• 


Raymond Professional Group. Inc . 
 . Engineer'S - Architects .. Consultants. Builders 

1001 16th Street· Moline, Illinois 61265 

Tel: (309)157-9800· Fax: 1309)757-1.812 

www.raymondgroup.com 

January 24,2001 

Mr. AI Kriegel 


Cargill Oilseed Processrng 


1110 12th Avenue S.W. 


P.O. Box 2817 


Cedar Rapids, Iowa 52406 


SUBJECT: PARTICULATE TES'"ING ON EMISSION POINT 

DUST COLLECTOR 

Dear Mr. Kriegel 

#009 - ELEVATOR 


• 

In accordance with The Raymond Professional Group, tnc. contract dated December 6, 

2000, Raymond is pleased to supply the results of particulate emission tests performed 

on January 10. 2001. Emission tests were conducted on Emission Point #009, the 

Elevator Dust Collector, for Particulate Emissions . 

We appreciate the opportunity to have been of service to you on this project and hope to 

assist you on your future engineering and environmental projects. 

Respectfully, 

~;::;SIONAL GROUP, INCORPORATED 

q~O!land Prol" Manager 

&v,~?r($' David M. Bloss 

Environmental Manager 

tam 

cc: File #518319 

• 

Formerly Doyen and Associtl!f!s, Incorporated; Raymond·BeUng, incarpomted; Raymond Management SeTTilCIBS, Inccrpomted; 


Raymond-NOBB, InC<>1pOmkld; and Raymond-Williams Limited 


i 

• Raymond Professional Group, Incorporated Report No. 518319 

I. INTRODUCTION 

In accordance with The Raymond Professional Group, Inc. (Raymond) Contract 

dated December 6, 2000, emissions tests were conducted on Emission Point #009, 

The Elevator Dust Collector for Particulate Emissions. 

Tests were performed on January 10,2001 by Tim Moriand and Jeff Ogden. The 

tests were coordinated with Mr. AI Kriegel of Cargill Corporation. Mr. Anthony 

Daugherty of the Linn County Health Department was on site for the testing. 

The tests were conducted and data evaluated in accordance with U,S. 

Environmental Protection Agency (EPA) Methods 1-5, as listed in 40 CFR 60, 

Appendix A, and the Iowa Air Compliance Manual. 

DISCLAIMER 

The results from this stack test reflect the emission conditions at the time the tests 

• 

were conducted. Compfiance with conditions listed fn the source permit are 

determined by the regulatory agency responsible for enforcement of that permit. 

• 1 
Raymond Professional Group, . lncorgorated Report No. 518319 

, • ,

!

i 

II. SUMMARY OF RESULTS 

The following Table presents a summary of the emission testing performed by 

Raymond at Cargill Corporation located in Cedar Rapids, Iowa. See Appendices 

for data utilized a nd developed as part of the tests. . 

Particulate Emission Tests 


Emission Point #009 


Elevator Dust Collector 


Cedar Rapids, Iowa 


January 10,2001 


• 


Test 

Number 

Particulate Emissions 

gr/dscf Ib/hr 

1 0.0053 1.40 

2 0.0045 1.19 

3 0.0038 1.01 

Average 0.0045 1.20 

Stack Gas Average Velocity: 

Stack Gas Average Flow Rate: 

Stack Gas Average Temperature: 

Stack Gas Average Moisture: 

gr/dscf :::: grains per dry standard cubic foot 

ACFM =: Actual Cubic Feet per Minute 

64.073 ftlsec 

30,294 ACFM 

39.2° F 

1.1% 

;

, . 

2 

• 

Raymond Professional Group, Incorporated Report No. 518319 

IILTEST METHODS 

Emission Point #009, The Elevator Dust Collector, was tested for particulate 

emissions. The emissions were tested using EPA Methods 1-5, and the Iowa 

Compliance Sampling Manual Procedures. 

EPA METHODS 14 

EPA Method 1, "Sample and Ve!ocityTraverses for Stationary Sources", as revised 

August 14. 1986, is used to determine the quantity and location of velocity traverse 

points. The method el,ccounts forflow disturbances, both upstream and downstream 

of the sampling points. 

EPA Method 2. "Determination of Stack Gas Velocity and Volumetric Flow Rate (type 

S Pitot Tube}", is used to determine the flue gas velocity and flow rate. An S-type 

pitot tube is connected to an inclined manometer (O.OO-1.00 inches of water incline 

• . range and 1.0 to 10,0 inches water vertical range) to measure velocity pressures in 

the flue. Temperatures are measured with a type K thermocouple attached to a 

calibrated digital temperature indicator. 

EPA Method 3, "Gas Analysis for CO2• O2, O Excess Air, and Dry Molecular 2 

Weight", uses an integrated gas sample collected during the test period for 

determination of gas composition by orsat analyzer. The orsat analyzer is used to 

determine the percent carbon dioxide and oxygen, which is subtracted from 100% to 

determine the percent nitrogen. 

EPA Method 4, "Determination of Moisture Content in Stack Gases", is accomplished

by weighing the impingers before and after tests. The weight gain is used to 

calculate the moistUre content of the flue gas. . 

-. -:! ~ 

EPA METHOD 5 

EPA Method 5 is the "Determination of Particulate Emissions from Stationary 

Sources", EPA Reference Methods 1 through 4 are used to determine the sampling 

paints, flue gas velocity, gas composition and moisture content. Based on these 

preliminary measurements, a sampling nozzle of appropriate diameter is selected to 

maintain isokinetic sampling . 

• 3 
• Raymond Professional Group. Incorporated Report No. 518319 

The stack gas is drawn through a calibrated stainless steel nozzle into a heated, 

glass~lined probe and through a heated filter assembly held at 250 ;!; 250 F. The gas 

, then passes through an ice-cooled impinger train. The moisture in the flue gas is 

condensed as it passes through the ice-cooled impingertrain, which is maintained at 

a temperature of 68°F or less as it leaves the last impinger. The first, third and 

fourth impingers are modified by replacing the high velocity tip with a one-half inch 

inside diameter glass tube. The second impinger is of the standard GreenburgSmith design. The gas then flows through a leak!ess vacuum pump, a dry gas meter 

and a calibrated orifice. The dry gas meter and orifice are calibrated before and after 

each sampling event. 

