduction
1995
(%)
20-50%
For facilities that have paint shops
there is an expectation of a reduction
of 38% in D001 by this date.
50-75%
45-55%
5-15%
5-15%
Estimated
Reduction
2009
(%)
50-75%
Attendees believed that there is
reasonable expectation for waste
reduction of about 1%/year reduction
in waste generation thereafter.
50-95%
60-80%
10-30%
10-30%
29
-------
Comments on SIC 4911 Continued
EPA
Waste
Code
Waste
Description
Quant
Gen
Tons
1986
Estimated
Reduction
1989
(%)
Estimated
Reduction
1995
(%)
Estimated
Reduction
2009
(%)
F003
F005
U211
U242
P030
W001
WL02
WC01
WP01
WP02
WT01
WT02
Spent nonhalogenated solvents:
xylene, acetone ethyl acetate,
ethyl benzene, ethyl ether,
methyl isobutyl ketone, n-butyl
alcohol, cyclohexanone,
methanol; still bottoms from
recovery of above spent solvents
Spent nonhalogenated solvents:
methyl ethyl ketone. carbon
disulfide, isobutanol, pyridine,
benzene, 2-ethoxyethanol, 2-
nitropane; still bottom from
recovery of above spent solvents
and spent solvent mixtures
Methane, Tetrachloro-; Carbon
Tetrachloride
Spent cyanide plating bath
solutions from electroplating
Cyanides (Soluble cyanide Salts)
PCB
Lab Packs DW
EHW (Carcinogenic Dangerous
Wastes)
EHW (Halogenaied
Hydrocarbons)
DW (Halogenated Hydrocarbons)
EHW (Toxic Dangerous Wastes)
DW (Toxic Dangerous Wastes)
.26
1.34
.08
.01
.07
1,216.7
.17
.22
3.34
2.31
4.19
2.29
No Comment on waste Reduction.
There was, however, a concern that
PCB Waste Haulers should be
certified by the state.
No Comment
No Comment
10%
10%
40-60%
20-50%
50%
10-60%
10-25%
85-95%
50-75%
75%
20-60%
20-40%
1 Wastes in Bold identify hazardous wastes that qualified for reduction analysis by EPA Region X.
2Hazardous waste stream data from 1986 Washington Generator Annual Dangerous Waste Reports.
3Estimate represents percentage waste reduction based on "Groundtmthing" Meeting.
30
-------
SOG HAZARDOUS WASTE OUTPUT 1VBC - IOAHU
Sara Sara
11 12
0.301
1.320
0.005
0.023
0.014
0.166
0.114
0.150
0.002
0.236
0.065
0.119
0.345
0.027
0.029
0.010
0.009
0.009
0.009
0.007
0.035
0.012
0.105
0.013
0.043
Sara
13
1.506
6.600
0.026
0.1U
0.070
0.829
0.571
0.752
1.180
0.326
0.199
0.086
0.092
0.091
0.069
0.350
Sara
U
0.151
0.660
0.003
0.011
0.007
0.083
0.057
0.075
0.001
0.118
0.033
0.060
0.173
0.013
0.015
0.005
0.004
0.005
0.005
0.003
0.017
0.006
0.052
0.006
0.021
Sara Sara
15 16
1.431
6.270
0.025
0.109
0.066
0.018
1.192
3.454
0.266
0.295
0.100
-0.176 0.088
0.183 0.092
0.182 0.091
0.138 0.069
0.047
0.419
0.051
0.171
Sara
17
1.506
6.600
ERR
0.026
0.114
0.070
0.059
0.524
0.064
0.214
-------
SQG HAZARDOUS WASTE OUTPUT 1987 IDAHO
Sara Sara Sara Sara Sara Sara Sara
11 12 13 U 15 16 17
0.364
2.722
0.766
0.893
0.016 0.158 0.008 0.158 0.316
0.032 1.270 0.016 0.317 0.635 0.317
1.198
0.040 0.020
0.022 0.011
0.256 0.128 1.023
0.022
0.373 0.186 1.491
12.298 6.149 49.190
4.340 2.170 17.361
4.288 2.144 17.151
0.024 0.012 0.095
3.727 1.863 14.906
0.228 0.114 0.913
3.977 1.988 15.907
0.033 0.016
0.003 0.002
0.013 0.006
0.002 0.001
-------
SOG HAZARDOUS WASTE OUTPUT 1987 - IDAHO
Sara
11
Sara
12
Sara
13
Sara
U
Sara
15
Sara
16
Sara
17
0.024 0.012 0.121
0.022 0.011 0.109
0.0(5 0.022 0.223
0.074 0.037 0.372
1.198 33.003 19.056 16.501 127.898 6.180 ERR
-------
SCO HAZARDOUS WASTE OUTPUT 1989 - IDAHO
Relevant SICs
Industry Group at the
2-dlglt level
Metal Manufacturing
Construction
Motor Freight Terminals
furni ture/Uood
Manufacturing and
Ref inishing
Printing/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
Waste
Ouant i ty Hazardous
(Tons/yr/emp) Waste Generated
(National) For SQGs
1985 By Industry
1989 Based on In Idaho
Employment Industrial 1989 Sara Sara
Estimate Croup (Tons/yr) 1 2
0.007695
2140.8
10428.7
37.1
181.1
96.9
0.001760
2994.5
2035.6
2453.4
0.000119
983.6
0.001213
4071.2
1173.0
0.004170
1544.7
4441.7
347.6
376.7
0.001630
366.7
0.003179
212.5
222.4
200.0
161.4
0.000894
475.3
0.000553
695.1
6134.8
763.7
2536.4
16.474
80.253
0.285
1.394
0.745
5.269
3.582
4.317
0.117
4.939
1.423
6.441
18.521
1.449
1.571
0.598
0.675
0.707
0.636
0.513
1.511
0.384
3.391
0.422
1.402
1.647
8.025
0.029
0.139
0.075
0.878
0.597
0.720
0.023
1.235
0.356
0.644
1.852
0.145
0.157
0.100
0.096
0.101
0.091
0.073
0.378
0.064
0.565
0.070
0.234
Sara Sara Sara Sara Sara Sara Sara
3456789
0.659
3.210
0.011
0.056
0.030
0.351
0.239
0.288
0.005
0.494
0.142
0.258
0.741
0.058
0.063
0.020
0.019
0.020
0.018
0.015
0.076
0.026
0.226
0.028
0.093
1.647
8.025
0.029
0.139
0.075
0.878
0.597
0.720
0.012
1.235
0.356
0.644
1.852
0.145
0.157
0.050
0.048
0.051
0.045
0.037
0.189
0.064
0.565
0.070
0.234
0.494
2.408
« 0.009
0.042
0.022
0.263
0.179
0.216
0.004
0.370
0.107
0.193
0.556
0.043
0.047
0.015
0.014
0.015
0.014
0.011
0.057
0.019
0.170
0.021
0.070
6.672
32.503
0.116
0.565
0.302
1.756
1.194
1.439
0.051
2.576
7.408
0.580
0.628
0.100
0.096
0.101
0.091
0.073
0.378
0.077
0.678
0.084
0.280
Sara
10
O.M4
1.852
O.K5
0.157
Educational & Vocational
Total
0.000871
-------
SOC HAZARDOUS WASTE OUTPUI 19oy - IDAnu
Industry Group
Shops
wholesale and
Retail Sales
Relevant SICs
at the
2-digit level
82.
83
Total
51
52
53
1989
Employment
Estimate
763.7
0.0
1232.3
2558.2
4263.7
Uaste
Quant i ty
(Tons/yr/enp)
(National)
1985
Based on
Industrial
Group
0.000552
Hazardous
Uaste Generated
For SOGs
By Industry
In Idaho
1989
(Tons/yr)
0.665
0.680
1.411
2.352
Sara
1
0.023
0.047
0.078
Sara .
2
0.133
0.113
0.235
0.392
Sara
3
0.053
0.045
0.094
0.157
Sara Sara
4 5
0.133
0.119
0.247
0.412
Sara Sara
6 7
0.040
0.034
0.071
0.118
Sara
8
0.085
0.176
0.294
Sara
9
0.133
0.113
0.235
0.392
Sara
10
TOTALS
1129.969 0.801 183.901 70.367 0.000 175.953 0.000 53.428 5.127 404.724 4.869
-------
SOC HAZARDOUS WASTE OUTPUT 1989 - IDAHO
Sara Sara Sara Sara Sara Sara Sara
11 12 13 14 15 16 17
0.391
2.978
0.789
0.974
0.016 0.158 0.008 0.158 0.316
0.032 1.270 0.016 0.317 0.635 0.317
1.306
0.0(3 0.022
0.024 0.012
0.279 0.139 1.116
0.022
0.408 0.204 1.631
13.030 6.515 52.118
4.599 2.299 18.395
4.531 2.266 18.125
0.024 0.012 0.095
3.929 1.964 15.714
0.278 0.139 1.113
4.189 2.095 16.758
0.035 0.018
0.003 0.002
O.OU 0.007
0.002 0.001
-------
buu nnlAKUuua
Sara Sara
11 12
0.329
1.605
0.006
0.028
0.015
0.176
0.119
O.K4
0.002
0.247
0.071
0.129
0.370
0.029
0.031
0.010
0.010
0.010
0.009
0.007
0.038
0.013
0.113
0.014
0.047
Sara
13
1.647
8.025
0.029
0.139
0.075
0.878
0.597
0.720
1.235
0.356
0.199
0.096
0.101
0.091
0.073
0.378
Sara
14
0.165
0.603
0.003
0.014
0.007
0.088
0.060
0.072
0.001
0.123
0.036
0.064
0.185
0.014
0.016
0.005
0.005
0.005
0.005
0.004
0.019
0.006
0.057
0.007
0.023
Sara
15
1.565
7.624
0.027
0.132
0.071
0.019
0.100
0.193
0.202
0.182
0.147
0.051
0.452
0.056
0.187
Sara Sara
16 17
1.647
8.025
ERR
0.029
0.139
0.075
1.288
3.704
0.290
0.314
0.096
0.101
0.091
0.073
0.064
0.565
0.070
0.234
-------
SOG HAZARDOUS WASTE OUTPUT 1989 IDAHO
Sara
11
Sara
12
Sara
13
Sara
U
Sara
15
Sara
16
Sara
17
0.027 0.013 0.133
0.023 0.011 0.113
0.047 0.026 0.235
0.078 0.039 0.392
1.306 35.183 21.221 17.592 136.548 6.593 ERR
-------
SOG HAZARDOUS WASTE OUTPUT 2009 - IDAHO
Industry Group
Pesticide End-Users
Pesticide Application
Services
Chemical Manufacturing
Wood Preserving
Formulators
Laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Relevant SICs
at the
2-digtt level
Total
79
84
Total
07
(9
73
Total
28
Total
24
Total
28
Total
72
Total
72
73
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
2009
Employment
Estimate
459.9
1594.8
345.7
530.0
536.7
1064.6
1642.9
2861.9
954.0
530.0
1589.9
46.7
398.7
10239.2
3613.8
4322.3
15.4
3408.8
200.0
3986.4
13587.0
8773.4
774.7
3577.3
459.9
Waste
Quantity
(Tons/yr/emp) k
(National)
1985
Based on
Industrial
Group
0.001350
0.002803
0.002465
0.001059
0.002424
0.006960
0.002777
0.009364
0.000955
0.046071
0.000150
Hazardous
las'e Generated
For SOGs
By Industry
In Idaho
2009
(Tons/yr)
0.621
4.471
0.969
1.486
1.323
1.127
3.982
19.920
2.649
1.472
14.888
-
0.045
18.369
471.727
166.492
199.131
0.709
157.047
9.214
183.655
-
1.318
0.116
0.538
0.069
Sara Sara
1 2
0.165
1.127
0.332
0.996 8.964
0.662
0.368
2.127
-
0.022
3.061
78.621
27.749
33.188
0.118
26.175
1.536
30.609
-
0.264
0.023
0.108
0.014
Sara
3
0.033
0.066
0.132
0.074
0.851
-
1.225
31.448
11.099
13.275
0.047
10.470
0.614
12.244
-
0.105
0.009
0.043
0.006
Sara Sara
4 5
0.083
0.166
0.331
0.184
2.127
-
3.061
78.621
27.749
33.188
0.118
26.175
1.536
30.609
0.264
0.023
0.108
0.014
Sara Sara
6 7
0.025
0.050
0.996
0.099
0.055
0.638
0.918
23.586
8.325
9.957
0.035
7.852
0.461
9.183
0.079
0.007
0.032
0.004
Sara Sara
8 9
0.331
0.664
6.972
0.662
0.368
4.679
6.735
172.966
61.047
73.015
0.260
57.584
3.379
67.340
.
0.527
0.047
0.215
0.028
Sara
10
0.662
0.368
2.127
-------
SQG HAZARDOUS WASTE OUTPUT 2009 - IDAHO
Industry Group
Metal Manufacturing
Construction
Motor Freight Terminals
Furniture/Wood
Manufacturing and
Ref inishing
Printing/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Relevant SICs
at the
2-digit level
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
2009
Employment
Estimate
2669.4
20351.9
50.0
437.3
80.0
3613.8
2129.2
2017.6
1440.8
4258.4
1788.7
2018.5
5879.2
530.0
466.7
383.3
319.0
312.9
200.0
200.0
621.1
1060.0
9161.3
1070.6
4240.0
Waste
Quant i ty
(Tons/yr/emp) I
(National)
1985
Based on
Industrial
Group
0.007695
0.001760
0.000119
0.001213
0.004170
0.001630
0.003179
0.000894
0.000553
Hazardous
taste Generated
For SOGs
By Industry
In Idaho
2009
(Tons/yr)
-
20.542
156.616
-
0.385
3.366
0.616
6.359
3.747
3.550
0.171
5.166
-
2.170
8.417
24.515
2.210
1.946
0.625
1.014
0.995
0.636
0.636
1.975
0.586
5.064
0.592
2.344
Sara Sara
1 2
-
.
