a. ~--- -D [)_,-8 C· 

ll-1-002 

RECEIVED 

'l 

JUL 3 D ·i 

REGION 7 . j 

TfXAS AIR CONTROL BOARD ___ n 

Exhaust Emission Sampling 

Acme Brick Company J~/ 

Sealy, TX (2 7_.. ( t7 

June 18, 1991 Armstrong Environm~ntal, Inc. Project W-1059-91 

Report Prepared For: 

Mr. Dick Ethier 

Acme Brick Company P.O. Box 397 

Sealy, TX 77474 

Report Prepared June 21, 1991 By: Armstrong Environmental, Inc. 4747 Irving Blvd. Suite 204 Dallas, Texas 75356 

(214) 631-0021 

AP-42 Section 

Reference 

Report Sect. 

Reference 

I 
I ' 

I ; 

ACME' 

BRICK 

d'mt I I .PI 

July 1, 1991 RECEIVED 

JUL 3· J991 

REGION 7 

TEXAS AIR CONTROl BOARD 

<; 

Randy Hami 1 ton 

Texas Air Control Board 

Permits Division 

.· ..._~~ 

6330 Hwy 290 E 

Austin, Tx. 78723 

Dear Mr. Hamilton: 

This is the test that was done by Armstrong Environmental, Inc. 

in regard to our permit R-9540. 

If you have any questions, please call. 

Sincerely, 

;!~~ 

R. Ethier 

Regional Engineer 

cc: Jodena Henneke 

Region 7 

INc. ! I 'i C~ry 5 /-.., ( 

?'""~ ;VIc..ot..._~, 

ACME BRICK COMPANY 

A DMslon d Justin lndustl1e8, Inc. 

D n AtW "C/7 _ SEALY. TEXAS 77474 - TEL: 4091885-4124 

I 

f 
CONTACT REPORT--MRI Project No. 4602-01 

From: 

Date of Contact: 

Contacted by: 

Company/Agency: 

Telephone Number: 

Brian Shrager, Environmental Engineering 

Department 

April 19, 1995 

Telephone 

Acme Brick Company 

(817) 382-3573 

Person(s) Contacted/Title(s) 

Mike Vickers 

CONTACT SUMMARY: Mr. Vickers was contacted to obtain 

production rates for the 6/18/91 emission test conducted at Acme 

Brick in Sealy, Texas. The report stated that 16 cars per day 

were being produced, but did not include the number of bricks per 

car or the weight of a fired brick. Mr. Vickers stated that the 

fired bricks weighed 4 pounds each, and that each kiln car 

carried 14,400 bricks. These data will be used to determine the 

tons per hour of fired brick produced during the test. In 

addition, Mr. Vickers stated that the kiln scrubber is a packed 

bed tower that uses 1/8" to 3/8" limestone as the scrubbing 

media. 
I. 

TABLE OF CONTENTS 

I. INTRODUCTION 

II. SUMMARY 

III. PROCEDURES 

IV. APPENDICES 

A - CALCULATION SUMMARIES 

B - ANALYTICAL SUMMARIES 

C - FIELD DATA SHEETS 

D - OPACITY SHEETS 

E - PRODUCTION DATA 

F - EQUIPMENT CALIBRATIONS 

G - RESUMES 

Page 

1 

2-19 

20 

21-29 

30-49 

50-59 

60-65 

66-68 

69-94 

95-99 
1.· 

I. INTRODUCTION 

A series of tests were performed on the Kiln exhaust stack and 

the Dryer Room exhaust stack at the Acme Brick facility in Sealy, 

TX on June 18, 1991. 

The purpose of this test series was to determine compliance with 

the Special Provisions of Permit R-9540. 

Testing was conducted following procedures detailed in Title 40: 

Code of Federal Regulations (40:CFR). 

Sampling was performed by Richard Taylor, Jerry Salinas, Larry 

Whicher, Tom Armstrong and Matt Taylor of Armstrong 

Environmental, Inc. using four NAPP Model 31 sampling trains. 

Sampling was performed over a seven hour period. 

Submitted by: 

Armstrong Environmental, Inc. 

Richard 

~~ Taylor 

Project Manager 

RT/os 

@ 

1 
a. 

II. SUMMARY 

A series of tests were performed on the Kiln exhaust and the 

Dryer Room exhaust at the Acme Brick facility in Sealy, TX on 

June 18, 1991. 