The sampling rate is adjusted during the sampling period to maintain isokinetic 

conditions. At isoklnetic conditions, the velocity ofthe stack gas entering the nozzle 

should be equal to the stack gas velocity at the sampling point. These condrtions are 

maintained by adjusting the pressure drop across the orifice meter relative to the 

stack gas velocity pressure. The proper orifice differential is determined by , 

calculation. 

• Priorto each test run, the test trains are leak checked at fifteen inches of vacuum. At 

the conclusion ofeach test. the system is leak checked at the highest vacuum drawn 

during the sampling period. Allowable leakage rate under EPA Reference Methods 

is 0.02 cubic feet per minute. . 

After each test, the particulate samples are carefully recovered. The filter is removed 

from the holder with tweezers, placed in a petri-dish and sealed with tape. The 

nozzle, probe assembly and front half of the filter holder are rinsed with acetone. A 

probe brush is used to remove particles which adhere to the walls of the nozzle, 

probe and filter assemblies. The washing is collected in sample containers and 

transported to the laboratory for analysis. 

The acetone washing ofthe front halfofthe particulate sampling train (nozzle, probe 

assembly and front half of the filter holder) is quantitatively transferred to a 

desiccated tared 250-milliliter beaker. The volume of acetone is recorded and 

evaporated to dryness. The beaker with sample is desiccated and weighed to a 

constant weight, to the nearest O.1-milligram. 

For purposes of definition. the term "constant weight" means a deviation of no more 

than ±O.5 milligrams between consecutive weighings,' conducted at intervals of not 

less than six hours apart. 

• 4 
• Raymond Professional Group, Incorporated Report No. 518319 

• 

, 

A blank sample is obtained from each lot of acetone used during the test program. 

The blanks are processed and analyzed in the same manner as a particulate 

sample. 

Filters from the particulate test runs are removed from their sample containers and 

placed in a desiccator for a 24 hour period prior to weighing to a constant weight. 

The impinger contents are recovered by pouring the original 01 water and any 

moisture collected in the first three impingers into a graduated cylinder. The total 

volume is measured and recorded. The water is then transferred to a glass or plastic 

bottle. The liquid portion of the impinger train is then rinsed, at Jeast twice, with DI 

water and the contents are added to the irnpinger catch. A blank sample of rinse DI 

water Is set aside in a separate container for use as a blank sample. 

In the lab, the impinger contents are analyzed for organic and inorganic condensable 

matter as follows: the impinger contents are transferred to a separatory funnel and· 

first extracted with three 25 milliliter portions of ethyl ether and three 25 milliliter 

portions of chloroform. The two extractions are combined in a tared 250 mL beaker 

and evaporated to dryness. The remaining water fraction is placed in its own 250 mL 

tared beaker and also evaporated to dryness. Following evaporation, both sets of 

beakers are placed in a desiccator for a 24 hour period then weighed to the nearest 

0.1 mg. The water fraction represents the inorganic condensable material and the 

ethyl ether/chloroform fraction represents the organic condensable material 

• 5 
IMPINGER TRAIN OPTIONAL, MAY BE REPLACED -;. o . ~T~::::NSOR .BY AN EQUIVALENT CONDENSER

. . 

HEATH] AREA THERMOMETER .' 'j.".

: 0 . THERMOMETER

CHECK 

VALVE 

VACUUM. 

LINE' . \ 

. 

TEMPERATURE 

SENSOR 

PITOT TUBE 

. I 

REVERSE·TYPE 

PI TOT TUBE 

t, .

11 'STACK 

U-WAll 

fl.L J' • 

FILTEA HOLDER 

. --;- ­ - - - - - - - -1 1.....---1'--. 

I 

I 

I 

PITOT MANOMETER 

MAIN VALVE 

DRY GAS METER AIR·TlG HT 

PUMP 

Partlcula.le.s.amPllni.traln. 

-J:-:: 

. , 

_f. ~_ -- -- -­ . ,.•.._ ..... .~ ••••••

SAMPLE POINT' SCHEMATIC 


PI 'InrG(~\'l} o')SE'PCf p(cr:(sSJ~ P}&;I7INo. Stdck Oidme~eq Upstredm DIsturbance 5.3'2. 

D.II.p. }.; }V.O I ltJ • Stack Diameters Oownstred~ 01 stu~bance -1': <~2 

Source .e ItUCt/u! du,:r (!o}J#Clor ~. of Sdmple Ports ? ­

St.dck Oi dmeter ""3 8 II No • of S~mp 1ePo i nts_---I<?~'/_·__ 

; . SAMPLE POINTS i <AT EACH PORT 

FROM .§ tOENAL!. 

POINT "::ES~ANCE 

NO. . ( i tlches') 

J. ,,0 

?->t:J" 1. 

i)'YB '3 

, • .,.> 'i t 

';( ').~ (q I' e. ) j. Y'7 

7" ?1.).Y'7 t t ~ ?~.g> 0 0; . 3)·17 

)v 3>S'1 

)/ '3~Y7"" 

)t 37.'1'" -;to.}" 

, 

' ;~ 1 

• 

, 

) 

