ca;g;,r . 

Cedar Rapids, Iowa 


West Soybean Plant 


Emission Test Report 


for 


Two Soybean Storage Bins - EP 101 


January 24, 2007 

Thompson Environmental Consulting, Inc. 


Environmental Engineering, Permitting and Compliance Services 
{

'... 

EMISSION TEST REPORT 


for 


Cargill Incorporated 


on the 


Two Soybean Storage Bins (EP 101) 


located in 


Cedar Rapids, Iowa 


on 


January 24, 2007 


Conducted by 

Comprehensive Emission Services, Inc. 


P.O. Box 910 


Waukee, Iowa 50263 


(515) 987-0200 


Project No. 407 

. (

"\.. i· 

- '... ..:.... ',., 
TABLE OF CONTENTS . , 

( 

CONTENTS 


Preface........................................................................ · ................................................2 


Introduction ................................................................................................................ '3 


Summary of Results ... : ............................................................................................... 4 


Sampling and Analytical Procedures ..........................................................................5 


M17 Sampling 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 - Posttest Calibrations 


Appendix F ~ Process Data 


Appendix G - Opacity Certification 


TABLES 

Table 1, Summary ofTest Results for the Two Soybean Storage Bins (EP 101) ......4 


Table 2, Particulate Emission Results for the Two Soybean Storage Bins (EP 101) 7 


. FIGURES 

Figure 1, M17 Sampling Apparatus ...........................................................................6 

PREFACE 

( 

This report summarizes the results ofthe data collected for compliance testing performed 

at the Cargill Incorporated facility in Cedar Rapids, Iowa. To the best of our knowledge, 

the data in this report are accurate and complete. Any questions concerning this report 

should be directed to Mr. Tim Titus or Mr. Matt Milligan. They may be reached by 

phone at (515) 987-0200. 

February 12, 2007 . 

2 
INTRODUCTION 


An emission test was conducted by Comprehensive Emission Services on the Two 

Soybean Storage Bins (EP 101) at the Cargill Incorporated facility in Cedar Rapids, Iowa. 

Three Method 17 with 202 backbalfparticulate sampling runs and three Method 9, 

Opacity rtins were perfonned. The testing fulfills the requirements for testing in the 

LCHD Pennit #A TI 5003. The testing was perfonned on January 24, 2007. 

Coordinating the field tests: 

Tim Titus - Comprehensive Emission Services, Inc. 


Amelia Denning - Cargill Incorporated 


Lisa Schmidt - Thompson Environmental Consulting, Inc. 


Conducting the field tests: 

Taylor Daily - Comprehensive Emission Services, Inc. 


Mason Woltz - Comprehensive Emission Services, Inc. 


Matt Milligan - Comprehensive Emission Services, Inc. 


Witnessing the field tests: 

Joseph Strahan - Linn County Air Quality Division 

The appendices to this report contain the following information and data: 

Appendix A: Example Calculations 


Appendix B:. Laboratory Data Fonus 


Appendix C: Field Data Fonus 


Appendix D: Pretest Calibrations 


Appendix E: Posttest Calibrations 


Appendix F: Process Data 


Appendix G: 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 

10mg are shown with a '<'symbol in the following tables to indicate that actual samples 

were less than the assmned 10 mg catch. Both the actual and the assumed emission rates 

can be found in Appendix C. 

Table 1 smnmarizes the test results for testing performed on the Two Soybean Storage 

Bins (EP 101). Three Method i 7 with 202 backhalf p.?rticulate sampling runs and three 

Method 9, Opacity runs were performed. The testing fulfills the requirements for testing 

in the LeRD Permit #ATI 5003. 

The allowable limit for PM is 0.0861blhr and 0.01 gr/dscf. 

The allowable limit for Opacity is 0%. 

No blank corrections were performed. 

Table 1 


Summary ofTest Results 


Two Soybean Storage Bins (EP 101) 


units Run 1 Run 2 Run 3 

PM Net Weight g <0.0100 <0.0100 <0.0100 

PM Emission gr/dscf <0.0024 <0.0024 <0.0025 

PM Emission Rate lblhr <0.021 <0.021 <0.021 

Flow Rate acfin 952 947 948 

Flow Rate dscfm 1,005 991 978 

Isokinetics % 99.2 99.5 99.8 

Run Start Time HH:MM 9:32 12:08 14:09 

Run Stop Time HH:MM 11:38 13:41 15:40 

Date of Test mmldd/yr 01124/07 ·01/24/07 01124107 

Opacity % 0.0 ·0.0 ·0.0· 

Run Start Time HH:MM 9:41 12:22 14:19 

Run Stop Time HH:MM 10:41 13:22 15:19 

Date of Test mmlddlyr 01/24/07 01/24/07 01124107 

4 

i 
SAMPLING AND ANALYTICAL PROCEDURES 


Sampling Procedures 

Particulate emissions were determined 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 of Stack Gas Velocity and Volumetric Flow Rate" 

Method 3 - "Gas Analysis for Carbon Dioxide, Oxygen, Excess Air and Dry 

Molecular Weight" 

Method 4 - "Determination for Moisture Content in Stack Gases" . 

Method 17 - "Determination ofParticulate Emissions from Stationary 

Sources (In-Stack Filtration Method)" 

Method 202 - "Condensible Particulate Emissions" . 

Method 9 - "Determination ofVisual Emissions 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. 

SampliRg Locations 

A total of 12 sample points were used to determine particulate emissions. The sample 

time per point was 7.5 minutes, for a total sampling time of90 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 

Methods 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 tared beakers and evaporated to dryness. The back -half water was 

collected and separated jnto organic and in-organic parts. The samples were then 

transferred to tared beakers and evaporated to dryness .. 

5 

, ,~ : 
/ ....--.. 

. Stack In-stack ~ Exit Temp 

Thermocouple 

~I"

Fi~lta~r~~~~~~s~am~PI~e~p~ro~b~e~=~~=~~~~) 

Probe 

Nozzle S Type Pitot Tul;le 

Ice Bath 

.' Sample Line 

Thermocouples Fine Vacuum 

.0 

Adjust . Gauge 

Orifice 

Dry 

Gas 

Meter 

Leak Free 

Pump 

Schematic of Method 17 Sampling Train 

Figure 1 
Table 2 


Particulate Emission Results 


lWo Soybean Storage Bins (EP 101) 


Parameters Units Run 1 Run 2 

PM Emissions 

Weight Collected g <0.0100 <0.0100 

Actual gr/dscf <0.0024 <0.0024 

Emission Rate lb/hr <0.021 <0.021 

Stack Flow Rates 

Velocity ftlmin 4,849 4,821 

Actual acfin 952 947 

Standard Conditions dscfin 1,005 991 

Sampling Results 

Isokinetics % 99.2 99.5 

Sample Volume dscf 64.023 63.296 

Ave. Stack Temperature of 33 36 

Ave. Square Root AP inches H20 1.2545 1.2430 

Ave. LlH inches H20 1.61 1.61 

Ave. Meter Temperature of 72.3 74.2 

Oxygen % 21.00 21..00 

Carbon Dioxide % '0.00 0.00 

Moisture Collected ml 1.0 '·5.0 

Moisture % H20 0.1 0.4 

Run Start Time HH:MM 9:32 . 12:08 

Run Stop Time HH:MM 11:38 13:41 

Sampling Time minutes 90 90 

Date orfest mmlddlyr 01124/07 01124/07 

Opacity % 0.0 0.0 

Run Start Time HH:MM 9:41 12:22 

Run Stop Time HH:MM 10:41 13:22 

Sampling Time minutes 60 60 

Date ofTest mmlddlyr 01/24/07 01/24/07 

Run 3 

<0.0100 

<0.0025 

<0.021 

4,827 

948 

978 

-'.' ~ 

99.8 

62.669 

41 

1.2375 

1.58 

73.6 

21.00 

0.00 

10.0 

0.7 

14:09 

15:40 

90 

01'/24/07 

0.0 

14:19 

15:19 

60 

01124107 

7 

Appendix A 


Example Calculations 


\. . 
Symbol 

Qa 

As 

Bws 
 Cp 


Cstd 


Dn 

dscfm 

g 

gr/dscfin 

ID 

Md 


Ms 


Qstd 

Pb 

Ps 

SP 

Tm 

Ts 

·Vi 

Vf 

Vm 

Vmstd 

Vs 

We 

Wtgain 

y 

8 

% H20 

% C02 

%02 

%I 

~H 

~p 

NOMENCLATURE . 

Description 

Actual cubic feet per minute 

Area of stack 

Percent water 

Pitot tube calibration coefficient 

Concetration of particulate dry basis, standard conditions 

Diameter ofnozzle 

Dry standard cubic feet per minute 

Grams 

Grains per dry standard cubic feet per minute . 

Inside diameter of stack 

Molecular weight, dry stack gas 

Molecular weight, stack gas 

Stack flow rate, dry standard conditions 

Barometric Pressure 

Stack pressure 

Static pressure 

Average meter temperature 

Temperature of stack 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 I 

\­

Percent oxygen by volume, dry i 

Percent isokinetic 

Pressure drop across orifice meter 

Gas.velocity pressure 
PARTICULATE CALCULATION EQUATIONS 

Run! 