Sampling was performed following procedures detailed in Title 40: 

Code of Federal Regulations. 

Results of this test series are summarized in Tables 1 and 2. 

Witnessing the test series was Mike Vance of the Texas Air 

Control Board. 

The emission rates for Sulfur Dioxide, Hydrogen Fluoride, and 

Particulate Matter in lbs/hr. are as follows: 

2 

3 

Average 

RUN t 

1 

2 

3 

Average 

KILN EXHAUST STACK 

POLLUTANT EMISSIONS,lb/hr ALLOWABLE 

Particulate 4.107 7.3 

HF 0.0675 0.6 

S02 12.14 28.4 

Particulate 4.241 7.3 

HF 0.0762 0.6 

S02 12.56 28.4 

Particulate 4.903 7.3 

HF 0.0846 0.6 

S02 12.47 28.4 

Particulate 4.417 7.3 

HF v--0.0761 0.6 

S02 v12. 37 28.4 

DRYER ROOM EXHAUST STACK 

POLLUTANT EMISSIONS,lbs/hr ALLOWABLE 

S02 0.4261 0.6 

HF <0.0107 0.3 

S02 0.4445 0.6 

HF <0.0113 0.3 

S02 0.5140 0.6 

HF <0.0134 0.3 

S02 0.4615 0.6 

HF <0.0118 0.3 

2 
II. . 

Opacity readings were taken for three hours on the Kiln exhaust 

during the test repetitions. No visible emissions were detected. 

Test results indicate that these two sources are in compliance 

according to the Special Provisions of Permit number R-9540. 

3 7 
I. 

SUMMARY OF EMISSIONS TEST DATA 

TABLE: 1 

PLANT: Acme Brick 

LOCATION: Kiln Exhaust 

OPERATOR: R. Taylor, J. Salinas 

TEST DATE: June 18, 1991 

REPETITION: 1 

STACK GAS 

Temperature, F 

Velocity, fps 

Volume Flow, acfm 

Moisture, % 

C02, % 

02, % 

SAMPLE 

scfm 

scfh 

Start Time, hrs:min 

Finish Time, hrs:min 

Volume, scf 

Isokinetic Ratio % 

SULFUR DIOXIDE 

Sample Weight, mg 

Concentration, ppm 

Emissions, lb/hr 

HYDROGEN FLUORIDE 

Sample Weight, mg 

Concentration, ppm 

Emissions, lbs/hr 

Particulate 

Sample Weight, mg 

Concentration, gr/scf 

Emissions, lbs/hr 

OPACITY 

Highest 6 min. Ave. 