i 

•

, 

• 


• 


PARTICULATE RESULTS 

Company CARGILL OILSEED PROCESSING 

City CEDAR RAPIDS, IOWA 

Source ELEVATOR DUST COLLECTOR 

Test Team TIM MORLAND & JEFF OGDEN 

Test Date WEDNESDAY 1-10-01 

Parameter 1 2 3 averageunits 

=-==~~=========;;~================================;===~===~~===~~~ 

P bar )0.08 30.02 30.06 30.05 in Hg 

SqRt(delta P) 1.147 1.162 1.164 1.158 in water 

T stack 500.2 499.7 497.6 499.2 deg R 

Cp 0.84 0.84 0.84: 0.84 no units 

l? static -11.00 -11. 00 -11.00 -11.00 in water 

A· stack 7.88 7.88 7.88 7.88 aq ft 

C02 0.0 0.0 0.0 0.0 percent 

02 20.8 20.8 20.8 20.8 percent 

CO 0.0 0.0 0.0 0.0 percent 

N2 79.2 79.2 79.2 79.2 percent 

M dry 28.832 28.832 28.832 28.832 Ib/lb*mole 

M stack 28.698 28.713 28.113 28.708 Ib/lb*mole 

B ws 0.012 0.011 0.011 0.011 mole fract 

V imp 5 2 3 3 ml 

V 89 7.21 9.06 8.17 8.15 gm 

V meter 4S .112 46.153 46.644 45.970 cubic ft 

y 1.0083 1. 0083 1.00B3 1.00B3 no units 

Delta H 1. 678 1.720 1. 725 1.708 in water 

T meter 526.4 527.8 531.6 528.6 deg R 

L post 0.016 0.002 0.003 0.007 cfm 

Theda 60.0 60.0 60.0 60.0 min 

Particulate wt. 0.0163 0.0140 0.0119 0.0141 gm 

Blank -0.0004 -0.0004 -0.0004 -0.0004 gm 

D nozzle 0.188 0.188 0.188 0.188 inches 

Results 1 :2 3 averageunits 

==========================~~=====~======~====~==========~~=~====== 

P stack 29.271 29.211 29.251 29.245 in 

P meter 30.203 30.146 30.187 30.179 in Hg 

V water 0.579 0.524 0.529 0.544 cubic ft 

V meter (std cond) 46.221 47.073 47.297 46.864 cubic ft 

V stack 63.530 64.378 64.309 64.073 ft/sec 

Q stack 30751 31172 31313 31079 dscfm 

Isokinetic rate 102.404 102.884 102.908 102.732 percent 

C part 0.0053 0.0045 0.0038 0.0045 gr/dscf 

C' part 1.3991 1.1911 1.0069 1.1990 Ib/hr 
• 


• 


SAMPLE CALCULATION - TEST NO. -()~ 

J', 

PInt CC. 

Purpose Co 

Supliag T.ocaHOI -z.-:.!r:'L.:..!.L:-:!........,~.!!:.-L.l.....----';.,...:...--f:-;.~-~~"'-'::::.:..,;,.:.::....,J!;.......::- Piut calditiou ..p...~!.:....!..=::...-_________ 

~--:;r_____ D&te ~~_ 

fest Procedm ~~(£l......t.J....IC..,,~u..:..._.L-_--__ _ '1~/"-.~___ nate {. ) 7·01 

Necessary Data: 

B1n 

Vm 

..6.H 

1,6. P 

Tm 


Ts 


Ps 


Pb 


As 

Au 

y 

Cp 

Collection Interval, ----'=b'---u__ mi,n 

Water Colleeted, ) 2. ZI gm 

Particulates Collected1 

Meter Volullle, 'Lj"S.)J 7.. 

Avera.ge Meter Pressure, ). ( 7 S in H20 

A";'erage r- Velocity Pressure, ). ) L}7 jin H20 

Average Meter Temperature, Ct. ,/ of + 460 = S~{. 1/ oR 

Average Stack Temperature, ~t1. L of + 460 ;:;: §vo. L oR 

Stack Absolute Pressure, ?0~ '/'71 in Hg 

Barometric Pressure, 3£.() '6 in Hg

Stack Area, 7. 8~ ft2 

Probe Nozzle 'Area, ). CZ))(J~-¥ ft2 

Dry Gas Meter Calibration Factor, ).006..J 

Pitot Tube Coefficient, D·8'/ 

stack Gas Composition: 

% CO2 _-..:::D~__ % 02 :;20' If 

X,CO r %N2 Q9.'? 
., 	 SAMPLE CALCULATION - TEST NO. - c:J/L< 

lobBo. C; J '6)} '7 

Moisture Content of Stack Gas, Bws 

• 

'i 

, 1. Hater Collected in Impingers, sCF 

VWlstd:: 0.0414 ft3/gm (L7. 7 ( gm) 

V td:: g. 5: 7C,SCF w,s , 

2. 	 Moisture Content of Stack Gas, BW8 

Bws Vw,std :: 

Vw,std + Vm,std 

B:: fJ.!3r:7 SCF 

ws "~CF +1-)J4u DSCF 

:;; O.o)~ Bws 

c. Molecular Weight of Stack Gas, Ib/lb~mole 

1. Dry Molecular Weight, Md 

M'd ::: I>xBx 

Md :: O.44(~% CO2) + O.32~% 0Z} + O.28(~% CO) + O.28~$~% N2) 

Md ::: dB. S}Llb/lb-mole 

• 


2. Wet Molecular Weight, Ms 


Ms ::: Md(l-Bws ) + 18(Bws ) 


M Q!6.S>1. (l..oQ}'t ) + l8(O.~J1 )
 s 

Ms =d8.b'7g'lb/lb-mole 

B. 

SAMPLE CALCULATION - TEST NO. - ~~ 

Plnl - UdC7( ~0)?1/5 J'd/l, Job 10. S/(s3/7

U. Average stack. Gas Velocity, Vs 

Vg = KpCpj Ts Jb,P 


PsMs 


Vg = 85.45 fps :I: D.8~1 * / Se>6.1. oR ;. * J.) 't2Jin H20 

V~in Hg *;I~b/lb-mole 

V s =b>. ):>i> IpS 

; 

. ; 

E. Average Stack Gas Volumetric Flow Rate, Qs 

Qs ; (3600 sec/hr) VSAg(l-Bws)f!stdl rp~l LpstdJ [TJ . 

Q ; (3600 secihr){b3.~ofPs)(7.~ ft2)(1~'OIL)[ S300 R J s 29.92 in fig 

• Q =h~'Jb)Cl( 'DSCFH 

s . 