1. Volume of meter 

V,1l = (511.636 -446.700)x 1.004 

2. Volume of meter, standard conditions (68° ,29.92 in.Hg) 

~" +460 

17.65X65.l96X(29.50+ 1.61) V _ 13.6 

m(s/d) - 72.3 + 460 

3. Percent moisture by volume 

100 x 0.4707 x 

B = 100 x 0.4707 x 1.0 

1VS 0.04707 x + 64.023 

4. Molecular weight, dry stack gas 

Md 0.16 X %C02 +0.04X%02 +28.0 

M~ =O.l6x 0.00+0.04x 21.00+28.0 

Mti =28.84 

.\ 
5. Molecular weight, stack g 

-- •..., >"_ •••• 

Ms == 28.84x (1- 100 0.1) +18 X(l- lOa} 0.1 1

M.I

. ;::::: 28.83 

6. Stack Pressure 

.P. p. + SP u b 13.6 

P = 29.50 + 0.00 .f 13.6 

P.v = 29.50 inch. Hg 

7. VeloCity of stack gas 

V." = 60x 85.49x C x Ts + 460 x( tt;;;) p . P x M :oJ up o'l'g 

s .r 

I . 

V, = 60 x 85.49 x 0.99 x J 33 + 460 x 1.2545 . V29:50x28.83 

V" = 4,849 ftlmin 

8. Percent isokinetic 

%1 = ____100 x (Ts +460)x V,lI(.,Jd) ---.::..-::...._-..:...._='L-__ 

17.65x ex V. x Ps x (1- Bw.r)x 7fx(Dn)2 . 100 24 

100 x (33 +460)x 64.023 %1 = ------~--..!..-------

17.65 x 90 x 4,849 x 29.50 x (1 ~~~ )x n:x(0.~:O)2 

%1 99.2 
9. Area of stack 

(

ID).2 :TCX ­24 

6.00J2 A = rex -­ .1' ( 24 

to. Stack volumetric flow rate actual conditions 

Qa =VxA ,0; S 

Q 4,849 X 0.20 a 

Qa 952 acfm 

11. Stack volumetric flowrate, standard conditions (68",29.92 in.Hg) 

17.65x V, x A, xP. X('l- Bw.,) • ,. 100 

QSld = ----T--+-4-6-0-"::"---=­

s 

17.65X4,849XO.20X29.50X(1- 0.1) ",' 1 00 

Q"ld = ------33-+-4-60---"-----1:­

o."ld =1,005 dscfm 

12. Grains per d.t.] sta.'1dard cubic feet 

15.43 x Wt gain 


Vm(sld) 


15.43 x 0.0038 

C,\'/d 64.023 


,C :::: 0 .0009 gr/dscf 
 s1d 
13. Emission rate 

Ib 60 x Wt g•in x QSld 

= hr 453.5924x Vm(std) 

Ib 60 x 0.0038 x 1,005 

= hr 453.5924x 64.023 

lb 

= O.0081b/hr hr 

l, .. 
AppendixB 


Laboratory Data Forms 

Project Number: ::r-.---=.4..,;:..0....;:7- __-:---;-__ 

Plant Name: Car;) tl { 'lJe..s 1­

. Date: . /-.9.5 ~o tAnalysis Type: ----I/-'?-:..,.;/:....;2;;..0-=2._____ f' 10 I 


Run 1 

Type Identification Final Tare Net 

Number Weight Weight Weight 

Filter p /1~ J ;..&01 ~ c;l. ·t,ort(; .(}OoJ 

Probe Rinse ( ml) B LII> Z to 'J. IS" ::(,) , '6. IS S.'-/ .. DOI~ 

Front HalfWeight ,OOlll 

Organic ( nil) e.. ti7l/ J to, .V¥b l /0{g. fJt{S l • oot \) 

Inorganic. P L//~·7 IJD.1 hlf;;. 130.~l.o31- . ohiO 

Total Net Weight /},OO3~ 

R'Iln2 

Type Identification Final Tare Net 

Number Weight Weight Weight 

Filter p /1& z. J<. 'o8Lj ~. &DBLf ~ f}O(J iJ 

Probe Rinse ( nil) B l/1:J3 7«. 0 -:). "t' 1S. o-=t-tJJl{ ~ oat) 

Front Half Weight .00/3 

Organic ( nil) <: (.jJ'/t/ !OI.'1Jc,,;). I0 I.43.L}'1 •. 00(1 

Inorganic p '-111-0 l:t'/. 1J ~tl 1'1- to .32;JG:, ,,(0 ).:2­

Total Net Weight 0,00'1$ 

Run 3 

Type Identifica.tion r:· Final Tare Net 

Number Weight Weight Weight 

Filter p 1'"1-&3 2. {,:J-1J J. &>;)10 " (JOO5 

Probe Rinse ( nil) B .L/ f '3 </ 7-~. l-1-YO t to. r=r ~ lb' _.0 oj?... 

Front HalfWeight ~ OOfS" 

Organic ( ml) (, L/1t{S 10;1,/100 I.01.·/~94 ~ooe" 

Inorganic D '-Ir+ ( /3'1. 1./1 t). 131-. 43ytf 001] 

Total Net Weight .(), OOJCf 

Identification 

F= 3 inch filter P 47mm filter B ";' 150m! Beaker C 250ml Beaker . D = 400ml Beaker 
- - -

--- ---

FINAL WEIGHT 

WEIGHING SHEET Ej> /0 I 

Time 

Date 

Analyst 

IDNo. 

I..!IJ'-

LIt») 

I,/(JV 

t- l.fj 

LjJ VI.( 

J,J tl5 

l//I,p ~ 

1-)1 TO -

l-/Irl 

Check Weight 

Check Weight 

Check Weight 

Run 

1 

Weighing (grams) 

234 5 

Average 

Final 

Weight 

~C 

=E-=== 


-'- S-­

Tare 


Weight 


Net 


Weight 


COMPREHENSIVE 

EMISSION 

SERVICES 
TARE WEIGHT 


WEIGHING SHEET 


Time I S ~3D 

Date I~· 1\·6Cn 18-18-~ 

Analyst II\'\ I /11. 

Weighing (grams) 

ID No. . 1 ··2 3 

'2.<'0 tJ38 

L,~ 

'Z. .4>'Z?.~ 

'1.-.~ 18e 

). (q ZS:7 

.~ 27L.l 

cftJ 2'23 

.(C~( 5 

Check Weight. O.;:>S 1.. I :;). J,..:;> 5"'1. 

4 5 

C CoMPREHENSIVE 

....' =- E EMISSION 

S SERVICES 
TARE WEIGHT 

WEIGHING SHEET 

Time I . !S6 7 ~ tz. . Date . 11--1 :-()~ Il~ 8"Of:; 

Analyst /J1.A I/;tfl -,:­

Weighing (grams) 

ID No. l1 I' 2 I 3 4 5 

Check Weight 1wO. O/2. 

~ C COMPREHENSIVE 

. E . EMISSION 

S SERVICES 
........--. 

TARE WEIGHT 

WEIGHING SHEET 

Time 

Date 

Analyst 

IDNo. 

1 

Check Weight 

Weighing (grams) 

2 3 4 5 

Average 

{DO. 57-V; "Z­

/01. 

CoMPREHENSIVE 

EMISSION 

SERVICES 

... ,••,.,_ ..__ ~.~~__' ____•__•___.............. _________.._.. "w_._.__ ..___...... 

~ 

~ a

rI) 

ff3 § ~ ~ ?11 ~ 

~rT~C/j c.S~ 

IIIIIII~I~ 

~IIIIIIIIIIIII 
Appendix C 


Field Data Forms 

Run No. 1, assumed 10mg 

Location: Cargill West (EP 101) 

Date: Jan.24,2007 

. Project # 407 

% 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::: 


Vet Molecular Weight= 

Sampling Time (Minutes):::: 


Nozzle Diameter(lnches)= 


stack Round or Square= 


Stack Dimention A (Inches)= . 


St';c~ck Dimention 8 (lnches)= 


Equivilent Diameter (inches)= 


Stack Area (Square Feet) = 


Pitot Coefficient:::: 


Average Square Root of Delta P (inches H20)= 


Stack Velocity (Actual, ftlmin)= 

. Flow Rate (Actual, Cubic ftimin)= 

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 (lbihr)= 


Particulate Loading - Total Catch Including Impingers 


"'articulate Weight Net (g)= 


,-'articulate Loading, Dry Std. 68 Deg (grJscf)= 


Emission Rate (Iblhr)= 


Percent lmpinger Catch= 


99.2 

446.700 

511.636 

1.004 

0.005 

65.196 

64.023 

29.50 

0.00 

29.50 

21.00 

0.00 

1.0 

0.1 

72.3 

1.61 

1.5833 

33 

28.84 

28.83 

90.0 

0.160 

Round 

6.no. 

6.06:. 

6.n 

0.20 

0.99 

1.2545 

4,849 

952 

1,005 

0.0018 

0.0004 

0.004 

0.0100 

0.0024 

0.021 

82.00 
Run No. 1 

Location: Cargill West (EP 101) 

Date: Jan. 24,2007 

Project # 407 

% 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 Diqxide= 


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= 


Vet Molecular Weight= 


Sampling Time (Minutes)= 


Nozzle Diameter(lnches)= 


Stack Round or Square:::: 


Stack Dimention A (Inches)= 


Stack Dimention B (Inches): 


Equivilent 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. 68Deg (grlscf)= 

. Emission Rate (Iblhr)= 

Particulate Loading - Total Catch Including Impingers 


'articulate Weight Net (g)= 


rlarticulate Loading, Dry std. 68 Deg (grlscf)= 


Emission Rate (Ib/hr)= 


Percent Impinger Catch= 


99.2 

446.700 

511.636 

1.004 

0.005 

65.196 

64.023 

29.50 

0.00 

29.50 

21.00' 

0.00 

1.0 

0.1 

72.3 

1.61 

1.5833 


33 


28.84 

28.83 

90.0 

0.160 

Round 

6.00 .'..... 

