AP-42 Section Number:    1.8
Reference Number;
Title:
34
Source Test Report for Particulate
Emissions Boilers 3 and 4: Atlantic
Sugar Association
                        November
             1991

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        SOURCE TEST REPORT
               for
       PARTICIPATE EMISSIONS
         BOILERS 3 AND 4
    ATLANTIC SUGAR ASSOCIATION
      BELLEGLADE. FLORIDA
       NOVEMBER 20 & 21. 1991
            Prepared for:

        KLEEMAN ENGINEERING
        4300 NW 44TH STREET
   FT. LAUDERDALE, FLORIDA  33319
            Prepared by:

AIR CONSULTING AND ENGINEERING. INC.
    2106 N.W. 67TH PLACE. SUITE 4
    GAINESVILLE, FLORIDA 32606
          (904) 335-1889
            287-91-08

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                                TABLE OF CONTENTS
SECTION
1 .0
2.0
3 -0
4 .0
5.0
5.1


PROCESS DESCRIPTION AND OPERATION 	 	 	

FIELD AND ANALYTICAL PROCEDURES 	 	 ,
P ARTICULATE MATTER SAMPLING & ANALYSIS — EPA METHOD 5 ... 	
. . . . 1
. . . . 2
. . . . S
. . . . 6
. . . . 8
	 8
APPENDICES
        APPENDIX A—COMPLETE EMISSION DATA
                      AND  SAMPLE CALCULATIONS

        APPENDIX B—FIELD  DATA SHEETS

        APPENDIX C—LABORATORY ANALYSIS

        APPENDIX D—PRODUCTION RATE CERTIFICATION

        APPENDIX E—QUALITY ASSURANCE
                      AND  CHAIN OF CUSTODY

        APPENDIX F—PROJECT PARTICIPANTS

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                                LIST OF TABLES






TABLE                                                           PAGE




  1       EMISSION SUMMARY—BOILER 3	   3




  2       EMISSION SOMMARY—BOILER 4			   4









                                LIST OF FIGURES







FIGURE                                                          PAGE




  J       SAMPLING POINT LOCATION—BOILERS 3 AND 4	   7




  2       EPA METHOD 5 SAMPLING TRAIN	   5
                                      II

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                    7
    AIR CONSULTING
  & ENGINEERING, INC.
                        2106N.W. 67th Place • Suite 4 • Gainesville, Florida • 32606
                       	1              (904) 335-1889  FAX (904) 335-1891
                                REPORT CERTIFICATION
  To the best of my knowledge, all applicable field and analytical
procedures comply with Florida Department of Environmental Regulation
requirements and all test data and plant operating data are true and correct.
                                    /*£
                              Da'gmlf/Neck
                               Date

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1.0 INTRODUCTION

On November 20 and 21, 1991, Air Consulting and Engineering, Inc. (ACE),
conducted paniculate emission testing on the Wet Scrubber Outlet of Boilers 3
and 4 at Atlantic Sugar Association in Belleglade, Florida.

Testing was performed to demonstrate compliance with the current Florida
Department of Environmental Regulation (FDER) operating permit.

United States Environmental Protection Agency  (EPA) Method 5 was utilized for
the emission testing.

Mr. Ken Tucker of the FDER observed a portion of the testing.

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2.0 SUMMARY AND DISCUSSION OF RESULTS

Boilers 3 and 4 demonstrated compliance with the permit conditions.

Tables 1 and 2 are summaries of the emission results and flue gas parameters.

Paniculate emissions averaged 49.90 pounds per hour (fbs/Hr) and 0.216 pounds
per million BTU (Ibs/MMBTU) and  49.83 Ibs/hr and 0.213 .Ibs/MMBTU for Boilers 3
and 4, respectively.

Allowable emissions are 69.56 Ibs/Hr and 0.300 Ibs/MMBTU for Boiler 3 and
67.86 Ibs/hr and 0.290 fbs/MMBTU for Boiler 4. No oil was used during
compliance testing.

Complete emission summaries, field data sheets and laboratory data are
presented in Appendices A, B, and C, respectively.

Production rate summaries are provided  in Appendix D.  This data was obtained
from control room recordings of  steam flow, temperature, and pressure as
well as feed water temperature and pressure.  Residue integrator and  oil meter
readings were recorded at the beginning and end of each paniculate run by Mr.
Frank Kleeman of Kleeman Engineering.

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Table 1   Ernieaion Summary
          Boiler 3
          Atlantic Sugar Association
          Balleglade, Florida
          November 20, 1991
Number
1
2
3
AVERAGE
SCFMD
66683
68650
67748
67694
Temp.
164
157
162
161
Moisture
26.
27.
29.
27.
9
3
0
7
Iba/Hr
47.
54.
47.
49.
29
17
84
90
Iba/MMBTU
0.
0.
0.
0.
206
240
202
216
Iba/Hr
69
68
71
69
.01
.57
.10
.56
Iba/MMBTU
0.300
0.300
0.300
0.300

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Table 2   Emission Summary
          Boiler 4
          Atlantic Sugar Association
          BellegLade, Florida
          November 21, 1991
Run
Number
1
2
3
AVERAGE
Flow Rate
SCFMD
68285
67603
68053
67980
Stack
Temp.
Of
172
174
175
174
Stack
Moisture
%
26.7
28.8
2S.6
28.0
Partlgulate
Iba/Hr
45.28
49.80
54.42
49.83
Emissions
Ibe/MMBTO
0.200
0.218
0.221
0.213
allowable
Iba/Hr
65.77
66.31
11.50
67.86
Emissions
Ibe/HMBTU
0.290
0.290
0.290
0.290

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3.0 PROCESS DESCRIPTION AND OPERATION

Boilers 3 and 4 at Atlantic Sugar Association are spreader stoker design used
primarily for residue fuel firing.  Supplemental oil firing may also be
utilized but was not used during the emission test series.

Boilers 3 and 4 averaged 117,300 and 118,367 pounds per hour {Ibs/Hr} steam
production over the three test run period (see Appendix D for production
data).

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4.0 SAMPLING POINT LOCATION

The sampling point location consists of a scrubber outlet stack 71.5" in
diameter.  The stack has two sample ports 90 digrees apart.  The ports were
located 405" from an upstream disturbance and 150" from the outlet.
       i
Twenty test points were sampled for each test run.  The traverse points were
located as shown in Figure 1,  The stack configuration is such that there Is
no reason to evaluate the presence of cyclonic flow.

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    71.5"
      0
Xl
            15°"
                                TSAVESSS Fain

                                !   IUMBE1
            450"
s\
1

2

3

4

5

6

7

8



10
        DISTANCE F5CH

        IIS I BE STACK

            WALL
                                                      1.8

                                                      5'8

                                                      10.5


                                                      «-2

                                                      24'4

                                                      «7-l

                                                      55.3


                                                      6I
Figure 1

Sampling Point Location
Boilers 3 and 4
Atlantic Sugar Association
Belleglade, Florida	
                               AIR  CONSULTING
                                        and
                                  ENGINEERING

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5.0 FIELD AND ANALYTICAL PROCEDURES

5.1 Paniculate Matter Sampling and Analysis--EPA Method 5 (Glass Probe)


Paniculate matter samples were collected by the paniculate matter emission

measurement method specified by the United States Environmental Protection

Agency.  A schematic diagram of the sampling train used is shown in Figure 2.

All participate matter captured from the nozzle  to,  and including, the filter

was included in the calculation of the emission rate of particulate matter,



PREPARATION OF EQUIPMENT

   1.  FILTERS - Gelman type "A"  filters were placed in a drying
       oven for two hours at 105 degrees C, removed and placed in
       a standard desiccator containing indicating silica gel, allowed
       to cool for two hours, and weighed to the  nearest 0,1 mg. The
       filters were then re-desiccated for a minimum of six hours and
       weighed to a constant weight (less than 0.5 mg change from
       previous weighing).  The average of the two constant weights
       was used  as the tare weight.

   2.  NOZZLE,  FILTER HOLDER, AND SAMPLING PROBE - The nozzle, filter
       holder, and sampling probe  were washed vigorously with soapy
       water and brushes, rinsed with distilled water and acetone, and
       dried prior to the test program. All openings on the sampling
       equipment were sealed while in transit  to the test site.

   3.  IMPINGERS - The Greenburg-Smith impingers were cleaned with a
       warm soapy water solution  and brushes, rinsed with distilled
       water and acetone, and  dried. The impingers were sealed tightly
       during transit.

TEST PROCEDURE

Prior to performing the actual particulate matter sample runs, certain stack

and stack gas parameters were measured. These  preliminary measurements

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• THERMOCOUPLE

      ORSAT PROBE
4        HEATED FILTER HOLDER


	          ~~
               HEATED PROBE

          RE VERSE-TYPE PITOT TUBE
                                                                           THERMOMETER
                  PITOT MANOMETER
                                                                       VACUUM LINE	j^
                ORIFICE
                          FLEXIBLE TEFLON TUBING
                   THERMOMETERS     BY- PAS S VALVE
                                                        tOO ML H2O
                                                            MAIN VALVE
         MANOMETER
                                                               «- SILICA GEL
                                                                VACUUM GAUGE
                            DRY TEST METER
                                   AIR-TIGHT PUMP
FIGURE 2

EPA METHOD 5 SAMPLING TRAIN
                                                               AIR  CONSULTING
                                                                         and
                                                                  ENGINEERING

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included the average gas temperature, the stack gas velocity head, the stack
gas moisture content, and the stack dimensions at the point where the tests
were being performed.  The stack gas temperature was determined by using a
bi-metallic thermocouple and calibrated pyrometer.  Velocity head measurements
were made with calibrated type "S" pilot tube and an inclined manometer.
Velocity head measurements of 0.05 inches H20 or less were measured utilizing
a micromanometer,                                     f

The sampling traverse points were selected so that  a representative sample
could be extracted from the gas stream.  The traverse points were located in
the center of equal areas, the number of which were dependent upon the
distance upstream and downstream from flow disturbances.

Each paniculate matter  test run consisted of sampling for a specific amount
of time at each traverse point. The type  "S" pitot tube was connected to the
sampling probe so that  an instantaneous velocity head measurement could be
made at each traverse point while making the test run. The stack gas
temperature was also measured at each traverse point. Nomographs were used to
calculate the isokinetic  sampling rate at each traverse point during each test
run.

The gases sampled passed  through the following components: a stainless steel
nozzle and glass probe; a glass fiber filter; two impingers each with 100 ml
                                        10

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of distilled deionized water; one impinger dry; one impinger with 200 grams of
silica gel; a flexible sample line; an air-tight pump; a dry test meter; and a
calibrated orifice.  The second impinger had a standard tip, while the first,
third, and fourth impingers had modified tips with a 0.5 inch I.D, opening.

Sample recovery was accomplished by the following procedures:
   1, The pre-tared filter was removed from its holder and placed in
      Container 1 and sealed, (This is usually performed in the lab.)
   2. All sample-exposed surfaces prior  to the filter were washed with
      acetone and placed in Container 2, sealed and the liquid level
      marked.
   3, The volume of water from the first three impinoers was measured
      for the purpose of calculating the  moisture in the stack gas and
      then discarded.
   4. The used silica gel from the fourth impinger was transferred to
      the original tared container and  sealed.

LABORATORY ANALYSIS
The three sample  containers from each sample run were analyzed according to
the following procedures;
   1. The filter was dried at 10i degrees C for three  hours,  desiccated
      for a minimum of one hour, and weighed to the nearest 0.1 mg. A
      minimum of two such weighings six hours apart was made to determine
      constant weight.
   2. The acetone from Container  2 was transferred to a tared  beaker and
      evaporated to dryness at ambient  temperature and pressure,
      desiccated for 24 hours, and weighed to the nearest 0.1  mg. A
      minimum of two such weighings six hours apart were made to determine
      constant weight.
   3. The used silica gel in its tared container was weighed to the nearest
      0,1  gram.
                                         11

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The total sample weight included the weight of material collected on the
filter plus the weight of material collected in the nozzle, sampling probe,
and front half of the filter holder.