30) 7?15 D~C FIh 

F. Pollutant Mass Rate, PMR 

PMR; _ ~ ..........- * 


Vm,std 

PMR ;0.015'0;. gm

Yl11 J DSCF 

Qg 

454 gm/lb 

*bgYI)D{JUSCFH 

454gm/lb 

PMR ::: ).3'7a 1-) Ib/hr 

G. Pollutant Concentration, Cstd 

C = ~ * 15.43 grains/gm std 


Vm,std 


C ""O.oJS"c, gm :I: 15.43 grains/gm std l/6.t1 I DSCF 

C ::::O.ov~J grains/DSCF std 
SAMPLE CALCULATION - TEST NO. -VV'-t • l1"t Cc,I;:; ;I/ 0 .1 SUe ( fr"'?'551" 7 J)e;", I I.b~. 5 / '6JJ<;

H. 	 Isokinetic Variation, %1 

%1 = lOOTgVm;stdPstd 

(60 sec/Min)eVpsAnPsTstd(l-Bws) 

XI = nOO){5ao·t.~){Y6.77'DSCFi(29.92 !n Hg) 

(60 sec/min) (b D min) Q.5Y-'fps) (l."1lXlc~9 ft2) (~1.n Hg) (~3QoR) (1...P,~~ 

%I ::)01.2 Y..:% 

I • 	 Comments a.nd Remarks; 

• 

• 

•• 

S2mpling 211d Velocity Iraversa Point Determination' '. 

EPA Method 1 

II mer~ :r:~n .a ~(\d t Ci~r.;lit4fl .r:: it ~;:';! 

Iji~ .. Ij 12 ~ '-t. U.$. a or 9 ~t1!.;~ 

NC. OF paRiS US2::J -----r.,.----­

_ __L " PCF\i INSIDE OIA~I=TE::; 2 

if l " 

--yrr 

I 

I 

NO. OF PORTS AVAll. • .l,SI.E 

S;·::.JI'IAL£NT OIAl.IEi'!.=\: 

(1 S 't OE ,,-;"''"..: T W'II:";":': 

*.... ~... O~~~7M'" 't'11Cfn 

) , I~ 

LS.7 

~().~ 

J=.~ 

, I 6.; ~.' ....- : : ~.,~ t,LJ Hl.,i 

1 ~ !~:: :,.~ !'1.-\. 

t,.~ s.;" 

l •. $ t ~ • , 

, ;:i•.': ';" 'I ~ .. ~=.~ il.. S ti.: 

3~.'" 47.: 

9~6! ~o.~ 

H.~ 

9'15.1' 

.-;.! ..... '" 

:7.3 :::.: 

.1 :.! • A • 

17. ! r~.:l 

to.3 

0IS;':'N<:a I OISiANC::;' I t=-~CM INSiG5 F;;\CJ..A ~Lri"~iOEI 

·rYAl,.!.. C:= rOn ':"= 

Ctl' nat ~t:1~~ ;lo;n[=I c!e: I't U) !~iiCX 'W'1U~ 

~.O in .. lOf ~C3-e:X <li<L ,.,,1 in. 

o.,s itt. lot $(::"':X (:\:3.K 11 Co <1--\ 1('1~ 

;.'l ;n 

Figure 6-1. 

i' 
PART1CULATE FIELD DATA 


Page One 


Page OF,',,_--.,..r;_ 

C0D2j,'O O,I9.PrJ ?rtJCPSS)~' ... nt Run No. O'jJ.r-L

•; urea 1151 Co))eCM Filter No. c; 3J 

Procli!ss Weight Rat~ ; NouIe Diameter - in. O.IRS 

: Sample L~c. Ceq 0,( r £1 J.s ~ 1:d Ambient Temp. 

, Test Crew 1!VJ -:::s c) , Min.J point 

Imp, Box No. ~0404:...!4-.l:::~--r---··-·---- . Day/Date \1JeJOt~Jt,,'1 I~jio 1 Test Started Ended 00; tD

/'j 7 

: Pb in Hg 2 V .t/ 'b SCHEMAT1C or: STACK (CROSS SECTION) 

: Pitot Cp _0_,~.;:::-v}:;;--_________ CV 

Meter Q, H@ .......J...)._'_8;:..;S=--:., 
 ..../________

, Y Factor ) .00 C?) 

Est, Yo Moisture OOJ;tJ t(

; Psg - Static [Juct Press .......-r---+l.... 1_·_0____ 


Probe Liner Material ___ G....:J_q __
5_)_~____ 

.•......-----------:----=----1 

, 

..: 

• 

Page Two 

Page L OF ~ 

•. 

RU~~~ Filter No. 9 } I 

Ambient Temp. "01/ d ' 

- Test Started 07St __ Ended O~Ot? 

Meter Leak Rate CFM: Before (. v J1 cQ). J '? "Hq After (/.v I t @ I s 

Pitot Tube Leak Test Before Before '. , V After V K Factor 

PARTICULATE FIELD DATA 


<. :;; ., Gas Sample Temp. at: ..". "..--+ Q

0­ ...... =. ~ <II "'

"'~ .,

cr .,..!2. dry gas meter 1~ :.. §:~~: .., ~.:;£

o­ :-.0- ~d.S!.. m '":3 .,,~ "";;;-c;l Ol. ::; ~l/I .. 

c.. Out.let ~ "T1~!JJ 

...," 

iii' 

a 

l::". ;. 

if 

. 

<II 

~ 

,~~"C;;£f;; ::: I. Itn .' '~~ 

~ :.A!,;::F 
PARTICULATE! FIELD DATA 

Page One 

P::lge OF:'. (; 

Run No. :11P---...~~ 

'. Filter No. a; ') t 

No:t::':;le Diameter - in. O. J 38 

Ambient Temp. 

Min./ point 

Test Started Ended 

SCHEMATlC OF STACX (CROSS SECTION) (j) , 

0<70) 

, . 

~lttl~ali, :;" ...... ""':"" . 

• 

PARTiCULATE FIELD DATA 

Page Two 

Puga L-) OF ~ 

PI'nt tE~rl Ct.)ii" PCcJCPS.1in j Run No. 1;1A::O erce ___ CoU_M " Filter No, :3 z.. 

rr ---i)

: Test Crew ~;t--;:) ;; Ambient Temp. d S~ ~~~~----~~=

, Day I Date \.NeJ , }'re, C? I Test Started 00'1 b Ended,) tJ 1./ f 

Meter Leak Rate CFM: Before (/ I 0 (JJ (c) J 0 "Ho After 0 I (J/) z.. @. / V "Hq J 

Pitot Tube leak Test Before Before I Z After " , V K Factor )" '2 ") 

GaS Sampill Temp. 3t" 

dry ga!> meter 

.". 

