# ea$/f Cargill Incorporated Cedar Rapids
- West 

# EMISSION TEST REPORT Soybean Storage Tank C-IO (EP 95) May 26,2004

Thompson Environmental Consulting, Inc.

a member of THE COMPUANCE GROUP



### Environmental Engineering. Permitting and 

### Compliance Services

### E:MISSION TEST REPORT for Cargill Incorporated on the Soybean Storage Tank C-IO (EP 95) located 

### in Cedar Rapids, Iowa on 

### May 26, 2004

Conducted by 

### Comprehensive Emission Services, Inc. 1112 

### Maple Street West Des Moines, Iowa 50265 (515) 225-7372 Project 

### No. 5604

"'.'."­

### TABLE OF CONTENTS

CONTENTS
Preface........................................................................................................................2 Introduction................................................................................................................3 Summary ofResults ...................................................................................................4 Sampling and Analytical Procedures .........................................................................5 Method 17 Saznpling Apparatus .................................................................................6 Test Results ................................................................................................................7 Appendix A
- Example Calculations Appendix B
- Laboratory Data Forms Appendix C
- Field Data Forms Appendix D
- Pretest Calibrations Appendix E
- Post-test Calibrations Appendix F - Process Data Appendix G
- Opacity Certification



### TABLES Table 1, Summary ofTest Results Soybean Storage Tank C-lO (EP 95)................ 

### ..4 Table 2, Particulate Emission Results Soybean Storage Tank

# e-l 0 (EP 95) ...........7


### FIGURES Figure 1, Method 17 Saznpling Apparatus ................................................................6

1

### PREFACE
This report summarizes the results ofthe data collected on a compliance demonstration test at the Cargill Incorporated facility 

### in Cedar Rapids, Iowa. To the best of our lmowledge, the data 

### in this report are accurate and complete. Any questions concerning this report should be directed to 

### Mr. Tim Titus or 

### Mr. Dan Deatsch. They may be reached by phone at (515) 225-7372.

Dan Deatsch

June 7, 2004



### (

.

- ... / "'" 2

### INTRODUCTION An emission test was conducted by Comprehensive Emission Services, Inc. on the Soybean Storage Tank: C-IO (EP 95) at the Cargill Incorporated facility in 

### Cedar Rapids, Iowa. Three Method 17 with 202 backhalfparticulate sampling runs and three Method 9, Opacity runs were performed. The testing fulfills the requirements for testing in

### the LCPHD Permits CDS#00010 and AT! 

### #4492. The testing 

### was performed on May 

### 26, 2004. Coordinating the field tests: Tim Titus
- Comprehensive Emission Services, Inc. Amelia Denning
- Cargill Incorporated Lisa Schmidt
- Thompson Environmental Consulting, Inc. Conducting the field tests: Jay Titus
- Comprehensive Emission Services, Inc. Dan Deatsch
- Comprehensive Emission Services, Inc. Matt Milligan
- Comprehensive Emission Services, Inc. Witnessing the field tests: Amy Drahos
- Linn County Air Quality 

### Division

The appendices to 

### this report contain the following information and data: 

### Appendix A: Appendix B: Appendix C: Appendix D: Appendix E: Appendix F: Appendix G: 

# ( ) Example Calculations Laboratory DataForms FieldDataForms Pretest Calibrations Post-test Calibrations Process Data Opacity Certification

3

### SUMMARY OF RESULTS 

### In accordance with current IDNR protocol, when less than 10 mg of sample is collected, 10 mg ofsample catch is used for calculations. Sources with sample collections less than 10 mg are shown with a '<'symbol in the following tables to indicate that actual samples were less than the assumed 10 mg catch. Both the actual and the assumed emission rates can be found in Appendix C, Table 1 summarizes the test results for testing perfonned on the Soybean Storage Tank C10 (EP 95). Three Method 17 with 202 backhalfparticulate sampling 

### runS and three . Method 9, Opacity runs were used for testing. The testing fulfills the requirements for testing 

### in the LCPHD Permits CDS#OOO 1 0 and ATI #4492. The testing was performed on May 26, 2004.
The allowable limit for PM is 0.01 gr/dscf. The allowable limit for Opacity is 0%.
No blank corrections were performed.


### Table 1 Summary ofTest Results Soybean Storage Tank C-IO (EP 95) Units Run 1 Run 3 Run 4 PM Net Weight g 

### <0.0100 <0.0100 <0.0100 PM Emissions gr/dscf <0.0024 <0.0021 <0.0021 PM Emission Rate lblhr <0.02 <0.02 <0.02 Flow Rate acfm 1,062 1,030 1,307 

### Flo\vRate 

### dscfrll 1,056 1,004 00') /.Jw 

### Isokinetics % 99.2 98.8 99.0 Start Time HH:MM 8:24 10:35 12:44 Stop Time HH:MM 10:26 12:36 14:46

Opacity % 0.0 0.0 0.0 Start Time HH:MM 8:30 10:40 13:33 Stop Time HH:MM 9:30 11:40 14:33

4

### SAMPLING AND ANALYTICAL PROCEDURES Sampling Procedures Particulate emissions were detennined by

# u.s. Environmental Protection Agency (EPA) Methods 1,2,3,4, 17,202 and 9. These Methods are titled; Method 1 - "Sample and Velocity Traverse for Stationary Sources" Method 2 - "Determination ofStack Gas Velocity and Volumetric Flow Rate (Type S Pitot Tube)" Method 3 - "Gas Analysis for Carbon Dioxide, Oxygen, Excess Air and Dry Molecular Weight" Method 4 - "Detennination for Moisture Content in Stack Gases" Method 17
- "Determination ofParticulate Emissions from Stationary Sources (In-Stack Filtration Method)" Method 202
- "Determinationfor Condensible Particulate Emissions from Stationary Sources" Method 9 - "Visual Determination ofthe Opacity ofEmissions From Stationary Sources" These methods appear in detail 

### in Title 40, Code ofFederal Regulations (CFR), Part 60, Appendix A. The Sampling Apparatus is shown in Figure 1 on Page 6. All equipment was calibrated at Comprehensive Emission Services' office prior to shipment to the test site. 

### Sampling Locations A total of24 sample points were used to determine PM emissions. The sample time per point was 5 minutes, for a total sampling time of 120 minutes per test run. The stack sampling point locations can be found along with the field data sheets in Appendix C. 

### Analytical Procedures The particulate emission rate was determined following procedures detailed in EPA Method 17 and 202. Particulate samples collected on Whatman glass fiber filters were analyzed gravimetrically. The probe and nozzles were rinsed with acetone. The rinse was transferred to tarred beakers and evaporated to dryness.