DATA
The field data sheets, calculation sheets, and nomenclature definitions are
included in the appendices of this report.
                                           12

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       APPENDIX A
COMPLETE EMISSION DATA
         AND
 SAMPLE CALCULATIONS

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BOILER 3

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PLANT;
SOURCE:
DATE;

RUN NO.:
BEGIN TIME:
EMD TIME;
TOTAL RUN TIME;
BAROMETRIC PRESSURE;
STACK PRESSURE;
NOZZLE DIAMETER:
METER CDRft. FACTOR:
FINAL METER;
INITIAL  METER;
STACK AREA;
     PORT-POINl
AIR CONSULTING and ENGINEERING
    COMPLETE EMISSION DATA

ATLANTIC SUGAR ASSOCIATION
NUMBER 3 BOILER
11-20-91

         1                   IMP!
   0336                     SILI
   0939                     PERC
     60.00 ruin.             PERC
     30.20 "Hg              "F"
     30.20 "Hg.
      .225 inches           F'ARl
          -
         2-5
         2-6
         2-7
         2-8
         2-9
         2-10
          ERAGES
AVG. VELOCITY HEAD
AVG. STACK TEMP.:
AVG. METER TEMP.:
AVG. ORIFICE DIFFEF
HETER STANDARD CUB!
<7, H20 VAPOR:
GAS MOL. UIT. DRY;
GAS MOL. UT. WET;
1. EXCESS AIR;
AVG. STACK VEL.CFF-i
ilr.BTUH HEAT  INPUT;
PERCENT I30KINETIC
I . UU3
230.331 cubic
139.954 cubic
27.883 sq. ft
VELOCITY HEAD

1 . 1 50
1 . 1 50
1 , 1 SO
i . 1 00
1 . 1 00
1 .050
1 . 000
.320
. 730
. 600
. 950
1 .050
1 . 100
1 . 1 00
1 . 1 SO
1 . 1 50
! . ISO
i . 1 50
.920
.920


RUN
0.0002761
( ^ j. i-l
i 1 . Ui
_-,_-,-.-., 1 £ A
- — i b**
_ o 1

IMTIAL;— 1.66
: FEET; 	 40.322
1 -~I L «I|
1 4. •„' . 3

	 - _ .
-» 	 	 	 ' 2b.b3
~T i i ~
— / i . i b
	 63 . 32
____: :: :: : : ^ •_"'*-* • *- ' ^T
	 101 .77
£ J,
J I" ,
ft.

SQUARE RT.
VEL. HEAD
1 . 072
1 . 072
1 . 072
1 . 049
1 . 049
1 . 025
1 . 000
0 . 906
0 .854
0,775
0.975
1 . 025
i .049
1 . 049
1 .072
1 .072
1 .072
1 .072
0 . 959
0 , 959
1 .009
1

"H20
F
F
"H20








FILTER mg.
WASH rng .

ORIF.
OIFF.
1 .800
1 .800
1 - 800
1 . 700
I . 700
1 . 700
1 . 700
1 . 600
1 .300
1 .300
1 , 500
1 .700
1 . 700
1 .700
1 .300
1 .800
i .sou
1 . 300
1 . 500
1 .500
1 . 660


VOL. FLOW
VOL. FLOW

PARTICULAT


POUNDS PER
POUNDS PER
GRAINS/ SCF
GRAINS/ SCF
GRAINS /SCF
POUNDS PER
L^S/nMSTU"
2
9

STACK
TEMP .
1 65
175
172
173
163
163
1 63
161
159
'157
156
157
1 55
157
162
1 63
16S
168
1 65
165
164


ACFM ;
SCFMD ;

E DATA ;


HOUR;
SCF :

<5 B% 02
§50% EA
MMBTU :
F "FACTOR
07 . 0
.2

METER
TEMP.
77
76
76
77
"j "7
78
79
79
80
30
;•! 1
'If ~.'
O-ii.
83
O-J*
34
34
35
85
85
c" i


1 06767
66633




-17 . 294
0.00001 13
0 . 083
U . U9U
0. 094
0. 206
0 . "i 9 4.

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                    SAMPLE CALCULATIONS  -  RUN
NOZZLE AREA (FT. 2)
AVe. VELOCITY HEAD:
METER STND, FT3:

PERCENT H20;

Mw DRY:
Mw W
% EXCESS AIR;

STACK VEL.CFPS);

X ISOKINETIC:
 (Dn/12)!2x3, 14-16/4
 < AVG , SQ . RT . > ! 2
 ( Mf -M i ) xMCFx ( AVG , DRF . 0 1 FF . /
 1 3 , 6 ) ) /29 . 32 ) x( S28/ ( Tr»+4SO ) )
 < ( IMP+SG)x( ( C IMP+SG ):K , 0474) +
 SCF)x)00
 < ( 02%y, , 32 ) +C02%x . 44 )+ C 1 00-( 0251+C02
 )x, 23
 ( Mw  DRYx ( I -%H20/ 1 00 ) 3 +*H20x , 1 S
 X.0'2/ ( ( ( 1 00-C »02+»CD2) )x , 2&4)-«D2 ) t
 1 00
 85 . 43x . 84x ( AVS . SQ . RT , VEL , HD . ) x C ( Ts
     FLOW CACFM):
STND. FLQUKSCFMEj);

F'ARTICULATE LB/HR:

PARTICULATE LB/SCF)
GRAINS/SCF;
•3R/SCF (5 8% 02:
QR/SCF t SOX E.fi. ;
LB/MMBTU :
LB/MMETU "F" FACTOR
 C C Ts-HtEG ) xSCFx2992 J / C 52SxFPSxT I HEx
 An  xPs x SOx(]-%D2/100)
 FPS x 60 x As
 ACFMsi523/ ( Ts+460 )x( 1 -%H20/ 1 00 ):=<:
 (Ps/29.92)
 PROBE+FILTER wg./ 453600 x (SCFHD/
 SCF? x £0
; PROBE+FILTER B,g./453bOO /SCF
 LB/SCF x 7DDO
 U 2 . 3/ ( 20 - 9-%02) )x GR/SCF
 SR/SCF x < ( 1 00+ SiE . A . ) / 1 50 J
 ( LB/HR )/(LB/MMBTUH)
: LB/SCF x "F"  FACTOR x (20.9
 /20.9-SQ2)
0,000276
63. S2

40,322
71 . 16
1 01.77
IOS767

f.
47,294
0.000011S
0.0827
0,OS97
0.0'344
0.206

0. 194

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PLANT:
SOURCE;
DATE:
AIR CONSULTING and ENGINEERING
    COMPLETE EMISSION DATA

ATLANTIC: SUGAR ASSOCIATION
NUMBER 3 BOILER
11-20-9l
RUN NU.;
BEGIN TlhE;
END TIME:
TOTAL RUN TIME;
BAROMETRIC PRESSURE:
STACK PRESSURE;
NOZZLE DIAMETER:
METER CORK. FACTOR;
FINAL METER:
INITIAL METER:
STACK AREA;
     PORT-POINT
         2-4.
         2-10
AVG- VELOCITY HEAD
AVG. STACK TEMP.:
AVG. METER TEMP.:
AVG. ORIFICE DIFFEF
METER STANDARD CUB]
% H2D VAPOR;
GAS MOL. UT. DRY;
GAS MDL. UT. WET:
% EXCESS AIR;
AVG. STACK VEL.CFPS
,1r1BTUH hit AT  INPUT;
PERCENT ISCKINETIC
1 024
1 1 26
60-00 niin.
30.20 "Hg
30.20 "Hg.
.225 inches
If ~\ f~1 ' J
. UU J
271 .357 cubic ft.
230.574 cubic ft.
27.833 sq. ft.
VELOCITY HEAD SQUARE RT ,
VEL. HEAD
1 . 000 1 . 000
1 . 050 1 . 025
1 . 150 1 .072
1 . ! 50 ( . 072
1.150 1.072
1 . 1 50 1 . 072
1 . 1 50 1 . 072
1 . 1 00 1 . 049
1 . 000 1 . 000
1 . 000 1 . 000
1 . 1 50 1 , 072
1 . 1 50 i . 072
1 . 1 00 1 . 049
"t . 1 00 1 . 049
1 . 1 00 1 . 049
1 .100 1 .049
1 . 1 50 1 . 072
1 . 000 1 . 000
.940 0.970
.300 0.349
1C\ O * — *

RUN 2
0 . 0002761
t 1 ,-|.-( II U^'H
i 1 . Uo n.iU
1C ""* r
5/ F
	 _ o~7 C
	 — ,-jy )-
:NTIAL; — i .63 "H20
• CCCT ' jin ~~r~'C
• rtt 1 i uU . /Oo
i -~,~t •"'
•~'O j-i ,%
.ild . OU
•~C C'"'
i.O . 3O
"? 1 1 £
/I.I b
	 65.39
	 227.49
	 	 yq 07
SILICA GEL gnis, 9.3
PERCENT G2 9.0
PERCENT C02 3.0



"F" FACTOR 9366

P ARTICULATE
FILTER lag. 227
WASH mg . 16.

, DRIF. STACK
DIFF. TEMP.
1 . 600 1 54
1 . 700 1 55
1 .800 156
t . 800 1 So
i . 300 1 55
1 . 800 1 57
1 . 700 1 56
1 . 700 1 57
1 . 600 1 53
1 . 600 1 55
1 . 300 1 55
1 . 800 1 65
1 .700 164
1 . 700 1 65
1 .700 159
1 .700 157
1 .800 155
1 . 600 1 53
1 .500 155
1 - 450 1 56
1 . 693 1 57


VOL. FLOW ACFM :
j jr",| r— t i— 11 t i™"-/~«^Vir~f i
VOL . FLOU bCFMD ;
PARTICIPATE DATA :


POUNDS PER SCF ; 0,
GRAINS/SCF;
GRAINS/SCF (550% EA
POUNDS PER MMBTU:
LE:S/MMBTUr'F'' FACTOR


.9
9

METER
TEMP .
34
34
84
84
35
oc
• 36
86
C* /
87
S3
C'C-
83
88
39
90
90
90
90
31
37


1 09402
t.ob-30



•b4 . b/U
0000132
0 . 093
0 . i O I
0 . 1 Cb
(J , ^ il i J
n -~- " o

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                    SAMPLE CALCULATIONS:  -  RUN   2
N02ZLE AREA (FT. 2)  CDr./l 2) !2x3.1 41 6/4                            0.000276
AVG.VELQCITY HEAD:  (AVG.SQ.RT.)!2                                65.33
ilETER STND, FT3:    (Mf-Hi )xMCF;:<( AVG. ORF. DIFF. /
                    13,B))/23.32)x(S28/C Tm+460))                  40.736
PERCENT H20:         ((1HP+8G3xC((IMP+SGXx,0474) +
                    SCF)x100
Mw DRY;             (C02%x.22>+CQ2»x.44:> + nOQ-(02UCQ2           23.80
                    )x.28
Mw MET:             (1% DRYxCl-%H2Q/10Q)mH20x.l3               26 . S3 '
'1 EXCESS AIR:       mi/C C C100-(»02+%CQ2) )x.2643-»D2)*
                    100  ,                                         71.16
STACK VEL. (FF'S):    S5 .49x. 84.x(AVG. SQ, RT . VEL . HD. )x( ( Ts
                    +•460) / (PsxMwWET))! . 5                          bS. 39
% ISOKINETIC;       C(Ts+460)xS-CFx2992)/(528>-;FPSxTIMEx
                    An xPs x 60xC1-I02/100)                       93.87
VOL.  FLOW CACFM):   FF'S x SO x  As                                 109402
STND. FLDWiSCFMO; !  ACFMx528/CT5+460)x(l -5JH20/100)x
                    (Ps/25.923                                    S8650
PARTICIPATE LB/HR;  PRDBE+FILTER  iftg./4SS600  x (3CFMD/
                    SCF) x SO                                     54.570
PARTICULATE LB/SCF) IF'ROBE+FILTER  mg./453600  /SCF                  0.000013/
SRAINS/SCF:         LS/SCF x 7000                                 0-0527
QR/SCF $ 87* 02:     C12.9/(20.9-102) >x GR/SCF                    0.100&
SR/SCF 5 50% E.A.;  SR/SCF x ((100+  %E,A.)/1SO)                   0.1058
LB/MHBTU;           (LB/HR)/(LB/MHBTUH)                           0,240
LB/MilBTU "F"  FACTOR:LB/SCF x "F"  FACTOR x (20.9
                    /20.9-%Q2)                                    0.21S

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                         CDMPLctfc  EMISSION DATA
PLANT;
SOURCE;
DATE;

RUN to.:
BEGIN TIME;
END TIME:
TOTAL RUN TIME;
BAROMETRIC PRESSURE:
STACK PRESSURE;
.NOZZLE  DIAMETER:
METER CQRR- FACTOR;
FINAL METER:
INITIAL METER:
STACK AREA;
     FORT-POIN1
            ATLANTIC SUGAR ASSOCIATION
            NUMBER 3 BOILER
         1-6
         1-10
         2-9
         2-10
AVS, VELOCITY HEAD
AVG, STACK TEMP,:
AVS. METES TEMP,:
AVG, ORIFICE DIFFERS
METER STANDARD CUBIC
» H2Q VAPOR:
GAS MCL. WT. DRY;
SAS MDL, UT. MET;
% EXCESS AIR:
AVG .  STACK MEL .
•Zi
1225
1351
60.00 Nil TV
; 30.20 "Hg
30.20 "Hg.
,225 inches
" .^/NCf
i „ MV^1
313.511 cubic
272. 33S cubic
27.333 sq. ft
VELOCITY HEAD

1 . 1 00
1 . 200
1 . 200
i.20u
1 , 1 00
1 . 1 00
1 .200
1 . 100
1 . 000
.850
. 300
. 990
1 . 1 1>0
1 . 1 00
1 .100
1 . 200
1 . 300
1 . 1 00
1 . 1 00
1 . 1 00










f t .
ft.