-I = . .,­

- '" =-"' 

Outlet 

~·o 

~c: . !il 

"..,., 
_____ __ _ 

PARTICUu\TE FJELD DATA 

Page One 

: nt Cc,m! i1 0, }CUc{ 2( "U>5}~j 

• rc~ 11>51 CoLJec/vL 

Nozzle Diameter - in. 

RC.£IJ5~ ;Ed Ambient Temp.

Test Crew ~=:f.:...:-~~_c) . Min.1 point 

Imp. Sox No. +'-'UI..4--"----,.-------­

j[lay I Date '" • 01 Test Started 

. , Pb in Hg :;tl , 0 SCHEMArrC OF ST~C"OSS SECTION) 

.1 Pitot Cp 0 . ce., t,.} -, Meter ~ H@--..-i=-)-.'~8-S-t-/-------

. Y 

Est. 

ractor 

% Moisture -L..~7'--d:--C/}..::.:::..i>----- } .00 <6) O.:JQ};Ur

; Psg - Static Duct Pres:::; ---r---ll.....J'-"_tJ_____ 


. Probe Wner Material _G..,...;7..,...;'1-5->_______ 


• . t-;.-~-;-'-~~-·~:-~--~-·.~--------Im-p-i"-m-e~-.-.Q-IU-m-5-m-I)~-·~-·----.--.---------~I--·-,·-.---··-·_-_-~~~

I .j o H~ijal.i-.~.. " ;: .......-:-. ....._­

. I" S~.lf~Ge~W~i~=- rI 

• 

PARTICULATE' FIELD DATA 


Page Two 


' Pan' 0(:,II C7. is-f' J p[vCRS ~In , Run No. ,-

Page 

• ree lli2i CoDe(:jV1 =_ Filter I:f­ r1 ----D , Test Craw +;t-'I ~ ij Ambient Temp. 3 () , 
 : Day I Date \.tvt J. .0 , Test Started .lIJr-::1..,:;---]Ir-'--f;-nd-e-d--"l!=~;j-7

! Meter leak Rate CFM: 8efore ~--~~~~~~ a ~(J;)t " kHq Af~ ,O/)::J @ b "Hg

Pitot Tube Leak Test Before After K Factor' j _2. "/ ----­

Gas Sample Temp. :Jr' 

dry gas mete!'" 
B(lIUG LABORATORltS 

lABORATORV IlArA 

L ? 

Sheet: 0 f ..;> 


Anal Y7.e-d-by-:-~l~)-h-.-h---::()-r7r9-n----:(~--= 

Date: 1 - J 7.. - 0 J 

Tare Weight final lJeigbt Weight Gain 

'i Iter No. (m9,) (1\19) (1119 )

<!IT 

- ;...,---­

'ro6e &front Half Wash:& ImQinq~r 'Nater ! Back . r:::;-S r I -;"0 .0) E9 Extractio~v 1 \later SOl!l~,~ (organic)V . (inDrganic~ 

(inal Wt.:: Of7 L/1Sl 'is I1Ig. iindWt.= Jo~(;3).JI mg_ linalwt.= )~) 0't.7 mg. J 

Tz Wt.= :17,1-/226 Ing. hre Itt.::: /0 0 , o?",?"7 mg. rare 'ilt. = 1'dfObt. C:> CJlg. 

.it • . 

, 

Gain ::: 

;; G2. 1. mg. !It. Gain = __..___J;....._/_ mg. 'ilt. Gain :: D'2 mg. 

~c !one Blank: (100 mIL) '.ia ce r Blank: (tOO mIl) Slank Correction Calc~lations:· - , samo a salllp e 


i"in~l Wt.:: C~ l/;)2. ~~. mg. tina! 'J\:.::: r; ~ 3.7'). v mg. Acetone :: Uml x O. Y 1119/100ml::: O.~ mg.
 ro.,,. G ) lL ')7. IL mg. Tare 'ilt.:::; G3 '3 ") s\.::> mg. 'liater ='i (J 0 ml x 0 mg/100ml:: 0 mg. 


;.t. 'Gain = CJ· "L mg. I~t. Gain :: O. i) m9. Corrections for Blanks: (). 'i mg{­

~ ~l Particulate: M:!isture: 

'i1 ter .... __ • . • • . • • •• • •• • • • • • • .. • • • . •. __L....I.:..•...,7'---- mg. Si lica Gel 

Fr !t~f!alf Wash ....................... ___C1..;..;...."l.::.-_:......... mg. ';/eight Aft~r. g. 307, z ! 

Ex 'action (organic) •• , ............... __.......____ mg. ''''eight Be fore, g. 3c;o·c,)U 

',4ablr Solubles (inorganic) ............ __.,-0....,·,...7..:.-__ mg. Weight Collechd, g. 7.1 I 

tin :rrected Particulate fotal •••••••• - _--.-JJ.{,....,,;:,,_.::!;3-.-__ ITtg. Volume Collected, mI. /YL:!t 

Correction for Blanks ................. _--==(£7-'_"...:.,/",,)_·__ 1119· Impinger 

~E iParticulate Total 15· <=) mg. Volume After, m!. i • • • • • • • • • • • • • • • •• --"--"~--

Volume Before, mI. 

Volume Collected, ml. 

Total Volume 1'oisture 

.4f Int-Kalf includes sampling train components up to and lllcludillg tile filter. 

I 

Back-Half is from tbe filter, up to and including the third impinger • 

• 

ml ........._---­
8£lIHG LABORATORIES 

LABORATORY DA TA 

She!!t: 	 -2. 	 of '3 ---------I~~----A·~ -7~--~------- Analyzed by: -J.} h-, C(t.? r 'inc ( 


Oat;: -)-_f-I-r)-=(~"-o.:....;J~~~--

Tare Weight tinal lila i qht '~eight Gain 


(mq) (1119) (o1IQ) 


G;;}6. iJ 	 G5).1. 

Total HI ter Gain:' =====L::J.::,;:~==== (rug) 

ImoinQer water ! 