-" 5 i...._ ..

Stack In-stack Thermocouple Exit Temp Filter SamplEi Probe 

# ----...'" 

# J
Probe Nozzle SType Pitat Tube



### Ice Bath Sample Une Thermocouples Fine Vacuum Adjust Gauge Orifice

# ~

# o I I

-



### Meter Leak Free Pump 

## Schematic of Method 17 Sampling Train Figure 1

,.,.,**.-~** .. , ,'''' . """,."**-.--~.~** -----,-_..

## _ .._-**.~~""**

### Table 2 

### PM Emission Results 

### Soyl 

### bean 

### Storage 

### Tan

### kC-1 0 (EP 95) Parameters Units Run 1 Run 3 Run 4 PMEmissions Actual grJdscf <0.0100 <0.0100 <0.0100 Weight Collected 

### g <0.0024 <0.0021 <0.0021

Emission Rate lblhr <0.02 <0.02 <0.02 StackFlow Rates Velocity ftlmin 5,406 .5,245 5,282

Actual acfm 1,062 1,030 1,037 Standard Conditions dscfin 1,056 1,004 992 Sampling Results Isokinetics 

### % 99.2 98.8 99.0 Sample Volume dscf 64.777 74.626 73.901 Avg. Stack Temperature 

## OF 64 76 86

Avg. Square Root 

### aP inches H20 

### 1.3623 1.3075 1.3049 Avg.MI inches H 2

### O 1.03 1.40 1.38 Avg. Meter Temperature 

## OF 71.7 83.5 91.2 Oxygen 

### % 21.00 21.00 21.00 Carbon Dioxide % 0.00 0.00 0.00 Moisture Collected 

### m1 15.0 13.5 17.0 Moisture 

### % H2

### 0 1.1
. 0.8 1.1 Run Start Time 

### HH:MM 8:24 10:35 12:44 Run Stop Time 

### HH:MM 10:26 12:36 14:46 Sampling Time minutes 120 120 120 Opacity % 

### 0.0 0.0 0.0 Start Time 

### HH:MM 8:30 10:40 13:33 Stop Time 

### HH:MM 9:30 11:40 14:33 Sampling Time minutes 60 60 60

7

# Appendix A Example Calculations

### Symbol Qa 

### As Bws 

## C

p Cstd 

### Dn dscfin 

### g gr/dscfm 

### ID 

### Md 

### Ms Qstd Pb 

### Ps 

## SP Tm Ts Vi Vr 

### Vm Vmstd Vs 

### We Wtgain 

### y 9 % H2O % 

### C02 %02 

### %1 LlH LlP 

### NOMENCLATURE Description . Actual cubic feet per minute Area ofstack Percent water Pitot tube calibration coefficient Concetration ofparticulate dry basis, standard conditions Diameter ofnozzle Dry standard cubic feet per minute Grams Grains per dry standard cubic feet per minute Inside diameter ofstack Molecular weight, dry 

### stack gas Molecular weight, stack 

### gas Stack flow rate, dry standard conditions Barometric Pressure Stackpressure Static pressure Average meter temperature Temperature ofstack gas Initial meter reading Final meter reading Volume meter, actual Volume meter, standard conditions Average stack gas velocity Total moisture collected Total particulate matter collected

.Meter condition factor Sampling time Percent moisture by volume Percent carbon dioxide by volume, dry Percent oxygen by volume, dry 

### Percent isokinetic Pressure drop across orifice meter Gas velocity pressure

\'.

### PARTICULATE CALCULATION EQUATIONS 

### Runl 1. 

### Volume of meter

., j. 

# v'n = 

### (178.457 -114.200)x 1.014

2. 