2.054
15.662
-
0.038
0.337
0.062
1.060
0.624
0.592
0.034
1.292
-
0.543
0.842
2.452
0.221
0.195
0.104
0.145
0.142
0.091
0.091
0.494
0.098
0.844
0.099
0.391
Sara
3
.
-
0.822
6.265
-
0.015
0.135
0.025
0.424
0.250
0.237
0.007
0.517
-
0.217
0.337
0.981
0.088
0.078
0.021
0.029
0.028
0.018
0.018
0.099
0.039
0.338
0.039
0.156
Sara Sara
4 5
-
.
2.054
15.662
.
0.038
0.337
0.062
1.060
0.624
0.592
0.017
1.292
-
0.543
0.842
2.452
0.221
0.195
0.052
0.072
0.071
0.045
0.045
0.247
0.098
0.844
0.099
0.391
Sara Sara
6 7
.
0.616
4.698
.
0.012
0.101
0.018
0.318
0.187
0.178
0.005
0.387
-
0.163
0.253
0.735
0.066
0.058
0.016
0.022
0.021
0.014
0.014
0.074
0.029
0.253
0.030
0.117
Sara Sara
8 9
.
.
8.320
63.430
.
0.156
1.363
0.249
2.120
1.249
1.183
0.075
3.367
9.806
0.884
0.778
0.104
0.145
0.142
0.091
0.091
0.494
0.117
1.013
0.118
0.469
Sara
10
0.842
2.452
0.221
0.195
Educational & vocational
Total
0.000871
-------
SOG HAZARDOUS WASTE OUTPUT 2009 -- IDAHO
Industry Group
Shops
Wholesale and
Retail Sates
Relevant SICs
at the
2-digit level
82
83
Total
51
52
53
2009
Employment
Estimate
1070.6
0.0
1563.3
3(08.8
5681 .A
Uaste
Ouant i ty
(Tons/yr/enp)
(National)
1985
Based on
Industrial
Group
0.000552
Hazardous
Waste Generated
For SOGs
By Industry
In Idaho
2009
(Tons/yr)
0.933
0.862
1.880
3.134
Sara
1
0.029
0.063
0.104
Sara
2
0.187
0.144
0.313
0.522
Sara
3
0.075
0.057
0.125
0.209
Sara Sara
4 5
0.187
0.151
0.329
0.548
Sara Sara
6 7
0.056
0.043
0.094
0.157
Sara
8
0.108
0.235
0.392
Sara
9
0.187
0.144
0.313
0.522
Sara
10
TOTALS
1522.386 1.192 244.902 93.390 0.000 233.523 0.000 71.038 7.706 546.775 6.866
-------
SOG HAZARDOUS WASTE OUTPUT 2009 -- IDAHO
Sara Sara
11 12
0.411
3.132
0.008
0.067
0.012
0.212
0.125
0.118
0.003
0.258
0.109
0.168
0.490
0.04 A
0.039
0.010
0.014
0.014
0.009
0.009
0.049
0.020
0.169
0.020
0.078
Sara
13
2.054
15.662
0.038
0.337
0.062
1.060
0.624
0.592
1.292
0.543
0.208
0.145
0.142
0.091
0.091
0.494
Sara
14
0.205
1.566
0.004
0.034
0.006
0.106
0.062
0.059
0.002
0.129
0.054
0.084
0.245
0.022
0.019
0.005
0.007
0.007
0.005
0.005
0.025
0.010
0.084
0.010
0.039
Sara
15
1.952
14.879
0.037
0.320
0.058
0.027
0.104
0.290
0.284
0.182
0.182
0.078
0.675
0.079
0.313
Sara Sara
16 17
2.054
15.662
0.038
0.337
0.062
1.683
4.903
0.442
0.389
0.145
0.142
0.091
0.091
0.098
0.844
0.099
0.391
-------
SOC HAZARDOUS WASTE OUTPUT 2009 -- IDAHO
Sara
11
Sara
12
Sara
13
Sara
14
Sara
15
Sara
16
Sara
17
0.037 0.019 0.187
0.029 0.014 0.144
0.063 0.031 0.313
0.104 0.052 0.522
1.992 46.695 32.494 23.347 182.503 8.550 21.412
-------
SOG HAZARDOUS WASTE OUTPUT 1987 - OREGON
Industry Group
Pesticide End-Users
Pesticide Application
Services
Chemical Manufacturing
Wood Preserving
Formulators
Laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Relevant SICs
at the
2-digit level
Total
79
84
Total
07
49
73
Total
28
Total
24
Total
28
Total
72
Total
72
73
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
1987
Employment
Estimate
791.3
2183.1
695.3
816.3
513.3
4171.6
1571.4
4407.8
1469.3
816.3
2448.8
840.0
545.8
17814.2
6287.4
7363.4
180.2
44145.1
4041.1
7330.5
33458.0
17114.6
10033.0
5509.8
791.3
Waste
Quantity
(Tons/yr/enp) V
(National)
1985
Based on
Industrial
Group
0.001350
0.002803
0.002465
0.001059
0.002424
0.006960
0.002777
0.009364
0.000955
0.046071
0.000150
Hazardous
(aste Generated
For SQGs
By Industry
In Oregon
1987
(Tons/yr)
1.068
-
6.120
1.949
2.288
1.266
4.417
3.809
30.680
4.080
2.267
22.931
-
0.803
25.145
820.713
289.663
339.238
8.301
2033.799
186.175
337.724
-
2.572
1.508
0.828
0.119
Sara Sara
1 2
0.158
4.417
0.317
1.534 13.806
1.020
0.567
3.276
-
0.401
4.191
136.786
48.277
56.540
1.384
338.966
31.029
56.287
-
0.514
0.302
0.166
0.024
Sara
3
0.032
0.063
0.204
0.113
1.310
-
1.676
54.714
19.311
22.616
0.553
135.587
12.412
22.515
-
0.206
0.121
0.066
0.010
Sara Sara
4 5
0.079
0.159
0.510
0.283
3.276
-
4.191
136.786
48.277
56.540
1.384
338.966
31 .029
56.287
-
0.514
0.302
0.166
0.024
Sara Sara
6 7
0.024
0.048
1.534
0.153
0.085
0.983
-
1.257
41.036
14.483
16.962
0.415
101.690
9.309
16.886
0.154
0.090
0.050
0.007
Sara Sara
8 9
0.316
0.635
10.738
1.020
0.567
7.207
9.220
300.928
106.210
124.387
3.044
745.726
68.264
123.832
.
1.029
0.603
0.331
0.048
Sara
10
1.020
0.567
3.276
-------
SOG HAZARDOUS WASTE OUTPUT 1VIU - Oktuun
Industry Group
Metal Manufacturing
Construction
Motor Freight Terminals
Furniture/Wood
Manufacturing and
Ref imshmg
Printing/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Relevant SICs
at the
2-digit level
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
1987
Employment
Estimate
10002.1
19087.7
222.9
17778.7
744.7
6287.4
8343.2
4826.9
2454.5
16686.4
2754.9
7497.2
12466.1
816.3
1020.7
366.7
436.6
546.3
SOO.O
437.4
2306.8
1632.5
21939.3
2907.0
6932.6
Waste
Quantity
(Tons/yr/emp) I
(National)
1985
Based on
Industrial
Group
0.007695
0.001760
0.000119
0.001213
0.004170
0.001630
0.003179
0.000894
0.000553
Hazardous
laste Generated
For SOGs
By Industry
In Oregon
1987
(Tons/yr)
0.000
0.000
76.971
146.887
0.000
1.716
136.815
5.730
11.064
14.681
8.494
0.291
20.244
0.000
3.342
31.262
51.982
3.404
4.256
0.598
1.388
1.737
1.590
1.391
7.334
0.902
12.128
1.607
3.832
Sara Sara
1 2
0.000
0.000
7.697
14.689
0.000
0.172
13.681
0.573
1.844
2.447
1.416
0.058
5.061
0.000
0.836
3.126
5.198
0.340
0.426
0.100
0.198
0.248
0.227
0.199
1.833
0.150
2.021
0.268
0.639
Sara
3
0.000
0.000
3.079
5.875
0.000
0.069
5.473
0.229
0.738
0.979
0.566
0.012
2.024
0.000
0.334
1.250
2.079
0.136
0.170
0.020
0.040
0.050
0.045
0.040
0.367
0.060
0.809
0.107
0.255
Sara Sara
4 5
0.000
0.000
7.697
14.689
0.000
0.172
13.681
0.573
1.844
2.447
1.416
0.029
5.061
0.000
0.836
3.126
5.198
0.340
0.426
0.050
0.099
0.124
0.114
0.099
0.917
0.150
2.021
0.268
0.639
Sara Sara
6 7
0.000
0.000
2.309
4.407
0.000
0.051
4.104
0.172
0.553
0.734
0.425
0.009
1.518
0.000
0.251
0.938
1.559
0.102
0.128
0.015
0.030
0.037
0.034
0.030
0.275
0.045
0.606
0.080
0.192
Sara Sara
8 9
0.000
0.000
31.173
59.489
0.000
0.695
55.410
2.321
3.688
4.894
2.831
0.128
12.505
20.793
1.361
1.702
0.100
0.198
0.248
0.227
0.199
1.833
0.180
2.426
0.321
0.766
Sara
10
3.126
5.198
0.340
0.426
Educational & Vocational
Total
0.000871
-------
SOC HAZARDOUS WASTE OUTPUT 1987 - OREGON
Industry Group
Shops
Wholesale and
Retail Sales
Relevant SICs
at the
2-digit level
82
83
Total
51
52
53
1987
Employment
Estimate
2907.0
0.0
3433.2
44145.1
73575 . 1
Waste
Quantity
(Tons/yr/emp)
(National)
1985
Based on
Industrial
Group
0.000552
Hazardous
Waste Generated
For SOGs
By Industry
In Oregon
1987
(Tons/yr)
2.533
1.894
24.348
40.580
Sara
1
0.063
0.812
1.353
Sara
2
0.507
0.316
4.058
6.763
Sara
3
0.203
0.126
1.623
2.705
Sara Sara
4 5
0.507
0.331
4.261
7.101
Sara Sara
6 7
0.152
0.095
1.217
2.029
Sara
8
0.237
3.043
5.072
Sara
9
0.507
0.316
4.058
6.763
Sara
10
TOTALS
4746.459 3.761 773.517 300.972 0.000 752.987 0.000 227.263 19.091 1708.499 13.953
-------
Sara Sara
11 12
0.000
0.000
1.539
2.938
0.000
0.034
2.736
0.115
0.369
0.489
0.283
0.006
1.012
0.000
0.167
0.625
1.040
0.068
0.085
0.010
0.020
0.025
0.023
0.020
0.183
0.030
0.404
0.054
0.128
Sara
13
0.000
0.000
7.697
14.689
0.000
0.172
13.681
0.573
1.844
2.447
1.416
5.061
0.000
0.836
0.199
0.198
0.248
0.227
0.199
1.833
Sara
14
0.000
0.000
0.770
1.469
0.000
0.017
1.368
0.057
0.184
0.245
0.142
0.003
0.506
0.000
0.084
0.313
0.520
0.034
0.043
0.005
0.010
0.012
0.011
0.010
0.092
0.015
0.202
0.027
0.064
Sara Sara
15 16
0.000
0.000
7.312
13.954
0.000
0.163
12.997
0.544
0.047
6.252
10.396
0.681
0.851
0.100
0.397 0.198
0.496 0.248
0.454 0.227
0.397 0.199
0.120
1.617
0.214
0.511
Sara
17
0.000
0.000
7.697
14.689
0.000
0.172
13.681
0.573
0.150
2.021
0.268
0.639
-------
SOG HAZARDOUS WASTE OUTPUT 1987 - OREGON
Sara Sara Sera Sara Sara Sara Sara
11 12 13 U 15 16 17
1.068
6.120
1.949
2.288
0.016 0.158 0.008 0.158 0.316
0.032 1.270 0.016 0.317 0.635 0.317
3.068
0.102 0.051
0.057 0.028
0.655 0.328 2.621
0.401
0.838 0.419 3.353
27.357 13.679 109.428
9.655 4.828 38.622
11.308 5.654 45.232
0.277 0.138 1.107
67.793 33.897 271.173
6.206 3.103 24.823
11.257 5.629 45.030
0.103 0.051
0.060 0.030
0.033 0.017
0.005 0.002
-------
SQG HAZARDOUS WASTE OUTPUT 198/ - OREGON
Sara
11
Sara
12
Sara
13
Sara
U
Sara
15
Sara
16
Sara
17
0.101 0.051 0.507
0.063 0.032 0.316
0.812 0.406 4.058
1.353 0.676 6.763
3.068 ISO.486 64.574 75.243 581.188 19.688 52.167
-------
SOG HAZARDOUS WASTE OUTPUT 1989 -- OREGON
Industry Group
Pesticide End-Users
Pesticide Application
Services
Chemical Manufacturing
Wood Preserving
Formulators
Laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Relevant SICs
at the
2-digit level
Total
79
84
Total
07
49
73
Total
28
Total
24
Total
28
Total
72
Total
72
73
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
Waste
Quantity
(Tons/yr/emp) Ua
(National)
1985
1989 Based on
Employment Industrial
Estimate Group
0.001350
851.5
0.002803
2389.6
731.3
893.3
0.002465
513.3
0.001059
4334.1
0.002424
1571.4
0.006960
4824.0
0.002777
1608.0
893.3
0.009364
2680.0
0.000955
840.0
0.046071
597.4
19435.1
6859.4
7738.6
178.0
46341.3
4405.6
7764.9
35639.2 0.000150
18220.5
10532.1
6030.0
851.5
Hazardous
ste Generated
For SQGs
By Industry
In Oregon
1989 S
(Tons/yr)
1.149
6.699
2.050
2.504
1.266
4.589
3.809
33.577 1.
4.465
2.481
25.096
"
0.803
27.522
895.389
316.020
356.524
8.201
2134.979
202.969
357.736
2.738
1.583
0.906
0.128
iara Sara
1 2
0.158
4.589
0.317
,679 15.110
1.116
0.620
3.585
-
0.401
4.587
149.231
52.670
59.421
1.367
355.830
33.828
59.623
.