281.2 

66.41 

48005 

31391 

1883483 

8.142 

3.0 

18.0 

9:55am 

9:59am 

29.367 

97.33 

86.24 

38.94 

12.14 

0.2472 

0.6934 

0.0675 

29.04 

0.0153 

4.107 

0 

4 

2 

282.5 

65.86 

47607 

31225 

1873479 

7.705 

4.0 

18.0 

11:42am 

12:45pm 

29.319 

97.68 

89.53 

40.49 

12.56 

0.2775 

0.7869 

0.0762 

30.10 

0.0158 

4.241 

0 

3 

281.3 

66.43 

48024 

31527 

1891614 

7.770 

3.0 

18.5 

1:08pm 

2:10pm 

29.614 

97.72 

88.98 

39.81 

12.47 

0.2956 

0.8650 

0.0846 

34.81 

0.0181 

4.903 

0 
I. 

SUMMARY OF EMISSIONS TEST DATA 

TABLE: 2 

PLANT: Acme Brick 

LOCATION: Dryer Stack 

OPERATOR: L. Whicher, T. Armstrong 

TEST DATE: June 18, 1991 

REPETITION: 1 

STACK GAS 

Temperature, F 

Velocity, fps 

Volume Flow, acfm 

Moisture, % 

C02, % 

02, % 

SAMPLE 

scfm 

scfh 

Start Time, hrs:min 

Finish Time, hrs:min 

Volume, scf 

SULFUR DIOXIDE 

Sample Weight, mg 

Concentration, ppm 

Emissions, lb/hr 

HYDROGEN FLUORIDE 

Sample Weight, mg 

Concentration, ppm 

Emissions, lbs/hr 

105.8 

57.71 

67975 

59860 

3591585 

5.292 

0 

21 

8:50am 

9:20am 

15.450 

0.824 

0.7167 

0.4261 

<0.0212 

<0.0579 

<0.0107 

5 

2 

108.5 

56.39 

66414 

58696 

3521744 

4.544 

0 

21 

9:53am 

!0:23am 

14.522 

0.824 

0.7625 

0.4445 

<0.0213 

<0.0622 

<0.0113 

3 

108.5 

56.95 

67078 

57914 

3474850 

6.748 

0 

21 

!0:55am 

!1:25am 

12.389 

0.824 

0.8938 

0.5140 

<0.0216 

<0.0744 

<0.0134 
a. l'=l'l~,.. --·:.i 1· :; , .. ~ ; ':- ··a· r. • . ; , .'. • ! ":_-) , I 

'--' L' -..a~ ~ ~ 

GENERAL PROVISIONS 

R-9540 

MA39 5/90 

1. Equivalency of Methods - It shall be the responsibility of the holder of this permit to demonstrate or otherwise justify the equivalency of emission control methods, sam- pling or other emission testing methods and monitoring methods proposed as alternatives to methods indicated in the provisions of this permit. Alternative methods shall be applied for in writing and shall be reviewed and approved by the Executive Director prior to their use in fulfilling any requirements of this permit. 

2. Sampling Requirements - If sampling of stacks or process vents is required, the holder of this permit must contact the Quality Assurance Division of the Texas Air Control Board (TACB) prior to sampling to obtain the proper data forms and procedures. The holder of this permit is also responsible for providing sampling facilities and con- ducting the sampling operations at his own expense. 

3 • Appeal - This · permit may be appealed pUrsuant to Rule 103. 81 of the Procedural Rules of the TACB and Section 382.032 of the Texas Clean Air Act. Failure to take such appeal constitutes acceptance by the applicant of all terms of the permit. 

4 • Construction Progress - Start of construction, construction interruptions exceeding 45 days and completion of construc- tion shall be reported to the appropriate regional office of the TACB not later than 10 working days after occurrence of the event. This provision shall not apply to operating permits. 

5. Recordkeepinq - Information and data concerning production, operating hours, sampling and monitoring data, if appli- cable, fuel type and fuel sulfur content, if applicable, shall be maintained in a file at the plant site and made available at the request of personnel from the TACB or any local air pollution control program having jurisdiction. The file shall be retained for at least two years following the date that the information or data is obtained. 

6. Maintenance of Emission control - The facilities covered by this permit shall not be operated unless all air pollu- tion emission capture equipment and abatement equipment are maintained in good working order and operating properly during normal facility operations. 

6 
1 .. 

I 

SPECIAL PROVISIONS 

R-9540 

1. This 

listed permit covers only those sources of emissions in the attached Sources table entitled 11Emission - MaximUlll Allowable Emission Rates, 11 

sources are limited and those to the emission conditions specified limits and other in that attached table. 

2. Fuel fired in the brick manufacturing facility limited to pipeline is 

other fuel will quality natural gas. Use of any require a modirication to this permit. 

3. Emission 

opacity as 

from 

determined 

the kiln stack shall not exceed 5 percent 

occurrence of visible by EPA Reference Method 9. The emissions so determined be considered a violation shall also 

matter of the hourly particulate (PM) mass emission 1. limit of Special Provision No. 

4. 

and 

The 

other 

holder 

testing 

of this permit shall perform stack sampling as required to establish pattern and quantities the actual of air contaminants into the atmosphere being emitted 

Sampling shall from the kiln and dryer stacks. be conducted appropriate procedures in accordance with 

Manual and EPA Reference of the TACB Sampling Procedures Method 9 for opacity. 

The holder of this permit is responsible sampling and for providing testing facilities and conducting sampling and the testing operation at his expense. 

A. The 

contacted 

TACB Regional 

as 

Office in Houston shall be soon as testing less than 45 days is scheduled but not prior·to sampling pretest meeting. to schedule a 

The notice shall include: 

1. Date for pretest meeting. 2. Date sampling will occur. 3. Name of firm conducting sampling. 4. Type of sampling equipment s. Method to be used. or procedure to be used in sampling. 