### Volume of meter, standard conditions (68" ,29.92 

### in.Hg)
17.65x 

# Vm**x(~** + 

# 1lH) V _ 

### 13.6

m{std)
- 

### T + 460 III 

### 17.65x 65.157x (29.88'+ 1.03) V _ 

### 13.6

m{std}
- 

### 71.7 +460
V,n(std) 

### = 

### 64.777 ft3 

### 3. Percent moisture by 

### volume 

### B 

# = 100x 0.4707 

### xWc

\9$ 

### 0.04707 x We 

### + Vm(sId) 

### B 

## = 100x0.4707x+15.0

ws 

### 0.04707x15.0+64.777 B10'$ 

# =1.1 

### % 4. Molecular weight, dry 

### stack gas 

### Md =0.16x%C02 

### +%02 +28.0 

### Md =O.16xO.00+21.00+28.0 

### Md =28.84

### 5. Molecular weight, stack g 

# Ms = 

### Md 

# X(l- B ws )+18X(1_Bws) 100 100
Ms

# =28.84X(1-~)+18X(1-~) . 100 100 M. 

## = 28.72 6. Stack Pressure 

## SP P 

## = P. 

### +­

.r b 

### 13.6 

### P 

## = 29.88+ 0.23

• 13.6**~** 

# = 29.90 inch. Hg 7. Velocity of stack gas
Vs 

# = 60x 85.349 x 

### C p 

### x
Vs 

## = 60x85.349xO.99x 64+460 X 

### 1.3623 29.90 

### + 28.72 

# v.. = 5,406 

### ftlmin 8. Percent isokinetic 100 

### x

## (T + 460)

### x Vm(.j'(d) g 

### %1 "=**----~~-~~.....<----:** 

### 17.65x8x 

### V. 

# xp"

# X(l- Bws

# .)X1fx(Dn 

# )2

. 100 24 

### 1OOx (64 + 460

## )'x64.777 %1 

### =**----~-~-----':----------:** 

### 17.65 x120x 

### 5,406 x 

### 29.90 x

# (1**~)x** 1fx(0.136)2 100 24 %1 

# = 99.29. Area of stack 

# ID)2 A :::: n-x ­

s 

# (24



### _ (6.00)2 

### A - n-x -­

s 

### 24

10. Stack volumetric flow rate actual conditions


### Q :::: 5A06 

### x 0.20

a 

### Ql1 :::: 1,062 acfm 11. Stack volumetric flowrate, standard conditions (68·,29.92 in.Hg) 

### 17.65x xAs xP s

# X(l- -ffo) Ts 

### + 460 17.65X5,406XO.20X29.90X(1-

# ~) 100 

### Qstd :::: 64 

### + 460
Qstd :::: 1,056 dscfm 12. Grains per dry standard cubic feet



### :::: 15.43xWtgaih C

Sld 15.43 x 0.0049 

### Cstd 64.777 

### ; = 0 .0012 gr/dscf 

### C

std

### 13. Emission rate Ib 60 x 

### Wtgain x QSld -::::: 

### hr 

### 453.5924 x 

### Vm(std) Ib 60xO.0012xl,056 == 

### hr 453.5924 x 

### 64.777 Ib = 

### O.Ollblhr hr



### )

# AppendixB Laboratory Data Forms

\ ) " " /

### Project Number:

# ~~::""'..Ir:~-=t)_t/..:..- ____ 

### Plant Name: 

# &r!l i , I Date: 

### S- 

# n "'-of Analysis Type: 

## 1+ I 

### 2. CJ 

## Z­ 

# ,6p 75 Runl Type Iden:tification Final 

### Tare Net Number Weight Weight Weight Filter 

# p /39(3 

# ';tbl'1r**:;{~** 

## b 

# r!-f 

# S

.. 0.00 

# '2 Probe Rinse ( ml) 

## B**33~8** 

# -::r'-. t0

### T~ 

# -=t-b,!o&1 ,,00 

### J J Front HalfWeigbt 

### /0 0 

# 1,] Organic ( ml) 

# c**3~'f** 

# I J0 

## 2. <?s'1-)(J)

## 10~-¥1--/4 

## .. "'0'3 J Inorganic 

### }) 3¥B L( 

# I'S**~.OG** 

## '3;A**1~7.0b~1-** ;0005

, Total**~et** Weight ." 00 

# I-I,!

. Run2 Type Identification Final 

### Tare 

## I Net Number Weight Weight Weight Filter 

# r 1399**l.-bo~O L~6(j)**  

## =}-3 ," O®cv-=;-' Probe Rinse ( ml) 

# B 33i.o9 (;5**~** 

# 11- t-&zf 

# b5.f1-d-.1­ _OO£) 

### I Front HaIfWeight ,**O(?O~** Organic ( ml) 

## ( 3&'IL 

## lo3,j-b54':r {<13 

## .'1-(:, 

## '3 if '

... OO-;;tO Inorganic 

# D 31./&5**13bJf~** 

# n**13b.4f>1{i~** ,<Of}O 

# 1­ Total Net weight 

# ,**~o3.5** Run 3 Type Identification Final 

# L Tare Net Number Weight Weight Weight Filter 

# P i t.f 00 

## '?.holl ?. .

## b OtfJ

# -:r. ,(.700,/ Probe Rinse ( ml) 

# B 33tO 

# h?-,6'1tif5 b1.61-{1J' ,.. 0'001.-/ FrontHalfWeight

### 'OOO~ Organic ( ml) 

# c.. 3& t./3 /05. 

## -:r-1J'1 L{**If)3~t-~Q** 

## ,;**o~** 

### G 

# '1 Inorganic 

# .D**3l{8~** 

## 153.1r1;}1**1~3.i5--JJ** 

# 1

- .. 0005 Total Net Weight 

### "t:f7b"31­ Identification F 

## =3 inch filter P 

### = 47mm filter B = I50mlBeaker C = 250ml Beaker D 

### = 400ml Beaker

## - - ... -

...**~.** I, 

## FINAL WEIGHT WEIGHING SHEET Time Date Analyst IDNo. Ron 1



# t> s 

# ?vl!io
Cheek Weight Check Weight CheckWejght . Ch!;}ck Weight Weighing (grams) 234 5 Net Weight Average

Final Weight

### 7~61'1**~c** 

# =-E­ -' 

# 'S**,~** Tare Weight



### COMPREHENSIVE EMISSION SERVICES''-.-" 

## TARE WEIGHT 

## WEIGHING SHEET Time Date Analyst ID No.

Check Weight 1



### 5-d6,)1... Weighing (grams) 2 3



# S:tJo.sz.

< 4< 5



## :;;. 06 {O 

# d. &t30?t!J 

# :;. t. 5 

# 7t.JJ 

## :;? 

## 058'}

< 

## t. 5/3{P

to8fJ3 2· (P1'l5 d. t01-'S



# -== COMPREHENSIVE EMISSION

< SERVICES

## TARE 

## WEIGHT WEIGHING SHEET Time**iD~()f** Date

### 5"-5~oi Analyst 

# . D5
ID No. 1 

## 1, 

## 3357­ 

# 67,of!& s3!? 0 "11'."¥**G~f** 

# 3359 '1--::t ' 

## '3,;1 Q'Y 

# 33&>0**4~.** 

## &-:fr.f1 

## "3 

# 3ft, 

# I (J (P. 

# tf aO/'**3:>~Z** 

# -:r1. 0 

# rq..1 .3:;:(03 

# U4.1-Dz:f1**]:J~** 

### l( 

# 1-&. /11f 

# 31102**~t** 

## t, Ell.l15"**33~to** 

## fJlt.ZJ95 

# 33br**(;~,** 

### 3/ d

# J.3ioB '1to.1OluiP CheckWc;:ight '";j 

### 0**~** 

### -03

# [if 1:;;1.-;} 

# s- 'J**~vt.f** 

# ./16
. Weighing (grams) 2 3 

### (;1- 

## .DL/ f Y 

# fY. }lMJI'1 71.3J..t b**(,~** 

## . l.i

## 1- l( 

## J' 

# b&. 'Y()of 

## '1-1,O3?!)' 

# U, 7D?Y? 

## 1&.(t8'0 

# ."71'. Bt15" 

# /Ju. 11q7­ 

# ulL. d31> f/g.IO&7 " 

### '"7D.o3r

# r.f .
4 

# • • ' it<**'~"',,:9.':ot** . '.**'~'~** 

### '''1 .>"", •••t:..**.~** ..**~** ".**,;r.··~** 

# ....."**1\'~~·'** $! "., .**~.,:** .

# Ij.';~

# .. ::::......**<~:~_I** Average 5 i 

# ItT. D4'Bi**i:~.~iJJla~** 

## 1-T.3a01 

## i9lP. &.

## -=t4)?**G;~.** 

## 4CD"1­ 

## '1-1 . O"'i{:f-

### d 

### lul.,:-=f

## 004 1-&. 

## r:rTCJ 

# 1-"1-. J(.,q5 l.ol.o. 

## 1?rq (p 

## ft,b.Cl313 

## 1-(.,. 10

## u -:}­



# ::. C
-- COMPREHENSIVE 

# B EMISSION 

# § 

# S**~** SERVICES

## TARE WEIGHT 

## WEIGHING SHEET Time Date Analyst ID No. 1

Check Weight Weighing (grams) 2 3



## 'g3?7­



## , fcf7- 

## J



# !.a57-S 4 5 Average



### '7fi.o ,**~5 ~·t13itl**  

## fJi. '1t.**~** 

## 5-:r,'>' ':/-¥. '1Q,,2**~** 

### &,.. 

### tfO"':}-S' iPS. 105Q D 

### {pIP. 

### 13DI../ 

## 11. ;n· L{ 

## I .

ec;MPREHENSIVE EWSSION

### ~ERVICES

.... ,-.. ".-., .. ,... ......... .**--~**- .. -".;. 