0.548
0.317
0.181
0.026
Sara £
3
0.032
0.063
0.223
0.124
1.434
-
1.835
59.693
21.068
23.768
0.547
142.332
13.531
23.849
.
0.219
0.127
0.072
0.010
iara Sara S
4 5
0.079
0.159
0.558
0.310
3.585
-
4.587
149.231
52.670
59.421
1.367
355.830
33.828
59.623
.
0.548
0.317
0.181
0.026
iara Sara !
6 7
0.024
0.048
1.679 11.
0.167
0.093
1.076
1.376
44.769
15.801
17.826
0.410
106.749
10.148
17.887
_
0.164
0.095
0.054
0.008
iara Sara
8. 9
0.316
0.635
.752
1.116
0.620
7.887
10.092
328.309
115.874
130.726
3.007
782.826
74.422
131.170
.
1.095
0.633
0.362
0.051
Sara
10
1.116
0.620
3.585
-------
SOG HAZARDOUS WASTE OUTPUT 1989 -- OREGON
Industry Group
Metal Manufacturing
Construction
Motor Freight Terminals
Furniture/Wood
Manufacturing and
Ref inishing
Printing/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Relevant SICs
at the
2-digit level
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
1989
Employment
Estimate
52532.5
11002.0
21046.5
226.2
19485.9
768.0
6859.4
8668.1
4606.4
2579.5
17336.2
3015.0
7697.7
13211.0
893.3
1082.5
366.7
477.9
613.4
500.0
463.9
2368.5
1786.7
23550.5
3127.8
7579.3
Waste
Quant i ty
(Tons/yr/emp) V
(National)
1985
Based on
Industrial
Group
0.007695
0.001760
0.000119
0.001213
0.004170
0.001630
0.003179
0.000894
0.000553
Hazardous
laste Generated
For SQGs
By Industry
In Oregon
1989
(Tons/yr)
0.000
0.000
84.665
161.961
0.000
1.740
149.952
5.910
12.071
15.253
8.106
0.306
21.033
0.000
3.658
32.098
55.088
3.725
4.514
0.598
1.519
1.950
1.590
1.475
7.530
0.988
13.018
1.729
4.190
Sara Sara
1 2
0.000
0.000
8.467
16.196
0.000
0.174
14.995
0.591
2.012
2.542
1.351
0.061
5.258
0.000
0.914
3.210
5.509
0.373
0.451
0.100
0.217
0.279
0.227
0.211
1.883
0.165
2.170
0.288
0.698
Sara
3
0.000
0.000
3.387
6.478
0.000
0.070
5.998
0.236
0.805
1.017
0.540
0.012
2.103
0.000
0.366
1.284
2.204
0.149
0.181
0.020
0.043
0.056
0.045
0.042
0.377
0.066
0.868
0.115
0.279
Sara Sara
4 5
0.000
0.000
8.467
16.196
0.000
0.174
14.995
0.591
2.012
2.542
1.351
0.031
5.258
0.000
0.914
3.210
5.509
0.373
0.451
0.050
0.109
0.139
0.114
0.105
0.941
0.165
2.170
0.288
0.698
Sara Sara
6 7
0.000
0.000
2.540
4.859
0.000
0.052
4.499
0.177
0.604
0.763
0.405
0.009
1.577
0.000
0.274
0.963
1.653
0.112
0.135
0.015
0.033
0.042
0.034
, 0.032
0.282
0.049
0.651
0.086
0.209
Sara Sara
8 9
0.000
0.000
34.289
65.594
0.000
0.705
60.731
2.394
4.024
5.084
2.702
0.135
12.839
22.035
1.490
1.806
0.100
0.217
0.279
0.227
0.211
1.883
0.198
2.604
0.346
0.838
Sara
10
3.210
5.509
0.373
0.451
Educational & Vocational
Total
0.000871
-------
SOG HAZARDOUS WASTE OUTPUT 1989 -- OREGON
Industry Group
Shops
Wholesale and
Retail Sales
Relevant SICs
at the
2-digit level
82
83
Total
51
52
53
1989
Employment
Estimate
3127.8
3581.5
46341.3
77235.4
Waste
Quant i ty
(Tons/yr/emp) I
(National)
1985
Based on
Industrial
Group
0.000552
Hazardous
taste Generated
For SQGs
By Industry
In Oregon
1989
(Tons/yr)
2.725
"
1.975
25.559
42.598
Sara
1
0.066
0.852
1.420
Sara
2
0.545
"
0.329
4.260
7.100
Sara
3
0.218
"
0.132
1.704
2.840
Sara Sara
4 5
0.545
"
0.346
4.473
7.455
Sara Sara
6 7
0.163
"
0.099
1.278
2.130
Sara
8
0.247
3.195
5.325
Sara
9
0.545
"
0.329
4.260
7.100
Sara
10
TOTALS
5060.706 4.017 824.099 320.562 0.000 801.989 0.000 242.100 20.519 1822.103 U.864
-------
SQG HAZARDOUS WASTE OUTPUT 1989 -- OREGON
Sara Sara Sara Sara Sara Sara Sara
11 12 13 14 15 16 17
1.149
6.699
2.050
2.504
0.016 0.158 0.008 0.158 0.316
0.032 1.270 0.016 0.317 0.635 0.317
3.358
0.112 0.056
0.062 0.031
0.717 0.359 2.868
0.401
0.917 0.459 3.670
29.846 14.923 119.385
10.534 5.267 42.136
11.884 5.942 47.537
0.273 0.137 1.093
71.166 35.583 284.664
6.766 3.383 27.063
11.925 5.962 47.698
0.110 0.055
0.063 0.032
0.036 0.018
0.005 0.003
-------
SQG HAZARDOUS WASTE OUTPUT 1989 -- OREGON
Sara Sara
11 12
0.000
0.000
1.693
3.239
0.000
0.035
2.999
0.118
0.402
0.508
0.270
0.006
1.052
0.000
0.183
0.642
1.102
0.075
0.090
0.010
0.022
0.028
0.023
0.021
0.188
0.033
0.434
0.058
0.140
Sara
13
0.000
0.000
8.467
16.196
0.000
0.174
14.995
0.591
2.012
2.542
1.351
5.258
0.000
0.914
0.199
0.217
0.279
0.227
0.211
1.883
Sara
14
0.000
0.000
0.847
1.620
0.000
0.017
1.500
0.059
0.201
0.254
0.135
0.003
0.526
0.000
0.091
0.321
0.551
0.037
0.045
0.005
0.011
0.014
0.011
0.011
0.094
0.016
0.217
0.029
0.070
Sara
15
0.000
0.000
8.043
15.386
0.000
0.165
14.245
0.561
0.049
0.100
0.434
0.557
0.454
0.421
0.132
1.736
0.231
0.559
Sara Sara
16 17
0.000
0.000
8.467
16.196
0.000
0.174
14.995
0.591
6.420
11.018
0.745
0.903
0.217
0.279
0.227
0.211
0.165
2.170
0.288
0.698
-------
SQG HAZARDOUS WASTE OUTPUT 1989 - OREGON
Sara
11
Sara
12
Sara
13
Sara
14
Sara
15
Sara
16
Sara
17
0.109 0.054 0.545
0.066 0.033 0.329
0.852 0.426 4.260
1.420 0.710 7.100
3.358 160.281 69.747 80.140 619.663 20.653 56.611
-------
SQG HAZARDOUS WASTE OUTPUT 2009 -- OREGON
Industry Group
Pesticide End-Users
Pesticide Application
Services
Chemical Manufacturing
Wood Preserving
Formulators
Laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Relevant SICs
at the
2-digit level
Total
79
84
Total
07
49
73
Total
28
Total
24
Total
28
Total
72
Total
72
73
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
Waste
Quantity Hazardous
(Tons/yr/enp) Waste Generated
(National) For SQGs
1985 By Industry
2009 Based on In Oregon
Employment Industrial 2009 Sara Sara
Estimate Group (Tons/yr) 1 2
0.001350
1398.6
0.002803
7204.2
958.2
1423.5
0.002465
620.0
0.001059
4349.7
0.002424
1898.1
0.006960
7686.7
0.002777
2562.2
1423.5
0.009364
4270.4
0.000955
680.9
0.046071
1801.1
27621.0
9748.6
10230.4
176.9
60547.9
5818.2
11330.9
50059.6 0.000150
25289.4
13760.9
9608.3
1398.6
1.888
20.195
2.686
3.990
1.529 0.191
4.605 4.605
4.600 0.383
53.502 2.675 24.076
7.115
3.953
39.988
0.651
82.976
1272.523
449.126
471.324
8.151
2789.489
268.047
522.023
-
3.800
2.068
1.444
0.210
1.779
0.988
5.713
0.325
13.829
212.087
74.854
78.554
1.358
464.915
44.675
87.004
-
0.760
0.414
0.289
0.042
Sara Sara Sara Sara Sara
34567
0.038
0.077
0.356
0.198
2.285
-
5.532
84.835
29.942
31.422
0.543
185.966
17.870
34.802
-
0.304
0.165
0.116
0.017
0.096
0.192
0.889
0.494
5.713
-
13.829
212.087
74.854
78.554
1.358
464.915
44.675
87.004
0.760
0.414
0.289
0.042
0.029
0.058
2.675 18
0.267
0.148
1.714
-
4.149
63.626
22.456
23.566
0.408
139.474
13.402
26.101
-
0.228
0.124
0.087
0.013
Sara Sara
8 9
0.382
0.767
.726
1.779
0.988
12.568
-
30.425
466.592
164.679
172.819
2.989
1022.813
98.284
191.408
-
1.520
0.827
0.578
0.084
Sara
10
1.779
0.988
5.713
-
-------
SQC HAZARDOUS WASTE OUTPUT 2009 -- OREGON
Industry Group
Shops
Wholesale and
Retail Sales
Waste
Quantity Hazardous
(Tons/yr/emp) Waste Generated
(National) For SQGs
1985 By Industry
Relevant SICs 2009 Based on In Oregon
at the Employment Industrial 2009 Sara
2-digit level Estimate Group (Tons/yr) 1
82
83
Total
51
52
S3
4061.5
0.000552
4504.4
60547.9
100913.2
3.538
2.484 0.083
33.395 1.113
55.658 1.855
Sara
2
0.708
0.414
5.566
9.276
Sara Sara Sara Sara Sara
34567
0.283
0.166
2.226
3.711
0.708
0.435
5.844
9.740
0.212
0.124
1.670
2.783
Sara Sara Sara
8 9 10
0.708
0.311 0.414
4.174 5.566
6.957 9.276
TOTALS
6978.745 5.7261129.964 438.940 0.0001098.112 0.000 331.880 30.1682512.288 20.476
-------
SOG HAZARDOUS WASTE OUTPUT 2009 - OREGON
Sara Sara
11 12
0.000
0.000
2.306
4.753
0.000
0.031
5.430
0.129
0.572
0.510
0.206
0.008
1.055
0.000
0.291
0.713
1.456
0.119
0.112
0.010
0.065
0.046
0.023
0.026
0.209
0.052
0.626
0.075
0.220
Sara
13
0.000
0.000
11.529
23.767
0.000
0.153
27.149
0.646
2.859
2.551
1.032
5.277
0.000
1.457
0.208
0.654
0.457
0.227
0.261
2.091
Sara
14
0.000
0.000
1.153
2.377
0.000
0.015
2.715
0.065
0.286
0.255
0.103
0.004
0.528
0.000
0.146
0.356
0.728
0.059
0.056
0.005
0.033
0.023
0.011
0.013
0.105
0.026
0.313
0.037
0.110
Sara
15
0.000
0.000
10.953
22.579
0.000
0.145
25.792
0.614
0.065
0.104
1.309
0.913
0.454
0.523
0.210
2.504
0.299
0.880
Sara Sara
16 17
0.000
0.000
11.529
23.767
0.000
0.153
27.149
0.646
7.130
14.556
1.187
1.120
0.654
0.457
0.227
0.261
0.262
3.130
0.374
1.100
-------
SQG HAZARDOUS WASTE OUTPUT 2009 - OREGON
Sara
11
Sara
12
Sara
13
Sara
14
Sara
15
Sara
16
Sara
17
0.142 0.071 0.708
0.083 0.041 0.414
1.113 0.5S7 5.566
1.855 0.928 9.276
5.350 219.470 111.129 109.735 854.309 26.359 84.840
-------
SQG HAZARDOUS WASTE OUTPUT 1987 WASHINGTON
Industry Croup
Pesticide End-Users
Pesticide Application
Services
Chemical Manufacturing
Wood Preserving
Fornulators
Laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Relevant SICs
at the
2-digit level
Total
79
84
Total
07
49
73
Total
28
Total
24
Total
28
Total
72
Total
72
73
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
1987
Employment
Estimate
1662.6
3501 .8
138.1
1473.7
2721.8
2811.6
8332.1
7957.8
2652.6
1473.7
4421.0
0.0
606.7
875.5
36283.4
12805.9
8950.2
627.5
72116.1
2273.0
11486.8
100.0
29934.8
16390.0
9947.3
1662.6
Waste
Quantity
(Tons/yr/etrp) I
(National)
1985
Based on
Industrial
Group
0.001350
0.002803
0.002465
0.001059
0.002424
0.006960
0.002777
0.009364
0.000955
0.046071
0.000150
Hazardous
laste Generated
For SOGs
By Industry
In Washington
1987
(Tons/yr)
2.244
-
9.816
0.387
4.131
6.710
2.977
20.194
55.389
7.366
4.092
41.399
0.580
40.333
1671 .607
589.979
412.341
28.908
3322.448
104.717
529.206
0.015
4.498
2.463
1.495
0.250
Sara Sara
1 2
0.839
2.977
1.683
2.769 24.925
1.841
1.023
5.914
0.290
6.722
278.601
98.330
68.723
4.818
553.741
17.453
88.201
0.003
0.900
0.493
0.299
0.050
Sara
3
0.168
0.337
0.368
0.205
2.366
-
2.689
111.440
39.332
27.489
1.927
221.497
6.981
35.280
0.001
0.360
0.197
0.120
0.020
Sara Sara
4 5
0.419
0.841
0.921
0.512
5.914
-
6.722
278.601
98.330
68.723
4.818
553.741
17.453
88.201
0.003
0.900
0.493
0.299
0.050
Sara Sera
6 7
0.126
0.252
2.769
0.276
0.153
1.774
2.017
83.580
29.499
20.617
1.445
166.122
5.236
26.460
0.001
0.270
0.148
0.090
0.015
Sara Sara
8 9
1.677
3.366
19.386
1.841
1.023
13.011
14.789
612.923
216.326
151.192
10.599
1218.231
38.396
194.042
0.006
1.799
0.985
0.598
0.100
Sara
10
1.841
1.023
5.914
-------
SOG HAZARDOUS WASTE OUTPUT 1987 - WASHINGTON
Relevant SICs
Industry Group at the
2-digit level
Metal Manufacturing
Construction
Motor Freight Terminals
Furniture/Wood
Manufacturing and
Ref imshing
Printing/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
Waste
Quantity Hazardous
(Tons/yr/emp) Waste Generated
(National) For SOGs
1985 By Industry
1987 Based on In Washington
Employment Industrial 1987 Sara Sara
Estimate Group (Tons/yr) 1 2
0.007695
3612.9
4502.6
9656.7
18487.4
13485.1
5041 . 1
13023.6
1211.9
0.001760
12805.9
5623.2
6531.0
0.000119
2983.4
0.001213
11246.4
4817.2
4973.6
12657.