SQUARE RT
VEL. HEAD
1 .049
I .035
1 .09S
1 . 09-5
1 .049
1 .049
1 .095
1 . 049
1 . 000
0.922
0,343
0 . 995
1 .049
1 .049
1 . 049
1 .095
1 . 1 40
1 . 049
i .049
1 . Ui9
1 , 049
IhKlNGER mi
SILICA 6EL gros.
PERCENT 02
PERCENT CD2
"F" FACTOR

PARTICULATE

FILTER mg.
UlASH mg .












. ORIF. STACK
DIFF. TEMP
] .760
1 . 920
1 .920
1 .920
I .760
1 . 760
1 .920
1 . 760
1 . 600
1 , 360
1 .440
1 . S80
} . 760
1 . 760
1 . 760
1 . 920
2 . 080
1 .760
1 .760
1 . 760
1 .763

158
1€1
1 63
165
163
1 65
16:
158
160
1 60
1 30
1 55
1 -55
165
167
1SB
168
163
170
168
162
340
3 . 0
8.5
3 . 0
3366



204 . 6
11.7

METER
TEMP .
37
87
37
37
37
36
36
86
87'
87
88
oo
89
39
39
30
90
50
90
90
83
RUN 3
0,0002761
; 	 1 . 1 0
™.™ BB.BB, ««!»—«» »«.— | fc^
:NTIAL: — i.~6
' , r ^ ' ' * ~'.-,q ' r-
* .^ „• . *J
	 , — . 29 78
s~t ^ _*.? _,
	 . C,l f~i1

"H2Q
c
"H2D




VOL. FLOW ACFM
VOL. FLDU SCFMD

*
-

11 1 353
67743
PARTICULATE DATA :
POUNDS PER HOUR
POUNDS PER SCF
GRAINS^SCF;
.
;

47.337
rt GoOO i ] ft
0 , 082
       CFPS)	
MflETUK
PERCEN
EA
             NPU

GRAINS/SCF 450% hA     0.090
POUNDS PER nhBTlj:      0.202
        Li "F" FACTOR     0.186

-------
 SAMPLE CALCULATIONS - RUN  3
NOZZLE AREA (FT,2)
AVS.VELOCITY HEAD;
METES STND. FT3:

PERCENT H2D;

M* DRV:


% EXCESS AIR:

STACK VEL. (FF'S):

% ISuKINETICl

VOL, FLOW (ACFM):
STND. FLQy(SCFMD):

PARTICIPATE LB/HR:

PARTICIPATE LB/SCF)
GRAINS/'SCF ;
GR/SCF S 33 02:
GR/SCF § 50% E.A,:
LB/MHBTU;
LB/MMBTU "F:I FACTOR
 (AvG.SQ.R'T, ) !2
 ( Mf -Hi ) xMCFx < AVS , ORF . DI FF . /
 1 3 , 6 ) ) / 23 , 32 ) x ( S2S / ( T w+460 )
 SCFJxlOO
 C ( Q2Sx . 32 ) -J-CD2XX . 44 ) -(- H 00- ( D22.+C02
 )x.2S
 ( Hw DRYxC 1 -%H20/ 1 00) ) -«-XH20x , 1 S
 X-D2/( ( < 1 00-( K02+XC02) )x .264>-%02>#
 1 00
 85 . 43x . S4x( AV6 , SQ , RT , VEL , HD , Jx( ( Ts
 4-460 > / ( PsxMwWET ) ) ' , 5
 C ( Ts+460)x£CFx2392)/ ( 528xFPSj
-------
BOILER 4

-------
PLANT;
SOURCE:
DATE :

RUN NO.;
BEGIN TIME;
END TIME;
TOTAL RUN TIME;
BAROMETRIC PRESSURE;
STACK PRESSURE;
NOZZLE DIAMETER;
METER CDRR. FACTOR;
FINAL METER:
INITIAL METER:
STACK AREA:
     PORT-POINT
         1-1
         -,  .^
         J ~~«i
         1-3
         1-4


         1-6
         1-7


         1-9
                    AIR CONSULTING and ENGINEERINS
                        COMPLETE EMISSION DATA

                    ATLANTIC SUGAR ASSOCIATION
                    NUMBER 4 BOILER
                    11-21-91
         •"/	C*

         2-y

         2-10
       AVERAGES

NOZZLE AREA (SQ.FT. J
AVG. VELOCITY HEAD
AVG - STACK TEMP . :
AVG. METES TEMP, :
AVG, ORIFICE DIFFEF
hETER STANDARD CUB3
% H20 VAPOR;
             DRY;
             WET:
GAS KOL. UT.
GAS MOL. UT.
% EXCESS AIR;
AVG -  STACK: VEL , ( FP
rfMBTUH HEAT INPUT;
PERCENT ISOKINETIC
0938
60.00 tain.
30. 13 "Hg
30. 18 "Hg.
.225 inches
1 , 003
354,077 cubic
313,701 cubic
27.S89 sq. ft
VELOCITY HEAD

.950
1 . 1 00
] .100
1 . lOn
1 .200
1 . 200
1 . 1 00
1 . 1 00
1 . 1 00
. 380
1 ,200
1 . 400
1 .300
1 . 200
1 . 1 00
1 . 1 00
, 950
, 320
, 830
. 870


RUN
0.0002761
i ] r,r
. — I . uc
7f-f
—
	 73
NT1AL ! 	 1 .73
• ctrpT * Aft A1 4
r CC 1 * **v . 3 1 **
' ""'.*" "7
J ^W . '
i~,,~. S'i£L
*-? . u'C
	 w«, 	 Vh, t £,y
— 	 * — — — l^^ ^ y v
	 S6 12
	 226,72
	 '(10 0£






ft.
ft.

SQUARE RT
VEL. HEAD
0 , 975
1 . 043
1 .043
i .049
1 . 095
1 . 035
I .043
1 .049
i . 049
0 . 330
1 -095
I , 1 83
i . 1 40
1 ,095
1 .043
1 .049
0 . 975
0 . 306
0,311
0 . 933
1 . 033
1

"H20
C"
F
"H20








PERCENT 02
PERCENT C02
"F" FACTOR-

PART I CULATE


FILTER mg.
UASH tftg .

ORIF. STACK
DIFF. TEMP.
1 . 520 1
1 . 760 1
1 . 760 i
1 . 760 1
1 . 320 "1
1 ,320 1
1 . 760 "i
1 .760 1
1 .760 1
i . S70 1
I .920 1
2 , 240 i
2 . 080 1
1 .320 1
1 . 720 I
1 . 720 1
[ . 520 i
1,310 1
1 . 330 1
1 . 330 i
1 . 732 I


VOL, FLOU ACFM
VOL. FLOU SCFMD

PART I CULATE DATA

POUNDS PER HOUR;
POUNDS PER SCF :
GRAINS/SCF:
GRAINS/SCF 4 S%
GRAINS/SCF 450%
POUNDS PER HMBTU
LBS/MMBTU"F"FACT











S3
70
7k'
73
70
70
70
70
70
74
-,,-,
75
74
75
73
75
75
74
7o
76
72



",

;




02
EA

•DR
9.7
9,2
93bS



1 86 . S
1 S . 6

METER
TEMP.
fc>5
66
6t,
66
68
63
70
71
71
72
73
/ *
75
76
76
77
78
79
73
80
73


1 1 0643
682S5



45.279
U . 0000 1 1 1
0.077
0 , 033
0 . 034
0 . 200
(i . 1 93

-------
                    SAMPLE CALCULATIONS - RUN
N022LE AREA (FT.2)
AVG.VELOCITY HEAD;
METER STND. FT3;

PERCENT H2Q:

Hw DRV:

Mw WET:
X EXCESS AIR; -

STACK VEL.(FPS):

% ISDKINETIC:

VOL. FL-DU CACFM):
STND. FLOU(SCFMD);

PARTICULATE LB/HR;

PfiRTICULATE LB/SCF)
GRAINS/SCF:
GR/SCF $ SJ5 02:
GR/SCF § SOX E.A.:
LB/MMBTU:
LB/HMBTU "F;F FACTOR
 (Dn/ 12)! 2x3. 141 6/4
 (AVG.SQ.RT. )!2
 ( Mf -Mi )xMCFx ( AVe . QRF . D I FF . /
 13.6 ) ) /'2'3 . 92 )x ( S2S/ ( Trii-f-460 ) )
 < (IMP+3G)x((( IMP+SG)>c.0474> +
 SCF)xlOO
 ( < 02«x . 32)+C02Sx . JU) + ( 1 00-( D2X+CD2
 )%.28
 ( Mw DR Yx ( 1 -XH20/ 1 00 ) ) +2H20x , 1 S
0.000k'7b
66.12
 1 00
 85 . 43x . S4x( AVG , SQ . RT . VEL , HD . )x.( C Ts
           .lwUET))! .5
         ) xSCFx2992 ) / ( 52SxFPSxTIMEx
 An  xPs x bQxU-%02/100)
 FPS x £0 x As
 ACFMx52S/ ( Ts+dbO )x ( 1 -XH20 / 1 00 ) x
 (Ps/25 . 92)
 PROEE+FILTER mg./4S3600 x  CSCFMD/
 SCF) x 60
IPROBE+FILTER mg./453bOO /SCF
 LB/SCF x 7DDD
 ( 12. 9/C20. S-%D2))x SR/SCF
 GR/SCF x ( ( 1 00+ %E . A . J / 1 50 )
 (LB/HR)/(LE/MMBTUH)
:L3/SCF x "F" FACTOR  x (20.9
 /20.9-X02)
4.0.914
66.12

:00,SB
}10653
0-000011
0.0774
0.0891
0.0943
0,200

0.193

-------
PLANT:
SOURCE:
DATE:

RUN NO,;
BEGIN TIME;
END TIME;
TOTAL RUN TIME;
BAROMETRIC PRESSURE;
STACK PRESSURE:
NOZZLE DIAMETER-
METER CORR, FACTOR:
FINAL METER;
INITIAL METER;
STACK AREA:
     PORT-POINT
AIR CONSULTING and
    L-UMFLETE EMISSION uATA

ATLANTIC SUGAR ASSOCIATION
NUMBER 4 BOILER
11-21-91
         1-4
         1-5
         i-e
         1-8
         2-5
         2-6
         2-7
         2-9
         2-10
AVG. VELOCITY HEAD
AVG. STACK TEMP.;
AVG. METER TEMP.:
AVG. ORIFICE DIFFERE
METER STANDARD CUBIC
& H2D VAPOR:
GAS DDL. WT. DRY;
GAS MCL, WT. UET:
% EXCESS AIR:
AVG. STACK VEL.
MMBTUH HEAT  INPUT;
PERCENT ISDK INET 1C  :
2
101S
1149
60 . 00
30 . 1 S
30 . 1 8
. 225
1 -009
396 , 269
354.701
27 . 889



win.
"Hg
"Hg.
inches
c ub i c f t .
cubic ft.
sq. ft.
VELOCITY HEAD SQUARE RT

1 . 400
} . 300
1 . 400
J . i 00
1 .200
1 . 200
1 . 1 00
. 900
. 900
.300
1 . 300
1 . 200
1 . 200
1 . 200
"1 , 1 00
1 . 1 00
1 . 1 00
- 950
. 950
. 920

0,0002761
*

:NTIAL: —
• r EC. i •
	

	
VEL. HEAD
1.183
1 , 140
i .183
1 . 049
"i . 095
i . 095
1 .049
0 . 349
0 . 949
0 . 349
: . 1 40
1 .095
1 . 095
1 . 095
1 . 049
1 , 049
i -049
0 , 975
0.975
0 . 959
1 .056
RUN 2
1.12 "H20
174 F
81 F
1 .79 "H2D
29 . 92
26 . 43
7C, Xfi
67 , 54
IMPINGER ml
SILICA GEL gins.
PERCENT 02
PERCENT CQ2
"F" FACTOR-

PART I CULATE
FILTER rr.cj.
WASH ing .