## TARE WEIGHT 

## WErGHrNG SHEET Time 

## &/'Vf:5 Date 

### 5-03- GJ

## V Analyst**1h_IJ~** 

# #t-A Weighing (grams)

COMPREHENSIVE EMISSION SERVICES. ID No. 

### lI 2 3



### ,...

".,

...



# -
Check Weight 

## I/RO, oVdD 

## 111m ,bOd

### 0 4 5

### '--_
.. ' 

## TARE WEIGHT 

## WEIGHING SHEET Tilne 

# /0 :Jo Date 

## 5-S-'Drj Analyst 

# Dfr
ID No. 1 

# C**p~VZ** 

## (01,11036 

## 3t. 

# Vj ID3.1F1D "Swr(l(**[o~.** 

## 015':2**"J~** 

# V S 

## {Oa-. (0

### <1 

# Lfr 

# 3., V" t 

## 03. '1 l

# u4 }(Pl/1 /O&.qCJSD 

# Jt:,ftt 1 

# oil. t/'S'11 

# ;{; Y7 f**DJ~~IO)o** J.{p 

## S"D ID171fY**3~** 

# sl 'D4.l/11 ) 'J (gS2-­ 

## I**u~.** 

# 51?O, (Ilt 

# J".5:>**qt.31~r**

Check Weight**!~C).a:?>06** 

## '1:2 0 

### 5:**1--(j~**



# ,Oft Weighing (grams) 2 3 (f)

### ~.1&t{ 

### 0 

## 1 

# b3· l' 'l;j.D 

### I

## oli. (yt5**~** 

## /DJ-. uQ 

## 4 l.P**Lrl~** 

## .. '1/&{P 

# I()IR::')? ),2 

## loL{.Q59F /7JI./.1/.05D 

## l(it./.g I

## Y't ' 10l{.. t[ 

## t 7 d

## IDl.{. 

## S'ljo3 

# 17 -31<11 tOO. oD 0 i) 4 

### .
5 

# •**~~~:~~<~1:::,,': ,\$j~'**  .•**m·l,~** 

## , '



# .**:I~' ~~**  

# .:.:.. ?**~.if** '-:«-.**-:::e:"~** 

# .. •••••• : 1>;/ ".: .\:**~.?:"A** '" Average 

## 1 0

## 3·Th3'1. 103, "':f i?1-0 IDCo, 01- 

### 5;) 

## lOa. (PQ<./l 

## 103, Cj I 

## iPS' 

## fDu·'195/**lO4.tj5q~** 

## 104.405D 

# 104. ¥I)?l? 

### i04. lj (

# -:t- ") J

# 04. 5'<i?O 

# "> OJ<6 

## .3 r1?4

COMPREHENSIVE EMISSION SERVICES...• 

## TARE WEIGHT WEIGHING SHEET Time Date Analyst IDNo. 1 

### .:)-'1- 

### -oLjWeighing (grams) 2 3' 

## is''1.0UJ 

### J. (f

# 1'.5& .1..{ 

### f?:> ., 

## ;r·llA I 

### r ..... • I . _ .

### "7~a 

### 0 I .-. T'/ I 

### I

Check Weight 

## IfD.03l13 

# I ll-a,D'3Q 4 5 Average 

### \5'1.0 {per={

### r~L.L\~o4

. 1 IJ**I~** ,.,......,.­ 

## luto.34Q5

COMPREHENSIVE EMISSION SERVICES

# Appendix C -Field Data Forms

i 

# I I 

# I I- 

# iRun No. Location: Date: Project 

### # 1. assume 10mg Cargill CR West (EP 95) May 26. 2004 5604 

### % Isokinetic= 99.2 Initial Meter**Volum~** (Cubic Feet)= Final Meter Volume (Cubic Feet)= Meter FactorFinal Leak Rate (cu Ftlmin)= Net meter Volume (Cubic Feet)= Gas Volume (Dry Std Cubic Feet 68 De9)= 114.200 178.457 1.014 0.000 65.157 64.777 Barometric Pressure (in Hg) = Static Pressure (Inches H20)= Stack Pressure (in Hg)= 29.88 0.23 29.90 Percent Oxygen :::: Percent Carbon Dioxide::: Moisture Collected(ml)= Percent Water= 21.00 0.00 15.0

1.1 Average Meter Temperature (F)= Average Delta H ( in H20)= Average Delta P (inches H20)= Average Stack Temp (F)=

. pry Molecular Weight= ··'Wet Molecular Weight:::: 71.7 1.03 1.8875 64 28.84 28.72 Sampling Time (Minutes)= Nozzle Oiameter(lnches)= Stack Diameter (lnches)= Stack Area (Square Feet) = Pitot Coefficient=: Average Square Root of Delta P (inches H20)= 120.0 0.136

6.00 0.20 0.99 1.3623 Stack Velocity (Actual. ftlmin)= Flow Rate (Actual. Cubic ftImin)= Flow Rate (Std, Dry, Cubic ftlmin 68 Deg)= 5,406 1,062 1,056 Particulate Loading - Front Half Particulate Weight Net (9)=**Pati~ulate** Loading, Dry Std. 68 Deg (grlscf)= Emission Rate (lblhr)= 0.0013 0.0003 0.00 Particulate Loading - Total Catch Including Impingers
( Particulate Weight Net (9)=

.Particulate Loading, Dry Std. 68 Oeg (grlscf)= )Emission Rate (!blhr)=

Percent Impinger Catch= 0.0100 0.0024 0.02 87.00Run No. 1 Location: Cargill CR West (EP 95) Date: May 26,2004