6.00 

6.77 

020 

0.99 


1.2545 


4,849 


952 


1,005 


0.0018 


0.0004 


0.004 

0.0038 


0.0009 


0.008 

52.63 
Run No. 2, assumed 10mg 

Location: Cargill West (EP 101) 

Date: Jan,24,2007 

Project # 407 

% 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 Oeg)= 


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= 


Vet Molecular Weight= 


Sampling Time (Minutes)= 


Nozzle Oiameter(lnches)= 


Stack Round or Square= 


stack Dimention A (Inches)= 


Stack Dimention B (Inches)= 


Equivilent 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 Oeg (grlscf)= 


Emission Rate-(Ib/hr)= . 


Particulate Loading - Total Catch Including Impingers 


[ "'articulate Weight Net (g)= 

" -·,"Particulate Loading, Ory Std. 68 Oeg (grlscf)= 

Emission Rate (Iblhr)= 

Percent Impinger Catch= 
Run No. 2 


Location: Cargill West (EP 101) 


Date: Jan.24,2007 


.oroject# 407 

% Isokinetic= 99.5 

Initial Meter Volume (Cubic Feet)= 512.000 

Final Meter Volume (Cubic Feet)= 576.435 

Meter F actor= 1.004 

Final Leak Rate (cu Ftlmin)= 0.004 

Net meter Volume (Cubic Feet)= 64.693 

Gas Volume (Dry Std Cubic Feet 68 Deg)= 63.296 

Barometric Pressure (in Hg) = 29.50 

Static Pressure (Inches H20)= 0.00 

Stack Pressure (in Hg)= 29.50 

Percent Oxygen = 21.00 

Percent Carbon Dioxide= 0.00 

Moisture Collected(ml)= 5.0 

Percent Water= 0.4 

Average Meter Temperature (F)= 74.2 

Average Delta H ( in H20)= 1.61 

Average Delta P (inches H20)= 1.5742 

Average Stack Temp (F)= 36 

Dry Molecular Weight= 28.84 

Vet Molecular Weight= 28.80 

Sampling Time (Minutes)::= 90.0 

Nozzle Diameter(lnches)= 0.160 

Stack Round or Square= Round 

Stack Dimention A (Inches)= 6.00 

Stack Dimention B (lm:;hes)= 6.00 

Equivilent Diameter (inches)= 6.77 

Stack Area (Square Feet) = 0.20 

Pitot Coefficient::: 0.99 

Average Square Root of Delta P (inches H20)= 1.2430 

Stack Velocity (Actual, ftlmin)= 4,821 

FIO\AI Rate (Actual, Cubic ftImin)= 947 

FIO\AI Rate (Std, Dry, Cubic ftlmin 68 Deg)= 991 

Particulate Loading - Front Half 

Particulate Weight Net (g)= 0.0013 

Paticulate Loading, Dry Std. 68 Deg (grlsc1)= 0.0003 

Emission Rate (Ib/hr)= 0.003 

Particulate Loading - Total. Catch Including Impingers 

"larticulate Weight Net (g)= 0.0048 

·rlarticulate Loading, Dry Std. 68 Deg (grlscf)= 0.0012 

..':: Emission Rate (Ib/hr)= 0.010 

Percent Impinger Catch= 72.92 
Run No. 3, assumed 10mg 

Location: Cargill West (EP101) 

Date: Jan. 24,2007 

Project # 407 

% 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: 


Vet Molecular Weight= 


Sampling Time (Minutes)::: 


Nozzle Diameter(lnches)= 


Stack Round or Square::: 


Stack Dimention A (Inches)= 


Stack Dimention B (inches)= 


Equivilent Diameter (rnches)= 


Stack Area (Square Feet)::: 


Pitot Coefficient= 


Average Square Root of Delta P (inches H20)= 


Stack Velocity (Actual, ftlmin)= 


Fiow Rate (Actual, Cubic ftlmin)= 


Flow Rate (Std, Dry, Cubic ftlmin 68 Deg)= 


PartiCUlate Loading - Front Half 


Particulate Weight Net (9)= 


Paticulate Loading, Dry Std. 68 Oeg (gr/scf)= 


Emission Rate (Iblhr)= 


Particulate Loading - Total Catch Including Impingers 


'Jarticulate Weight Net (g)= 


c'articulate Loading, Dry Std. 68 Deg (gr/scf)= 


Emission Rate (Iblhr)= 


Percent lmpinger Catch= 


99.8 

576.900 

640.627 

1.004 

0.007 

63.982 

62.669 

29.50 

0.00 

29.50 

21.00 

0.00 

10.0 

0.7 

73.6 

1.58 

1.5625 


41 


28.84 

28.76 

90.0 

0.160 

Round 

6.00 

6.00 '. 

6.77 

0.20 

0.99 


1.2375 


4,827 

948 

978 

0.0015 


0.0004 


0.003 

0.0100 


0.0025 


0.021 

85.00 
Run No. 3 

Location: Cargill West (EP 101) 

Date: Jan. 24, 2007 

Project # 407 

% Isokinetic= 

Initial Meter Volume (Cubic Feet)= 


Final Meter Volume (Cubic Feet)::: 


Meter F actor= . 


Final Leak Rate (cu FtJmin)= 


Net meter Volume (Cubic Feet)= 


Gas Volume (Dry Std Cubic Feet 68 Deg)= 


Barometric Pressure (in Hg) = 


Static Pressure (InGhes 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= 


Vet Molecular Weight: 


Sampling Time (Minutes)= 


Nozzle Diameter(lnches)= 


Stack Round or Square= 


Stack Dimention Po (lnches)= 


Stack Dimention r.1:·(lnches)= 


Equivilent Diameter (inches)= 


Stack Area (Square Feet) ::: 


Pitot Coefficient= 


Average Square Root of Delta P (inches H20)= 


Stack Velocity (Actual, ftlmin)= 


Flow Rate (Actual, Cubic fUmin)= 


Flow Rate (Std, Dry, Cubic ft/min 68 Deg)= 


Particulate Loading - Front Half 


Particulate Weight Net (g)= 


Paticulate Loading, Dry Std. 68 Deg (grlscf)= 


Emission Rate (Iblhr)= 


Particulate Loading - Total Catch Including Impingers 


"?articulate Weight Net (g)= 

\ ..•jarticulate Loading, Dry Std: 68 Deg (grlscf)= 

. Emission Rate (lb/hr)= . 

Percent lmpinger Catch= 

99.8 

576.900 

640.627 

1.004 

0.007 

63.982 

62.669 

29.50 

0.00 

29.50 

21.00 

0.00 

10.0 

0.7 

73.6 

1.58 

1.5625 


41 


28.84 

28.76 

90.0 

0.160 

Round 

6.00 ..., 6.00' 

6.7.7 

0.20 

0,99 


1.2375 


4,827 

948 

978 

0.0015 


0.0004 


0.003 

0.0034 


0.0008 


0.007 

55.88 

I 
COMPREHENSIVE 

EMISSION 

SERVICES 

Project Number . Project Leader --'---ri--:--------­

w 

L/0 7- .fVl.l'''1, 

Meter Operator --'-___________ Run Number.,.,..-"'"t"..----------:" 

Date t). 4-[J t Lab Person _.__--::'~-------

Support Personnel -1.-1--'-.,",-D_~___________ SampleTYl" rY1 n[&0 J-


Plant (,<'11"5 Ii \ tv';) 
 Lo~on ___tG~~e_~/O~\_________ 


J 

Assumed Moisture % A /" Meter Number _4_'__ . ..-" 

Minutes Per Point (min.) Oven Number J 

. Sampling Time (min.) _~.L.,1J;::...-_ Umbilical Number j.,() 0 

Meter Factor Y I·() tJ t/ Pitot Number --,-1-;.11__ 

Meter AH@ l,:} 'Y 3 Probe Number ....It~'1__ 

Pitot Coefficient Cp ,q1 Probe Length ---" J/ 

___ 

:d 

Stack Axis 1 (inch.) --lO~~__ Nozzle Type ---£.)...:;>__ Schematic ofTesting Location 


(, 1/ 


J....1r I 

c:..fijeUW 

6~~·p 

Stack Axis 2 (inch.) --=:...--...,,~ 1, (0 

Barometric Pressure (in. Hg) 

. if fJ) Static Pressure (in. HaD) ______ 

• {(,.,U Nozzle Diameter (inch.) _...!..-___-,...._ .-...;:..... 

Initial Meter Volume (ft3) ¥I{~ .-:.{o 0 

Final Meter Volume (ft3) 5 I;" 3 6 

Leak Rate Before " tJ-P 't CFM@ ;c: 15 in. Hg 

Leak Rate After "Od r CFM@ ~ in. :E!g. 

Pitot Leak Check t:;..­ Before 1/: After 

RECOVERY DATA 


Orsat Impingers 


Trial %C02 %C02+%02 %02. 