19024.
1473.
1856.
1944.
700.
789.
440.
795.
3894.
2947.
20418.
4220.
12199.
0.004170
7
7
7
5
0.001630
1
0.003179
4
4
1
6
0.000894
7
0.000553
3
9
6
2
74
142
38
100
9
22
9
11
0
13
6
52
79
6
7
3
2
2
1
2
12
1
11
2
6
.312
.268
.793
.222
.326
.535
.895
.493
.354
.645
.034
.780
.330
.145
.741
.169
.227
.510
.399
.530
.382
.629
.287
.333
.743
7.431
14.227
3.879
10.022
0.933
3.756
1.649
1.915
0.071
3.411
1.509
5.278
7.933
0.614
0.774
0.528
0.318
0.359
0.200
0.361
3.096
0.272
1.881
0.389
1.124
Sara Sara Sara Sara Sara Sara Sara
3456789
2.972
5.691
1.552
4.009
0.373
1.502
0.660
0.766
0.014
1.364
0.603
2.111
3.173
0.246
0.310
0.106
0.064
0.072
0.040
0.072
0.619
0.109
0.752
0.156
0.450
7.431
14.227
3.879
10.022
0.933
3.756
1.649
1.915
0.035
3.411
1.509
5.278
7.933
0.614
0.774
'
0.264
0.159
0.179
0.100
0.181
1.548
0.272
1.881
0.389
1.124
2.229
4.268
1.164
3.007
0.280
1.127
0.495
0.575
0.011
1.023
0.453
1.583
2.380
0.184
0.232
0.079
0.048
0.054
0.030
0.054
0.464
0.081
0.564
0.117
0.337
30.096
57.619
15.711
40.590
3.777
7.512
3.298
3.831
0.156
21.112
31.732
2.458
3.096
0.526
0.318
0.359
0.200
0.361
3.096
0.326
2.257
0.467
1.349
Sara
10
5.278
7.933
0.614
0.774
Educational t Vocational
Total
0.000871
-------
SOG HAZARDOUS WASTE OUTPUT 1987 -- WASHINGTON
Industry Group
Shops
Wholesale and
Retail Sales
Relevant SICs
at the
2-digit level
82
83
Total
51
52
53
1987
Employment
Estimate
4220.6
0.0
5534.6
72116.1
120193.6
Waste
Quant i ty
(Tons/yr/emp)
(National)
1985
Based on
Industrial
Group
0.000552
Hazardous
Waste Generated
For SQGs
By Industry
In Washington
1987
(Tons/yr)
3.677
3.053
39.775
66.291
Sara
1
0.102
1.326
2.210
Sara
2
0.735
0.509
6.629
11.049
Sara
3
0.294
0.204
2.652
4.419
Sara Sara
4 5
0.735
0.534
6.961
11.601
Sara Sara
6 7
0.221
0.153
1.989
3.315
Sara
8
0.382
4.972
8.286
Sara
9
0.735
0.509
6.629
11.049
Sara
10
TOTALS
644636.271
7597.423 6.407 1248.678 486.131 0.000 1216.236 0.000 367.367 33.026 2730.075 23.378
-------
SQG HAZARDOUS UASTE OUTPUT 1987 WASHINGTON
Sara Sara Sara Sara Sara Sara Sara
11 12 13 U 15 16 17
2.244
9.816
0.387
4.131
0.084 0.839 0.042 0.839 1.677
0.168 6.731 0.084 1.683 3.366 1.683
5.559
0.184 0.092
0.102 0.051
1.183 0.591 4.731
0.290
1.344 0.672 5.378
55.720 27.860 222.881
19.666 9.833 78.664
13.745 6.872 54.979
0.964 0.482 3.854
110.748 55.374 442.993
3.491 1.745 13.962
17.640 8.820 70.S61
0.001 0.000
0.180 0.090
0.099 0.049
0.060 0.030
0.010 0.005
-------
SOG HAZARDOUS WASTE OUTPUT 1987 - WASHINGTON
Sara Sara
11 12
1.486
2.845
0.776
2.00A
0.187
0.751
0.330
0.383
0.007
0.682
0.302
1.056
1.587
0.123
0.155
0.053
0.032
0.036
0.020
0.036
0.310
0.054
0.376
0.078
0.225
Sara
13
7.431
14.227
3.879
10.022
0.933
3.756
1.649
1.915
3.411
1.509
1.056
0.318
0.359
0.200
0.361
3.096
Sara
14
0.743
1.423
0.388
1.002
0.093
0.376
0.165
0.192
0.004
0.341
0.151
0.528
0.793
0.061
0.077
0.026
0.016
0.018
0.010
0.018
0.155
0.027
0.188
0.039
0.112
Sara
15
7.060
13. SIS
3.685
9.521
0.886
0.057
0.528
0.636
0.717
0.400
0.723
0.217
1.505
0.311
0.899
Sara Sara
16 17
7.431
14.227
3.879
10.022
0.933
10.556
15.866
1.229
1.548
0.318
0.359
0.200
0.361
0.272
1.881
0.389
1.124
-------
SOG HAZARDOUS WASTE OUTPUT 1987 -- WASHINGTON
Sara
11
Sara
12
Sara
13
Sara
U
Sara
15
Sara
16
Sara
17
0.147 0.074 0.735
0.102 0.051 0.509
1.326 0.663 6.629
2.210 1.105 11.049
S.S39 243.065 78.561 121.533 941.185 33.803 62.440
-------
SOG HAZARDOUS WASTE OUTPUT 1989 -- WASHINGTON
Industry Group
Pesticide End-users
Pesticide Application
Services
Chemical Manufacturing
Wood Preserving
Formulators
Laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Relevant SICs
at the
2-digit level
Total
79
84
Total
07
49
73
Total
28
Total
24
Total
28
Total
72
Total
72
73
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
Waste
Quant i ty Hazardous
(Tons/yr/emp) Waste Generated
(National) For SQGs
1985 By Industry
1989 Based on In Washington
Employment Industrial 1989 Sara Sara
Estimate Group (Tons/yr) 1 2
0.001350
1790.7
0.002803
3840.7
975.5
1638.2
0.002465
2910.7
0.001059
2920.5
0.002424
8910.3
0.006960
8846.0
0.002777
2948.7
1638.2
0.009364
546.1
0.0
0.000955
606.7
0.046071
960.2
39106.9
13802.4
9486.5
629.7
75961.2
2486.1
12255.1
0.000150
100.0
31815.7
17263.9
11057.6
1790.7
2.417
10.766
2.735
4.592
7.176
3.092
21.596
61.572 3.
8.188
4.549
5.113
-
0.580
44.236
1801.686
635.889
437.052
29.009
3499.595
114.535
564.603
0.015
4.781
2.594
1.662
0.269
0.897
3.092
1.800
.079 27.707
2.047
1.137
0.730
0.290
7.373
300.281
105.982
72.842
4.835
583.266
19.089
94.100
0.003
0.956
0.519
0.332
0.054
Sara Sara Sara Sara Sara
34567
0.179
0.360
0.409
0.227
0.292
-
2.949
120.112
42.393
29.137
1.934
233.306
7.636
37.640
0.001
0.382
0.208
0.133
0.022
0.448
0.900
1.023
0.569
0.730
-
7.373
300.281
105.982
72.842
4.835
583.266
19.089
94.100
0.003
0.956
0.519
0.332
0.054
0.135
0.270
3.079 21
0.307
0.171
0.219
-
2.212
90.084
31.794
21 .853
1.450
174.980
5.727
28.230
0.001
0.287
0.156
0.100
0.016
Sara Sara
8 9
1.794
3.599
.550
2.047
1.137
1.607
-
16.220
660.618
233.159
160.253
10.637
1283.185
41.996
207.021
0.006
1.912
1.038
- 0.665
0.108
Sara
10
2.047
1 137
0.730
-
-------
SQG HAZARDOUS WASTE OUTPUT 1989 -- WASHINGTON
Industry Group
Metal Manufacturing
Construction
Motor Freight Terminals
Furniture/Wood
Manufacturing and
Ref inishmg
Printing/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Relevant SICs
at the
2-digit level
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
1989
Employment
Estimate
7238.7
4758.8
10491.8
20190.5
14797.0
5385.6
15248.7
1295.9
13802.4
5840.9
6308.4
3162.2
11681.9
9651.5
5528.8
12834.3
20125.8
1638.2
1948.6
2079.1
768.1
893.1
413.0
835.1
3949.0
3276.3
3219S.1
4555.8
13276.3
Waste
Ouant i ty
(Tons/yr/emp) V
(National)
1985
Based on
Industrial
Group
0.007695
0.001760
0.000119
0.001213
0.004170
0.001630
0.003179
0.000894
0.000553
Hazardous
taste Generated
For SQGs
By Industry
In Washington
1989
(Tons/yr)
-
80.739
155.374
-
41.445
117.345
9.972
24.288
10.278
11.101
0.375
14.173
-
6.708
53.517
83.921
6.831
8.125
3.389
2.442
2.839
1.313
2.655
12.555
1.811
17.797
2.518
7.339
Sara Sara
1 2
-
-
8.074
15.537
.
4.144
11.735
0.997
4.048
1.713
1.850
0.075
3.543
-
1.677
5.352
8.392
0.683
0.813
0.565
0.349
0.406
0.188
0.379
3.139
0.302
2.966
0.420
1.223
Sara
3
-
-
3.230
6.215
.
1.658
4.694
0.399
1.619 '
0.685
0.740
0.015
1.417
-
0.671
2.141
3.357
0.273
0.325
0.113
0.070
0.081
0.038
0.076
0.628
0.121
1.186
0.168
0.489
Sara Sara
4 5
-
.
8.074
15.537
.
4.144
11.735
0.997
4.048
1.713
1.850
0.038
3.543
.
1.677
5.352
8.392
0.683
0.813
0.282
0.174
0.203
0.094
0.190
1.569
0.302
2.966
0.420
1.223
Sara Sara
6 7
-
.
2.422
4.661
.
1.243
3.520
0.299
1.214
0.514
0.555
0.011
1.063
-
0.503
1.606
2.518
0.205
0.244
0.085
0.052
0.061
0.028
0.057
0.471
0.091
0.890
0.126
0.367
Sara Sara
8 9
.
.
32.699
62.927
16.785
47.525
4.039
8.096
3.426
3.700
0.165
21.407
33.568
2.732
3.250
0.565
0.349
0.406
0.188
0.379
3.139
0.362
3.559
0.504
1.468
Sara
10
5.352
8.392
0.633
0.813
Educational & Vocational
Total
0.000871
-------
SQG HAZARDOUS WASTE OUTPUT 1989 -- WASHINGTON
Industry Group
Shops
Wholesale and
Retail Sales
Relevant SICs
at the
2-digit level
82
83
Total
51
52
53
Waste
Quantity
(fons/yr/emp) I
(National)
1985
1989 Based on
Employment Industrial
Estimate Group
4555.8
0.0
0.0005S2
5815.5
75961.2
126602.1
Hazardous
Jaste Generated
For SOGs
By Industry
In Washington
1989
(Tons/yr)
3.969
"
3.207
41.896
69.826
Sara
1
0.107
1.397
2.328
Sara
2
0.794
0.535
6.983
11.638
Sara
3
0.318
0.2H
2.793
4.655
Sara Sara
4 5
0.794
0.561
7.332
12.220
Sara Sara
6 7
0.238
~
0.160
2.095
3.491
Sara
8
0.401
5.237
8.728
Sara
9
0.794
*
0.535
6.983
11.638
Sara
10
TOTALS
701393.565
8066.050 6.910 1325.850 515.708 0.000 1290.228 0.000 389.860 35.916 2898.188 19.154
-------
SOG HAZARDOUS WASTE OUTPUT 1989 -- WASHINGTON
Sara Sara
11 12
1.615
3.107
0.829
2.347
0.199
0.810
0.343
0.370
0.008
0.709
0.33S
1.070
1.678
0.137
0.163
0.056
0.035
0.041
0.019
0.038
0.3U
0.060
0.593
0.084
0.245
Sara
13
8.074
15.537
4.144
11.735
0.997
4.048
1.713
1.850
3.543
1.677
1.130
0.349
0.406
0.188
0.379
3.139
Sara
14
0.807
1.554
0.414
1.173
0.100
0.405
0.171
0.185
0.004
0.354
0.168
0.535
0.839
0.068
0.081
0.028
0.017
0.020
0.009
0.019
0.157
0.030
0.297
0.042
0.122
Sara
15
7.670
14.761
3.937
11.148
0.947
0.060
0.565
0.698
0.811
0.375
0.759
0.241
2.373
0.336
0.979
Sara Sara
16 17
8.074
15.537
4.144.