.Project # 5604 % Isokinetic= 99.2 Initial Meter Volume (Cubic Feet)= 114.200 Final Meter Volume (Cubic Feet)= 178.457 Meter Factor- 1.014 Final Leak Rate (cu Ftlmin)= 0.000 Net meter Volume (Cubic Feet)= 65.157 Gas Volume (Dry Std Cubic Feet 68 Oeg)= 64.777 Barometric Pressure (in Hg) = 29.88 Static Pressure (Inches H20)= 0.23 Stack Pressure (in Hg)= 29.90 Percent Oxygen = 21.00 Percent Carbon Dioxide= 0.00 Moisture Collected(ml)= 15.0 Percent Water= 1.1 Average Meter Temperature (F)= 71.7 Average Delta H (in H20)= 1.03 Average Delta P (inches H20)= 1.8875 Average Stack Temp (F)= 64 

## 'pry Molecular Weight= 28.84 'Wet Molecular Weight= 28.72 Sampling Time (Min utes) = 120.0 Nozzle Oiameter(lnches)= 0.136 Stack Diameter (Inches)= 6.00 Stack Area (Square Feet) = 0.20 Pitot Coefficient= 0.99 Average Square Root of Delta P Onches H20)= 1.3623 Stack Velocity (Actual. ftlmin)= 5,406 Flow Rate (Actual, Cubic ftlmin)= 1.062 Flow Rate (Std, Dry, Cubic ftlmin 68 Oeg)= 1,056 Particulate Loading - Front Half Particulate Weight Net (g)= 0.0013 Paticulate Loading, Dry Std. 68 Deg (grlscf)= 0.0003 Emission Rate (Iblhr)= 0.00 Particulate Loading - Total Catch Including lmpingers Particulate Weight Net (g)= 0.0049

.Particulate Loading, Dry Std. 68 Deg (grlscf)= 0.0012
" ) Emission Rate (Iblhr)= 0.01 Percent lmpinger Catch= 73.47Run No. 2, assume 10mg Location: Cargill CR West (EP 95) Date: May 26,2004 .Project# 5604 % Isokinetic'= Initial Meter Volume (Cubic Feet)= Final Meter Volume (Cubic Feet):::: Meter Factor- Final Leak Rate (cu Ftlmin)= Net meter Volume (Cubic Feet)= Gas Volume (Dry Std Cubic Feet 68 Deg)= Barometric Pressure (in Hg) = Static Pressure (Inches H20)= Stack Pressure (in Hg)= Percent Oxygen ::: Percent Carbon Dioxide::: Moisture Collected{ml)= Percent Water= Average Meter Temperature (F)= 

### Average Delta H ( in H20)= 

### Average Delta P (inches H20)= Average Stack Temp (F)= Dry Molecular Weight= 'Wet Molecular Weight= Sampling Time (Minutes)::: Nozzle Diameter{lnches)= Stack Diameter (Inches)= Stack Area (Square Feet) =

. Pitot Coefficient=



### Average Square Root of Delta P (inches H20)= Stack Velocity (Actual, ftlmin)= Flow Rate (Actual, Cubic ftlmin)= Flow Rate (Std, Dry, Cubic ftlmin 68 Deg)= Particulate Loading - Front Half Particulate Weight Net (g)= Paticulate Loading, Dry Std. 68 Deg (grlscf)= Emission Rate (Ib/hr)= Particulate Loading - Total Catch Including Impingers Particulate Weight Net (g)=

.Particulate Loading, Dry Std. 68 Deg (grlscf)= . ) Emission Rate (Iblhr)=

Percent Impinger Catch= 98.8 178.900 254.496 1.014 0.000 76.654 74.626

29.88

0.23 29.90 21.00

0.00 13.5

0.8 83.5 1.40 1.7292 76 28.84 28.75 120.0 0.150

6.00 0.20 0.99 1.3075

5,245 1,030 1,004
0.0008 0.0002 0.00
0.0100 0.0021 0.02 92.00Run No. 2 Location: Cargill CR West (EP 95) Date: May 26, 2004 Project # ·5604 

### % Isokinetic= Initial Meter Volume (Cubic Feet)::: Final Meter Volume (Cubic Feet)= Meter Factor- Final leak Rate (cu Ftlmin)= Net meter Volume (Cubic Feet)= Gas Volume (Dry Std Cubic Feet 68 Deg)= Barometric Pressure (in Hg) ::: Static Pressure (Inches H20)::: Stack Pressure (in Hg)= Percent Oxygen = Percent Carbon Dioxide= Moisture tollected(ml)= Percent Water- Average Meter Temperature (F)= Average Delta H ( in H20)= Average Delta P (inches H20)= Average Stack Temp (F)= Dry Molecular Weight= ·Wet Molecular Weight= Sampling Time (Minutes)::: Nozzle Diameter(lnches)= Stack Diameter (Inches)::: Stack Area (Square Feet) =

. Pitot Coefficient= Average Square Root of Delta P (inches H20)= Stack Velocity (Actual, ftlmin)= Flow Rate (Actual, Cubic ftlmin)= Flow Rate (Std, Dry, Cubic ftlmin 68 Oe9)= PartiCUlate Loading - Front Half Particulate Weight Net (g)= Paticulate Loading, Dry Std. 

### 68 Oeg (gr/set)= Emission Rate (Ib/hr)= Particulate Loading - Total Catch Including Impingers PartiCUlate Weight Net (g)= Particulate Loading, Dry Std. 

### 68 Deg (gr/set)::: j Emission Rate (Ib/hr)=

Percent Impinger Catch= 98.8 178.900 254.496 1.014 0.000 76.654 74.626

29.88

0.23 29.90 21.00

0.00 13.5

0.8 83.5 1.40 1.7292 76 28.84 28.75 120.0 0.150

6.00 0.20 0.99 1.3075

5,245 1,030 1,004
0.0008 0.0002 0.00
0.0035 0.0007 0.01 77.14Run No. 3, assume 10mg Location: Cargill CR West (EP 95) Date: 

### May 26, 2004 Project 

### # 5604 

### % Isokinetic= 99.0 Initial Meter Volume (Cubic Feet)= 255.100 Final Meter Volume (Cubic Feet)= 331.023 Meter Factor= 1.014 Final Leak Rate (cu Ftlmin)= 0.000 Net meter Volume (Cubic Feet)= 76.986 Gas Volume (Dry Std Cubic Feet 68 Deg)= 73.901 Barometric Pressure (in Hg) = 29.88 Static Pressure (Inches H20)= 0.23 Stack Pressure (in Hg)= 29.90 Percent Oxygen ::: 21.00 Percent Carbon Dioxide= 0.00 Moisture CoUected(ml)::. 17.0 Percent Water- 1.1 Average Meter Temperature (F)= 91.2 Average Delta H (in H20)= 1.38 Average Delta P (inches H20)= 1.7250 Average Stack Temp (F)= 86 Dry Molecular Weight:::: 28.84 Wet Molecular Weight= 28.72 Sampling Time (Minutes)= 120.0 Nozzle Diameter{lnches)= 0.150 Stack Diameter (Inches)= 6.00 Stack Area (Square Feet) 