1 , \ .~. 

2 .~ , !n \e,,~"\. \ 

3 ~~\ 

Avg " I. 

Final Initial DifferenCe 

Impinger 1 <1> /0 tJ -5 

Impm,~er2 loG> fllO ~ 

Impinger3 ide:> j()1> <5 

Impinger4 87{P .~:pl; {p 

Impinger 5 

Iinpmger 6 

Impinger7 

. Condition/Color Total C1vJ,.)r/ I

Notes: .. Filter Number: P Jtt/ 

.0 1 
Field Data Sheet 

/

Run No -------;--=--- ilO'r 

ProjectNo. --1-'-----­

Location ,tZpic t 

1-)1-- D-q Date W. 

Operator 1/: >3:z. 

Start Time ~-----

Stop Time --L:...:...L.J\,l----­

'N°!f 

C = COMl'REHENSM 

,=. E = EMlSSIO:N 

S~ SERVICES 
- -- - -- --

- --

-,"c --­ - -- COMPREHENSNE =E=­ EMISSION 

S SERVICES 

L!01­ Project Number___.t..r._______ Project Leader ---lJV1~._tV1_\_._______ 

RMNumber___1 ________________ All, IiI.}. Meter 0perator ---!.III_________ 

Date ]-' ~ 1-\-, t) "1- lab Person ___--,.________ 

,AI!\1/:;.oJ.. Sample Type ( v l f'i' Support Personnel ----.;,_,_0_-________ 

Plant L4fj!-H Ve~A C,i.. 

"Location t:eII) t 

Assumed Moisture % 

l' 

Meter Number _...:.(__ 

Minutes Per . Point (min.) _,_J_ "1 -- Oven Number ' " --­ I 

Sampling Time (min.) qJ Umbilical Number J.0;:/ 

Meter Factor Y j.. (l R Pitot Number -.!.:!U:..L-__ 

Meter tlH@ ), 11J Probe Number -'-.,M__ 

Pitot Coefficie~t Cp ... 1t Probe Length -17­

Stack Axis 1 (inch.) Ii Nozzle Type J Schematic ofTesting Location 

/ II 

StackAxis 2 (inch.) W n f"'j 

B arometric . P (' Hg) pA.-/f, .J t ressure m. ____ 

Static Pressure (in. H;zO) t t.{ 'b 

Nozzle Diameter (inch.) _.·...t./-'G""--=-o___,: ;.' 

Initial Meter Volume (ft3) ::;/';z. -0 t? c.I 

Final Meter Volume (ft3) 5f" t./ J) 

~~.Rate Before . ~ 0 0 3 CFM@ ~ 15 

Leak: Rate After • a t.? t.f CFlVr@ 7­ in.H~ " 

hi. Hg I 

Pitot Leak: Check ~ ....Before /" After v 

Orsat Implngers 

Final Initial Difference 

Impinger 1 (1)' ItJcJ .--" 

- ./ 

Impinger2 Ibd IOU /)

..... 

Impinger3 10 cJ !()u 0 

Impinger4 51j ?-.. 7-fl. fo 

Condition/Color Total :;,­

Trial %C02 %C02+%Oz %02 

1 ~. "­

2 I~ A\)\~\ 

3 / 'Vi 1­

Avg 

flIt.;) Filter Number: 
Field Data Sheet 

RunNO_~-------------- Project No. . "l 

. Location <!;.v!0[~Ij1ele 

Date Im___

M·wJ Operator----=-----­

Start Time i d- ; i) '6,--'____ 

Stop Time 1/1./ l ---'_l-_____ 

Nc \, 

C = COMPREHENSM 

=. E _ EMISSION 

S~ SERVICES 
- - - -

-c - ,. --­

-­ -

- ---- COMPREHENSIVE 

--

=E=­

- EMISSION 

S SERVICES 

Project Number--.:::--________ '-101 _ ~{a1,

Run Number___________ 'J _ Meter 

Project 

Operator 

Leader --:-r-r-------­

.....:-/1;.....;1...,:.WL..::....ol.._________ 

'j- ;} r1- 0--::::;' Lab Person ___---,,,-_______ Dme~~_____~----------

Sample Type (11:J /;;',0 L Support Personnel _:foL-'_0________ 


Plant (~rj ! 'II VV.u +- L.~ 

Location Efe luI 


.. I . 

Assumed Moisture %. Meter Number ~ Minutes P~r Point (min.) q,S .Oven Number -- '. 

Sampling Time (min.) i () .Umbilical Number ?-C>t)J 

Meter Factor Y I, {) V Y Pitot Number !;J!? 

Meter aH@ /. r:J '2f '3 Probe Number _1_.4....,.-_ 

Pitot Coefficient Cp , q C; Probe Length 3 I 

Cd 55 StackAxis 1 (inch.) Nozzle Type ---::;-.:...__ Schematic ofTesting Location CIJ 

Stack Axis 2 (inch.) ---.,;.-__ 

;Zq'JiJ Barometric Pressure (in. Hg) 


Static Pressure (in. HP) t q8 
 . ',,­

N ozz.~I D'lametW (.me. h) __• 1M .: __0 _

. 

Initial Meter Volume (ft') S-:76v qtJO . 

Final Meter Volume (ft') h Clf!)·" J.. '} 

Leak Rate Before 

Leak Rate After D 

.. qoJ CF14@ 

{) 01CFM@ .,-7.. 

<! 15 i:::.1!L 

';;:'Hg 

Pitot Leak Check t"......···Before {/ After 

RECOVERY DATA 


Orsat Impingers 


e 1:](. J 

Trial %C01 %C01+%O:z %02 

1 t 

2 ,j 'hl'e(\ 7 

3 1'TV Ie/" 

i\.vg. 

Finai Initial Difference 

Impinger 1 9;­ /tJJ -r 

Impinger2 /0 0 i tJO 0 

Impinger3 / t,7 D li10 {/ 

Inlpinger4 ].10 (;15 15" 

Condition/Color Total 10 

Notes: Filter NUlilber: 
Field Data Sheet 

Run No __J______ Project No. -----­

Location (c.lr~F It We,:>+- C, -A .. 

Date 1-),t./.-07­

jI/l ,vV-' Operator--.:..-----­

Start Time _;Z_~-,O_q____ 

Stop Time ~~...::----

I 

[ 

! 

j 

COMPitEmlSlVE . 

EMIssiON· 

SBRVICBS 

I 
prel.lm.inary Velocity 

P:ant ProJeot No. . , ·l~)-!./·-o t 


Date ~/"J lo.cation (.::; tJI (I G',2,) r 

. stack t.D.---------­ . 0 ({ P/tot Cp ~. I ( .--""~' 

Stallo Pressure In HP '~'q cD 


Barometer Pressure In. Hg,~ :t .. J 


Start Tlmae__.-:---:------­


Stop. Trme9-_...,---'--~---

. Operators 

. SCHEMAT[COFTRAVERSSPOiNT!.AYOvr 

FInal Pltot, Le'~ Check at :::-$" HlP' P I F 

TravsCS6 Velo~ty ,staok Oyolonlo Ftdw 

Point Head Tem~; DaTen1'!!na'l!on .. 

NUmber AP . QF AP at.Q<' Angle. Wtilof.\ ' ,In. HaC R'ererenca Y1ekIs1\\ N'uu. 'J:,p 

III ;Jw 0 1'7i .

,. /) 2.2. Qg~ "t­

,J 'J,1 Q''1 

l( 1.1/ :2~ 

)' I, } :l~ ... 

.G .'1:Z. :?-1 

'5,r /. . '-.

~ ~'1 

:J. 1~5- . ;Z'b 

J I ~ I ; ,~~ 

i( /vS' ~~ 

S J,:~ i ;;·:1 

l; 1- 5~ 1):.% . 

Note&: 
Total Number of POints(B, 12, 16,20,24)= 12 EP 101 

Stack Diameter or LengthOnches)= 6 

Round Square 

'oint Distance 

1 0.3 1 0.3 

2 0.9 2 0.8 

3 1,8 3 1.3 

4 4.2 4 1.8 

5 5.1 5 2.3 

6 5.7 6 2.B 

7 3.3 

8 3.8 

9 4.3 

10 4.8 

11 5.3 

12 5.8 

If stack diameter is less than 24 inches each. point must be greater than 0.5 inches from wall 

if stack diameter is greater than 24 inches each point must be greater than 1.0 inches from wall 

( . 
() 

c:9 

() 

() 

0 

0 

{} 

(} 

V 

0 

0 

0 

0 

0 

0 

d 

b 

. 	 EP}\ 

\'ISIBLE EMISSION OBSERVATION FORM 1 IFoImN\Ji:ri:)Q1 Ie.1~N I I'I I~f 01 2... ] 

!··~Q1e~OSA . 	2Il3!" Oher. 	 J L....CC!"llnlJed __ OO_IiI!O_._Fam_~_. _____---1!_,-LI-..LI---LI---LI~-,J

CJ 

2 :0 :I 

, ( 

1 -

IJ""'~ 

water. Clr()!:ial P\lJmIt 

End 0 D!llaohed 0 None 

1 I. 

I-End I I 

1 { 

End 

RH Ferl::ent ~ \ '---...~";J . 

. 	12 

13 c) 

14 .C) 

15 () 

.16 \) 

l7 0 18 0 

19 0 .....":;.; 

'20 . 

fRlNDMN 

~ 

Of ::M.­ 0 

. 1 

200 fEEl t ~ I Skit...... 