11.735
0.997
10.703
16.784
1.366
1.625
0.349
0.406
0.188
0.379
0.302
2.966
0.420
1.223
-------
SOG HAZARDOUS WASTE OUTPUT 1989 -- WASHINGTON
Sara Sara Sara Sara Sara Sara Sara
11 12 13 U 15 16 17
2.417
10.766
2.735
A. 592
0.090 0.897 0.045 0.897 1.794
0.180 7.199 0.090 1.800 3.599 1.800
6.157
0.205 0.102
0.114 0.057
0.146 0.073 0.584
0.290
1.475 0.737 5.898
60.056 30.028 240.225
21.196 10.598 84.785
14.568 7.284 58.274
0.967 0.483 3.868
116.653 58.327 466.613
3.818 1.909 15.271
18.820 9.410 75.280
0.001 0.000
0.191 0.096
0.104 0.052
0.066 0.033
0.011 0.005
-------
SOG HAZARDOUS WASTE OUTPUT 1989 - WASHINGTON
Sara
11
Sara
12
Sara
13
Sara
U
Sara
15
Sara
16
Sara
17
0.159 0.079 0.794
0.107 0.053 0.535
1.397 0.698 6.983
2.328 1.164 11.638
6.157 257.854 87.804 128.927 999.154 35.399 68.941
-------
SQG HAZARDOUS UASTE OUTPUT 1989 -- WASHINGTON
industry Group
Pesticide End-Users
Pesticide Application
Services
Chemical Manufacturing
Wood Preserving
Formulators
Laundries
Other Services
Photography
Textile Manufacturing
Vehicle Maintenance
Equipment Repair
Relevant SICs
at the
2-digit level
Total
79
84
Total
07
49
73
Total
28
Total
24
Total
28
Total
72
Total
72
73
Total
73
84
Total
22
Total
07
16
17
42
44
52
55
75
Total
46
48
59
76
79
Waste
Quantity
(Tons/yr/emp) Ua
(National)
1985
1989 Based on I
Employment Industrial
Estimate Group
0.001350
1790.7
0.002803
3840.7
975.5
1638.2
0.002465
2910.7
0.001059
2920.5
0.002424
8910.3
0.006960
8846.0
0.002777
2948.7
1638.2
0.009364
546.1
0.0
0.000955
606.7
0.046071
960.2
39106.9
13802.4
9486.5
629.7
75961.2
2486.1
12255.1
0.000150
100.0
31815.7
17263.9
11057.6
1790.7
Hazardous
ste Generated
For SQGs
By Industry
n Washington
1989 !
(Tons/yr)
2.417
10.766
2.735
4.592
7.176
3.092
21 .596
61.572 3,
8.188
4.549
5.113
-
0.580
44.236
1801.686
635.889
437.052
29.009
3499.595
114.535
564.603
0.015
4.781
2.594
1.662
0.269
Sara Sara
1 2
0.897
3.092
1.800
.079 27.707
2.047
1.137
0.730
-
0.290
7.373
300.281
105.982
72.842
4.835
583.266
19.089
94.100
0.003
0.956
0.519
0.332
0.054
Sara i
3
0.179
0.360
0.409
0.227
0.292
-
2.949
120.112
42.393
29. 137
1.934
233.306
7.636
37.640
0.001
0.382
0.208
0.133
0.022
>ara Sara S
4 5
0.448
0.900
1.023
0.569
0.730
-
7.373
300.281
105.982
72.842
4.835
583.266
19.089
94.100
0.003
0.956
0.519
0.332
0.054
lara Sara
6 7
0.135
0.270
3.079 21
0.307
0.171
0.219
-
2.212
90.084
31.794
21 .853
1.450
174.980
5.727
28.230
0.001
0.287
0.156
0.100
0.016
Sara Sara
8 9
1.794
3.599
.550
2.047
1.137
1.607
-
16.220
660.618
233.159
160.253
10.637
1283.185
41.996
207.021
0.006
1.912
1.038
0.665
0.108
Sara
10
2.047
1.137
0.730
-------
S>Uli HAZARDOUS WASTE uuifUT 2UUT -- UASnimiiON
Industry Group
Metal Manufacturing
Construction
Motor Freight Terminals
Furniture/Wood
Manufacturing and
Ref inishing
Printing/Ceramics
Cleaning agents and
Cosmetic Manufacturing
Other Manufacturing
Paper Industry
Analytic & Clinical
Laboratories
Relevant SICs
at the
2-digit level
Total
25
33
34
35
36
37
38
39
Total
17
24
40
Total
42
Total
24
25
76
Total
26
27
73
32
Total
28
Total
07
30
31
32
Total
26
Total
73
80
82
89
2009
Employment
Estimate
1093.8
5746.1
13243.6
28845.1
20148.4
6496.3
36851.3
1727.0
17429.3
5857.0
4936.1
4562.7
11714.1
1458.4
8813.5
13152.9
25634.4
2611.4
2198.4
2828.3
1207.1
1451.9
400.0
942.2
4047.1
5222.8
56999.7
5901.9
21327.0
Waste
Quant i ty
(Tons/yr/emp) V
(National)
1985
Based on
Industrial
Group
0.007695
0.001760
0.000119
0.001213
0.004170
0.001630
0.003179
0.000894
0.000553
Hazardous
laste Generated
For SQGs
By Industry
In Washington
2009
(Tons/yr)
.
.
101.915
221.975
.
49.992
283.586
13.290
30.670
10.307
8.686
0.541
14.212
.
10.693
54.845
106.891
10.889
9.167
4.610
3.838
4.616
1.272
2.995
12.866
2.887
31.508
3.262
11.789
Sara Sara
1 2
.
.
10.192
22.198
.
4.999
28.359
1.329
5.112
1.718
1.448
0.108
3.553
.
2.673
5.485
10.689
1.089
0.917
0.768
0.548
0.659
0.182
0.428
3.217
0.481
5.251
0.544
1.965
Sara
3
.
.
4.077
8.879
.
2.000
11.343
0.532
2.045
0.687
0.579
0.022
1.421
.
1.069
2.194
4.276
0.436
0.367
0.154
0.110
0.132
0.036
0.086
0.643
0.192
2.101
0.217
0.786
Sara Sara
4 5
.
.
10.192
22.198
.
4.999
28.359
1.329
5.112
1.718
1.448
0.054
3.553
2.673
5.485
10.689
1.089
0.917
0.384
0.274
0.330
0.091
0.214
1.608
0.481
5.251
0.544
1.965
Sara Sara
6 7
_
_
3.057
6.659
_
1.500
8.508
0.399
1.534
0.515
0.434
0.016
1.066
0.802
1.645
3.207
0.327
0.275
0.115
0.082
0.099
0.027
0.064
0.482
0.144
1.575
0.163
0.589
Sara Sara
8 9
_
_
41.276
89.900
20.247
114.852
5.382
10.223
3.436
2.895
0.238
21.938
42.756
4.356
3.667
0.768
0.548
0.659
0.182
0.428
3.217
0.577
6.302
0.652
2.358
Sara
10
5.485
10.689
1.089
0.917
Educational & Vocational
Total
0.000871
-------
SOG HAZARDOUS WASTE OUTPUT 2009 -- WASHINGTON
Industry Group
Shops
Wholesale and
Retail Sales
Relevant SICs
at the
2-digit level
82
83
Total
51
52
53
2009
Employment
Estimate
5901.9
0.0
7435.9
98243.0
163738.3
Waste
Quant i ty
(Tons/yr/emp) \
(National)
1985
Based on
Industrial
Group
0.000552
Hazardous
laste Generated
For SQGs
By Industry
In Washington
2009
(Tons/yr)
5.U2
-
4.101
54.185
90.308
Sara
1
0.137
1.806
3.010
Sara
2
1.028
-
0.684
9.031
15.051
Sara
3
0.411
-
0.273
3.612
6.021
Sara Sara
4 5
1.028
-
0.718
9.482
15.804
Sara Sara
6 7
0.308
-
0.205
2.709
4.515
Sara
8
0.513
6.773
11.289
Sara
9
1.028
-
0.684
9.031
15.051
Sara
10
TOTALS
937489.265
10749.898 9.8611760.867 682.405 0.0001707.250 0.000 516.711 52.9283857.307 33.735
-------
SOG HAZARDOUS WASTE OUTPUT 2009 -- WASHINGTON
Sara Sara Sara Sara Sara Sara Sara
11 12 13 14 15 16 17
2.038 10.192 1.019 9.682 10.192
4.440 22.198 2.220 21.088 22.198
1.000 4.999 O.SOO 4.749 4.999
5.672 28.359 2.836 26.941 28.359
0.266 1.329 0.133 1.263 1.329
1.022 5.112 0.511
0.344 1.718 0.172
0.290 1.448 0.145
0.011 0.005 0.087
0.711 3.553 0.355
0.535 2.673 0.267
1.097 0.548 10.969
2.138 1.069 21.378
0.218 0.109 2.178
0.183 0.092 1.833
0.077 1.537 0.038 0.768
0.055 0.548 0.027 1.096 0.548
0.066 0.659 0.033 1.319 0.659
0.018 0.182 0.009 0.363 0.182
0.043 0.428 0.021 0.856 0.428
0.322 3.217 0.161
0.096 0.048 0.385 0.481
1.050 0.525 4.201 5.251
0.109 0.054 0.435 0.544
0.393 0.196 1.572 1.965
-------
SOG HAZARDOUS WASTE OUTPUT 2009 - WASHINGTON
Sara Sara Sara Sara Sara Sara Sara
11 12 13 14 15 16 17
3.713
16.919
2.458
7.320
0.122 1.220 0.061 1.220 2.440
0.245 9.793 0.122 2.448 4.896 2.448
9.815
0.326 0.163
0.181 0.091
2.096 1.048 8.384
0.258
2.317 1.159 9.269
75.837 37.919 303.349
26.766 13.383 107.064
21.021 10.510 84.084
1.037 0.519 4.148
150.871 75.436 603.484
4.361 2.180 17.443
28.154 14.077 112.617
0.001 0.000
0.261 0.130
0.134 0.067
0.106 0.053
0.017 0.008
-------
SOG HAZARDOUS WASTE uuirul £\iur --
Sara
11
Sara
12
Sara
13
Sara
14
Sara
15
Sara
16
Sara
17
0.206 0.103 1.028
0.137 0.068 0.684
1.806 0.903 9.031
3.010 1.505 15.051
9.815 341.202 129.831 170.601 1328.314 43.072 106.000
-------
APPENDIX I
Projections of Household Hazardous Waste Generation
-------
ALASKA
Household
Hazardous Waste
Lower Sara 2
POPULATION (tons) (tons)
1985
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
539.151
542.151
537.080
534,940
536,848
539,375
541,754
552,115
562,475
572,836
583,197
593,557
603,918
614,279
624,639
635,000
645,361
655.721
666.082
676,443
686,803
697,164
707,525
717,885
728,246
738,607
738
742
735
732
735
738
742
756
770
784
798
812
827
841
855
869
883
898
912
926
940
954
968
983
997
1,011
24.60
24.74
24.50
24.41
24.49
24.61
24.72
25.19
25.66
26.14
26.61
27.08
27.55
28.03
28.50
28.97
29.44
29.92
30.39
30.86
31.34
31.81
32.28
32.75
33.23
33.70
Sara 3
(tons)
98.40
98.94
98.02
97.63
97.97
98.44
98.87
100.76
102.65
104.54
106.43
108.32
110.22
112.11
114.00
115.89
117.78
119.67
121.56
123.45
125.34
127.23
129.12
131.01
132.90
134.80
Sara 4
(tons)
24.60
24.74
24.50
24.41
24.49
24.61
24.72
25.19
25.66
26.14
26.61
27.08
27.55
28.03
28.50
28.97
29.44
29.92
30.39
30.86
31.34
31.81
32.28
32.75
33.23
33.70
Sara 5
(tons)
98.40
98.94
98.02
97.63
97.97
98.44
98.87
100.76
102.65
104.54
106.43
108.32
110.22
112.11
114.00
115.89
117.78
119.67
121.56
123.45
125.34
127.23
129.12
131.01
132.90
134.80
Sara 9 Sara 11 Sara 12 Sara 15
(tons) (tons) (tons) (tons)
184.49
185.52
183.78
183.05
183.70
184.57
185.38
188.93
192.47
196.02
199.56
203.11
206.65
210.20
213.74
217.29
220.83
224.38
227.92
231.47
235.02
238.56
242.11
245.65
249.20
252.74
24.60
24.74
24.50
24.41
24.49
24.61
24.72
25.19
25.66
26.14
26.61
27.08
27.55
28.03
28.50
28.97
29.44
29.92
30.39
30.86
31.34
31.81
32.28
32.75
33.23
33.70
98.40
98.94
98.02
97.63
97.97
98.44
98.87
100.76
102.65
104.54
106.43
108.32
110.22
112.11
114.00
115.89
117.78
119.67
121.56
123.45
125.34
127.23
129.12
131.01
132.90
134.80
184.49
185.52
183.78
183.05
183.70
184.57
185.38
188.93
192.47
196.02
199.56
203.11
206.65
210.20
213.74
217.29
220.83
224.38
227.92
231 .47
235.02
238.56
242.11
245.65
249.20
252.74
-------
ALASKA
F
YEAR -
1985
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
Household
Hazardous Waste
Upper Sara 2
OPULATION (tons) (tons)
539.
542.
537|
534.
536.
539.
541
552.
562.
572
583,
593.
603,
614,
624,
635,
645,
655!
666,
676.
686,
697,
707
717,
728.
738.