## = 0.20

. Pitot Coefficient= 0.99 Average Square Root of Delta P Onches H20)= 1.3049 Stack Velocity (Actual, ftlmin)= 5,282 Flow Rate (Actual, Cubic ftlmin)= 1,037

.Flow Rate (Std, Dry, Cubic ftlmin 68 De9)= 992 ParticUlate Loading - Front Half ParticUlate Weight Net (g)= 0.0008 Paticulate Loading, Dry Std. 68 Deg (grlscf)= 0.0002 Emission Rate (Ib/hr)= 0,00 Particulate Loading - Total Catch Including lmpingers Particulate Weight Net (g)= 0.0100 ,Particulate Loading, Dry Std. 68 Deg (grlscf)= 0.0021**~,** .)Emission Rate (Iblhr)= 0.02 Percent' Impinger Catch= 92.00Run No. 

### 3 Location: Cargill CR West (EP 95) Date: May 26,2004 Project # 5604 % Isokinetic= Initial Meter Volume (Cubic Feet)= Final Meter Volume (Cubic Feet)= Meter Factor- Final Leak Rate (cu Ftlmin)= Net meter Volume (Cubic Feet)= Gas Volume (Dry Std Cubic Feet 68 Deg)= Barometric Pressure (in Hg) = Static Pressure (Inches H20)= Stack Pressure (in Hg)= Percent Oxygen = Percent Carbon Dioxide= Moisture Collected(ml)= Percent Water- Average Meter Temperature (F)=
. Average Delta H ( in H20)= Average Delta P (inches H20)= Average Stack Temp (F)=

.\Dry Molecular Weight= AJVet Molecular Weight=

Sampling Time (Minutes)= Nozzle Diameter(lnches)= Stack Diameter (lnches)= Stack Area (Square Feet) = Pitot Coefficient= Average Square Root of Delta P (inches H20)= Stack Velocity (Actual, ftlmin)= Flow Rate (Actual, Cubic ftlmin) = . Flow Rate (Std, Dry, Cubic ftlmin 68 Deg)= Particulate Loading - Front Half Particulate Weight Net (g)= Paticulate Loading, Dry Std. 68 Deg (gr/set)= Emission Rate (Iblhr)= Particulate Loading - Total Catch Including Impingers Particulate Weight Net (g)= Particulate Loading, 

### Dry Std. 68 Deg (gr/sct)= }Emission Rate (Ib/hr)=

. Percent Impinger Catch= 99.0 255.100 331.023 1.014 0.000**76~986** 73.901

29.88

0.23 29.90 21.00

0.00 17.0

1.1 91.2 1.38 1.7250 86 28.84 28.72 120.0 0.150

6.00 0.20 0.99 1.3049

5,282 1.037

992
0.0008 0.0002 0.00.
0.0037 0.0008 0.01 78.38

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End SII{ Condllo!1B End Slat nd End '17 

## () 

# 0 

# a 0
i 18 

## 0 

# 0 

# 0 0

;9 

### () 

## 0 

# 0 

# 0 ; 20 

# 0 

# 0 /J 

# 0 Source Layout Sl:eIoh 21 

## CJ (J 

# 0 0 22 

# 0 () () 

# 0 23 

## 0 

# 0 0 

# D**X~1'oi'It** 

# I 24 

# 0 (j () 

## (] 25 

### () 

## () () 

# 0 Dt _FEET 0



# I - FEfT 

# 'j

I , 

# 1llI._ 26 

# 0

# %i~ (j 27 

# 0 () 28 

## () 

# 0 

# 0 /J 2'1 

# 0 (j 

# 0 /J 30 

### f) 

## () 

# O· d

V!CF1.l

"· \ :' 

# AppendixD Pretest CalibrationsMETER CALlBRA TION Operator Daniel Boes K Factor 0.6274 Date May 14,2004 Meter Number 

### 5 }Previous Y Factor 1.009 Orifice Number 23 j 

### RUN 1 RUN2 Meter Volume Final Cubic Feet 97.465 103.082 Initial Cubic Feet 91.900 97.500

Net Cubic Feet 5.565 5.582 Meter Temperature Inlet Initial Oeg. F 65.0 68.0 Final Oeg. F 68.0 70.0 Outlet Initial Oeg.F 63.0 64.0 Final Deg.F 64.0 66.0 Avg. Meter Temp Oeg.F 65.0 67.0 Time sec 420.0 420.0 Meter Delta H inches H2O 2.20 2.20 Barometric Pressure inches Hg 30.10 30.10 

### Room Temperature ') i. Initial Oeg.F 71.0 71.0
. Final Deg.F 71.0 72.0 Avg.Room Temperature Oeg.F 71.0 71.5 Pump Vacuum inches Hg 17 17 Vcr (std) dscf 5.737 5.734 Vm (std) dscf 5.658 5.654 Y Factor 1.014 1.014 Delta H@ 1.969 1.953 Average Y 1.014 Average Delta H@' 1.961 +/- 2% Criferia Percent of Avg Y 0.01 PASS +/- 5% Criteria Percent of Final Y 0.49 PASS

# CONSOLE WORK SHEET Operator: 

# l)y\**~-c..\ ~2**  . K Factor: O. (D;;) 

## ?:;e-i Date: 

# s: l4 

# -0-4 Meter LD. 

# '5

_____ __ __ Previous Y Factor: J

### .00::1 Orifice Number: _[)=-.--,.,,::.,s

_____

METER VOLUME Units



### . Rnal 

### 'ff! Inital 

### ff! meter Tempera.tura 

### INLET '

. Initial :OF Final 

### OF OUTLET Initial 

### OF Final of Time 

### seo Meter ll.H**In.~O:** Barometrio Pressure In. Hg Room Temperature Initial of Finar 

### OF Pump Vacuum In. Hg' 

### ,



# . , Run Number 1 

# 0'1.**q,~** 

## <; 

# 9/9 0 

### 0 

## lje) 

# /1 <6

, 

# &3 

# '. '" &4 4Jo ,J,9­ 3:) .­ j0



# .i-I



# 'tl V?­ 2 

## lO3.,0l'd. 

# '11 . .5"cD 

# (., y, --;}{) 

# It!4

. tJlI1 if

J 

# 0 ;).:;J ·3D f IO



## ":1-1**~.** I '--::z I , 

### ! "



### COMPREHENSIVE' EWSSION 

# SERVICES.
/ ;



# .. IORIFICE BRACKETING Operator Daniel Boes BRACKET ORIFlCES: Date May 14, 2004 Orifice No. 1 23 ! 1. K Factor 0.6274 ;Jieter Number 