~ 0::=: ~\J!1\8 

&.<> -EfT 

.('I :"-ex .tV e. I 

VEOF1.l 

tmlVNclihArrr1H 21 

25 

26 

27 

28 

29' 

30 
EPA 

VISIBLE EMISSION OBSERVATION FORM 1 

IMelhoci Vied ICroie ens) 

Melhod9 20M I I I I I I 

CcrnP"l'lVNane -

. S 4. {lVl.e" c:? < ;:::-rc:; i<v tFaoIIIYN<:!me 

$!)$t~ 

Cit{ IStm t

P 

\\ , RIlCeS$ \ 11IrIt# Operallng Mod& 

Icontrc:I~ Ope!allng Mode 

anJIIiIC:n Font 

I 

HElilnof Emllll. f't. Hellnof Em\sI1, PI. Rei. to OI:lGeM!t 

stat End stat End Il!IIalOa III Iin"ist. pt, OI!eonon III EmIoo. PI. (Dsgreecl 

sat End SIal End 

Describ& I'lume IIOCt{jJOUnd.

- en<! ~t:dcr aky Condltlro 

SIal End SIal End 

Wlnd.Speed 'MndIlract!or\ 

SIal End stat End NnbIentTemp. wat IUb Terrp. IAIl Percent 

stat End 

Ot _1m 0 

I _lifT I • I 

-,.,.. 

ObsEIrvation Dole 1inoZona lSlatllme I

Endtrna .. 

.~ 0 15 30 45 ComrnecIIs 

1 0 0 (') 0 

2 ·cD 0 0 () 

3 () 0 (9 0 '. 

" ~ 0 0 () 

I> D 0 0 c) 

6 0 0 () 0 

7 0 0 0 cJ Q 0 0 (,) D 9 0 C 0 D 10 0 C 0 0 11 () C) 0 U 12 0 " 0 C) 

13 0 ~ 0 0 14 0 0 ,() 0 

T5 0 0 0 () 

16 0 C 0 0 

11 .0 C e, () 

T8 0 0 c) c9 

19 " 0 0 0 

2Q 8 .() () 0 

21 ([) 0 d 0 

22 " 0 0 U 

23 0 0 c? () 

24 . 0 0 0 CJ 

25 0 0 C) 0 26 0 C) (9 0 27 C 0 0 0 

28 0 0 l\ 0 

29 Q 0 D 0 

so 0 0 0 d 

lCA::loelve($ Nane (l'JInI) 

CA::loeIve(,~ 1tkl1e 

~By 1tkl1e 

VEOF1.1 

I 

EPA 


VISIBLE EMISSION OBSERVATION FORM 1 


l~1MA alSB Otler. : I 


! • End 

\ , End 

wetPJb TEI/Tl). IiH _ 

~-t.O'-W::_E!;!.!Snd'--'_'_----'L.....-_....... L....-_-1--___..,.J 

Dl u_ n 

I ;;;i ~""fEET I ClI:isslva!'a FOOtton t ~ 

1tIit_ . 

140· ~ a:::::: - - - ~ - - - - - ;;~Un; - - - - - ~ • 

VEOF1.1 

0j~"-()7- 1Im,ZCltl~ iiIaI"lhl& lEndTI-n. e~ ~/CI I I:; .' 27.- It. z.'- ' ~ 0 15 3() -45 Commenfil 

1 . eJ 0 !J 0 

2 gt% (;) 0 

a () 0 

4 0 0 0 0 6 0 () D .0 

6 0 0 0 0 - .. -,-' -'0 '-U'1-0-' t? .-. ._._--_. 

8 D D 0 0 9 0:0 D- O 

10 () 0 0 0 

11 0 0 0 0 

12- 0 0 0 0 

13 0 0 d 0 14 0 0 0 0 . 15 0 0 0 0 . 16 0 0 0 0 

17 0 0 0 0 

IS 0 D 0 0 19 Q ·0 0 0 20 0 0 D 0 

21 D 0 0 0 

22 V V 0 0 23 0 -0 () {) 

,24 0 C 0 0 25 :> o 0 () 

26 0 

~g 0' 

27 U f) 

I 28 0 0 

29 0 D b D 

30 D C> D 0 

. 

..:;.,.. 
EPA 

VISIBLE EMISSION OBSERVATION FORM 1 .~~ [i?~1 W- ::2-~ "2... te!t1l:=i;lcle~ 2OOB· Oller. I· '-~_. _Of\_'\IEO_Fam_~ ________-.l..I--LI--l.I---JII--IL........J .' 

canpcnyNcrne 

-54~ FacIllyName 

1. Slreet~ 

CIt\' 

Ii 

Pr<lOe8$ VI 

C<:nlJOI EqJp-nen! 

DIsta10G 10 El!'/s!. Pt. 

SICr! . End 

De&alb& Plume Boo):g,OIHld 

Il\Im 

IIoo~CdQ' 

SIc!f End WInd.~ 

SIc!f End 

I\ml:lentTEifT1l). 

Slat End 

VEOF1.l 

;:(J J(«P\. I . 

ISlate I~ 

I

Urit 

# OpetQl[jg Mode 

0pe1a!ng Mode . 

""" Ill!<\'Ccn<I1Ions 

Slat· 

Vlnd llIeclton 

ISIat 

IweTIIJPTemp. 

.­ ............... , .. - ., --, . , 

End 

End 

IRH Peroent 

Of _FEET D 

I~_FEET .1 

-..,... 

I 

ObsaniOlk:ii 0c:I!a 

~ 0 15 

1 0 () 

2 (:) (() 

3 0 0 4 t9 0 Ii 0 0 6 0 0 7 0­ r:) 

s· 0 tI 

9 () 0 10 <!) 0 

11 .() D 12 V C> 

13 0 0 

M 10 0 15 6 0 16 0 (j 

17 0 0 18 (J U 19 0 0 

20 0 0 21 0 0 22 0 0 

23 V c) 

24 () '0 2S 0 rJ 26 t7 () 

27 tJ 0 

28 0 0 

29 0 () 

ao (!) (::) 

Cb!eMll'S Na'na (P<Inll 

Cl:lIeIItef.~e 

IQlIIII!eCIIlV 

lImaZOIl& Sltr!1ImI! IEndlhla 

30 45 ComrTlEilIs 

0 0 

e 0 

0 0 

D f) 

{) 0 

0 0 

a & 

tJ 0 

tJ () 

() 0 

0 0 

(') CJ 

0 cJ 

0 C) 

() <:::; 

0 0 ; 

0 0 

0 0 

0 O. 

0 0 "':-r 

0 0 

0 0 

0 0 

0 C) 

(}J 0 

0 0 

{) 0 

C D 

t) D 

d ~ 

I

Dae 

I

Dae 
Form 

Source Lciyout slistoh 

, , 

, r 

Of ~4m n 

"[~er ( 10 "I

.--I Iij.- -~"-~. --.". s~:~d)--- ----- ~ a;= W.nd ---..:... 

VEOFl.l 

IJ:'1'Por ~:tf4f stalTil( II IErdTma 1$.'/1 

Mil I} 15 30 I 45 CorrmImIs 

1 0 0 0 0 

2 0 0 0 0 

3 0 0 0 0' 

4 () 0 0 0 6 0 0 0 0 

6 {) 0 0 0 

.z " .0 :0 " 0 : .0- -. -~."'.-.'" ~." . 

a to 0 0 D 9 0 0 0 '0 

Hi a b () 0 

n 0 0 0 (\ 

"ill C> 0 0 (') 

19 e v 0 14 0 0 0 0 15 0 010 0 16 0 0 0 0 

D () 0 0 

0 0 c 0 

0 0 G" o. 

20 0 .. 0 cr- - 21 0 0 0 

22 C) 0 0 0 

:23 () 0 () 0 

114 (9 () () 0 

~ 0 0 0 

0 0 0 

0 0 0 

llIl 0 .J2jo 0 29 0 0 0 0 

30 0 0 0 0 

'," . '. 
I

EPA 


VISIBLE EMISSION OBSERVATION FORM 1 

MBlhod Ihed (Ct'eI& Onel I L.~M~~~9___·~2~=-__~2~~B___~~.~======~==~ 

Ca1\paIIYNane 

e 

fSI!'>E'Ikttess 

Cily 

!DeIciIb<> EmI!s!Cn I'Ol1I 

HE!gt 01 EmIis. 1'1. 

Slat . 

DIsIct1e&Io En1e1. Pt. 

stat 

-S41X1L 

\ 

\~ 

End ' 

End 

12.1 Fr/.J -vI· ' ., 

r

ci9 11lP 

1IeIg,tor EmJs$.1'I. ReI. 10 0b00Nar 

stat . End 

IlI!eeIIon It> imIl18. PI. (Oegr&a<} 

mat End 

I 

, 

!lmw.NQ1hAlro.v 

DlN DuN 

·0 

x ClboeMJtICln ~ 

I 

Of _I'm 0 

1 

__ I 

. ~ 

--­

. 

ObseNo1Ion Da\l!l 

i~ 0 T5 

1 6 CJ 2 c9 (F 

3 () (!) 