. ORIF. STACK
DIFF. TEMP.
2.240 1
2 . 030 1
2 , 240 1
1 . 760 1
1 . 920 1
i . 320 1
1 . 760 - 1
1 . 440 1
1 . 440 1
1 . 440 1
2 . 080 1
1 . 920 I
1 . 920 1
1 . 320 1
i . 760 1
1 . 760 i
1 . 760 1
1 . 520 1
1 . 520 • 1
1 . 470 1
1 , 794 1
VOL. FLQU ACFM
VOL, FLOW 3CFMD
PART I CULATE DATA
POUNDS PER HOUR:
POUNDS PER SCF ;
GRAINS/SCF:
GRAINS/SCF (550S
345
y
9
9
9

o
1



75
75
77
/ 4
70
75
75
75
76
76
70
76
75
75
76
75
70
72
j _£_
74
i \
02
C A
. 1
. 'Z
•7
- f
366

13.9
1 .0

METER
TEMP .
/ c>
/t«
78
73
73
-T.-,
J '_'
79
80
SO
80
81
t-*v
83
83
34
84
84
85
35
85
31
1 1 3025
67603
49 , 79S
0,0000123
0 . 086
0 . 095
0 . 1 00
                                           CR     0.205

-------
                    SAMPLE CALCULATIONS - RUN  2
NOZZLE AREA fFT.2)  (Dn/12)12x3.1416/4                           0.000276
AMS.VELOCI TV HEAD 1  CAVG.SQ.RT.))2                               67.S4
METER STND.  FT3:     (Mf-Mi)xMCFx(AVG.ORF.DIFF . /
                    1 3.6))/29.92)x C 52S/(Tm+460))                 41.463
PERCENT H2D:        ((IMP+SG)x( (C If!P+SG)x . 0474) +
                    SCF)x100
Mw DRY;             (C02%x.32:i+CQ2Xx.44) + (100-
-------
PLANT:
SOURCE;
DATE:
                    AIR CONSULTING  and  ENGINEE
                        COfcFLETt  EMISSION DATA

                    ATLANTIC SUGAR  ASSOCIATION
                    NUMBER  4 BOILER
                    11-21-91
HVf-i WO. ;
BEGIN TIME:
END TIME;
TOTAL RUN TIME:
BAROMETRIC PRESSURE;
STACK PRESSURE I
NOZZLE DIAMETER;
METER CORR. FACTOR;
FINAL METER;
INITIAL METER!
STACK AREA:
     PORT-POINT
         1-1
         1-2
         J ™*ta*
         1-4
         1-S
         1-6
         1-9
         1-10
                                                                  355
         2-3
         2-4
         2-5
         2-6
         2-7
         2-10
       AVERAGES

NOZZLE AREA(SQ.FT.
AVG, VELOCITY HEAD
AVG. STACK TEMP.I
AVG. METER TEMP.I
AVG, ORIFICE DIFFE
MET
(M it -~'n
A* n^-i-f
GAS MOL. WT, DRY:
6AS MOL, WT. WET:
  cyfccc SIR'
It wAwi^-_*w Pi 4 r\ *
AVG. STACK VEL.CF
rtHBTUH HEAT  INPUT
PERCENT ISCKINETIC  :	
1245
1348
SO . 00
30. IS
30 . 1 S
,225
439 . 874
396 . 703
i, .00^
VELOCITY

1 . 1 00
I . 200
1 .300
\ - "i 00
i . 200
1 . 200
"I .300
1 . 1 00
1 .000
1 . 000
1 . rdOQ
1 . 400
1 . 400
1 . 200
1 .200
. 950
. 950
, 900
, 900
.390



0.0002761
(
t


:NTIAL: —
;™ £^|"*T i
P lie i -
*
—-*—_--
-—.__„__


— * 	 •
: 	 __^, _ , _ _ , „, _ „_


in i n .
"Hg
"Hg.
inches
cubic ft.
cubic ft.
sq, ft.
HEAD SQUARE RT
VEL. HEAD
1 . 049
1 ,095
1 . 1 40
1 .049
1 , 095
1 .095
1 . 1 40
1 . 049
1 . 000
1 . 000
1 .133
1 . 1 S3
1 .183
1 . 095
1 ,095
0 . 975
0 . 975
0 . 949
0.349
0 . 943
1 -062
RUN 3

1 .13 "H20
175 F
f-j .-i r~
&jL r
} .32 "H20
^ -"» A'~! '1
ftw . Ui4
29 , 92
26.51
S3 . 87
£7 . 97
'™JAr- '-^r-i
SILICA GEL gms.
PERCENT 02
PERCENT CQ2
"F" FACTOR

P ARTICULATE
FILTER mg.
WASH m«g .










. ORIF. STACK
DIFF. TEMP
] . 760
1 ,320
2 . 030
1 . 760
1 .920
i .920
2 . 080
1 .760
1 . 600
1 . 600
2 . 2^0
2 , 240
2 . 240
1 .920
1 .920
1 . 520
1 .520
1 . 140
1 . 440
i . 420
1 .SIS


VOL. FLOW ACFM
VDL, FLOW SCFMD
PARTI CULATE DAT
POUNDS PER HOUR
PER SCF
QRAINS/SCF;
GRAINS/SCF (9 3%
GRAINS/SCF i550ft
r"jf%t thtr*'"*' ~*l~r". njiMr*,-r
r-lHiryl/."i l"^n rrrlf-. 1

167
176
176
17S
177
178
177
176
176
174
i /'ii
176
176
1 -7T
i / /
176
174
174
173
175
1 75
17S



I
A t
H .
;
*

02
CM
1):
8 . 6
1 0 . 0
9.5
9366


227 . 4
*$"*£. f

METER
TEMP .
79
79
79
*5»",
/ Z1
SO
so
81
31
SI
y2
82
S3
w3
83
83
S3
S3
oo
84
84
§2


1 13741
680S3

.54 . A. } y
0 .00001 33
0 . 033
0 . 1 1 0
0 . 11 7
I ! O -~i i
                                1 OS , 43
LBS/MMETU"F!1FAC"rOR

-------
                    SAMPLE CALCULATIONS - RUN  3
NOZZLE AREA (FT.2)  CDn/12)!2x3.!416/4                           0.000276
AVG,VELOCITY HEAD;  C AVG.SQ.RT.)!2                               67.97
HETER STND. FT3;    CMf-Mi)xMCFx(AVG.ORF.DIFF./
                    S 3. S)} /29. 32)x (S28/ (Tm+4SO)')                 43 .024
PERCENT H20;        aiHp+se)xuciMp+sG)x.e4?4;t-<-
                    8CF)x100

                    )x.2S
Mw y£T ;             C Mw DRYx (1 -XH20, /1 00)) +£H2Qx. 1S               26. S1
» EXCESS AIR:       %02/C((100-(*02+KC02):)x.264}-%02)*
                    100                                          88.87
STACK VEL. (FF'S) \    85. 49x.S4x(AVS.8Q.RT. VEL.HD. )x( (Ts
                    +4 6 0)/(PsxMwWET))!.S                         67 .97
% ISDKINETIC:       C(T3+460)xSCFx2992)/(528xFPSxTlM£x
                    An xPs x foOxC1-102/100)                      106.43
VOL.  FLOW (ACFM):   FF'S x 60 x As                                5)374]
STND. FLOU(SCFhD>;  ACFHxS2S/(Ts^460)x(1-%H20/100)x
                    (Ps/29.92)                                    63053
PARTICULATE LB/HR;  PROBE+FILTER ftig./4S3SQQ x 'SCFUO/
                    SCF) x 60                                    54.419
PARTICULATE LB/SCF)iPROEE+FILTER rwg./4S3600 /SCF                 0.000013^
GRAINS/SCF;         LB/SCF x 7000 ~                              0.0933
5R/3CF 
-------
    APPENDIX B
FIELD DATA SHEETS

-------
BOILER 3

-------
STACK SAMPLING FIELD DATA SHEET

              i-f/C,

SOURCP	/YU to

PLANT LOCATION

TYPE OF SAMPLING TRAIN

TYPE OF SAMPLES  _

DATE	// - ftQ-"l' RUN NO,
                                                   AIR CONSULTING
                                                 & ENGINEERING, INC.
                            LAftt?
                                                                                                       TEST ID.

                                                                                                       PAGE
                                                                                                                OF
                                                                             MAT'L PROCESSING RATE	
                                                                             GAS METER READINGS-  FINAL
                                              21O6  N, W. 67»h PLACE • Suhas 9 »IO
                                                GAINESVILLE, FLORIDA -326O6
                                                                                                        / jt /.
                                                                                                   NET,
                         p
TIME START.

SAMPLE TIME  <*i& /

ASSUMED MOISTURE,

NOMOGRAPH Cf 	L-
                      TIMP FMH
                              = 6 O  Tatnl mln

                            FDA     .7V..
                       PITOT CORK.
                                     7Y
                          .TEMP.
METER BOX NO,

NOZZLE CAL.
STACK DIMENSIONS

STACK AREA

STACK HEIGHT
                          7/.
                   .ft2 EFFECTIVE

                   _ff.
                                         .11?
                              DN3TRM.
STACK DIAMETER = UPSTRM.

PORT SIZE	In,  NIPPLE LENGTH

U CORD LENGTH 	

REMARKS:	
                                         .In,
•*— >*-».,
SIL GEL
ORSAT

NO /y WT »AIN "1."* m|
T^TAI finMnFN^ATP ^"2-^p.i

1 2
YP COg
% O2
% CO
% N2

3 4 AVG.
90
?, i?


B% « . F« RANGE •
LEAK CH
PREAfi
METER B
ORSAT B
PITOT Tl
POST-TE
POST-TE
PYROME
BOX OPI
ORSAT ANALYZER
ECKS
OSSm /«J "HgPOST,

O/$t1m /(p"H*
OX/PUMP GAS SAMPLE SYST
AQ

JBP NO. ^«S~"^ PRE-TP9T (£?/C
STM-J S~'2~-/ ° H^D/Sie
ST(-J J~. Z-X
rpu NO ^r"7ftfAj$ o
HjO/Sec

BATOR A4-"^/< PBORF HOI OFR /hn£-L~
 PORT AND
 TRAVERSE
  POINT
 NUMBER
         DISTANCE FROM
         INSIDE STACK
             WALL
          /COMMENTS
                        CLOCK
                        TIME
GAS METER
 READING

   (FT.3)
 STACK
VELOCITY
  HEAD
 METER ORIFICE
PRESS, DIFF, ("H^D5
                                                    CALC,
                                                           ACTUAL
STACK GAS
  TEMP

  (•F)
 SAMPLE
BOX TEMP
IMPINOER
  TEMR
  DRY GAS
«ETER TEMR
VACUUM
  ON
3AMPLE
 TRAIN
 ("HgJ
      3
                                                                                                    77
                                     //
                                           /• /
                                                      /•f
                                      /7S"
                                                             7,
                       affg
                                                                                                      74
                                                            / 7
                                                                                                      7
                                            7.
                                                     Li
                                                                                 2/0
                                                                       •ir
                                                                                                              V?