### 5 Orifice NO.2 12 Meter Y Factor 1.014 K Factor 0.3336 ORIFICE #1 ORIFICE #2 Meter Volume 

# ! Final Cubic Feet 108.768 113.891 Initia! Cubic Feet 103.100 108.800

Net Cubic Feet 5.668 5.091 Meter Temperature Inlet Initial Deg. F 72.0 72.0 Final Deg.F 72.0 72.0 Outlet Initial Deg.F 71.0 71.0 Final Deg. F 71.0 72.0 Avg. Meter Temp Deg. F . 71.5 71.8 Time sec 420.0 720.0 Meter Delta 'H inches H2O 2.20 0.62 Barometric Pressure inches Hg 30.10 30.10 Room Temperature

.**~:..** . Initial Deg. F 72.0 73.0 Final Deg.F 72.0 73.0 Avg.Room Temperature Deg.F 72.0 73.0 Pump Vacuum inches Hg 17 17 Vcr (std) Vm (std) Y Factor (brackets) dscf dscf 5.731 5.693 1.007 5.219 5.091 1.025 +/- 2% Criteria PercentofY P,Ll.$S 0.71 PASS 1.10

),

## - 

# -- - -- 

# BRACKETING WORK SHEET Meter f.D. 

# _S_...:...

_______**operat~r:** UCM\'\J fIDes Date: 

# 5· (4'- 0 

# if K Factor No.1 ;) 

## .fpC<

# 3Y Previous Y Factor 

# r0 

## I

# rj K Factor No.2 

# O. 333 b

' Units 1 :2 METER VOLUME ft3 Final 

### J 0 

### 'l?,**--=i-u~** 

# h .1"**~91** ftll Initial 

## \ () 3. \ C"'D 

## 10**~:gao** Meter Temp.erature INLET 

### OF Initial 

# td. -=t-'d OF final 

### -=j-;),

## '~:J OUTLET .' 

### .. 

### OF InItial' 

## -=t( 

# 1-\ OF**'~** Final 

# -=f-f sec Time· 

### .-.::t';;Z

### Lt~D Meter .6.H In. HIP 

## d·d
. f..g 

## cl.
..**~** , in. Hg Barometric Pressure 

# '3 0 .\0 

## 0CSLO Room Temperatura 

### OF Initial

### +~ 

## 4-3 OF Anal 

## -:t-J 

# "9'"\ In. Hg Pump Vacuum '1-'::;'" \ -:::j.. 

# =..c­

- - CO:MPREHENSIVE



## - = 

# E=

-- 

# -­ - 

# - - - - 

### - - 

### EM1SSION

.SERVICES,



## -- 

# S -=

­

....

. .... 

## ....**~**

# Appendix E Post-test CalibrationsMETER CALIBRATION Operator Matt Milligan KFactor 0.6274 Date May 27,2004 Meter Number 

### 5 l Previous Y Factor 1.014 Orifice Number 23

RUN 1 RUN2 Meter Volume Final Cubic Feet 336.958 342.640 Initial Cubic Feet 331.300 337.000

Net Cubic Feet 5.658 5.640 Meter Temperature Inlet Initial Oeg.F 74.0 75.0 Final Oeg.F 76.0 76.0 Outlet Initial Oeg. F 73.0 74.0 Final Oeg.F 74.0 74.0 Avg. Meter Temp Deg.F 74.3 74.8 Time sec 420.0 420.0 Meter Delta H inches H2O 2.20 2.20 Barometric Pressure inches Hg 29.64 29.64 : Room Temperature
.:. j Initial Deg.F 75.0 76.0 Final Deg. F 76.0 76.0
. Avg.Room Temperature Deg.F 75.5 76.0 Pump Vacuum inches Hg 17 17· Vcr (std) dscf 5.625 5.623 Vm {std} dscf 5.567 5.545 Y Factor 1.010 1.014 Delta H@ 1.933 1.947 AverageY 1.012 ,L\verage Delta H@ 1.940 +/- 2% Criteria Percent of Avg Y 0.18 PASS +/- 5% Criteria Percent of Final Y 0.18 PASS

# CONSOLE WORK SHEET

,,'I', 

### Operator:

# !lkt.t!: /til!

# l7411 K Factor:

__ '

# (_~~/?--=-1-L'( 

# ___ Date: 

# 5-OJ 

# 1-0 

# <{ Meter I.D. 

# 5 Previous Y Factor. 

# l 0 / 

# V Orifice Number:

_____

# ~"'--&;;..] 

# ____

METER VOLUME Units 'FInal ' ftS
'. Inltal 

### ff Meter Temperature INLET Initial 

### "F Final " 

### OF OUTLET Initial 

### "F Final 

### OF Tlma sac Meter AH In.Hp: Barometrio Pressure in. Hg Room Temperature InitIal 

### OF Final 

### "F Pump Vacuum In. Hg' Run NUmber 1

### ':3~-**95~** 

## 33/·300'

' , 

# rtf f/.p 

# 73 1-i.( 1.(2.0**~,;;;,** 

# ;21,(; t.(



# '1-5

c 

# -r(:;' (1-
. 2 

# 3 

# til.· ft;¥O, 

# 33 r1'(}OD



# 7-5 -=;-r,a '7-'1



# rtf L/Za

r?;:; 

# ;) 9·6t/ v I



# -=t(P 

# r& I 

# 7­ ':"C ­ CO:M:PREIIE.NSIVE' 

# =E EMISSION 

# ==- S**~** SERVICES.

i ,ORIFICE BRACKETING Operator Matt Milligan BRACKET ORIFICES: Date May 27,2004 Orifice No.1 23 K Factor 0.6274

### I~eter Number 

### 5 Orifice No.2 12 Meter Y Factor 1.012 K Factor 0.4041 ORIFICE #1 ORIFICE #2 Meter Volume Final Cubic Feet 369.958 375.337 Initial Cubic Feet 364.300 370.000

Net Cubic Feet 5.658 5.337 Meter Temperature Inlet Initial Oe9. F 

### 77.0 77.0 Final Oeg.F 77.0 77.0 Outlet Initial De9. F 

### 77.0 77.0 Fina! Oeg;F 77.0 77.0 Avg. Meter Temp Oeg.F 77.0 77.0 Time sec 420.0 600.0 Meter Delta H inches H2O 2.20 1.00 Barometric Pressure inches Hg 29.64 29.64**~oom** Temperature Initial De9. F· 77.0 77.0 Final Oe9. F 77.0 77.0 Avg.Room Temperature 06g. 