4 ~ ()

rn D 

" 0 t!J 

7 () ·0 ·....s..· .. '0 TO: 9 0­ 0 

TO 0 0 

IT 0 0: 

12 V 'f)' ' ' 

14 

15 (J 

16 0 \J 

17 19 V 18 f) () 

19 [) (9 

~n (:) [) 

21 o (] 22 m 23 0 O· 

24 0 () 

~ 0 '0 26 0 0 . '27 0 0 28 D 0 

'il9 D 0 

30 0 0 

a:.seoveIs Na'"ne tl'!In!I 

CbeNe/c $1gl6tI..re 

<Agan11£llloo 

C«tIl!ecIB\' 

!1lm"Zone S!a11lmG I~r"", 

, ~O' 45 COn'Vl1eI1l! .' 

CJ 0 

<.9 '0 

0 ~ 

C) () ;i{:H 

lD 0" ,". 

-'. 

0 () 

<9 0 .. 

"·0 ",6" ..'""-- ,­ ',': '.' .: .... ::~:-,'-

0 0 

0 0, ".­

() 0 

() 0 , 

0 0 

0 0 

~ V 

0 If) 

0 D , 

() '15 .. 

(:J O· 

17 0 , ", -,:..... 

0 0 

0 0 .. 

0 Q 

0 (j 

(] 0 

0 0 

0 a 

0 tJ 

0 0 

(J 0 

IDcie 

1~ 

VEOF1.l 
{ . 

AppendixD 


Pretest Calibrations 

Meter Calibration 

Operator 

3.te 

Meter Number 

Previous Y Factor 

Meter Volume 

Final 

Initial 

Net 

Meter Temperature 

Inlet 

Initial 

Final 

Outlet 

Initial 

'Final 

Avg. MeterTemp 

Time 

. ~eter DE;llta H 

Jarometric Pressure 

Room Temperature 

Initial 

Final 

Avg.ROMl T!3mperature 


Pump Vacuum 


Vcr (std) 


Vm (std) 


YFactor (brackets) 


Delta H@ 


+/- 2% Criteria , 


Bracketing Percent of Y 


Average Y Factor 


Average Delta H@ 


D.L ORIFICES: 


Jan. 10,2007 Orifice No. 1 Low 15 


K Factor 0.4146 

4 Orifice No.2 Mid 20 

1.007 K Factor 0.5311 

Orifice No. 3 High 	 23 

K Factor 0~6181 

ORIFICE 1 Low ORIFICE 2 Mid ORIFICE 3 High 

Cubic Feet 295.123 300.651 306.249, 

Cubic Feet 289.800 295.200 300.700 

Cubic Feet 5.323 5.451 5.549 

*" must be greater than 5 cubic feet 

Deg. F , 58.0 ' 60.0 	 61.0 

Deg.F 60.0 	 61.0 62.0 

Oeg.F 58.0 59.0 60.0 

Deg.F 59.0 60.0 61.0 

Deg.F 58.8 60.0 61.0 

sec 600.0 480.0 420.0 

inches H2O 0.87 1.50 2.00 

inches Hg 29.18 29.18 29.18 

Deg.F 59.0 59.0 60.0 

Deg.F 59.0 60.0 60.0 

Deg.F 59.0 ".- 59.5 60.0 

'inches Hg 20 	 18 17 

dscf 5.310 	 5.439 5.537 

dscf 5.293 	 5.416 5.510 

1.003 	 1.004 1.005 

1.732 	 1.822 1.794 

0.09 0.07 

PASS PASS 

1.004 Must be between 0.98 and 1.02 

1.783 
- - - - - -

METER CALIBRATION WORK SHEET 


Operator: ...:b~,L_,-'--___ y Meter I.D, ~~___ ___ 

I ­ \ o .... bl 

Date: -!...----!.I-----­ K Factor No.1 .....;If.'--Y--!....IL-Yu(o:::.--___ 

Previous Y Factor J # r.;o1 K Factor No.2 ---IL.1...:::5'::....:3::::;..·..!..!.11____ 

Leak Check K Factor NO.3 _"_Lu_._\..:::..8....:..\-,..___ 

METER VOLUME Units 

Final ft3 

Initial ft3 

Meter Temperature 

INLET 

Initial OF 

Final of 

OUTLET 

Initial· of 

Final of 

Time sec 

.:.c 

Meter LlH in.Hp 

Barometric Pressure in. Hg 

Room Temperature 

Initial' OF 

Final OF 

Pump Vacuum in. Hg 

1 Low 2Mid, , . 3 High 

;:zq5~ i~3 -=< 01) fo5"/ "} OC:" ';2tt q 

2~q. Bto ;z..o,S- :leO 300.7(fiJ 

5~ ~O (,., I 

(gD Col (0:2 

S'2S' ,~9 (L7D 

S1 .Coo , tol 

'00 '-180 420 

~87 ' ItS 2..0 

:2 ~t I/J ;l-l), I 1< -:;1. /g 

SCf S-q ·7nO 

SCJ {PO ~O 

:2fJ if: 17 

:..c·= - .- COMPREHENSIVE E= EMISSION 

-- S -- SERVICES 

." .~.: 
( 

AppendixE 


Post-test Calibrations 

Meter Calibration 

Operator T.O ORIFICES: 


'ate Jan. 25,2007 Orifice No. 1 Low 15 


K Factor 0.4146 


Meter Number 4 Orifice No.2 Mid 20 ' 


Previous Y Factor 1,004 K Factor 0.5311 


Orifice NO.3 High 23 

K Factor 0.6181 

ORIFICE 1 Low ORIFICE 2 Mid ORIFICE 3 High 

Meter Volume 


Final Cubic Feet 646.346 652.003 657.693 


Initial Cubic Feet 641.000 646.500 652.100 


Net Cubic Feet 5.346 ' 5.503 5.593 

* must be greater than 5 cubic feet 

," 'Meter Temperature 

Inlet 

Initial Oeg.F 60.0 62.0 62.0 

Final Deg.F 61.0 62.0 63.0 

Outlet " 

Initial Deg.F 60.0 62.0 62.0 

Final Deg.F 61.0 62.0 63.0 ' 

Avg. Meter Temp Deg.F 60.5 ' 62.0 62.5 

Time sec 600.0 480.0 420.0 


I\~eter Delta H inches H2O 0.86 1.50 2.00 


arometric Pressure inches Hg 29.30 29.30 29.30 


Room Temperature 


Initial' Deg.F 60.0 61.0 61.0 


Final Deg.F 61.0 62.0 62.0 


A,vg.Room Temoerature Deg.F 60.5 61}3 61.5 

Pump Vacuum, inches Hg 20 18 17 

Vcr (std) dscf 5.325 5.451 5.551 


Vm (std) dscf 5.320 5.469 5.560 


Y Factor (brackets) 1.001 0.997 0,998 


Delta H@ 1.695 1.787 1.764 


+/- 2% Criteria 


Bracketing Percent of Y 0.22 0.03 , 


PASS 'PASS 


Average Y Factor 0.999 Must be between 0.98 and 1.02 


Average Delta H@ 1.749 

METER CALIBRATION WORK SHEET 


operato~C n Meter 1.0. ____Ll--..I·t.....-__..,.--_ 

Date: ,)6\t). ?S ?(JO 7 K Factor No. 1 _",_L-,-IJ_~....:...~____ 

Previous Y Factor. J. DOl/ K Factor No.2 __.._>:_3_1...;..')____ 

Leak Check K Factor NQ. 3 _#_cP......:·1_8_1____

METER VOLU~E Units 1 Low .2Mid 3High 

Final ff (pl/{P 13'Ito iPS'2, ()C?3 6SZ~/t3 

Initial ff u,1/L(}()6 (0 llto.SoD 4>.5 Z ,J66 

Meter Temperature 

INLET 

Initial of (;Pb &7 (;:,2 

Final of 6.'1 I &2­ ~3 

OUTlET 

Initial of (PC) &.-z CRZ 

Final of (PI cPZ (/3 

Time sec 1#00 lf8b CfZ6 

Meter aH in. H2O .... Ii tJ(p / .. t;o 2.00 I 

Barometric Pressure in. Hg ~tff36 1Jt;,3rf ct24,50 

Room Temperature 

Initial of (po &f &1 

Final of (PI uf2 &'2 

Pump Vacuum in. Hg dO /8 II 

COMPREHENSIVE 


EMISSION 


SERVICES 
i . 


Appendix F 


Process Data 

LYNX Load, wllload Detail 


Cedar Rapids West 


Facility: Cedar Rapids West, GOS 


Truck unload 


Net Wgt Wgt Cert / Customer / 

Date Trace Id SOL Grade C/P Unit Id In Pounds Quantity Til M DKT FM SHBN DEF OKG BCFM PROT For Account; of 

SELECTION CRITBRlA: 


Facilities, Cedar Rapids West, GOS 


Services: load; Unload 


Modes, Truck; Rail; Barge; Vessel 


Weights Affeoting Inventory: 01/24/07 07:00,00 AM . 01/24/07 03;45,00 PM 


Commodity I Product Types. + All • 


Commodi ty I Products, YSB 


CustOll\ers. • All • 


~ 01/24/ 30040466 310549 llSll1'IS :>543 -1 54,900 915.00 au 57.5 11.1 0.3 0.90 Tame Benton Cooperative 

~ 8:05 AM SPL. 