151
151
080
940
848
375
754
115
475
836
197
557
918
279
639
000
361
721
082
443
803
164
525
885
246
607
.378
.385
,372
,367
,372
378
,384
,411
,437
,464
,490
.517
,543
.569
.596
.622
,649
,675
,702
,728
,755
,781
,808
.834
,861
.887
45.92
46.17
45.74
45.56
45.72
45.94
46.14
47.02
47.90
48.79
49.67
50.55
51.43
52.32
53.20
54.08
54.96
55.85
56.73
57.61
58.49
59.38
60.26
61.14
62.02
62.90
Waste * Container
Residue
Sara 3 Sara 4
(tons) (tons)
183.67
184.69
182.97
182.24
182.89
183.75
184.56
188.09
191 .62
195.15
198.68
202.21
205.73
209.26
212.79
216.32
219.85
223.38
226.91
230.44
233.97
237.50
241 .03
244.56
248.09
251.62
45.92
46.17
45.74
45.56
45.72
45.94
46.14
47.02
47.90
48.79
49.67
50.55
51.43
52.32
53.20
54.08
54.96
55.85
56.73
57.61
58.49
59.38
60.26
61.14
62.02
62.90
Sara 5
(tons)
183.67
184.69
182.97
182.24
182.89
183.75
184.56
188.09
191.62
195.15
198.68
202.21
205.73
209.26
212.79
216.32
219.85
223.38
226.91
230.44
233.97
237.50
241.03
244.56
248.09
251.62
Sara 9 Sara 11
(tons) (tons)
344.38
346.30
343.06
341.69
342.91
344.53
346.05
352.66
359.28
365.90
372.52
379.13
385.75
392.37
398.99
405.61
412.22
418.84
425.46
432.08
438.70
445.31
451.93
458.55
465.17
471.79
45.92
46.17
45.74
45.56
45.72
45.94
46.14
47.02
47.90
48.79
49.67
50.55
51.43
52.32
53.20
54.08
54.96
55.85
56.73
57.61
58.49
59.38
60.26
61.14
62.02
62.90
Sara 12
(tons)
183.67
184.69
182.97
182.24
182.89
183.75
184.56
188.09
191.62
195.15
198.68
202.21
205.73
209.26
212.79
216.32
219.85
223.38
226.91
230.44 '
233.97
237.50
241.03
244.56
248.09
251.62
Sara 15
(tons)
344.38
346.30
343.06
341 .69
342.91
344.53
346.05
352.66
359.28
365.90
372.52
379.13
385.75
392.37
398.99
405.61
412.22
418.84
425.46
432.08
438.70
445.31
451 .93
458.55
465.17
471.79
-------
ALASKA
Waste + Container
Residue
Lower Sara 2
POPULATION (tons) (tons)
1985
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
539,151
542,151
537.080
534,940
536,848
539,375
541,754
552,115
562,475
572,836
583,197
593,557
603,918
614,279
624,639
635,000
645,361
655,721
666,082
676,443
686,803
697,164
707,525
717,885
728,246
738,607
4,920
4,947
4.901
4,881
4,899
4,922
4,944
5,038
5,133
5,227
5,322
5.416
5,511
5,605
5,700
5,794
5,889
5,983
6,078
6,173
6.267
6,362
6,456
6,551
6,645
6,740
163.99
164.90
163.36
162.71
163.29
164.06
164.78
167.93
171.09
174.24
177.39
180.54
183.69
186.84
189.99
193.15
196.30
199.45
202.60
205.75
208.90
212.05
215.21
218.36
221.51
224.66
Sara 3
(tons)
655.97
659.62
653.45
650.84
653.17
656.24
659.13
671.74
684.34
696.95
709.56
722.16
734.77
747.37
759.98
772.58
785.19
797.79
810.40
823.01
835.61
848.22
860.82
873.43
886.03
898.64
Sara 4
(tons)
163.99
164.90
163.36
162.71
163.29
164.06
164.78
167.93
171.09
174.24
177.39
180.54
183.69
186.84
189.99
193.15
196.30
199.45
202.60
205.75
208.90
212.05
215.21
218.36
221.51
224.66
Sara 5
(tons)
655.97
659.62
653.45
650.84
653.17
656.24
659.13
671.74
684.34
696.95
709.56
722.16
734.77
747.37
759.98
772.58
785.19
797.79
810.40
823.01
835.61
848.22
860.82
873.43
886.03
898.64
Sara 9
(tons)
1.229.94
1,236.78
1,225.21
1,220.33
1.224.68
1,230.45
1.235.88
,259.51
,283.15
,306.78
,330.42
,354.05
,377.69
.401.32
.424.96
,448.59
1,472.23
1,495.86
1,519.50
,543.14
.566.77
.590.41
,614.04
,637.68
,661.31
,684.95
Sara 11
(tons)
163.99
164.90
163.36
162.71
163.29
164.06
164.78
167.93
171 .09
174.24
177.39
180.54
183.69
186.84
189.99
193.15
196.30
199.45
202.60
205.75
208.90
212.05
215.21
218.36
221.51
224.66
Sara 12 Sara 15
(tons) (tons)
655.97 .229.94
659.62
653.45
650.84
653.17
656.24
659.13
671.74
684.34
696.95
709.56
722.16
734.77
747.37
759.98
772.58
785.19
797.79
810.40
823.01
835.61
848.22
860.82
.236.78
,225.21
,220.33
.224.68
,230.45
,235.88
,259.51
,283.15
.306.78
.330.42
.354.05
.377.69
.401.32
,424.96
,448.59
,472.23
,495.86
,519.50
,543.14
,566.77
.590.41
.614.04
873.43 1,637.68
886.03 1,661.31
898.64 1,684.95
-------
ALASKA
YEAR
1985
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
POPULATION
539.151
542,151
537,080
534,940
536.848
539.375
541.754
552.115
562.475
572,836
583,197
593,557
603,918
614.279
624.639
635,000
645,361
655.721
666.082
676,443
686,803
697,164
707,525
717.885
728,246
738.607
Waste + Container
Residue
Upper Sara 2
(tons) (tons)
6,888
6,926
6,861
6,834
6.858
6.891
6,921
7,053
7,186
7,318
7,450
7,583
7,715
7,847
7.980
8.112
8.244
8,377
8,509
8,642
8,774
8,906
9,039
9.171
9,303
9,436
229.59
230.87
228.71
227.80
228.61
229.68
230.70
235.11
239.52
243.93
248.34
252.76
257.17
261.58
265.99
270.40
274.82
279.23
283.64
288.05
292.46
296.88
301.29
305.70
310.11
314.52
Sara 3
(tons)
918.35
923.46
914.83
911.18
914.43
918.74
922.79
940.44
958.08
975.73
993.38
,011.03
,028.67
.046.32
,063.97
,081.62
1,099.26
1,116.91
1,134.56
1,152.21
1,169.85
1,187.50
1,205.15
1,222.80
1,240.45
1,258.09
Sara 4 Sara 5 Sara 9
(tons) (tons) (tons)
229.59 918.35
230.87 923.46
228.71 914.83
227.80 911.18
228.61 914.43
229.68 918.74
230.70 922.79
235.11 940.44
239.52 958.08
243.93 975.73
248.34 993.36
252.76 1,011.03
257.17 1,028.67
261.58
265.99
270.40
274.82
279.23
283.64
288.05
292.46
296.88
301.29
305.70
310.11
314.52
,046.32
,063.97
,721.91
,731.49
,715.30
,708.46
,714.56
.722.63
,730.23
,763.32
,796.40
,829.49
,862.59
,895.67
,928.76
.961.85
.994.94
.081.62 2,028.03
.099.26 2,061.12
,116.91 2,094.21
,134.56 2,127.30
,152.21 2,160.39
,169.85 2,193.48
,187.50 2,226.57
,205.15 2,259.66
,222.80 2,292.75
,240.45 2.325.84
,258.09 2.358.93
Sara 11 Sara 12 Sara 15
(tons) (tons) (tons)
229.59 918.35
230.87 923.46
228.71 914.83
227.80 911.18
228.61 914.43
229.68 918.74
230.70 922.79
235.11 940.44
239.52 958.08
243.93 975.73
248.34 993.38
252.76 1,011.03
,721.91
,731.49
,715.30
,708.46
,714.56
.722.63
,730.23
,763.32
,796.40
,829.49
,862.59
.895.67
257.17 1,028.67 1,928.76
261.58 1,046.32 1,961.85
265.99 1.063.97 1,994.94
270.40
274.82
279.23
283.64
288.05
292.46
296.88
301.29
305.70
310.11
314.52
,081.62 2,028.03
.099.26 2.061.12
.116.91 2,094.21
,134.56 2,127.30
,152.21 2,160.39
,169.85 2,193.48
,187.50 2,226.57
,205.15 2.259.66
,222.80 2,292.75
,240.45 2,325.84
.258.09 2,358.93
-------
IDAHO
Household
Hazardous Waste
Lower Sara 2
POPULATION (tons) (tons)
i cni\
1985 1,035,740
1986 1,053,252
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
.070,764
,088,276
,105,788
.123,300
.138,262
,153,224
.168,186
,183.148
,198,110
,418
,442
.466
,490
.514
.538
.558
.578
,599
,619
.640
,211,404 1,658
,224,698 1,676
,237,992 1,695
,251,286 1,713
,264,580 1,731
,275,924 1,746
.287.268 1.762
.298.612 1.777
.309.956 1.793
,321,300 1.809
,334,052 1,826
,346.804 1,843
,359,556 1,861
,372,308 1,878
,385,060 1,896
47.26
48.05
48.85
49.65
50.45
51.25
51.93
52.62
53.30
53.98
54.66
55.27
55.88
56.48
57.09
57.70
58.21
58.73
59.25
59.77
60.28
60.87
61.45
62.03
62.61
63.19
Sara 3
(tons)
189.02
192.22
195.41
198.61
201.81
205.00
207.73
210.46
213.19
215.92
218.66
221.08
223.51
225.93
228.36
230.79
232.86
234.93
237.00
239.07
241.14
243.46
245.79
248.12
250.45
252.77
Sara 4
(tons)
47.26
48.05
48.85
49.65
50.45
51.25
51.93
52.62
53.30
53.98
54.66
55.27
55.88
56.48
57.09
57.70
58.21
58.73
59.25
59.77
60.28
60.87
61.45
62.03
62.61
63.19
Sara 5
(tons)
189.02
192.22
195.41
198.61
201.81
205.00
207.73
210.46
213.19
215.92
218.66
221.08
223.51
225.93
228.36
230.79
232.86
234.93
237.00
239.07
241.14
243.46
245.79
248.12
250.45
252.77
Sara 9
(tons)
354.42
360.41
366.40
372.39
378.39
384.38
389.50
394.62
399.74
404.86
409.98
414.53
419.08
423.63
428.17
432.72
436.61
440.49
444.37
448.25
452.13
456.50
460.86
465.22
469.59
473.95
Sara 11
(tons)
47.26
48.05
48.85
49.65
50.45
51.25
51.93
52.62
53.30
53.98
54.66
55.27
55.88
56.48
57.09
57.70
58.21
58.73
59.25
59.77
60.28
60.87
61.45
62.03
62.61
63.19
Sara 12
(tons)
189.02
192.22
195.41
198.61
201.81
205.00
207.73
210.46
213.19
215.92
218.66
221.08
223.51
225.93
228.36
230.79
232.86
234.93
237.00
239.07
241.14
243.46
245.79
248.12
250.45
252.77
Sara 15
(tons)
354.42
360.41
366.40
372.39
378.39
384.38
389.50
394.62
399.74
404.86
409.98
414.53
419.08
423.63
428.17
432.72
436.61
440.49
444.37
448.25
452.13
456.50
460.86
465.22
469.59
473.95
-------
IDAHO
Household Waste + Container
Hazardous Waste Residue
Upper Sara 2 Sara 3 Sara 4
POPULATION (tons) (tons) (tons) (tons)
1985 1.035.740
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
,053,252
,070,764
,088.276
,105,788
,123,300
,138,262
,153,224
,168,186
,183.148
,198,110
,211,404
,224,698
,237,992
,251,286
,264,580
.275,924
,287,268
,298,612
,309.956
,321,300
,334,052
,346,804
,359.556
,372.308
,385,060
2,646
2,691
2,736
2,781
2,825
2,870
2,908
2,946
2,985
3,023
3,061
3.095
3.129
3,163
3,197
3,231
3,260
3,289
3,318
3,347
3,376
3.409
3,441
3,474
3.506
3.539
88.21
89.70
91.19
92.68
94.18
95.67
96.94
98.22
99.49
100.76
102.04
103.17
104.30
105.44
106.57
107.70
108.67
109.63
110.60
111.56
112.53
113.62
114.70
115.79
116.87
117.96
352.84
358.81
364.77
370.74
376.71
382.67
387.77
392.86
397.96
403.06
408.16
412.68
417.21
421.74
426.27
430.80
434.66
438.53
442.39
446.26
450.12
454.47
458.81
463.16
467.50
471.84
88.21
89.70
91.19
92.68
94.18
95.67
96.94
98.22
99.49
100.76
102.04
103.17
104.30
105.44
106.57
107.70
108.67
109.63
110.60
111.56
112.53
113.62
114.70
115.79
116.87
117.96
Sara 5
(tons)
352.84
358.81
364.77
370.74
376.71
382.67
387.77
392.86
397.96
403.06
408.16
412.68
417.21
421.74
426.27
430.80
434.66
438.53
442.39
446.26
450.12
454.47
458.81
463.16
467.50
471.84
Sara 9 Sara 11
(tons) (tons)
661.58
672.76
683.95
695.14
706.32
717.51
727.06
736.62
746.18
755.74
765.29
773.78
782.28
790.77
799.26
807.75
815.00
822.24
829.49
836.73
843.98
852.13
860.27
868.42
876.56
884.71
88.21
89.70
91.19
92.68
94.18
95.67
96.94
98.22
99.49
100.76
102.04
103.17
104.30
105.44
106.57
107.70
108.67
109.63
110.60
111.56
112.53
113.62
114.70
115.79
116.87
117.96
Sara 12
(tons)
352.84
358.81
364.77
370.74
376.71
382.67
387.77
392.86
397.96
403.06
408.16
412.68
417.21
421 .74
426.27
430.80
434.66
438.53
442.39
446.26
450.12
454.47
458.81
463.16
467.50
471.84
Sara 15
(tons)
661.58
672.76
683.95
695.14
706.32
717.51
727.06
736.62
746.18
755.74
765.29
773.78
782.28
790.77
799.26
807.75
815.00
822.24
829.49
836.73
843.98
852.13
860.27
868.42
876.56
884.71
-------
IDAHO
POPULATION
1985 1,035,740
1986 1,053,252
1987 1,070.764
1988 1,088.276
1989 1.105,788
1990 1.123,300
1991 1,138,262
1992 1,153,224
1993 1,168,186
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
,183,148
.198,110
,211,404
,224,698
,237.992
,251,286
.264.580
.275.924
.287.268
.298.612
,309,956
,321.300
,334.052
.346.804
.359,556
2009 1,372,308
2010 1,385,060
Waste + Container
Residue
Lower Sara 2 Sara 3
(tons) (tons) (tons)
9,451
9,611
9.771
9.931
10,090
10,250
10,387
10,523
10,660
10,796
10,933
11,054
11,175
11,297
11,418
11.539
11.643
11.746
11.850
11.953
12.057
12.173
12.290
12.406
12,522
12,639
315.04
320.36
325.69
331.02
336.34
341.67
346.22
350.77
355.32
359.87
364.43
368.47
372.51
376.56
380.60
384.64
388.09
391.54
394.99
398.44
401.90
405.77
409.65
,260.15
,281.46
,302.76
,324.07
.345.38
,366.68
,384.89
,403.09
,421.29
,439.50
,457.70
,473.87
,490.05
.506.22
,522.40
,538.57
,552.37
,566.18
.579.98
,593.78
.607.58
,623.10
,638.61
413.53 1,654.13
417.41 1,669.64
421.29 1,685.16