Extractions' 


(organic)(f:; l.") 


Final Wt.~~ S¢~ ~ Tare Wt.:: '7~;) 5'00, D 


wt. Gain :; (J. '1l' 


Sack 

51>'" I 

. ::l~e a1 (100 0111) Ie ank: 1 Blank CiJrr~etion (;:lc~lations! - . sarno .8 

Acetone ;; 9 c.) ml x (,). Ymq/100ml:;: 6:.31'mg. 

'I/atel" }/dQ IIIl;c (;) mg/100mi '" <:::> mq. 

~inal 'oit. = (;} (/,;;--2)S :3.," G .). '/ '}? ? 

it. n::: 0,"') Corrections for Slanks: O. '/ mq/ 

io il Puticul~te: ,l.\Ji sture: :' "'-':~.:..:..:;.;;...;::".,::,. VI. V 

,"l ... t.ar .......... "" ..................... .., ....................... __......",.1..-.:::°;.,.....__ iug. 	 Sili.,C:l Gel 


;rnn;t-H;alf '!lash ••••••••••••••••••••••• ___1i..>.<.......__"l_'-._l1Ig. weight Af;!r, g. 


:x .~.cti()n (organic) ....... ...... ..... o. '6: mg. 'i/eight Before, g. 


-lat",r Solubles (inorganic:) ............ __.O,,:--_'_£)__ lIIq. Weight Col!.ect~d! g. 0.0", 


} L.J. 0 :.111 trected Particl1late Total ......... _......,...,~_-.-__ II1!1. Volume Coll:ectad, mI • 


Carrection fol" Blanks . . . .."" ........ _~~:_b,,:-'~~},--- mg • Imoinqer 


'1e1Particdate Total ••••••••••••••••• _.....L.)....:3:..-.--..;:.'____ IDg. 	 VQIume Aft!r, 1111. 

Ilohme Be fore, mI. 

Volume Collected, ml. ? di) 

Total Volume MJisture Collected l f, () b ml 

or ~t-HlIli includes sampling train components liP to and including the filtar. 

8o~~-Half is from the filter, up to and including the third impinger_ 

t

• 
fare 'lieight fillal '"eight ';/eiQht Gain 

7il tar No. (ma) (mq) • (mq) 

_V33 

Total fIlter Gain: =====&='='=== (mg) 

Imoioaer Water &aac~ , ~: Yash~ 

£:x:tnctiaru: S"Vl I 

(organic) m~) 

final Ioit. ;; -,.r...';""':;.J-"';-"';""':---IL.. mq. final '~t. ~J" 20. , 1119. tinal 'ilL '" _":-;{...~~~::.:....,-....:m9. r;, \

, Wt. :; Tare ''''to '" L?Zl{;J9.t mg. Tare 'tit.;: 

____.;...-__ mg. lit. Gain :; ) • V IIIg • '>It. Sa! n ::. 

'i/atH Stqnk: (100 mil) Blank Cor.actioq CJlctllations: 

pmp e 

rLnal 'lit.:; Co ~32 SiD mg. Acetone :; ) I;-'''''>::Il x 0. Y !1lg/10Qml :: O. ',,/ mg. 

Tm ''';t.::. G; ')?~.;> mg. 'liatar ;; Ve.4:..> ;111 x () mg/100ml:: 0 1119. 

lilt. Gain :: O·r) mg. Corrections for 8lanks: O· 'I ;ng/ 

,"tlishr'! : 

..... i 

:i. .. ~:er ... "" ............................................... __ 

+---=-___ 

...!.O!..~___ mq. Silica ridl 


Fr"?t-Hal f 'i/ash ............., .......... _~~:......:=----.:...._ mg .. 'Me i gil t .~ftar, g. 3v~'L 2 


.:; ~ac;tioll (organic) .................. __ mg. Weight '3c,V.<:/u SerJra, g. , 


'1Iat~r Solubles (inQrganic) ............ _---,,;...,:-...1...-___ mg. ',o/eight Coil'!ctad 1 g. ~')7 ; 


Ur. /rrected Particulat; fotal ......... _-s....q..,,---L.....-+--

i:QrreGtioo for Blanks .. o9' ........ -- ...................... -......-,,..-'-r-':::"""......--

I1Ig. 

mg • 

Volume 

Imoinoar 


Collected, ml. 
 ~ 

:if .; ?articulat~ rocal mg • .. ...... .. .... " " .. ,. ............ ---:-=--'--- Volume Mter, mL 2u>uv 
 'j lJolume 8efor~ , ml. 'd O;.J. <:..D 

)..tlV Vo lume Co Uected, atl ~ 

Tatal Volume Mii sture 1111 

-I ;nt-Half includes sampling train cOlllponents up to and including the fil hr. 

L~~k-fia1f is from the filter, up to ~nd including the third impinger • 

• 

METER CONSOLE CALIBRATION 

• 	 NamtS)}hJl10Ik,n~l D:m' Lj_;;-.U 0 

C(m~)k Illl, Or\" vi.LS m~:t~'r tlO, 7 Dr\' \J':.l~ 111l'{l'r rOl'rt'niol1 I':u:mr , ,.., (q.,. "> ;/5S"" ' ;'., -­

WI'\ (\':'it tnt'l\"r Illl,] 7'£l5~/o8 . C()I'I·p~·tinn f"Jrtor yw -::-0 .C7CJ ;;; f5 . 

B:11'tlllWtril' [In':-~un'. I'hJOJ.:2 G ill. I I,\{ fH'I'\'i!lll~ ~'~dibl'aliIlH ;lI\d tlaLl' C·)t· '7<::t 

.; . 

• 

T\tmll~·r.HU rt' 

Orifin· (;a~ \ !llu m", (;a" \'(}\umt' w{'\ I')ry J(J~ ml;'tl;'r 

manomcu.'1' w\:t I~":II II r: "';I,, ~('Hin)(. m~'u.:r Jnl'H'r :'>11-11:1' inl,-, OUlh:\ AY<:1"J.gC Tim... 