-------
                                             *1B CONSULTING
                                           I ENGINEERING, INC
                                                                                   TEST ID,

                                                                                   PAOE.
                                                                                                   OF
PORT AND
TRAVERSE
  POINT
 NUMBER
DISTANCE FROM
INSIDE STACK
    WALL
 /COMMENTS
CLOCK
TIME
                        QAS METER
                         READING

                           (fl.3)
 STACK
VELOCITY
  HEAD
                                            METER ORIFICE
                                           PRESS. DIFF. ("HgO)
                                             CALC.
                                            ACTUAL
STACK QAS
  TEMP
 SAMPLE
BOX TEMP
  LAST
IMPINOER
  TEMf?
  C°FJ
  DRY GAS
METER TEMP
VACUUM
  ON
SAMPLE
 TRAIN
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                                / 7
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-------
STACK
       ATMtfT^
             £
                                                   AIB CONSULT ING
                                                  & ENGINEERING, INC,
           Mu.
SOURCE	
PLANT LOCATION
TYPE OF SAMPLING TRAIN.
TYPE OF SAMPLES
                   >eJfp.  &LAP€, P/n&i
                                - i"
                             PM
                                               2106 N. W, 67lh PLACE-Suites 9a 10
                                                GAINESVILLE, FLORIDA 32606
TIME START
SAMPLE TIME.
                     .TIME END.
                                 //2L.4?
             A©
                 f   -g  fmln/frlls
ASSUMED MOISTURE A^p, %  FDA
                                     Total mln
NOMOGRAPH C,
               1. (f
                       PiTOT COHR.
WEATHER	
METER BOX NO.
NOZZLE CAL,_
                       H
                         _TEMP
                          i-qi
STACK DIMENSIONS .
STACK AREA  ^1-
STACK HEIGHT	
                       EFFECTIVE
                                         f |2
                     fr_
                              DN9TRM
STACK DIAMETER: UPSTRM	
PORT SIZE	In.  NIPPLE LENGTH
U CORD LENGTH	
                                         In
                                                                                                       TEST ID,
                                                                                                       PAQi
                                                                                                                 OF
                                                                             MAT'L PROCESSING RATE	
                                                                             GAS METER READINGS'  FINAL
                                                                                                INITIAL
                                                                                                   NET
                                                                              FILTER NO, ,
                                                                              SIL GEL NO.

                                                                              ORSAT
                                                      	IMP, VOL. GAIN,
                                                    	      WT.OAIN
                                                     TOTAL CONDEN3ATE
                                                                                                                313
                                                                                                                      ml.
                                                                                                                      ml.

% CO2
% 02
% CO
% N2
1




2




3




4




AVO,
£
-------

                                               AIR CONSULTING
                                              i ENGINEERING, INC
                                                                         P2/7. 
-------
STACK SAMPLING FIELD DATA SHEET
PI flNT
                                                    AIR CONSULTING
                                                  & ENGINEERING, INC.
PLANT LOCATION
TYPE OF SAMPLIN(| TRAIN
TYPE OF SAMPLES
DATE	^
TIME START
SAMPLE TIME
                                               21O6  N. W, 67ih PLACE-SulMsSaiO
                                                 GAINESVILLE, FLORIDA-32606
ASSUMED MOISTURE
NOMOGRAPH
Pb	5
WEATHER
METER BOX NO
NOZZLE CAL. _
STACK DIMENSIONS ,	
STACK AREA j£iU!gLf_ft2 EFFECTIVE
STACK HEIQHT  ..~~\*? _  tt.
                               DN3TRM.
STACK DIAMETER' UPSTRM,,
PORT SIZE   y    In, NIPPLE LENGTH
U CORD LENGTH ^i *«?'_„"
REMARKS'	
                                                                                 TEST ID,
                                                                                 PAGE

                                                       MAT'L PROCESSING RATE	
                                                       GAS METER READINGS' FINAL
                                                                          INITIAL
                                                                             NET.
                                                       FILTER NO, "^^H-M	IMP, VOL, GAIN
                                                       SU GEI NO    fj	       WT. GAIN
                                                                                                                   OF 'Z.
                                                                                                                        ft.3
                                                                                                                        f!.3
                                                                                                TOTAL
                                                                                                                        ml.
                                                                               ORSAT

% CO2
% 02
% CO
% N2
I




2




3




4




AVG,
n.o
*.•£


                                                                                                     Fo RANGE-
                                                                                      ORSAT ANALYZER
                                                                               LEAK CHECKS
                                                                            POST
                                                                                                               e1m
                                                                               METER BOX/PUMP
                                                                               ORSAT BAG
                                                                                                    GAS SAMPLE SYST
                                                                                                                  j \ _ ''
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                                                                             *Hfl
                                                                               PITOT^TUiE NO  "~\4y*  PRE-TPST
                                                                               POST- TEST H->  " ^€>  /
                                                                               POST-TEST(-).
                                                                               PYROMETER NO.
                                                                               BOX OPERATOR
                                                                                                                  .H^O/Sse
                                                                                                                  .H20/Sec
                                                                                                    PRQHF HOI OFP
 PORT AND
 TRAVERSE
  POINT
 NUMBER
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             WALL
           /COMMENTS
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TIME
                                GAS METER
                                 READING
                                   {FT.3!
 STACK
VELOCITY
  HEAD
 METER ORIFICE
PRESS, DIFF, ("HjOJ
                                                     CALC.
                                                            ACTUAL
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  TEMR
 SAMPLE
BOX TEMP
IMPINOER
  TEMI?
  DRY GAS
METER TEMP
    (°FJ
VACUUM
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SAMPLE
 TRAIN
  H
                                                                                7^7
                                           I :
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                *-.J /
                                           l-l
                                                             i no
                                                                               en

-------

                                           AW CONSULTING
                                         & ENGINEERING, INC.
                                                                                                        TEST ID.
PORT AND
TRAVERSE
  POINT
 NUMBER
DISTANCE FROM
INSIDE STACK
    WALL
 /COMMENTS
CLOCK
TIME
GAS METER
 READING
  STACK
VELOCITY
  HEAD
 METER ORIFICE

PRESS, DIFF, ("HgO)
STACK 0AS
  TEMP
                                                    CALC.
                                                   ACTUAL
 SAMPLE
BOX TEMP
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  TEMP
   ("FJ
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SAMPLE
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 ("Kg)
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-------
BOILER 4

-------
STACK SAMPLING FIELD DATASHEET
                                                                                                                  {
                                                                                              TEST ID,

                                                                                              PAGE   V  OF
                                                                              MAT'L PROCESSING RATE
                                                                              GAS METER READINGS'
                                                                                                 INITIAL
                                                                              FILTER I
                                                                              SIL GEL


                                                                              OR3AT
                                                                                      	IMP, VOL. GAIN
                                                                                      	      WT.GAIN

                                                                                     TOTAL CONDENSATE
                                                                                                   Fn RANGE"
                                                                           ORSAT ANALV1ER

                                                                     LEAK CHECKS

                                                                     PttEe.**? etm  ^&  "Hg
                                                                     METER BOX/PUMP ^

                                                                     ORSAT iAQ
                                                                     PITOT TUBE NO,
                                                                     PO3T-TEST(-M _
                                                                     POST-TE9T{-}_
                                                                     PYROMETER NO.
                                                                     BOX OPERATOR
                                                                                                   QA.P SAMPLE SYSt


                                                                                                   PHF.TCST   .
                                                                                                            .11?
                                                                                                            .ft.3
                                                                                      .ml.

                                                                                      'ml.

% .eog
% 02
% CO
% N2
" I




2




3




4




AVO.
at
-in


                                                                                                   PRQHg
 PORT AND
 TRAVERSE
  POINT
 NUMBER
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    WALL
 /COMMENTS
GAS METER
 READING
  iTACK
VELOCITY
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 METER ORIFICE
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                                                    CALC,
                                                   ACTUAL
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  TEMt
 SAMPLE
BOX TEMP
  LAST  •
IMPINOER
  TIMR
  - -'. P. '"I/':.
  OR y GAS
«ETER TEMP

   (*FJ
VACUUM
  ON
SAMPLE
 TRAIN
 THfll

-------
                                                     AIR CONSULTING
                                                   & ENGINEERING, INC
                                                                                                  TEST 10.

                                                                                                  PAGE.
                                                                                                                    .OF,
PORT AND
TRAVERSE
  POINT
 NUMBER
DISTANCE FROM
INSIDE STACK
    WALL
 /COMMENTS
CLOCK
TIME
GAS METER
 READ I NO

   If I.3)
 STACK
VELOCITY
  HEAD
 METER ORIFICE
PRESS, DiFF,
                                                      CALC,
                                                    ACTUAL
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  TEMP
 SAMPLE
BOX TEMP

  C°F>
  LAiT
IMPINOER
  TEMR
  DRY GAS
METER TEMP
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SAMPLE
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-------
STACK SAMPLING FIELD DATASHEET
PI ANT A"C>O efm
                                                                                                 L_OAJ SAMPLE S¥ST.
                                                                               PITOT TUBE NO.
                                                                               POST-TE3TC-M _
                                                                               POST-TE9T(-)_
                                                                               PYROMETER NO,
                                                                               BOX
                                                                                                    .PRE-TEST
                                                                                                      /    l-
                                                                                             ^ggi?PROHE HOLDER
 PORT AND
 TRAVERSE
  POINT
 NUMBER
          DISTANCE FROM
          INSIDE STACK
              WALL
           /COMMENTS
                                GAS METER
                                 READING
                                   (FT,3)
                      STACK
                     VELOCITY
                       HEAD
 METER ORIFICE
PRESS. DIFF. ("HgD)
                                                     CALC,
                                                             ACTUAL
STACK OAS
  TEMP
 SAMPLE
BOX TEMP
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IMPINQER
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  OR Y GAS
WETER TEMP
VACUUM
  ON
SAMPLE
 TRAIN
   . I
   "Z-
                                             .M
                                            \. *»'
                                                                                            ai

-------
                                                   AIR CONSULTING
                                                  & ENGINEERING, INC,
                                                                                               TFSTtfl
                                                                                                                 op
PORT AND
TRAVERSE
  POINT
 NUMBER
DISTANCE FROM
INSIDE STACK
    WALL
 /COMMENTS
CLOCK
TIME
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 READING

   (fl.3)
 STACK
VELOCITY
  HEAD
 METER ORIFICE
PRESS. DIFF. ("H^O)
                                                    CALC.
                                                   ACTUAL
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  TEMP
 SAMPLE
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-------
STACK SAMPLING FIELD DATA SHEET
                                                   AIR CONSULTING
                                                  & ENGINEERING, INC.
                                                                       TEST ID_

                                                                       PAGE   \
                                                                                                       OF
SOURCE
PLANT LOCATION
     OF SAMPL1NS TRAIN

TYPE OF SAMPLES.
naTF    U/t,i f&\ <	RUN
U-NTN-J
2106 N. W 67lh PLACE Sult«»98IO
GAINESVILLE, FLORIDA 32606
*
GAS MET
FILTER r
SIL GEL
ORSAT
Tuijiz^ui |« vj n*>ir
FBRFADINGS. FINAI *5'5"^. fe~l4 «»3
INITIAL
NET
JO ^^^^ IMP V
NO -^ '^
TOTAL CONE
• 1 2
% C02
% Og
% CO
% N2
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d'-»», »1 f.3

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IECKS
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VELOCITY
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 METER ORIFICE
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                                                    CALC.
                                                  ACTUAL
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 SAMPLE
BOX TEMP
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   '     "
  DRY GAS
*ETER TEMP

   C°F»
 VACUUM
   ON
 SAMPLE
; TRAIN
                                                                     1-1 n^i:
                                                                                            QO

-------
                                                    AIR CONSULTING
                                                  & ENGINEERING, INC.
                                                                                                TEST ID.
PORT AND
TRAVERSE
  POINT
 NUMBER
DISTANCE FROM
INSIDE STACK
    WALL
 /COMMENTS
CLOCK
TIME
GAS METER
 READING