Sara 4 Sara 5
(tons) (tons)
315
320
325
331
336
341
346
350
355
359
364
368
372
376
380
384
388
391
394
398
401
405
409
413
417
421
.04
.36
.69
.02
.34
.67
.22
.77
.32
.87
.43
.47
.51
56
!60
.64
.09
.54
99
°44
!90
.77
.65
.53
,260.15
,281.46
.302.76
,324.07
.345.38
( JOOaOO
,384.89
,403.09
.421.29
,439.50
,457.70
,473.87
.490.05
,506.22
,522.40
.538.57
,552.37
,566.18
.579.98
,593.78
,607.58
,623.10
,638.61
.654.13
.41 1,669.64
.29 1,685.16
Sara 9
(tons)
2.362.78
2.402.73
2.442.68
2,482.63
2.522.58
2.562.53
2,596.66
2.630.79
2,664.92
2.699.06
2.733.19
2.763.52
2.793.84
2.824.17
2,854.50
2,884.82
2,910.70
2.936.58
2.962.46
2.988.34
3,014.22
3,043.31
3,072.40
3,101.49
3,130.58
3.159.67
Sara 11 Sara 12
(tons) (tons)
315.04 .260.15
320.36
325.69
331.02
336.34
341.67
346.22
350.77
355.32
359.87
364.43
368.47
372.51
376.56
380.60
384.64
388.09
391 .54
,281.46
,302.76
,324.07
.345.38
.366.68
,384.89
,403.09
,421.29
,439.50
,457.70
,473.87
,490.05
,506.22
.522.40
.538.57
,552.37
.566.18
394.99 i;579.98
398.44 1,593.78
401.90 1.607.58
405.77 ,623.10
409.65 .638.61
413.53 ,654.13
417.41 ,669.64
421.29 ,685.16
Sara 15
(tons)
2,362.78
2,402.73
2,442.68
2,482.63
2,522.58
2.562.53
2.596.66
2.630.79
2,664.92
2,699.06
2,733.19
2,763.52
2,793.84
2,824.17
2,854.50
2,884.82
2.910.70
2.936.58
2,962.46
2,988.34
3,014.22
3,043.31
3,072.40
3.101.49
3,130.58
3,159.67
-------
IDAHO
Waste * Container
Residue
Upper Sara 2
POPULATION (tons) (tons)
VCAD > > < »
I CnK
1985
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
,035,740
,053,252
,070,764
,088.276
,105,788
,123,300
,138,262
.153.224
,168,186
,183.148
.198,110
,211,404
,224,698
,237,992
,251.286
,264,580
.275,924
2002 1,287.268
2003 1.298,612
2004 1,309,956
2005 1,321,300
2006 ,334,052
2007 .346.804
2008 ,359.556
2009 .372.308
2010 .385.060
13,232
13,455
13,679
13,903
14,126
14,350
14,541
14.732
14,924
15,115
15.306
15,476
15,646
15,815
15,985
16,155
16,300
16,445
16,590
16,735
16,880
17.043
17,205
17,368
17.531
17.694
441.05
448.51
455.97
463.42
470.88
478.34
484.71
491.08
497.45
503.82
510.20
515.86
521.52
527.18
532.84
538.50
543.33
548.16
552.99
557.82
562.65
568.08
573.51
578.94
584.37
589.80
Sara 3
(tons)
1
1
f
1
r
i
t
i,
1,
2,
2,
2,
2,
2,
2,
2,
2,
2,
2,
2,
2,
2,
2,
2,
2,
2,
764.21
794.04
823.87
853.70
883.53
913.35
938.84
964.32
989.81
015.30
040.78
063.42
086.07
108.71
131.36
154.00
173.32
192.65
211.97
231.29
250.61
272.34
294.06
315.78
337.50
359.22
Sara 4
(tons)
441 .05
448.51
455.97
463.42
470.88
478.34
484.71
491 .08
497.45
503.82
510.20
515.86
521.52
527.18
532.84
538.50
543.33
548.16
552.99
557.82
562.65
568.08
573.51
578.94
584.37
589.80
Sara 5
(tons)
1,764.21
1.794.04
1,823.87
1 ,853.70
1,883.53
1.913.35
1.938.84
1.964.32
1.989.81
2.015.30
2,040.78
2,063.42
2.086.07
2,108.71
2,131.36
2,154.00
2,173.32
2,192.65
2,211.97
2,231.29
2,250.61
2,272.34
2,294.06
2,315.78
2,337.50
2,359.22
Sara 9
(tons)
3,307.89
3,363.82
3,419.75
3,475.68
3,531.61
3,587.54
3,635.32
3,683.11
3,730.89
3,778.68
3,826.46
3,868.92
3,911.38
3.953.84
3,996.29
4,038.75
4,074.98
4,111.21
4,147.44
4,183.67
4,219.90
4,260.63
4,301.36
4,342.08
4.382.81
4,423.54
Sara 11
(tons)
441.05
448.51
455.97
463.42
470.88
478.34
484.71
491.08
497.45
503.82
510.20
515.86
521.52
527.18
532.84
538.50
543.33
548.16
552.99
557.82
562.65
568.08
573.51
578.94
584.37
589.80
Sara 12
(tons)
,764.21
,794.04
,823.87
.853.70
.883.53
,913.35
.938.84
.964.32
,989.81
2,015.30
2.040.78
2.063.42
2.086.07
2.108.71
2,131.36
2.154.00
2,173.32
2,192.65
2.211.97
2,231.29
2,250.61
2,272.34
2,294.06
2.315.78
2.337.50
2,359.22
Sara 15
(tons)
3.307.89
3.363.82
3,419.75
3,475.68
3.531.61
3,587.54
3,635.32
3,683.11
3.730.89
3.778.68
3,826.46
3,868.92
3.911.38
3,953.84
3,996.29
4,038.75
4,074.98
4,111.21
4,147.44
4,183.67
4,219.90
4,260.63
4,301.36
4,342.08
4,382.81
4,423.54
-------
OREGON
VC AD
YEAR
1985
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
POPULATION
2.675.800
2,661.500
2,690,000
2,717,450
2,743,324
2,768,682
2,793,609
2,817,968
2,841,672
2.864,720
2.887.178
2.909,153
2,930,672
2,951,838
2,972,682
2,993,264
3,013,685
3,034,037
3.054,412
3.074.747
3.094,977
3.115.207
3.135.437
3.155,667
3,175,897
3,196,127
Household
Hazardous Waste
Lower Sara 2
(tons) (tons)
3,663
3,643
3.682
3,720
3.755
3.790
3,824
3.857
3,890
3.921
3,952
3.982
4,011
4.040
4,069
4,097
4,125
4,153
4,181
4.209
4.236
4.264
4,292
4,319
4,347
4,375
122.08
121.43
122.73
123.98
125.16
126.32
127.46
128.57
129.65
130.70
131.73
132.73
133.71
_ 134.68
135.63
136.57
137.50
138.43
139.36
140.29
141.21
142.13
143.05
143.98
144.90
145.82
Sara 3
(tons)
488.33
485.72
490.93
495.93
500.66
505.28
509.83
514.28
518.61
522.81
526.91
530.92
534.85
538.71
542.51
546.27
550.00
553.71 '
557.43
561.14
564.83
568.53
572.22
575.91
579.60
583.29
Sara 4
(tons)
122.08
121 .43
122.73
123.98
125.16
126.32
127.46
128.57
129.65
130.70
131.73
132.73
133.71
134.68
135.63
136.57
137.50
138.43
139.36
140.29
141.21
142.13
143.05
143.98
144.90
145.82
Sara 5 Sara 9
(tons) (tons)
488.33 915.63
485.72 910.73
490.93 920.48
495.93 929.88
500.66 938.73
505.28 947.41
509.83 955.94
514.28 964.27
518.61 972.38
522.81 980.27
526.91 987.96
530.92 995.48
534.85
538.71
542.51
546.27
550.00
553.71
557.43
561.14
564.83
568.53
572.22
575.91
579.60
583.29
.002.84
,010.08
.017.21
,024.26
,031 .25
,038.21
,045.18
.052.14
,059.06
.065.98
.072.91
,079.83
,086.75
,093.67
Sara 11
(tons)
122.08
121.43
122.73
123.98
125.16
126.32
127.46
128.57
129.65
130.70
131.73
132.73
133.71
134.68
135.63
136.57
137.50
138.43
139.36
140.29
141.21
142.13
143.05
143.98
144.90
145.82
Sara 12 Sara 15
(tons) (tons)
488.33 915.63
485.72 910.73
490.93 920.48
495.93 929.88
500.66 938.73
505.28 947.41
509.83 955.94
514.28 964.27
518.61 972.38
522.81 980.27
526.91 987.96
530.92 995.48
534.85
538.71
542.51
546.27
550.00
553.71
557.43
561.14
564.83
568.53
572.22
575.91
579.60
583.29
,002.84
,010.08
,017.21
,024.26
,031.25
,038.21
.045.18
.052.14
.059.06
.065.98
.072.91
,079.83
,086.75
,093.67
-------
OREGON
VC AD
TEAK
1985
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
POPULATION
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
3
3
3
3
3
3
3
3
3
3
,675,800
,661,500
.690.000
.717.450
,743,324
.768,682
,793,609
,817,968
.841.672
.864.720
.887,178
,909,153
,930,672
,951,838
.972.682
.993.264
,013,685
,034,037
,054,412
,074,747
.094.977
,115.207
.135,437
,155,667
,175,897
,196.127
Household Waste * Container
Hazardous Waste Residue
Upper Sara 2 Sara 3 Sara 4 Sara 5 Sara 9
(tons) (tons) (tons) (tons) (tons) (tons)
6.837
6,800
6.873
6.943
7,009
7,074
7,138
7,200
7,260
7,319
7,377
7,433
7,488
7,542
7.595
7,648
7,700
7.752
7,804
7,856
7.908
7.959
8.011
8,063
8,114
8,166
227.89 911.56
226.67 906.68
229.10 916.39
231.44 925.74
233.64 934.56
235.80 943.20
237.92 951.69
240.00 959.99
242.02 968.06
243.98 975.91
245.89 983.57
247.76 991.05
249.60 998.38
251 .40
253.17
254.93
256.67
258.40
260.13
261 .87
263.59
265.31
267.03
268.76
270.48
272.20
,005.59
,012.69
.019.71
,026.66
,033.60
,040.54
,047.46
.054.36
.061.25
.068.14
,075.03
,081.92
,088.81
227.89 911.56
226.67 906.68
229.10 916.39
231.44 925.74
233.64 934.56
235.80 943.20
237.92 951.69
240.00 959.99
242.02 968.06
243.98 975.91
245.89 983.57
247.76 991.05
249.60 998.38
251.40
253.17
254.93
256.67
258.40
260.13
261.87
263.59
265.31
267.03
268.76
270.48
272.20
.005.59
,012.69
,019.71
,026.66
.033.60
.040.54
.047.46
.054.36
.061.25
,709.17
,700.03
.718.24
,735.77
,752.30
,768.50
,784.42
,799.98
,815.12
,829.84
,844.18
,858.22
,871.97
.885.49
,898.80
,911.95
,924.99
.937.99
,951.01
,963.99
.976.92
.989.84
.068.14 2.002.76
.075.03 2,015.68
,081.92 2,028.60
,088.81 2.041.53
Sara 11
(tons)
227.89
226.67
229.10
231.44
233.64
235.80
237.92
240.00
242.02
243.98
245.89
247.76
249.60
251.40
253.17
254.93
256.67
258.40
260.13
261.87
263.59
265.31
267.03
268.76
270.48
272.20
Sara 12 Sara 15
(tons) (tons)
911.56
906.68
916.39
925.74
934.56
943.20
951 .69
959.99
968.06
975.91
983.57
991.05
998.38
1,005.59
1,012.69
1,019.71
1,026.66
1,033.60
1,040.54
1,047.46
1,054.36
1.061.25
,709.17
,700.03
.718.24
,735.77
,752.30
,768.50
,784.42
,799.98
,815.12
,829.84
,844.18
,858.22
,871 .97
,885.49
,898.80
,911.95
.924.99
.937.99
,951.01
,963.99
.976.92
.989.84
1,068.14 2.002.76
1,075.03 2,015.68
1.081.92 2.028.60
1.088.81 2,041.53
-------
OREGON
YEAR
Waste + Container
Residue
Lower Sara 2 Sara 3 Sara 4 Sara 5 Sara 9 Sara 11 Sara 12 Sara 15
POPULATION (tons) (tons) (tons) (tons) (tons) (tons) (tons) (tons) (tons)
1985 2.675,800 24.417
1986 2.661,500 24,286
1987 2.690.000 24,546
1988 2.717,450 24,797
1989 2,743,324 25.033
1990 2,768,682 25,264
1991 2,793,609 25,492
1992 2,817,968 25,714
1993 2,841,672 25,930
1994 2.864.720 26,141
1995 2.887.178 26.345
1996 2,909.153 26.546
1997 2,930,672 26,742
1998 2,951,838 26,936
1999 2,972,682 27,126
2000 2.993.264 27,314
2001 3,013.685 27,500
2002 3,034,037 27,686
2003 3.054.412 27.872
2004 3,074.747 28.057
2005 3,094,977 28,242
2006 3,115,207 28,426
2007 3,135,437 28,611
2008 3,155,667 28,795
2009 3,175,897 28,980
2010 3,196,127 29,165
813.89 3,255.56
809.54 3,238.16
818.21 3,272.83
826.56 3,306.23
834.43 3.337.71
842.14 3,368.56
849.72 3,398.89
857.13 3,428.53
864.34 3,457.37
871.35 3,485.41
878.18 3,512.73
884.87 3,539.47
891.41 3,565.65
897.85 3,591.40
904.19 3,616.76
910.45 3,641.80
916.66 3,666.65
922.85 3,691.41
929.05 3,716.20
935.24 3,740.94
941.39 3,765.56
947.54 3,790.17
953.70 3,814.78
959.85 3,839.39
966.00 3,864.01
972.16 3,888.62
813.89 3.255.56 6,104.17
809.54 3,238.16 6,071.55
818.21 3,272.83 6.136.56
826.56 3,306.23 6,199.18
834.43 3,337.71 6,258.21
842.14 3,368.56 6,316.06
849.72 3,398.89 6,372.92
857.13 3.428.53 6,428.49
864.34 3,457.37 6,482.56
871.35 3,485.41 6,535.14
878.18 3,512.73 6,586.37
884.87 3,539.47 6.636.51
891.41 3,565.65 6,685.60
897.85 3.591.40 6,733.88
904.19 3,616.76 6,781.43
910.45 3,641.80 6,828.38
916.66 3,666.65 6,874.97
922.85 3,691.41 6,921.40
929.05 3,716.20 6,967.88
935.24 3.740.94 7.014.27
941.39 3,765.56 7,060.42
947.54 3,790.17 7.106.57
953.70 3.814.78 7,152.72
959.85 3.839.39 7.198.87
966.00 3.864.01 7,245.02
972.16 3,888.62 7,291.16
813.89 3.255.56 6,104.17
809.54 3,238.16 6,071.55
818.21 3,272.83 6,136.56
826.56 3,306.23 6.199.18
834.43 3.337.71 6.258.21
842.14 3,368.56 6.316.06
849.72 3,398.89 6,372.92
857.13 3,428.53 6,428.49
864.34 3,457.37 6.482.56
871.35 3,485.41 6.535.14
878.18 3.512.73 6.586.37
884.87 3.539.47 6.636.51
891.41 3,565.65 6,685.60
897.85 3,591.40 6,733.88
904.19 3,616.76 6,781.43
910.45 3,641.80 6,828.38
916.66 3,666.65 6,874.97
922.85 3,691.41 6,921.40
929.05 3,716.20 6.967.88
935.24 3.740.94 7.014.27
941.39 3.765.56 7.060.42
947.54 3,790.17 7,106.57
953.70 3,814.78 7,152.72
959.85 3,839.39 7,198.87
966.00 3,864.01 7,245.02
972.16 3,888.62 7,291.16
-------
OREGON
YEAR
1985
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
Waste + Container
Residue
Upper Sara 2
POPULATION (tons) (tons)
2,675,800
2.661.500
2.690,000
2.717,450
2,743,324
2.768,682
2,793.609
2,817.968
2.841.672
2.864.720
2.887,178
2.909,153
2,930,672
2.951.838
2,972,682
2,993,264
3,013,685
3,034,037
3,054,412
3,074,747
3.094,977
3.115.207
3,135,437
3,155,667
3.175,897
3,196,127
34,
34.