### F 77.0 77.0 Pump Vacuum inches Hg 17 20 Vcr (std) dscf 5.617 5.169 Vm (std) dscf 5.539 5.209 Y Factor (brackets) 1.014**0.~92** +/- 2% Criteria Percent ofY 0.21 1.96 PASS PASS- -



### - -


## -- - 

# BRACKETING WORK SHEET Meter I.D.

__ ">.:;;...-

______ 

### Operator: 

# }jalf1tt'llif 6 

## i1 Date: 

# 5'

# -;;n. -0 l( K Factor No.1

__ -.:;....1

# _~;.....;;;;:;_-:::;::...__.;L( __ Previous 

### Y Factor 

# f· D

# tl..- K 

### Factor No.2 ---,---:;..l 

### ....t.tf_o_l/.!....!..-f

___

·1 i ! METER VOLUME Final Initial . Units 

## tea ff" 

# , 3tc.CJ.CJ56 J&t/3IJ(J 2 

# '3T5.33r-. 3TOIODO Meter Temp'eratljre INLET Initial F.inal of 

### OF 

# 7-7­ 

# rr­**::;.~**

### i-~ OUTLET Initial Final 

### OF OF 

# ??­ 

# rr 1-t7-1­ Time
,­ Meter llH Barometric Pressure see in. 

## HzO in. Hg 

## tJZD 

## /;?;;? 

# ;;?9. 

# &y t/:;tJO 

## 1.0

.. (01( Room Temperature Initial Final Pump Vacuum 

### of of In. Hg ... 

# '97­ 1-r /-::;­ 

# 1--::r 

# 7-7­ odD 

# :.c -

­ 

### - 

# - - COMPREHENSIVE 

# -E­ ====- -:::::=:: 

### EMISSION 

# = - 

# s-=

­


## -- 

# - SERVICES. 

### ).

# AppendixF Process Data_______________________ _ 

### Compliance Emission Test Operating Data Owner: Cargill Cedar Rapids West Date: May 26, 2004 Source:EP 95 Soybean Storage Tank C-I0 Permit**#:,...;:44...:.;9;.;;2~·**_____
Maximum Continuous Process Rate (Manufacturers Rating)_36_0_t_o_nlhr

____________ HistoricalAverage Process**Rate:.;...360~t..:..onlhr** Historical Maximum Process Rate
. ..:.3-'-60

...... ___________________ ......

to....;nJ_hr Types and Sources ( if any) of Fuels normally Bumed._ N

_ /A

_______________ Type of Fuel Burned During this test .............____________________ N/A If Fuel is used Approximate Quantities of each listed above burned Annually
...... ___________ N;;.;;/A Recycling Capability Yes.

___ No 

## X Recycling in Progress Yes

___ No 

### X fmcess Data**D~!** jOg RYIl§

Process Rate (gallhr, Iblhr, tonslhr. etc.•.) Process Rate Wet Percent Moisture ("!o) Process Rate Dry How Process Rate was Oetermined Run 1 Run2w Run 3



# .

276 tonlhr 160 tonlhr 107 ton!hr Monitored truck loads
Person**Responsjbl~** for Data,.:.P..:;.au1:::.:.K;;.,;e,;;:;rr...;:&.:.,;Am:.=:.;.:eI:::;ia;:...;D;:....e:=D=D1=·D:!2,g

_____---
_______ Signmum

_____________________________________________________________ ntle/Position Facility Superintendent & Crush Department Superintendent ** please incih;8te in the sawe unit$. 

### as vour hjstom:a1 iaff2IJ1Ji1Von

# --

____________________________________ __ ',; 

### AIR POLLUTION CONTROL EQUlPl\1ENT OPERATING DATA Plant Cargill Cedar Rapids West Loc:ttion 1110 12th Avenue SW, Cedar Rapids, IA

, 

### Source Type Dust Collector I Partlcu1ate Rated Produc;tion 360 tonlhr Date May 26,2004 Tune

____**~Proouamn~·1~8~1~~-nlhr~--------** AirFlow Data .:,10.:,.1:...;7-=d::.sc.:..:fin:;;;;:....

______ RunNo. _1... ,2

..... ,_&_3

__________ MecbaniCll Collector: Tube Dia

____ in.. Number ofTubes Design 6p

____ i,n. HiO Gas Temp --,-
__ Of Observed 6p in HozO Design cfmJtube @ ObseIVed 6.p @ 

## orFanRated H.P. Operating Volts Operating Amps _'

_____



# - Primary Secondary FicldNo. SecondaIy Frim.aIy SpnrkRme Voltage (KV) Current (amps) Voltage (volts) Current (rna) (per min)

Scrubber: Type**_~________ ~p(across**  scrubber}
__________ in B.O. Fan Rated HP Operating Volts
______ Opernting Amps

______ Liquid Circ:'ulaIion Rate gal/min. % Make-up
____ Blowdown

______ gpm Scrubbing Water Change InteIVal

___________-­
____________ Settling Tank Cleaning Interval Baghouse: Pressu:re·Positive

__----,,...-;-__ Negative _X_____ No. Compartments _o_ne

__**~_** Type: Cle:ming 

### _c_om_p ....

I'_es_s_ed_a_ir________ CIe:m Cycle ·_1.;.....5

__________ 'min Avg. Baghouse 6,p

__________ in HlO .o.p Range Fan: Rated ID. 2 Ope:acng Volts 460 OperntiDg Amps _3_.7

_____ Cyclone:**T~e** __**~~** ______________ t.p

__-:-

___ inH'lO Diameter

___------­ Fan RncedEP

_________ Opernting Volts

_____ Operating Amps -----rPerson Responsible for Data Paul Kerr & Amelia Denning**Sj~rure** Title:Position Facility Superintendent & Crush Department Superintendent

10

# Appendix G Opacity Certification

# AEROMET

# ENGINEERINGINC. 

# Certification ofVisible Opacity Reading Jay Titus

,On 

# April 

# 13, 2004, qualified to conduct EPA Method 

# 9 Testsfor visible opacity in accordance with the rnethods established for such qualification in 40 CFR Part 60 AppendixA. Date: 04113104 

# Signature:

# ~~,-", Instructor, Aeromet Engineering Certificate expires: 10113/04