I 01/24/07 Jl004 0467 310550 l1SII1YS un -2 58,320 972.00 BU .58.0 9.S 0.4 0,70 Innovative Ag Services 

,1 8: 12 AM rJ.i SPL~ 

., 01/24/07 ~'a004046a noss] USIIlYS 5443 ·3 57,780 963.00 au 57,0 10.0 0.4 0,70 Northeast Iowa Coop I~. . ~. e,17 AM SPLoo 

1:: 01/24/07 930040469 310552 l1S111'i'S 1376 ·4 52,8:10 880,33 au 56:0 11.8 0.5 0.90 Innovative Ag services 

8:23 AM SPLa 

01/24/07 830040470 310553 USH2'lS 9282 -5 54,320 ))05.33 au 57.5 a:2 0.5 1.40 Marengo Elevator Company 

8:251 AM SPL. 

01/24/07 830040471 310554 USIIlYS 9759 ·6' 53,560 892,67 au 51.0 11.5 0.5 0.90 Northeast Iowa COop 

8,35 AM SI'Ld 

01/24/07 830040472 n05s5 USIHYS a837 ·7 53,860 a97,~7 5U 57.5 12,8 0.5 3.60 waukon Feed Ranch Inc 

8:47 AM Sl'L01/24/07 830040473 310556 USfllYS 3524 -a 53,180 aS6.33 SU 56.5 11,6 0.6 0.60 Northeast Iowa Coop 

8,51 AM BPI.. 

01/24/07 830040474 310557 USfl1YS 570 ·9 57,580 95,9.67 BU 57.0 11.4 0.4 1..00 Stoner Grain, Inc. 

8.57 AM SPL~ 

01/24/07 830040475 310558 USII1YS 422 ·10 60',460 l,G07.G7 Bl1 56.5 11.3 0.8 0.510 Stoner Grain~ Inc, 

lha3 AM SPI.­

01/2~/07'B3004047G 310559 US#lYS 0120 -11 51,500 BS8.33 au 57.0 11.3 0.6 o.ao Northeast Iowa Coop 

9:06 AM Sl'L= 

01/24/07 830040477 310560 US!l2YS 1378 -12 53,760 a96.33 au 56.5 10,8 0,5 1,40 Tama Benton Cooperative 

~,13 AM SPLm 

01/24/07 830040478 110561 USil1YS 14'02 ·13 53,040 884.00 au 56.5 11.6 0.8 O.BO Keystone Mercantile Co. 

9:20 AM SPlP 

01/24/07 830040479 310562 1JSUUS lUI ·H ~:" 340 922.33 au 57.5 10.3 0.7 3.20 West Side Grain 

r:

9:25 AM SPr.­

1/24/07 830040480 310563 USIIlY'S 9803 -15 58,140 969.00 SU 56.5 10.2 0.4 0,80 Tama Benton Cooperative 

9:37 AM SPL01/24/01 830040482 310564 l1Sft2YS san -17 54,040 900.67 BU 56,5 10.4 0.5 1.90 Tams Benton Cooperative 

!h42 AM SPL= 

01/24/07 830040481 310565 USillYS 5ao ·16 53,640 894.00 EU 57,S 10.2 0.4 0.60 Interstate Grain Service fl.",,, !h4? AM SPL= 1 .01/24/07 830040483 310566 USIIlYS 1403 ·18 53,080 884,1>7 BU 57.0 11.8 0.9 0.80 Keystone Mercantile Co. 

01/24/07 3:52 PM /opt/uxapps/batch/ob1oaunl.sqr ?age 
LYNX - Load/unload Detail 


Cedar RapidS West 


Facility: cedar Rapids West, GOB 


huck UnlQad 


Net wgt Wgt Cert / Customer 1 

Date Trace Id ElOL· Grade C/P Unit 1d In Pounde Quantity TIl M DKT I'M SHill" OSF OKG !lCl?M PROT FC:>T ACcount of 

10,04 AM BP~ 

.-01/24/07 630040484 310567 l)S1I2YS 1340 -19 55,560 926.00 IlU 55.5 10.9 \.2 0.80 KeYStone Mercan~ile Co. 

,. 10:09 AM SPL~ 

troU 01/24/07 830040465 310568 USIilYS 2462 -20 54,320 905.33 Bl) 57.0 10.4 0.6 0.&0 Tama Benton Cooperative 

....11-10: 15 AM SPL~ 

01/24/07 830040486 310569 UBIIlYS 174 -21 55,200 920.00 au 56.0 10.7 0.6 1.00 Glandorf, Daniel 

10,20 AM SPL= 

01/24/07 830040487 310570 USll2YS 9282 -22 53,160 886.00 au 58.0 9.1 0.6 1.S0 Marengo Blevator Company 

10;26 AM SPL. 

01/24/07 830040488 310571 USlIlYS 9909 -23 51,540 S59.00 BU 57.0 10.2 0.4 0.90 Norcheast Iowa Coop 

10:31 AM S~= 

01/24/07 830040489 310572 US1l2YS 8562 -24 57,020 950.33 BU 56.5 10.9 0.6 1.30 Ryan Cooperative
 ~u.t\! 10:36 AM SPL~ 

01/24/07 830040490 :nOS73 USII2.YS 13% - 25 :.54,940 915.67 BU 58.5 10.9 0.5 1.80 Northeast Iowa Coop


l 10:41 AM SPL= 


01/24/07 830040491 310574 USlI3YS 1315 -26 51,060 951.00 au 57.0 10.0 0.4 2.50 Tama Benton Cooperative 


lO:46 AM SPL=
 J.11 01/24/07 830040492 310575 US1I3YS 9759 -27 54,300 905.00 BU 5S.5 10.7 0.6 2.20 Northeast Iowa Coop 


4' 
 10:52 AM SPL= 


01/24/07 630040493 310576 USII2YS 0692 -28 54,660 911.00 BU 58.0 9.4 O.S 1.60 Tams Benton Cooperative 


10:58 AM SPLv 


"? 1,..'1 01/24/07 530040494 310577 USillYS 7763 -29 ) .. '"f 920 965.33 SU 56.5 10.9 0.5 0.80 Tama Benton cooperative 
 ... 
 11:02 AM SPL= 


01/24/07 830040495 nOS7S USII1YS 1065 -30 57,400 956.67 BU 57.0 10.1 0.5 0.50 Northeast Iowa Coop 


11:09 AM SPL01/24/07 830040496 31057~ USlI2YS 2064 -31 53,660 894.33 BU 56.0 10.7 0.6 1.BO Ryan Cooperative 


11;13 AM S~u 

01/24/07 830040497 nosao USIIIYS 2298 -32 53,640 894.00 IlU 57.0 8.7 O.S O.BO Marengo Elevator Company 


11:19 AM SPL= 


01/24/07 820040498 310581 USlln:S 4556 -33 55,S80 931.33 BU 56.5 10.1 0.6 0.70 Innovative Ag Services 


ll:25 AM SPL= 

01/24/07 830040499 3105B2 US#2YS 1214 -34 55,220 920.33 SU 57.5 10.7 0.6 1.40 Ryan Cooperative 

11,30 AM SPLm 

01/24/07 830040500 310583 usltllCS 9356 -35 58,800 980.00 IlU 58.0 10.1 0.5 0_70 Innovative Ag Services 

11:36 AM S~" 

.-ol/U/07 830040501 310584 USlt1YS 4399 -36 57.620 960.33 BU 57.5 9.7 0.4 0.90 Edgewood Feed Mill lnc 

11:41 AM SPLw 

01/24/07 830066002 31(}585 US#1YS 012(} - 37 50,260 837.67 eu 58.0 10.4 0.4 0.80 Northeast Iowa COop 

11:46 AM SPL01/24/07 830086003 310586 USillYS 8580 -38 54. ~40 915.G7 SU 57.S 9.6 0.8 0.90 VanDaele, Rick & Linda 

11:51 AM SI?L~ 

01/24/07 830066004 310S87 USlilYS 1257 -3S1 52,960 662.67 BO 57.5 11.0 0.4 0.70 Innovative Ag" Services 


11:56 AM SPL= 


01/24/07 830086005 310588 USUl'lS 9577 ·40 54,2QO 90~.OO BU 57.0 9.6 G.Q 0.70 Linn Coop Oil-Alburnett 


r


12: 04 PM S~. 

Ol/24/07 830086006 310589 USli1YS 570 ·41 57.200 953.33 BU 57.0 11.5 0.5 1. 00 Stoner Grain, Inc. 


o Vl 01/24/07 3: 52 PM /opt/uxapps/batch!Obloaunl.sqr page 2 

r-U . 

~ 
LYNX - Loau/un1oad Detail 


Ceda~ Rapids Nest 


Facility, Ceaar Rapids West, GaS 


Truck Unload 


Net W9t Wgt cext: / Customer / 

Date Trace Id eOL Grade e/p unit Id In Pounds Quantity Til M DKT FM SHBN DEF DKG BCFM PROT For Account of 

1;<,09 PM 6P1.= 

01/24/07 830Q66007 310590 USlIl;':8 6685 -4~ 53,360 8B~.33 SO' 57.5 11.0 0.4 0..70. 1.1no Coop Oil Co - Marion 

12,H PM BPLu 

01/24/07 830086008 310591 USlllYS 1552 -43 58,220 970.33 au 57.5 10.2 0.6 1.00 Innovative 1<g Servicea 

12,;<0 PM SPI.­

01/24/07 B30086009 310592 USII2YS 1246 -44 1'.3,500 891.67 eu 57.0 11.0. 0.7 1.40. Innovative Ag Services 

12:24 PM SPI,.. 