   (ft,3)
  STACK
VELOCITY
  HEAD
 METER ORIFICE
PRESS. DIFF, ("H^O)
                                                     CALC.
                                                   ACTUAL
STACK OAS
  TEMP

  t°F)
 SAMPLE
BOX TEMP
  LAST
fMPINOER
  TEMP
  DRY GAS
METER TEMP
VACUUM
  ON
SAMPLE
 TRAIN
 ("Mfl)

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-------
                        BOILER OPERATION PARAMETERS
DATE
                    RUN NUMBER
                                         BOILER NUMBER_j£ ______

                                         OIL METER FACTOR  A//,  Q+Lj-
                                                         — * ™ JU-HMLU.- *~_~

STEAM 1 NTEGRATOR FACTOR _XJ_QjP___ _____   SCRUBBER* S ) PRESS , DROP_f£;l ,
                    -»••       "             SCRUB6ERCS) GPM_ 33j2_,,
OPERATOR SieNATURE__t5.Ci ___ ___ - ___ __   SCRUBBER(S)H20 LEVEL __ ___ ,
                                         Ph( if  appl i cable? __ __ ___ ( ___
INITIAL INTEGRATOR
                                         FINAL INTEGRATOR
                            JJLt  t^JiJ^J^L^:.
 TIME
           OIL
                             STEAM
FEEDWATER
          METER
         READING
LBS,FLOW   TEMP
                                      PRESSURE
                                                    TEMP .
       PRESSURE
                   jL°IJL3.k
                               -T-To
                                        so
  IJ4T
                   if
                                                              3 To

-------
      APPENDIX C
LABORATORY ANALYSIS

-------
BOILER 4

-------
AIR CONSULTING a ENGINEERING, inc. PART1CULATE LAB DATA

PROBE RINSE
CONTAINER ! NUMBER IM-:StK^?o;
TOTAL VOLUME tmll
1st GROSS WEIGHT. { il^^v^jc ;:;,'-.'.;
2nd GROSS WEIGHT ( g J
AVERAGE ^GROSS^WElSmV^ | J JP&te
TARE WEIGHT ( g )
SUB NET WE10Hf^||i^|5||g^s,«
ACETONE BLANK ( g )
TOTAL NET WEIGHTf(m0)fi%f»?1?;;
RUN J_

/ STJ
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tot o^H
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SOURCE fl-fl/tfltrtC- *LL£-/fo. UNIT *-(£,

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DATE a TIME* ,,.W-^ ,s;oi?
DATE 8 TIME' u >X'Q,Olmg/g or OOOI°/o of fhe weigh) of ocatone
used be subtracted from the sample weigh).
FILTER
Fl LTER NUMBER -~:'f\ ?! '? f\ -< . .f
»s» GROSS WEIGHT (g)
2 nd GROSS WEIGHT (o > . .- < '* ' . '}
AVERAGE GROSS WEIGHT (fl)
TARE WEIGHT (fi> , ,;. \\ ;• , •
SU8 NET WEIGHT (g»
TGTACtier WEIGHT ?(mg)fip»':¥^':
TARE
BALANCE CHECK
SEE LAB BOOK
RUN-L
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DATE S TIME= /|-X J-tJ f fj, .!/)
DATE S TIME'- \\^- fl 1 OjSO


2nd GROSS WEIGHT
BALANCE CHECK
\^ lOfln V/
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-------
   APPENDIX D

PRODUCTION RATE
 CERTIFICATION

-------
BOILER 3

-------
                                                           t
PROCESS DATA                        INSTALLATION   '" ~  "
COMPANY r*   1-kNjTlC
DATE      t i  -7ft* 9 /
TYPE OF INSTALLATION  BkCft£S£  BoiLgfL

TYPE OF MATERIAL PROCESSED

TYPE OF FUEL USED  R&
TYPE OF POLLUTION CONTROL  SYSTEMl)VAl
PRESSURE DROP  (INCHES)     s   H- o       VG
REPORTED BY  ^^-^^)
              ^^-
                               NORMAL     RUN 1     RUN 2     RUN 3
                           A/    IT       io J       S-o o      :LU n
SCRUBBER WATER FLOW  (GPM)  $    nf       a o o     •  a. o "     "^^ °

-------
                      BOILER DATA SHEET
COMPANY .A

DATE  tf
INTEGRATOR  FACTOR.  * !.?9

FUEL  OIL USED.l^_Q_..Oi_*r	
s" • REPORTED BY


  . BOILER NO


 STEAM
                                	                   ,    FEED  WATER
                        0  PT,nM *i«K o PRESPITIRR      TEMP.	TEMP-... PRESSURE

-------

-------
                   AIR CONSULTING & ENGINEERING,INC.
                        Complete Emission Data
PLANT;    ATLANTIC: SUGAR ASSGCATIOM          DATE:     11-20-9)
LOCATION; BELL.E GLADE, FLORIDA               RUN NUMBER     i
SOURCE:   NUMBER 3 BOILER,  SCRUBBER OUTLET   TIME;     0332-332


          TIME INTERVAL	        60 MINUTES

       OIL;
          FINAL OIL	         0
          BEGIN OIL                                   0
          r ACi UR	         1

     STEAM:
          FINAL STEAM	    3S600S
          BEGIN STEAM                            3S4S37
          FACTOR	       100
          TEMPERATURE                               540 DEGREES F
          PRESSURE	       239 FSIG
                                                    254 PSIA
 FEEDWATER;
          TEMPERATURE	       23S DEGREES F
          PRESSURE                                  345 PS18
                                                    360 PS IA
HEAT INPUT;
          STEAM	    1285.6 BTU/LB
          FEEDWATER                               203.2 BTU/LB
          NET STEAM	    1082.3 BTU/LB
          STEAM RATE                             116900 LB/HR
          BOILER EFFICIENCY	      55.0 %
          TOTAL FUEL HEAT INPUT                  230.04 MMBTUH
          STEAM CALIBRATION FACTOR	      1.00

          OIL	      0.00 GPH
          OIL                            •        150000 BTU/GAL


          TOTAL HEAT INPUT COIL)	      0.00 MMBTUH
          TOTAL HEAT INPUT (NON-OIL)             230.04 MMBTUH

ALLOWABLES I
          ALLOWABLE EMISSION 	       .10 LB/hMBTU
          ALLOWABLE EMISSION (NON-OIL}              .30 L&/MM6TU

          TOTAL ALLOWABLE EMISSION	     69. 01 LB/HR
          TOTAL ACTUAL EMISSION                   47.29 LB/HR

          TOTAL ALLOWABLE EMISSION	     0.300 LB/MMBTU
          TOTAL ACTUAL EMISSION                   0.20t LB/MMBTU

-------
                       BOILER  OPERATION PARAMETERS-
PL ANT_-_

DATE	iLl^g^I-Ll-JRUM NUMBER	/

STEAM INTEGRATOR FACTOR	/£_£

OPERATOR SIGNATURE
INITIAL INTEGRATOR
                                                NUMBER___^2.

                                         OIL  METER FACTOR	

                                         SCRUBBER C S)  PRESS. DROP_3Jl, j
                                         SCRUBBER C S)  GPM_5OO	,	l.J>.
                                         SCRUBBERCS)H20 LEVEL	,__
                                         Ph< i f appl icable)	,	
                                         FINAL  INTEGRATOR
 TIME
           OIL
          STEAM

LBS~FLOUTEMP"
  FEEDWATER
          METER
         READING
                                      PRESSURE
TEMP .
PRESSURE

                      ?o
  ^00

-------
                     AIR CONSULTING 2i ENGINEERING, INC.
                          Complete Emission Dais
PLANT;     ATLANTIC  SUGAR ASSQCfiTI ON           DATE!      11-20-91
LOCATION:  BELLE  GLADE,  FLORIDA                RUN NUMBER     2
SOURCE:    NUMBER  3  BOILER, SCRUBBER OUTLET   TIME;      1021-1121


           TIME INTERVAL	         60 MINUTES

        OIL:
           I—Y fci,*! i   rrn «,— ,_.,-*——..*.««-.«»*»«„»,**—,—«.__,____________          A
           r i Nf!L_  U J. L.  -»-*-*«-«•««*«-.«-«»-.'«-.—«-*-«.*-*  «*««—,«.«.—**          \j
           BEGIN  OIL                                      0
           _
           r

     STEAM;
           FINAL  STEAM	—    357971
           BEGIN  STEAM                              358819
           rmw i QPt"~"~""*™*~'™™"™""~~"™"-"—~™^™^™-~'"---—*----———"---'        \ Q(J!
           TEMPERATURE                                  54S DEGREES F
           y""»C't'C*C!l JI"fC ——~._ .~^^~~~~-.~~-~-~~~~-. *<-*-. ———	:=	—*  _____^-        O 4 u D*~' 7 r1'
           rrVi-'-'-i^.'nc,   _«.^™»-~              -               *L.*I.-S r o J \a
                                                         260 PSIA
 rEEDwATER',
           TCtrtDCDiiT! iE'C	.	.	.		        •7'IC ncr-OC"CO C
           I CI II »»,nH I V;IVW   -™-~                   — —        X.WO Ljtwr\&WVf I
           PRESSURE                                      345 PSIG
                                                         360 PSIA
HEAT INPUT;
           STEAM	•	    5239.4 BTU/LB
           FEcDUATER                                 203.2 BTU/LB
           WET STEAM	•	    ] OS6. 1 BTU/L9
           STEAM  RATE                               115200 LB/HR
           SOILER  EFFICIENCY	      55.0 %
           TOTAL  FUEL HEAT INPUT                    227.49 MMBTUH
           STEAM  CALIBRATION FACTOR	      1.00

           OIL	.	      0,00 GPH
           OIL                                       150000 3TU/BAL


           TOTAL  HEAT INPUT COIL)	      0.00 ilMBTUH
           TOTAL  HEAT INPUT (NGN-OIL)         ,     227.49 MMBTUH

ALLOWABLES:
           ALLOWABLE EMISSION  (OIL)	        .10 LS/hMBTU
           ALLOWABLE EMISSION  (NON-OIL)                .30 LB/MhBTU

           TOTAL  ALLOWABLE EMISSION	     S3.25 LB/HR
           TOTAL  ACTUAL EMISSION                     54,57 LB/HR

           TOTAL  ALLOWABLE EMISSION	     0.300 LB/MMBTU
           TOTAL  ACTUAL EMISSION                     0.240 LB/MMBTU

-------
                        BOILER  OPERATION PARAMETERS
DATE
                    RUN NUMBER
                                         BOILER NUMBER ___ B;

                                         OIL METER FACTOR __
STEAM INTEGRATOR FACTOR____J^2_0_	    SCRUBBER (S)  PRESS . DROF_3t^» _+L* 2~
                                         SCRUBBERCS)  GPM__Jbj2Q., _
OPERATOR SIGNATURE	    SCRUBBER(S)H20 LEVEL	
                                         Ph(if  applicable)	..
INITIAL INTEGRATOR
                                         FINAL
 TIME
           OIL
                             STEAM
               FEEDWATER
          METER
         READING
                   LB3-FLOU
                              TEMP.
PRESSURE
TEMP.
PRESSURE
 10* 1
                                            o
  }\
                                            0
                                                                      tL
                                                                       Av«

-------
                     AIR CONSULTING & ENGINEERING,INC,
                          Complete Emission Oats
PLANT;     ATLANTIC SUGAR ASSOCATION           DATE;      11-20-91
LOCATION:  BELLE GLADE,  FLORIDA                RUN             3
SOURCE;    NUMBER  3 BOILER, SCRUBBER OUTLET   TIME;      1225-1351


           TIME INTERVAL	         60 MINUTES

        OIL;
           FINAL OIL	'--          0
           BEGIN OIL                                      0
           i™ HV." i ur\™ —™—<——— _*__.»,_.-._—.___—__-.__*»»,*.««,»«*„.„.»,          j

          1;
           c T hi&i  OTC &M———**-	——:	.	:___:	„	™,_.™	    C'C^tA""?—
           i 1 Mr1l_ W I i—Mi I                              -«^OMM / /
           BEGIN STEAM                              358879
           ™ ,"^ ,*"*~™-™--»- —————————-.—«-.«----        ^O-D r ii Q
                                                         261 RSI A