..lit, \' ,.... VII, I,... 'di' ItllI' ld· II 

'in, H:!() r,:! (,:1 OF OF .~ or min '/ 

Calcu!ation~ 

..lH 

.lH 

13.0 

.,. 

r ,".Pb"d _""' ~ \'d(Pb + ~~:) (I,.. + ~60) ,} ~ 

.lHq;; 

O,0317.lH [(I.... ~ -160)1;1 T 

Pb(ld -+- 460) 'Yw\/ I.... 

0.-:; O.O~G8 I,OV)6 I,,?)D 

1 ' () C).Ojj5 ), (7" 53 J.C"7Sl/ 

d. D 

3.0 

'-1. .) 

S',O 

O,j/}7L 

0, ;)")0(. 

o. -:nlJJ 

O·~7b' 

1. 000; 

).0 l3J 

.(;}01 

, Q 0 7"/ 

. '9<57 

.,~ d) 

70St..j 

' 7130 

• 

" '" Ratio nf .)'·I'Ur:H'y u( WI't !t'~1 nWl\'r I" ,II'\' 1\.,.1 m('\<'r, '1'ul"I':1I1<:\' = ± 0.01. 

.lll@ ;: Orilin' jln'~ur\' dirr"n'm;:!1 that ~in'":o U.7:", ,'fm uf <lir :.11 sa Of ~nd !!9.92 indw:I of m!:'rI'IIfY, in, 1I:!1l. '! 11'·f.ll\~·\' .: ::: (1.1;i iltdlt'3, 

Urifi~,· ':'II@ ,1.1I1Il1'! Ldllu'lh',,\,U I.;"'!) :!..O!I indw.... "" mudifit'Jtion m:ly bl' nt'c!:'ssary for somt' 

.,.II11i'lill~ ~iIU.ltit,,~,. 

figure -4-:'3. 	 Form for mo:ccr <;ocuolc c:::dibT:Jdon 

i 


i 

!--

CALtBRATtOH DATA: 

. p(t: .-jP5} . PAA!~~pro€DI • 


·Mdbod... • &Ad. Ii (){ Ap~lx /'0. or ~ 

O"'R par( 00 .'" .met1ded ~~ {olkrw..: 
 fne/i?r I 

t:By.•d<i1ns .. a.;'" &ct1Q~ 1:.:1..1 10 
 • 

M'\lho.:! 4." {Ql!crw..: . 
 C c,./I.brC;;I/~ )..I~'(.~do<sol~""'" ~w<d l:.. S(..,;£ ·C.....;..··· . 


....; ,".. .. ..,. 
 ) . Ja '- UJ 

I 

~ ·i.'&ft:~<:""" ).(,,(/1«1. 

..... 

• 

: l,>~cf Avg. F 

Tm- Outlet;.; 

Avg. 

:i.vg. 'F 

0.0319 Tm ) ~ 

Pbar 

F 

10 ­ V:n 

• r i 
'00)7 ~ R'7/ 


• 

METEk CONSOLE CAUBRATI0N 

/~, / prCXI'55/1?..:J )-)(0)" 01;J.m~' L.-C1cfjl ll O· ~/' nal~' 

• 


T<:mp<:r,Uun' 

OriCk.: (;;a \utum~- G~:. -:.)Ium,· 'I'.l't 11 r.~- ).(~~ tn..-t...!' 

rn:lnomt'll:r w.... t l~':il c!r~- ~J~ 

~~,tlin~. mltl<:r m ... t~'l' :H~'It:I' ~nll.'l Outh·( Av~r;j~": Time 

..HI. \' W' "'d' t w ' 'dl' tell)' It.!. II 

in. H ...l) r,:.I f\;\ "'r . "'f of or min i .lH@ - \ '/ :l;, .0 8J's:¢ 

~~.... .....) ~~~~~ ~,,7) lIe 7'6 'co "7.3 16'·~b o~ ).~"VI5 ).0 ~1C~(e;:<$I"\ .~ v.~~ ....)) 77 Sit? 7L IKe; i~.S'1.7 PM~ Ltt6 ? 

1.0 1 ~'~.t:'>(5 'f.''') ft; $./:1~ 11 'in 76 ?>}. C; 15. s'1:? ~."'$! ]'(,51<:> ... 

A ... <:r:l~1.' ~l''}~) j.,,'r$/ 

Calcul:lIiom 

r I .lH@ 

.lH 

"wP b!ld +4(0) --.,. 0.0:1 I i..\H [(I w -jo -1(0)8 r ..HI l:l,o \'d(Pb;' ..l.H )(tw +-160 '/,.,. Pb(ld + -toOl v w'l"­

1:l,S ..1. 

\.0 I 0 .. (;> 7, (" Ct ,ar;'7o~ /. G'7¥J5' 

\.0­ U -t:J7!>(" o .o,t:) /'2 ),({o e.. 

1.0 V,(:;17).~ 0' .0~<j.;,K 1-c cj i) 

.., Radel "r ..I,',ur:R}' (If wl't It'":>! mC'tt-!' til tlry tnt mI"'HT. '!'o!\'r:l1Il'l' "'" ± 0.02, 

..lll@ = Orilkl' pn'"ur,· dirr,'n'tHial (h;l( gin-:. o:m l'fm UI "ir at 68"F:md 29,92 illdws of m("r· 

• <'\11';, ill, lJ~n. '\.,h-r.III"(­ .; ::: n. E', it;dw~. 

Orifi{,' ..11 f@ ,1:",/1,1 f.tli IWlh',-\'U I,;l~l . :!.I)!I il1d1,·,. ur !l'Io<lific;-;nilJn m;:t~' U(" nt'cC'ssary (O( sam,' 

1> •.1111 plio.l: ~itu..l t iOll." 

Figure 4<1. torm for meter console (;?iibr.Hlon 
• 


! 