34.
34.
35.
35.
35.
36.
36.
36.
36,
37.
37.
37.
37.
38,
38,
38,
39.
39.
39.
39.
40.
40,
40.
«0.
183
001
365
715
046
370
688
000
302
597
884
164
439
,139.44
,133.36
.145.49
.157.18
.168.20
.179.00
,189.61
,199.98
,210.08
,219.89
,229.46
,238.81
,247.98
710 1.256.99
976 1,265.87
239 1.274.63
500 1,283.33
760 1,291.99
020 1,300.67
280 1,309.33
538 1,317.94
797 1.326.56
055 1,335.17
314 1,343.79
572 1,352.40
831 1,361.02
Sara 3
(tons)
4,557.78
4,533.42
4,581.97
4.628.72
4.672.80
4,715.99
4.758.45
4,799.94
4,840.31
4.879.57
4.917.83
4,955.26
4,991.91
5,027.96
5,063.47
5,098.53
5,133.31
5,167.98
5.202.68
5,237.32
5,271.78
5,306.24
5,340.69
5,375.15
5,409.61
5,444.07
Sara 4
(tons)
1.139.44
1.133.36
1,145.49
1.157.18
1.168.20
1.179.00
1,189.61
1,199.98
1.210.08
1,219.89
1.229.46
1,238.81
1.247.98
1,256.99
1,265.87
1,274.63
1.283.33
1,291.99
1,300.67
1,309.33
1,317.94
1,326.56
1,335.17
1,343.79
1,352.40
1,361.02
Sara 5
(tons)
4.557.78
4.533.42
4.581.97
4.628.72
4.672.80
4.715.99
4.758.45
4,799.94
4,840.31
4,879.57
4,917.83
4,955.26
4.991.91
5.027.96
5.063.47
5,098.53
5.133.31
5,167.98
5,202.68
5.237.32
5.271.78
5.306.24
5.340.69
5,375.15
5,409.61
5,444.07
Sara 9
(tons)
8,545.84
8,500.17
8,591.19
8,678.86
8,761.49
8,842.48
8,922.09
8,999.89
9,075.59
9,149.20
9,220.92
9,291.11
9,359.83
9,427.43
9,494.00
9,559.74
9,624.96
9,689.96
9,755.03
9.819.97
9,884.58
9,949.19
10,013.80
10,078.41
10,143.02
10,207.63
Sara 11
(tons)
1,139.44
1,133.36
1,145.49
1.157.18
1,168.20
1.179.00
1,189.61
1.199.98
1.210.08
1,219.89
1,229.46
1,238.81
1,247.98
1.256.99
1,265.87
1,274.63
1,283.33
1,291.99
1,300.67
1,309.33
1,317.94
1,326.56
1,335.17
1,343.79
1,352.40
1,361.02
Sara 12
(tons)
4,557.78
4,533.42
4,581.97
4,628.72
4,672.80
4,715.99
4,758.45
4,799.94
4,840.31
4,879.57
4,917.83
4,955.26
4.991.91
5,027.96
5.063.47
5,098.53
5,133.31
5,167.98
5,202.68
5,237.32
5,271.78
5,306.24
5,340.69
5,375.15
5,409.61
5,444.07
Sara 15
(tons)
8,545.84
8,500.17
8.591.19
8,678.86
8,761.49
8,842.48
8.922.09
8.999.89
9.075.59
9,149.20
9,220.92
9,291.11
9,359.83
9,427.43
9,494.00
9,559.74
9,624.96
9,689.96
9,755.03
9,819.97
9,884.58
9,949.19
10,013.80
10,078.41
10,143.02
10,207.63
-------
WASHINGTON
VC AD
TEAK
1985
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
POPULATION
4.603,538
4.659.537
4.716.638
4.777.563
4.838.514
4,899,389
4,960.319
5,021.457
5,082,891
5,144,720
5,206,990
5,268,819
5,330,880
5,393.441
5,455.825
5,518.711
5.581,647
5,645,280
5,709,713
5,775,031
5,841,299
5.908.437
Household
Hazardous Waste
Lower Sara 2
(tons) (tons)
0
0
0
0
6.301
6,378
6,456
6.539
6.623
6,706
6,789
6,873
6,957
7,042
7,127
7,212
7,297
7,382
7,468
7,554
7,640
7,727
7,815
7,905
7.995
8,087
0.00
0.00
0.00
0.00
210.04
212.59
215.20
217.98
220.76
223.53
226.31
229.10
231.91
234.73
237.57
240.39
243.22
246.08
248.92
251.79
254.66
257.57
260.51
263.49
266.51
269.57
Sara 3
(tons)
0.00
0.00
0.00
0.00
840.15
850.37
860.79
871.91
883.03
894.14
905.26
916.42
927.63
938.91
950.28
961.56
972.89
984.30
995.69
,007.16
,018.65
,030.26
.042.02
.053.94
,066.04
,078.29
Sara 4
(tons)
0.00
0.00
0.00
0.00
210.04
212.59
215.20
217.98
220.76
223.53
226.31
229.10
231.91
234.73
237.57
240.39
243.22
246.08
248.92
251.79
254.66
257.57
260.51
263.49
266.51
269.57
Sara 5 Sara 9
(tons) (tons)
0.00 0.00
0.00 0.00
0.00 0.00
0.00 0.00
840.15
850.37
860.79
871.91
883.03
894.14
905.26
916.42
927.63
938.91
950.28
961.56
972.89
984.30
AAC XA
yyp.ov
,007.16
.018.65
,030.26
,042.02
,053.94
.066.04
.575.27
,594.44
,613.97
.634.82
,655.68
,676.51
,697.36
,718.28
.739.30
,760.46
,781.77
,802.92
,824.16
,845.57
.866.92
,888.43
,909.97
,931.74
,953.79
.976.14
,998.82
1.078.29 2,021.79
Sara 11
(tons)
0.00
0.00
0.00
0.00
210.04
212.59
215.20
217.98
220.76
223.53
226.31
229.10
231 .91
234.73
237.57
240.39
243.22
246.08
248.92
251.79
254.66
257.57
260.51
263.49
266.51
269.57
Sara 12 Sara 15
(tons) (tons)
0.00 0.00
0.00 0.00
0.00 0.00
0.00 0.00
840.15
850.37
860.79
871.91
883.03
894.14
905.26
916.42
927.63
938.91
950.28
961.56
972.89
984.30
995.69
,007.16
,018.65
,030.26
,575.27
,594.44
,613.97
.634.82
,655.68
.676.51
,697.36
,718.28
,739.30
,760.46
,781.77
,802.92
,824.16
,845.57
,866.92
,888.43
,909.97
.931.74
,042.02 1,953.79
,053.94 1,976.14
,066.04 1,998.82
.078.29 2,021.79
-------
WASHINGTON
YEAR
1985
1986
1987
1988
1989
1990
1991
1992
1993
1994
1995
1996
1997
1998
1999
2000
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
POPULATION
4,603,538
4,659,537
4,716,638
4,777.563
4,838,514
4,899.389
4,960,319
5,021,457
5,082,891
5,144,720
5,206,990
5,268,819
5,330.880
5,393.441
5,455.825
5,518,711
5,581,647
5,645,280
5,709,713
5,775,031
5,841,299
5,908,437
Household Waste + Container
Hazardous Waste Residue
Upper Sara 2 Sara 3 Sara 4 Sara 5
(tons) (tons) (tons) (tons) (tons)
0
0
0
0
11,762
11,905
12,051
12,207
12,362
12,518
12,674
12,830
12,987
13,145
13,304
13,462
13,620
13,780
13,940
14,100
14,261
14,424
14,588
14,755
14,925
15.096
0.
0.
0.
0.
392.
396.
401.
406.
412.
417.
422.
427.
432.
438.
443.
448.
454.
459.
464.
470.
475.
480.
486.
491.
497.
503.
00 0.00
00 0.00
00 0.00
00 0.00
07
84
70
89
08
26
45
66
89
16
46
73
01
34
65
01
37
79
28
84
48
,568.27
.587.35
,606.80
.627.56
,648.32
,669.06
.689.82
.710.64
,731.57
,752.63
,773.85
.794.91
.816.05
.837.37
.858.62
.880.04
.901.48
.923.16
.945.11
,967.36
.989.94
20 2,012.81
0.00 0.00
0.00 0.00
0.00 0.00
0.00 0.00
392.07 1,568.27
396.84 1,587.35
401.70 1,606.80
406.89 1.627.56
412.08 1.648.32
417.26 1,669.06
422.45 1,689.82
427.66 1,710.64
432.89 1,731.57
438.16
443.46
448.73
454.01
459.34
464.65
470.01
475.37
480.79
486.28
491.84
497.48
,752.63
,773.85
,794.91
,816.05
,837.37
,858.62
,880.04
,901.48
,923.16
,945.11
,967.36
,989.94
503.20 2,012.81
Sara 9
(tons)
0.00
0.00
0.00
0.00
2,940.51
2,976.28
3,012.75
3.051.67
3,090.60
3,129.48
3,168.40
3,207.46
3,246.70
3,286.19
3,325.96
3,365.46
3,405.10
3,445.06
3,484.91
3,525.08
3,565.28
3,605.92
3,647.08
3,688.80
3,731.13
3,774.01
Sara 11 Sara*12
(tons) (tons)
0.00 0.00
0.00 0.00
0.00 0.00
0.00 0.00
392.07 1,568.27
396.84 1,587.35
401.70
406.89
412.08
417.26
422.45
427.66
432.89
438.16
443.46
448.73
454.01
459.34
464.65
470.01
475.37
480.79
486.28
,606.80
,627.56
,648.32
,669.06
,689.82
,710.64
,731.57
,752.63
,773.85
,794.91
,816.05
,837.37
,858.62
,880.04
,901.48
,923.16
.945.11
491.84 1,967.36
497.48 1,989.94
503.20 2.012.81
Sara 15
(tons)
0.00
0.00
0.00
0.00
2,940.51
2,976.28
3,012.75
3,051.67
3,090.60
3.129.48
3,168.40
3,207.46
3,246.70
3,286.19
3,325.96
3,365.46
3.405.10
3,445.06
3,484.91
3,525.08
3,565.28
3,605.92
3,647.08
3,688.80
3,731.13
3,774.01
------- |