           TOfPr^AT) IDC-*.	:—	^—-.__	:„:	.—*-„.-.«.        .-,.-,/» ^ l~ ~ - ~ 1" ~~ >~' f"
           i C,f IF u--™r* ! lJr\C,                     —«,-•*»,»«        ^i.-j.Ci U*C.wr\C.riCf i™
           PRESSURE                                     345 PSIG
                                                         360 PSIft
HEAT  INPUT;
           i'Thftrl           ———	    i v'31 .4 BiU/Lb'
           FEEDWATER                                 203.3 8TU/LB
           ME i  -"s I t_Hi 1  ™—*~~—     .           .>—.—    j y^ix s j y j y/ |_^
           STEAM RATE                                113800 LB/HR
           BOILER  EFFICIENCY	•—       55,0 %
           TOTAL FUEL  HEAT INPUT                   237.01 nMBTUH
           STEAM CALIBRATION FACTOR	       i.OO

            OTI ___-._™_™™»i™,«.«.__ „___      _*.________,_          •"* "~«M '"-r-iii
            j, |_         *™««* ™— ™.~._-  ______ -*.—-_—__*_ ^»-__™,™       ^f ^ ^tl.* \2f rr              *
           OIL                                       150000 BTU/SAL

                                                                              vs\
           TOTAL HEAT  INPUT COIL)	       0.00 MflBTUH  .    " "^
           TOTAL HEAT  INPUT (NQN-OIL)              237.01 MHBTUK  "

ALLOWABLES:
           ALLOWABLE EMISSION (OIL)	••	        .10 LB/MMSTU
           ALLOUABLE EMISSION (NON-OIL)                .30 LB/MMBTU

           TOTAL ALLOWABLE EMISSION	•—     71 .10 LB/HR
           TOTAL ACTUAL  EMISSION                    A7.S3 LB/HR

           TOTAL ALLOWABLE EMISSION-	     o.soo LB/MMBTU
           TOTAL ACTUAL  EMISSION                    0.202 L'3/MMeTU

-------
                       BOILER OPERATION PARAMETERS
DATE__Jirj^O_n,3_J	RUN NUMBER__~_.

STEAM INTEGRATOR FACTOR	LQ.Q__

OPERATOR 3I6NATURE
                                        BOILER NUMBER	

                                        OIL METER FACTOR
                                        SCRUBBERCS) PRESS . DROPjl/2 • J
                                        SCRUBBER(S) GPM_ J*jlO__ ,
                                        SCRUBBER ( S ") H20 LE VEL____
                                        Phi if  appl i cable) __ r_, __ _,
INITIAL INTEGRATOR
                                        FINAL INTEGRATOR
TIME
           OIL
STEAM
               FEEDUATER
         METER
        READING
                   LES , FLOW
 TEMP .
PRESSURE
TEMP ,
PRESSURE

-------
BOILER 4

-------
PROCESS DATA    .                   INSTALLATION
COMPANY h-Ti-f
V, WT\C J^i
J g-A PL ^s^)J -
DATE H ~ 3U - M £.1
                              NORMAL     RUN 1     RUN 2     RUN 3
               FLOW  (GPM)      3^"Q      33o      33^     3 3 d
PRESSURE DROP  (INCHES)         H • C>       H-Q     ^'Q       ^v^
REPORTED  BY

-------
                         BOILER DATA SHEET
coivffANY n TLA IN TIC  S\ic.

DATE   \ 1 -"7- 1- R '	

INTEGRATOR FACTOR_..2L1_Q_5	

FUEL OIL TTSFD   j\J n  Q \ U
                                               BY
                                     \C
                                                                     A _
                 BOILER NO
                                               .    I
                                   STEAM
    TTIOT!
                                          FEED WATER
                             ,  TT^MP.  . TOMP.
¥33
                      al
 4^
                               J.
    30 J
 11 30
                                                                  3 To
                i 9 i"l  /'
                                               1,30
                                 n
                    it
                                                   Xro
                                             3- .To  AV
                      ^ QO -
                    3-7M
                                             C--
  \ 3 *
•43V
                               S-f
                                              3.5-0
                               So
                                       L&f/fiJK. -
                                       . -..  .,, •j»——.—..»—»—»

-------

-------

-------
                   AIR CONSULTING &  ENGINEERING,INC.
                        Complete  Emission Data
PLANT:    ATLANTIC SUGAR ASSOCATIGN
LOCATION! SELLE GLADE, FLORIDA
SOURCE:   NUMBER d BOILER, SCRUBBER OUTLET
DATE;     51-21-91
RUN NUMBER      I
TIME;     0836-0938
           "IME INTERVflL-
        60 MINUTES
        JIL:
          FINAL OIL-
          FACTOR
                                                       v
                                                       0
          FINAL STEAM-
          BEGIN STEAM
           EMPERATURE
 p C.CUWH i trt;
          TEMPERATURE-
          PRESSURE

HEAT INPUT:
          ,--•!-£• ATI	
          ,-• i CHI I
          H *r~ "^ i~-— r~ •", »v*
          ! 1C. (  C' ', C.I-MI""""	
          STEAM RATE
          SOILER EFFICIENCY	
          TOTAL FUEL HEAT INPUT
          STEAM CALIBRATION FACTOR	
       100
       550 DEGREES F
       24.5 PS 13
       260 PSIA

       235 DEGREES F
       350 PSIG
       365 PSIA

    1231.7 BTU/LB
     203.3 ETU/L6
    10SS.4 BTU/LB
    114600 LB/HR
      55. 0 %
    226.78 MMBTUH
      1 .00
          OIL-
          OIL
      0.00 GPH
    150000 BTU/GAL
          TOTAL HEAT INPUT (DID	
          TOTAL HEAT INPUT (NON-OIL)
      0.00 MMBTUH
    226.78 WMBTUH
          ALLOWABLE EMISSION  COIL)	
          ALLOWABLE EMISSION  CNDN-DIL)
       .10 LS/HMBTU
       .29 LB/MMBTU
          TOTAL ALLOWABLE EMISSION	-—
          TOTAL ACTUAL EMISSION
     65.77 LB/HR
     45.27 LB/HR
          TDTAL ALLGUABLE EMISSION	
          TOTAL ACTUAL EMISSION
     0,230 LS/MMBTU
     0.200 LB/MMBTU

-------
                       BOILER OPERATION  PARAMETERS
                    RUN NUMBER

STEAM INTEGRATOR FACTOR	%__

OPERATOR SIGNATURE
                              BOILER NUMBER	

                              OIL  METER FACTOR
                                                                     I
                             SCRUBBERC S>  PRESS.DROP	,	
                             SCRUBBER C S )  GPM_	,_,	
                             SCRUBBER* 3) H20 LEVEL	,	
                             Ph< i 1  appl icable >	,	,,	
INITIAL INTEGRATOR Hf\fe^I?d	   FINAL  INTEGRATOR__7 JtSi^JL.	
 TIHE
OIL
TEAM
   FEEDWATER
______     _________
          METER
         READING
        LBS.FLOW   TEMP,    PRESSURE
                    J I O
                   flff ooo
                         o o
                                                        i

-------
              AIR CONSULTING S ENGINEERING,IMC.
                   Cofrtolete  Emission Data
PLANT:    ATLANTIC SUGAR  ASSOCATIQN
LOCATION: BELLE GLADE, FLORIDA
SOURCE:   NUMBER 4 BOILER,  SCRUBBER OUTLET
                                         DATE:      11-21-91
                                         RUN NUMBER     2
                                         TIME:      1018-1U9
          TIME INTERVAL
                                                 60 MINUTES
  OIL:
     FINAL DIL
STEAM ;
          FINAL STEAM
          BEGIN STEAM
          TEMPERATURE
 FEEDUATER1,
          TEMPERATURE
          PRESSURE

HEAT INPUT;
          STEAM
          FEEDUATER
                                             801513
                                             300361
                                                     *!
                                                     ^^ ^

                                                     272
                                                     350
                                                     365
                                                    DEGREES
                                                    T"-'~~- 7 ,'*"•
                                                    |- .-, ^ ^
                                                    PSIA

                                                    DEGREES
                                                    PSIQ
                                                    PSIA

                                                    BTU/LB
                                                    BTU/LB
          STEAM KATE
          E'OlLER EFFICIENCY
          TOTAL FUEL HEAT  INPUT
          i_._ir.__ f ^ f--?ii T i~*r>A t" T j~iA!  r
          o i CMH ^-i-*i_4C'hH s iUi-j  r
                                                  115700
                                                    55.0
                                                  22S.S4
                                                    -j /**A
                                                    f , yjj
                                                    LB/HR
                                                    %
                                                    MrtBTUH
          j~"t T i __
          u i L_
          OIL
                                             150000 BTU/SAL
          TOTAL HEAT  INPUT  (DIL)
          TOTAL HEAT  INPUT  (NON-OIL)
                                               0.00 MHBTUH
                                              28. 6 A MMBTUH
ALLOWABLES :
          AULGyABLE  EMISSION (OIL)
          ALLGUAELE  EMISSION (NON-OIL)
                                                .10 LB/MMBTU
                                                .29 LE/hMBTU
          TOTAL ALLOWABLE  EMISSION
          TOTAL ACTUAL  EMISSION
                                              SS.31 LB/HR
                                              43,79 LB/HR
           OTAL  ALLoyABLE EMISSION
           OTAL  ACTUAL  EMISSION
                                              0.290 LB/MMBTU
                                              0/218 LB/MMBTU

-------
                        BOILER OPERATION PARAMETERS
PLANT__  ___  ^

DATE	_U_~_?L-I:_!iA	RUN NUMBER

STEAM INTEGRATOR frACTDR_J^J_O_O

OPERATOR SIGNATURE   f' S \(~
                                          BOILER

                                          OIL  METER FACTOR__£y_Q,_£MJr_.

                                          SCRUBBERt S) PRESS,DROP_ ^f, Q..
                                          SCRUBBERCS) GPM  ^AT	,".."
                                          SCRUBBER 
-------
                   AIR CONSULTING & ENGINEERING,'INC.
                               e Ernies ion Data
PLANT;    ATLANTIC SUGAR ASSOCATION          DATE;      11-21-91
LOCATION: BELLE GLADE, FLORIDA               RUN NUMBER     3
SOURCE;   NUMBER 4 BOILER, SCRUBBER OUTLET   TIME:      1245-1345


          TIME INTERVAL	         60 MINUTES

       DILI
          FINAL OIL	—          0
          BEGIN OIL                                    0
          FACTOR	          I

     STEAM;
          FINAL STEAM	     804644
          BEGIN STEAM                             30339G
          FACTOR	        100
          TEMPERATURE                                550 DEGREES F
          PRESSURE	        266 PSIG
                                                     liol  Pt'iH
 i~ —1~ ~0 ! A T ~ ~< j
 rc.c.uwH i c.r..
          'TEMPERATURE	        235 DEGREES F
          PRESSURE                                   350 PS IS
                                                     365 PSIA
NEAT  INPUT;
          STEAM	     1233.9 BTU/LB
          FEEQWATER                                203,3 BTU/LB
           NET STEAM	     1 OSb . & BTU/LB
          STEAM RATE                              124800 LB/HR
           BOILER EFFICIENCY	       55.0 %
           TOTAL FUEL HEAT  INPUT                   24S.56 MMBTUH
           STEAM CALIBRATION  FACTOR	       1  .00

           QT._	       0,00 GPH
           OIL                                     150000 3TU/GAL


           TOTAL HtAT  INPUT (OIL)	       0.00 MMBTUH
           TOTAL HEAT  INPUT (NON-OIL)              2a£.5t> nMBTUH

ALLOWABLES:
           ALLOWABLE EMISSION (OIL)	         .10 LB/MMBTU
           ALLOWABLE EMISSION (NON-OIL)               .23 LB/MMBTU

           TOTAL ALLOWABLE EMISSION	      71.50 LB/HR
           TOTAL ACTUAL EMISSION                    54.41 L3/HR

           TOTAL ALLOWABLE EMISSION	     0.230 LB/MMBTU
           TOTAL ACTUAL EMISSION                    0.221 LB/MMBTU

-------
    APPENDIX E
QUALITY ASSURANCE
      AND
CHAIN OF CUSTODY

-------
                          STANDARD METER CALIBRATION
                             Meter Number 691751
Air Consulting and Engineering, Inc. (ACE) uses a dry gas meter for the
calibration standard.  This meter has been calibrated against a wet test meter
in triplicate.  This data was used to generate a standard meter calibration
curve (see next pagel.  Field meter calibrations are corrected to this curve
using the following formula;

              Y  x Y  - Y
               3.    S

              Y  « actual ratio of field meter to standard meter

              Y  ~ ratio of standard meter to wet test meter at a given
                    flow rate  (from Calibration Curve)

              Y = corrected ratio of field meter

The dry standard meter was calibrated on June 11, 1991. and is checked and/or
recalibrated at least annually.