;-; 

• 


-.l-l_~}!.....::...6_ ... o_)~_~ 

Tt:mp~'I";;lur\:' 

()ri{it'~' (;~~ HILum\:' Ga!> ."Iuln,' \\',-, ll..:y )(:l~ m...lcr 

tn:lI1Umt'lt'r wt't 11.'31 dl'~' ~J~ 

WII i 1'1)(. m~'It:r rn..·tt:r .'oh·lt'r Inl...! Oudl:l A~ ... r::~t' Timt' 

.lli. '"w· Yd' t .... Idi· 'duo Id­ /I 

in. H:?,1i f!:l ft:! <IF "F . .y .f' min i ..\H@ 

J." '~~ B..,J "".S'.}? ...V77 07. ·7 '6 $1:;­ .Clyj O~!I II/I). I); J. '?~" ~.D .~) 14~,?J;'A~''''') 77 .?i.I

! ~o '()7 ",·/~ 611'14-. 1·7?~L 

?.f) . 7:f; ~r..>I» ilfJ;:Sj f? ,.,.,) 7; '77 '-67. (f7. .; '(,., 7 b ,'*:;1 t 711}S 

1 I 

I I 

I I 

'\\'1:1":1)1;"­ p.<7'3Jl 

/ J. ?cOo 

Calculation:; 

-r I j,H@ I ---... -

...iIi O.Oj",H [('w .46"q'l Vw?b(ld +-460) 

.lH Vd(Pb +­ ..iH )(t w +-.Hi1'jf;.'r- Pbltd +-1(0) Vw 0 

1:3.5 • 

i d. w (/.) 'J7J 0.0,0, tJ? 1.6?e" 

?f) P.jl)7J 0' .J>;t:7J ~- J, ?";} fs'O 

?-t/ CP.} Lj7/ 0' 0C?3J } .?J Y s 

-I Ra~i" or ..1l'nJ.r:u--:, Dr Wt-t a-:.t Int't('r tcJ dry It.." m~·U'r. Toll-r:lI1C,' "" :!:. 0.02. 

.l1l@ .. Orilit't' prt.."utt' dirr"r~'!llial th:1l ~i\'l"" 0.75 "fm ur ail" al 68"Fand 2:9.92. inclw:I or m{'r· 

I'\lry_ in, II:!(J. 'lolt'r;lIln- -= =0.1;i irldw-s. ­

Ul'i(in' ..ill@' _,I.lnuld r.tI! ]u'I\':n-1\ I.:,!) - :!.ll!l indln. or tmlllific:.tdun m:lr Ix- n<."('"ssuy ror scm... 

>..It1lplilll-\ ,iIUJtillll.', 

Fig'uI'O: 4·.3. Form for mO:I<:r- como1.: c::dibntion 

-------------------------

• Compliance Emission Test 

Operating Data 

Owner: CC; ; 1) CcJ( t?=> r~;~~ oate:_1_-_l_o~.._()_,_ 

saurce:f>'eV~ dVJ1 COJ&Cjp. Permit #: LC~) D1t 00 C) 

Types and sduI'ces ( If any) of Fuels normally Burned 


Type of Fuel Burned During this test.______________________ 


If Fuel Is used Approximate Quantities of each listed above burned AnnuaJly________ 

Recyding Capability Yes~_ No X 


Recycling in Progress Yes__ No '"?f 


eero!3§S cata Dyring Runs 

Maximum Continuous Process Rate (Manufacturer's Rating)_____---l---!.-!---,..:-____ 

Historical AVerag~ ProceSs Rate,~____..I.-::d+_()_(.)_0_..JL.::::.::.:.!....:...:::.....:::_4_:,.L---­

Historical Maximum Process Rate.____-+.,l.(.,~~~-_4..c:::.:::::.~L--J-_____ 

Procass Rate ­

(gallhr, lblhr, tonslhr, etc ... ) 


rI'OCSS!!I Rate Wet 

Percent Moisture (%) 

ProcesS Rate Dry 

How PrrlCSSS Rate was 

Determined 

PersOI1 Responsible for Data,~.4c..t::...J/_...I..l<~r~r....J.'e....;ff--E..r?~I- ________--___ 

S~w~ ()f!~ _ 

l1UeJPosWon -ii:tJ:c.i;j.,~

• "'" Please farJicats in the same 1J.CJ.;ts as \tour hisforicallnfQ/TWltl!;a 
-------------------------------------

AIR POLLUTION CONTROL EQUIPMENT OPERATING DATA· 


• Actual Production 

R-u-n-N-o-.p-y.-~~b-h-I~-~;-;

1 rC;vffJt( 

.....:.....-;;~"'-'r'-"-~~~=-rr~--..+- Locatiop Cfo(c.r }2C?/ir/J..;:;r·// +--~~~'---I"'-=Z..a,~~...:...:::.l!!..:~~ Rated Production ____ ___ 

__~~~~__~~~~___________ 

Mechanical Collector: 


Tube Dia. in. No. of Tubes _. Design p __in. H20 @ Gas Temp _oF 


Observed AP ___in H20. Design dm/tube @ Observed AP @ of. 


Fan Rated HP. Operating Volts . Operating Amps 
-~

Electrostatic Precipitator: 

Primary Primary . Secondary Secondary Spark 

Field Voltage Current Voltage Current Rate 

No. (volts) (amps) (KV) (rna) (per min.) 

e. 


Scrubber: 


Type _~_______-,._ .e.p (across scrubber) _______in. H20. 


Fan Rated H.P. Operating Volts Operating Amps ____ 

Liquid Circulation Rate gal/min. % Make-up __~. Blowdown __............ gpm. 

Scrubbing Water Change Interval ____________________ 

Settling Tank Cleaning Interval _____________________ 

Baghouse: 


Pressure-Positive ----- . Neg,ltive X. . No. Compartments 16":5'" . 
 Type Cleaning I~ ~ Clean Cycle min. 
 If If • 0 Avg. Baghouse ~p ..( t:r in HP.AP Range 3.. - 7 In. H";! . 


Fan: Rated H.P. IlJd Operating Volts !-ur() Operating Amps __~_ 

Cyclone: 


Type _____ .o.p _____in. Hp. Diameter __________ 


Fan: Rated H.P. ____. Operating Volts ____ Operating Amps ____ 

Person Responsible for Data: ________________ 

• 

Signature:______....... _·-'..'";:--__________ ___ 
 '. TitTeIPosition: 

'Averages of operating dow taken <.luring utlu;)1 lcst run unless requestcd otherwise. 

A-6