01/24/07 830066010 310593 U8#2Y8 1340 -45 55,440 924.00. au 55.5 10.6 0.6 1.30 Keystone Mercantile Co. 


12,29 PM Spr,.. 


01/24/07 830086011 ·310594 USIi:U'S 9803 -46 56,360 939.33 au .57.0 10..5 0..4 0..70. Tama Senton Coope~ative 

12:35 PM SPI.­

01/24/07 830086012 310595 US#1YS 1605 -47 51,560 959.33 au 56.S 11.1 0..6 0..90. Innovative 1<9 Services 

12:42 PM SilL01/24/07 830086013 310596 UBUyS 0120 -48 55,260 921.0.0 au 57.5 9.3 0.5 0.80 VanDaele, Rick & Linda 

RIj~ 12:47 11M 	 SIII.-

01/24/07 830086014 310597 USlI2YS 6112 -49 51,260 B54.33 au 57.5 9.2 0..5 1.60 	 Devick Enterprises 

} 

12:52 PM SPL01/24/07 830086015 310598 UB II lYS 5834 -50 55,660 927.67 BU 56.5 10.1 O.S 0.80.' Tama Benton Cooperative 

12 d;o PM SPL~ 

01/24/07 830086016 31059~ US1I1YS 9759 -51 53,960 699.33 SU 57.S 11.0. 0.6 0.90 Northeast Iowa coop 


1:02 PM SPL. 

01/2~/07 630086017 310600 USUlYS 1247 -52 55,500 ~2S.00 BU 57.S 10.3 0.5 0..80 Innovative Ag Services 

1:07 PM Spt.., 

01/24/07 630086018 310601 USn1YS 174 - 53 54,729 912.00. SU 56.0 10.7 0..5 0..90 Glandorf. Daniel 

1,1) PM SPL~ 

01/24/07 830086019 310602 UBUYS 9356 -54 60,360 1,0.06.00 eu 57.5 .9.6 0.6 O.SO Innovative Ag Se~vices 

1.19 PM SPI.­

01/24/07 830086020 310603 USIIlYS 7902 -55 57,120 952.00. au 57.5 10... 0.5 0.70. Innovative Ag Services 

1,30 PM SPL. 

01/24/07 830066021 31060i UlHI1YB 8653 -56 57,240 95~.OO SU 57.0 11.2 0.5 0..80 Ryan Cooperative 

1:35 PM SPLa 

t1/24/07 830086022 310605 US#lYS 1402 -57 54,680 911.33 au 57.0 11.6· 0..8 0.80 Keystone Mercantile Co. 

1:40 PM SIlL" 

01/24/07 B30086023 UOS06 US!IlYS 465 -58 31.160 519.33 SU 56.0 13.5 0.5 0.70 Serbousek Farma Inc. 

1,43 PM SIlL~ 

01/24/07 830086024 310607 USIT1YS 4565 -59 55,120 928.67 SU 57.5 10.9 0.5 O.BO Innovative Ag Services 

1:49 PM SPL01/24/07 830066025 310608 USfflYS 1245 -60 56.860 947.67 au 57.5 10.9 0.5 0.80 Innovative Ag Services 

1:54 filM SPt.­

01/24/07 830096026 310609 US#lYS 492 -61 63,460 1,057.67 SU 56.5 11.2 0 .. 5 0.70 Keystone Mercantile Co. 

2.00 11M SPL~ 

01/24/07 830086027 310610 USUYS 1552 -62 '.,7,400 956.67 SU 57.5 10.0 0.6 0.90 Innovative Ag Services 

2,06 PM SPL" 

Ot/24/07 830086028 310611 USIIlY'S 5877 -63 53,800 896.67·SU 56.5 10.3 0.4 0.80 Tama Benton Cooperative 

tl.P\ 	 2:11 PM SPL· 

[ . 01/24/07 830086029 310612 USlIJ.YS 0692 -664 53,980 699.67 BU 58.0 8.9 0.6 0.90 Tams Benton Cooperative 

") 01/24/07' 3:52 PM /opt/uxapps/batch/obloaunl.sqr 	 Page 3 
LYNX Load/unload Peta~l 

Cedar Rapids west 


Facility, Cedar Rapids West, GOS 


Truck Unload 


Net !lgt Wgt cart / CUstomer / 

Dl.\te Trace 1C! BO~ Grade c/:I' Unit 10. In Pounds Quantity TW to! OKT FM SHBN DSF DKG BCI'M PROT FOr Account of 

2,17 PM SPV= 

Ol/24/07 830086030 3101S13 USlllYS 1374 -65, 56.680 944,67 au 56.S 10,6 O.S 0.90 Tama Benton Coope~ative 

2 :22 PM' SPLa 

01/24/07 830086031 310614 USlIlYS 3769 -66 52,660 877,67 au 57.0 10.4 0,6 0.80 Innovative Ag Services 

2,21 :I'M SPLz 

01/24/07 830086032 310615 US#lYS 0259 -67 5:2,080 868.00 BU 56.5 11,1 0.5 0,80 F J XrOb « Co . Walker 

2,32 PM SP~c 

01/44/07 830086033 310616 US#lYS 771S3 -68 57.280 954.67 BU 56.0 10,0 0,6 0.60 Tama Benton Cooperative 

2,37 PM SPL~ 

01/24/07 	830086034 nOol7 USl/lYS' 1403 -6~ 53,460 891.00 au 56.0 11,~ D,S 0,80 Keystone Mercantile Co. 

2,4) PM SPLm 

01/24/07 8300860j5 310618 USl/2YS 1375 -70 56.300 938,33 BU 57.0 9.~ 0.6 1.70 Tama Benton Cooperative 

2:48, PM SPLQ 

01/24/07 830086036 310619 USIIIYS 7238 -11 56,640 944,00 SU 57.5 10.8 0.6 1. 00 Circle J Grain 

~Uh 

') 2:55 PM SPL~ 

01/24/07 830086037 310620 USlilYS , 1065 -12 57,680 961,33 au 57.0 lO,3 0.6 O.SO Northeast Iowa Coop 

2:59 PM SPL01/24/07 830086038 310621 usltlYS 9356 -7,3 51,600 960.00 BU 56.S 10,5 0.5 0,90 Innovative Ag Se.vices 

3:05 PM SPL01/24/07 830086039 310622 USfl1YS 1246 -74 54,620 910,33 au 57.0 10.2 0.5 O.SO Innovative Ag Service. 

3: 10 PM SPL01/24/07 830086040 310623 US#lYS 7370 -75 51.160 853.00 au 56.5 11.1 0.4 0.70 F J Krob & Co • Walker ­

3,20 PM SP~

01/24/07 830086041 310624 USUYS 9759 -76 55,400 923.33 BU 57.5 10.8 0.4 0.60 Northeast Iowa Coop 

3:24 PM SP~_ 

01/24/07 830086042 310625 USlllYS 5324 -77 :",,180 936,33 au 56.5 12.4 .0.4 0.70 Innovative Ag Services 

3: 30 PM SPL= 

'01/24/07 830086043 310626 l1SlI1YS 9561 -78 57,000 950,00 au 56.S lZ.3 0.6 0.60 F J Krob I< Co • Ely 

3:35 PM SE'L~ 

01/24/07 830086044 310627 USlI1YS 561 -79 54.040 900.67 au 57.5 11.2 0.4 O.BO Gericke, Daryl 

3:41 PM SPL· 

TOtal 79 Units ~. 342,220 72.310.32 

summary of Unloads by Commodity/Product and Transportation Mode •• * 

YSB Truck unload 72.370.32 eu 57.0 10.5 0.5 1.02 

SPL= 

Total YSB Unload 	 12,310.:>2 au 57.0 10.5 0.5 1.02 

SPLm 

01/24/07 3: 52 'PM /opt/uxaPP9/batch/ohloaunl.sqr 	 Page 4 

____.._____.________...__~~_..... _. __'_.... _~,,~'._u_.~_._ ... w_ .~ __' •••••• _":'""""-.~---••-.~.-.--••••• 
LYNX - Load/Unload Detail 

Cedar Rapids West 

l'a<::ility, Cedar RapidS west, 00$ 

TlruCk Unload 

Net Wgt Wgt Cert CUstomer I 

Da te Trace I d SOL Grade C/F Un1t td In Pounds Quantity TW M DKT FM SHaN OISF OKG BCFM: PROT For Account Of 

Total Unload 72,370.32 

_.* End of Report **. 

01/24/07 3,52 PM {opt/uxapps/batch/obloaunl.sqr Page 5 
Appendix G 


Opacity Certification 


i 


I 

VISIBLE EMISSIONS EVALUATOR 


This is to certify that 

Matt Milligan 


met the specifications ofFederal Reference Method 9 (40 CFR Part 60, Appendix 

A, Method 9) and qualified a~) a visible emissions evaluator. Maximum deviation 

on white and black smoke did not exceed 7.5% opacity and no single error exceeding 15% opacity was incurred during the certification test conducted by Opaque 

Smoke School, LLC ofOverland Park, Kansas. This certificate is valid for six 

months from date of issue. . 

Des MQines, IA October 3, 2006 7669 

Location Date ofIssue Certificate Number 

VA.",,-

PresidenVDirector 

1'! ~ 

of Training . . :=•••CiKS ..5a::::HCi:::iL 

.id"", 

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