-------
      1.3-
      1.2
       1.0-
       0.9-
       0.8-
       O.7-
     §0.6-
     a
     a:


     I0*"
       0.4-
       02-
       O-l-
       0,0-
          I
         .96
 1     1     I     I     1     I
-93   .59   I,CO   I.OI   1,02   1.03
 STANDARD METS3 CSRRIGTICN FACTOR (Y)
                                                      1.03
STANDARD METER CALIBRATION
            CURVE

         JUNE II, 199!
                   AIR  CONSULTING
                            and
                     ENGINEERING

-------


AIR CONSULTING ft ENGINEERING
DflTi
METE
STD (
WET
AH
. "J


'.*
'-'
^f-

n
' c~
C '
f
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±1
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iii
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6-H-^l
R SERIAL N
3AS METER
STD
AH
__
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- /.*9r'.'
. / , w :>
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- ,7 . D
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- 1 3-
-Jl.7
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-a. i
»u«FB^,-7r/
TEMPERATURE JZf£_°F/ ASTM
STANDARD METER CALIBRATION
LEAK
BARO
GLASS THERMOMETER TEMPE
GAS VOLUME, WET TEST METER
INITIAL
O.O
^,&0%
}[. ?^ f )
0,0
ly M ^
If. 'Ml
(9,0
^i 75 1
H.7SO

"^.D"?/
JO.I3D,
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//.5-/3L
FINAL
^ ^ ,3^'
jJi •"* ' 1
li;>t ^O^>
(,Jm ,n'iij
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',.73 1
n.-tzo

/6.77O
^. 07 f
/o. ro
/^s", i^ b-
5.77^
//. 57 A.
/7. 9,'SC?
RATPH BY- -^*~4, •••?. .yCfift^*df
ACTUAL
5?6J^'
£T. 6 o ^
r". S'l *:.
6? • s',1 .'•! -lj
5,1/-/ 2^
^ ?/}':'•
6. 7j /
5",DJ J
.^i Of-c^
^> « '-"' / i
5". D6 1
•C.pL* C?
5", 771
5. 7 'i'1
5". II ^
GAS
f) s\ /J/1 i **~\
r.HFKK I/, VCtlS t!FM nl / <=*- In H*
METRIC PRESSU
HATURF 73 '
Rf 3^5, ' *T
»p
VOLUME, STD GAS METER
INITIAL
^ :',:), (>oC
*-v7. ^
X/, :;_ i^
L,
g /J,i9.">'7
frn.i»h'


^
'^.}3, 7eifT
%'/7. O'/'J

2rt7. f^S*
S^ST. /^35?
1^- /J3
-}fi
S"
f?
s*
^r
,"— *
«.-*
Y SCFM Y SCFH Y SCFM.
0.996 0.838 0.993 1.012 0.994 1.150
0.997 0.836 0.992 1.010 0.996 1.143
0.995 0.035 0.993 1.010 1.000 1.139
0.996 0.836 0.993 1.011 0..996 1.144
U i ngineenng




-------
AIR CONSULTING & ENGINEERING ANNUAL METER CALIBRATION
DATE
METE
DRY
£113
-.0?
-,13
-,tf
-,2i
-.3*
..#
/&- 3-^1
n BOX NUM
SAS METER
AVERAGE
AIID
#,T
|,0
I.S"
J..D
3,7
/of, 631
ACTUAL
I,3
6. / 1 3-
C,s'T7
£.0*7
5, :^7f
st>^
^.3^1

•* t/
r.iiFrK O. cTTIu CFM n, 1 y ,„ ,lr
METRIC PRESS1
RATURE At_?
JRE fT^l'LT'
F
GAS VOLUME, DRY GAS METER
INITIAL
S'SD, T'f
S'^7,/^
fTW.^/f
5^J^
$1+73^
3fa&l
FINAL
!T$&,£
9AW
<${&**&
WM&
^m tfo
s»S^/^
ACTUAL
II3
4>./7^>
c sv-f
i ---
t.oaS
S"",3f/
£ S"^
?,3fl7
In. Hg
TEMP
STD
METER
S7
^/
•z\
%l
%\
?l
TEMP
OF DRY
METER
§^
•g-,9-
g3,
73
*f
«r
.
TIME
(Mlnuits)
/^
10
Oj
—7
i
(?
S'
TIWER
/^





nELfh 11 Ya ocm ys Y
1.90") 1.003 0.378 1 .004 1.007
1.025 I.OOn 0.547 1.001 1.009
I.fl7l 1.010 0.661 1.000 1.009
1.937 .1.011 0.750 . 0.990 1.009
1.910 1.013 0.919 0.19fi 1.000
1.959 1.015 J.052 0.994 1.003
I1FJA11; 1.905 1.010 0.999 1.009

-------
AIR CONSULTING & ENGINEERING, inc. POST TEST CALIBRATION
DflTE
CLIEM
FLIGH
ASTW
.HS
H<
/,r
\\<
c
I
i
II _.*-(? "~_J7 ( „ MFTFB F)OX N"VBF« Y? 1 Fflk CHFCK tx ' O QO CFM at
T ^•*74/t^/7'C- ->(J*A£. /\££oO/£Tfj/an\iar.f 1 jn /Li~~£- -^ T T THPPM™
T SERVICE
1 GLASS TH
AVERAGE
/.7r
/.7,"
P/
ph 3o(/^/
ERMOMETER /
n. Hg. ACE BAR(
/ O OF/THFR
o *-^
•>METER P*> •~'O ' '^ In Hr]
wnr.nnpi F / / / °F ASTIU

GAS VOLUME, STANDARD METER
INITIAL
*/.*,
3,t.ni.
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FINAL
At,m
^.^
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ACTUAL
*m
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GLASS THERM
O In Ho
'Tf ^.,*
j 1 /.T^c
•SwQ.Sk [
ALIBRATFD BY: fj , ^. fl /C^ixC/"

RUN NUMBER
SCFM

n ] °'71
§U ... o.7i
U onsulling s
0 . •"" . : 3 0.71
O ngineenng ;
1 AVERAGES 0.71
ACTUAL
*..7r
j(O yjr£)
WM
TEMP
STANDARD
METER
72-
"W
id
"77
TEMP
OF DRY
METER
6z
*7 (0
^*«*p«^~
Cfi?
On ^T**"
TIME
(Mlnuiai)
3T
54
5^
STANDARD
M , C . F , DELTA H& M . C . F .
1 . 005 1 - 944 0 . 9S9
1 . 005 1 , 902 0 . 993
1 .005 1 .S6£ 0 .996
1 . 005 1 . 905 0 . 993
MAX.
VACUUM
In. Hg.
/z
^
'^


-------
AIR CONSULTING S ENGINEERING, inc. POST TEST CALIBRATION,
DATE
CHEN
FL1GH
ASTW
AHS
H<
1*

c
1
*
:AL
a
jgiimtBs
If 2-(j "~ J ) MFTFB Rnx NMMPF" Y? ._ 1 FflK HHFCK O ' .**
J ' i.l W o
-Stoft.S ^ *j
BRATFD BYt r-J , ^. fl lUjtAS
if
onsutting
; ngineenn
RUN NUMBER
SCFM
1 0.71
2 0,71
! ,-^ 0,71
9 ;
I AVERAGES 0.71
•
ACTUAL
X..7T
39. ^
Wt,
TEMP
STANDARD
METER
7^-
&>
n
7-Z~^
TEMP
OF DRY
METER
62.
ftfi)
81
&
TIME
3T
5H
/
55"
STANDARD
M.C.F. DELTA Ha M.C.F.
\ . O05 1 .944 0.9S9
1 , 005 1 . 902 0 . 993
1 . 005 1 . 868 0 , 396
1 , 005 1 ,905 0.993
MAX.
VACUUM
In, Hg
12.
n
"•


-------
AIR CONSULTING a ENGINEERING, INC.
                            PYROMETER CALIBRATION
   DATE
                   PYROMETER NUMBER
         SOURCE      GLASS THERMOMETER     PYROMETER
        (SPECIFY)    WITH NBS MERCURY ( °f }      (eF)
                              DEGREE
                             DIFFERENCE
PERCENT
DIFFERENCE
     ICE BATH

     AMBIENT

     HOT OVEN
TV/
                                        J71
               JLf.
                                               £>.<•/
  0.2.
   FDER-MAXIMUM 0° DIFFERENCE
   EPA
       (REF, TEMP *F + 460") -(PYROMETER TEMP
                REF, TEMP QF + 400°
                 3
                                            IOO i. 1,5%
   CALIBRATED BY'

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AIR CONSULTING 8 ENGINEERING, INC,
                                        PITOT TUBE  CALIBRATION
   DATE CALIBRATED
   15 PITOT TUBE ASSEMBLY LEVEL.
2  s A sin "Y »
               w * A sin 6=
R
                       In.
S »
               WAS CALIBRATION REOUIREO
                               PITOT TUBE.
                               ARE PITOT TUBE OPENINGS DAMAGED,
                       MOO"). S  *
                             A •
                                    in... 
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AIR CONSULTING AND ENGINEERING, Inc.
                          SAMPLE RECOVERY AND CHAIN OF CUSTODY
PLANT NAME_±
    SOURCE NAMF
    TYPE OF SAMPLE
                                       DATE
                                                / "L
                           \ V / "L&
                SAMPLE RECOVERED BY,
r>
                                PART ICULATE ANALYSES BY
        RUN NO
        RUN "°-
                          SAMPLE RECOVERY


                     CONTAINER  LIQUID LEVEL
                        NO.
             MARKED
                        COLOR
                                                 COMMENTS
                iLANK.
    FILTER BLANK
                              SILICA GEL

          RUN NO.  CONTAINER  Fl NAL WT.   INITWT.  NET WT.   CO(_OR
                   "2-
                                    200.0
                                    200.0
                         73
                                    200.0
                           0
                                    20O.O
                                    2OO.O
                                    EOO-0
                                    2OO.O
                                    2OO.O

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AIR CONSULTING AND ENGINEERING,  Inc.
                          SAMPLE RECOVERY AND CHAIN  OF CUSTODY
    PI ANT NflMC      ULf   j&UACt/ts    TF*T OflTF  ll'3l-1



    SOURCE NAME  A 	 PARTICULATE ANALYSES BY
                           SAMPLE RECOVERY


        RUN NO.       CONTAINER   LIQUID^EVEL   COLQR      COMMENTS




                           '7      -      Lf.
   /ACE TOWfr7 WATER BLANK,

   v - -fmR
    FILTER 1LANK
                                                OM
                              SILICA GEL


          OHM run  CONTAINER   FINAL WT   INIT. WT.   NET WT.    rnmo
          RUN IMO.      NQ        jgj       (aj       {flj     OOLOR






             /       V t      ZVf. 3   200,0     % 3
                                    200.0
fiat.
                                     2OQ.O




                                     2OO.O



                                     200.0




                                     200.0




                                     2OO.O




                                     200.0

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     APPENDIX F
PROJECT PARTICIPANTS

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        PROJECT PARTICIPANTS
AIR CONSULTING AND ENGINEERING. INC.
         Stephen L Neck, P.E.
           _Project Manager
               Team Leader
           J. Colleen Hodge
           Field Participant
            Christy Neck
          Laboratory Analysis
             Dagmar Neck
          Report Preparation
           Candace V.  Taylor
          Document Production
        KLEEMAN ENGINEERING
           Frank K/eeman
            Coordinator

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