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
-------
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
-------
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
-------
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
-------
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
-------
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.
-------
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.
-------
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
-------
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).
-------
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.
-------
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
-------
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
-------
• 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
-------
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
-------
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
-------
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
-------
BOILER 3
-------
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.
-------
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
-------
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
-------
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
-------
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
("HflJ
JJ-
0&S7
1.1
/ 7
2V2-
&
1,0
/,&
/fe
7?
0^03
.3
/
a
/a
Al, o
/.J
r/
7
75-7
237
d/S
/7
75-6
2-
Y
lit. oo
I.I
A 7
/.if
/(,*-
/o
3 6
/.t
//J
8
0133
2X3
10
i.r
/(of
.3-7
-------
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 \ _ ''
^^
*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
DISTANCE FROM
INSIDE STACK
WALL
/COMMENTS
CLOCK
TIME
GAS METER
READING
{FT.3!
STACK
VELOCITY
HEAD
METER ORIFICE
PRESS, DIFF, ("HjOJ
CALC.
ACTUAL
STACK GAS
TEMR
SAMPLE
BOX TEMP
IMPINOER
TEMI?
DRY GAS
METER TEMP
(°FJ
VACUUM
ON
SAMPLE
TRAIN
H
7^7
I :
\?
*-.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
LAST
IMPINOER
TEMP
("FJ
DRY GAS
METER TEMP
VACUUM
ON
SAMPLE
TRAIN
("Kg)
-7
2-
Is
•>
Mi
l-v
S-7
e
61
1*4*4
11
U
1. z:
ZM6
4:7
u\
x,
-------
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
DISTANCE FROM
INSlDf STACK
WALL
/COMMENTS
GAS METER
READING
iTACK
VELOCITY
WAD
METER ORIFICE
PRESS. DIFF, ("Hjp)
CALC,
ACTUAL
STACK OA3
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
STACK OAS
TEMP
SAMPLE
BOX TEMP
C°F>
LAiT
IMPINOER
TEMR
DRY GAS
METER TEMP
VACUUM
ON
SAMPLE
TRAIN
("Hg)
i
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v-n-z,
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ift
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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
LA1T
IMPINQER
TEMR
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
GAS METER
READING
(fl.3)
STACK
VELOCITY
HEAD
METER ORIFICE
PRESS. DIFF. ("H^O)
CALC.
ACTUAL
STACK OAS
TEMP
SAMPLE
BOX TEMP
LAST
IMPINOER
TEMR
DRY GAS
METER TEMP
. VACUUM
ON
SAMPLE
TRAIN
'
c
C
\\tfl
v.v
zn\
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T
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<:
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LI
160
VIM*?
nt
le?
C
c
-------
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
^^.-1^-= »,3
d'-»», »1 f.3
WT QAIN &(-£. ml
»FN«ATF"^?^^'-^' r»i
3 4 AVQ,
^.•€>
\e>
Fks F« RANGE*
LEAK CH
pBF ^,tf
METER B
ORSAT B
PI TOT Tl
POST-TE
POST-TE
PYROME
BOX OPE
ORSAT ANALYZER
IECKS
i£y ctm I'L' "Hgf>QST£
7^(9 ^4
OX/PUMP t^ flAS SAMPL E 9YST *^
AQ
J0F W0_ ^"l^Z, PBE-TP9T t9\£--
STI-4-1 ^-€> /
ST(-) 4? ."L, /
rFR wo AT\£-"5»
RATOB Ht^TTS^1^ PRO RE
^"^ hUO/S.c
*7> H^/Sac
MO, n«%«^^
PORT AND
TRAVERSE
POINT
NUMBER
DISTANCE FROM
INSIDE STACK
WALL
/COMMENTS
GAS METER
READING
(FT?)
STACK
VELOCITY
HEAD ;
METER ORIFICE
PRESS. DIFF,
CALC.
ACTUAL
STACK OA3
TEMR
SAMPLE
BOX TEMP
LAST
IMPINOER
TEMil •--•;
' "
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)
(
1
C
V. \
Vc?
V-C?
I. to
Bz
c
c
C
C
,
f
VM
\0
&*>
1-7
/
C ')
C
(
•v
-
i^r
>--
-------
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
&16 lii^c0(Slte;
IQI.IOQO
$MfPic>©:r
tot o^H
iSm&^Mr-
—
Ka-tf.fc,
RUN_-2"
t*-lo
*iQd$V$®%*
lO'Z.telO
/ai.tvJt?
ii';;-I=#pjii"0lK
,*~~
t'f." ",/.. ' "i *>J^V • > *"'"""
-.-••,.- --KJ; O'- -~:«-.
SOURCE fl-fl/tfltrtC- *LL£-/fo. UNIT *-(£,
^
RUN _s2L
^^^cfeai
/9 '?
^b' t:M^®-^
101. to r?
f^WK^^hl
/CV. C77S"3
%i-,: -i^^-*i
- —
:v: ^:;^:f-
BLANK
/v\?
#gR)/7«0A"V#
/*)/. ^SV7
'
/a/. tSVP
SS^SItod^l'"
—
•fc. --.•; V.'-5 ,'X\ .'. ,:^C.
'•-.= •-.««» .:../L) "•.>>?,:
LIOUIO 1 FVFI ^
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
"-•^3."57 ,
,) OoLO
>'! o ; &0 tfj
0 , fe. 0 b O
./ a?'*-•-
nuN_ii
5W^^.
0.(,35,2
- Y0,63.^-^.'
o. 45S'i9
•^o'-^^-m
0, 2J7V
'-v.vaMrfy^
Isf GROSS WEIGHT
BALANCE CHECK
lX mnn ^
BLANK
..s.» " ^ /O'." !'<3>£^f O---v...<-
« . VtfS/
&*&£*jo2¥>i-
o.Vodl
%^;w^^7-
o.ooaY
•> "•.-,,•...*/ * •
• -•• • '•". . -. _
o
DATE S TIME= /|-X J-tJ f fj, .!/)
DATE S TIME'- \\^- fl 1 OjSO
2nd GROSS WEIGHT
BALANCE CHECK
\^ lOfln V/
o«i0 L/ if7nr»0 • n*n v innnn i-^
%RH £»*-£ narp -i-i-^J
Slanoiur. f^AjMlAr/y MdflfcL,
%RH
Slgna
tt. narr M-W-^I
ur« CAsJLQ&f y. ^£tlA_'
-------
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
L
- , l*
±1
C
i
, 1*
.7
,7
:ALIB
iii
3c
6-H-^l
R SERIAL N
3AS METER
STD
AH
__
- Jj 7
... t ^y
- /.*9r'.'
. / , w :>
- i , o : /
-I.G
- 1.0
-- I,L
- ,7 . D
- 3 . t*
- 1 3-
-Jl.7
-3.7
-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,
c?,0
S.77^>
//.5-/3L
FINAL
^ ^ ,3^'
jJi •"* ' 1
li;>t ^O^>
(,Jm ,n'iij
U.'/'U
AL.^'^'I
',.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.
^r-^
FINAL
At,m
^.^
^"•^
ACTUAL
*m
#.«-
nw
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'
-------
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
-------
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
-------
APPENDIX F
PROJECT PARTICIPANTS
-------
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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