The purpose of the pretest meeting necessary sampling is to review the and testing procedures, provide the proper to 

pertinent data forms for recording 

for submitting 

data and to review the format procedures the test reports. 

A 

from 

written 

sampling proposed description of any deviation procedures specified in permit 

7 

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

/I 
I. ( / 

I 

/ 

I 

( 

DRAFT 

provision or TACB or EPA sampling procedures be made available shall 

pretest meeting. The 

to the 

Regional 

TACB at or prior to the 

Director of Director or the 

approve or disapprove 

the Quality Assurance Division may of any deviation specified from sampling procedures •. Requests testing for any pollutant to waive specified in B or c of this provision shall be submitted Permits Program. to the TACB 

B. Air contaminants exhaust stack to be tested for from the kiln include (but are not limited to) HF, so2 and PM. 

c. Air contaminants 

room exhaust to be tested for from the dryer include (but are not limited to) HF and so2 • 

D. 

the 

Sampling 

new maximum 

shall occur within 60 days after achieving production rate of 16 cars/day, but 

kiln 

no later 

following 

than 180 

the days 

completion after initial startup of the of construction on the plant expansion. If the normal production exceeds by more rate than 10 percent during sampling, the rate maintained the company must notify Regional Director the 

require additional in Houston and the TACB may sampling continued to demonstrate compliance with the emission limits of this permit. 

E. Two copies of the sampling forwarded report shall be 

is completed. to the 

Sampling 

TACB within 30 days after sampling reports shall follow the format requirements Sampling Procedures Manual. 

of Chapter 14 of the TACB 

distributed as follows: The reports shall be 

One copy to the TACB Regional Office one copy to in Houston. 

Office. the Permits Program, TACB Austin 

5. Hydrogen fluoride shall be sampled at the exit of the dry scrubber. The use of stain tube indicators or a portable analyzer specifically designed for measuring HF concentration in ppmv is acceptable Any other method approved for this evaluation. by the Regional Director or the Quality Assurance Division is also acceptable. A hot air probe or equivalent should be used with stain tubes to prevent introduction becuase of high of error in results stack temperatures. With stain tubes, three readings should be averaged to obtain one result. commencing 

sampling shall 

upon be 

initial startup of the dry scrubber, conducted on a weekly basis and shall 

8 

----· ·----------

/} 
a. .·. 

/ 

/' BY:TACB 9-20-90 ;11:56AM 03 .... 713 346 1159;# 5 

D·RAFT 

continue at this frequency for the first month of operation. Then, if these results consistently indicate scrubber outlet HF concentrations less than 7 ppmv (4 ppmv at maximum kiln air flow), the sampling shall be performed at least monthly. These measurements will be used as an indicator of compliance. If the measured concentration is above 7 ppm HF, the TACB shall be notified as soon as practical and additional testing may be required. 

6. Kiln exhaust shall be routed through the scrubber during all periods of kiln operation. Any bypassing of the scrubber or scrubber malfunction that may cause excessive emissions shall be reported to the Houston Regional Office as soon as practical, but not later than one week after such occurrence. Each report shall include a discussion of the conditions that necessitated the bypassing or caused the malfunction. If a full bed of limestone is not maintained, HF emission sampling shall be conducted daily during the period until the supply is r.eplenished. 

1. The following information shall be made and maintained by the source for a period of two years on a rolling retention basis and shall be made available on request to representatives of the TACB or EPA or any local air pollution control program having jurisdiction: 

A. The results of all HF emission indication tests of the scrubber exhaust. 

B. Any period of kiln operation during which the scrubber is bypassed. 

c. Limestone consumption of the dry scrubber. 

9 
13. 

'fl,j,j40 ll:l::t;+;o 

EMISSION SOURCES - MAXIMUM ALLOWABLE EMISSION RATES 

R-9540 

his table lists the maximum allowable emission rates and all sources of air contaminants on the-applicant's property covered by this permit. The emis- sion rates shown are those derived from information submitted as part of the application for permit and are the maximum rates allowed for these facil- ities. Any proposed increase in emission rates may require an application or a modification of the facilities covered by this permit. 

(1) 

(2) 

(3) 

(4) 

Kiln Exhaust Stack 

W/ Dry Scrubber 

Dryer Room Exhaust 

AIR CONTAMINANTS DATA 

Air Contaminant 

Na 3 

S02 (4) 

HF (4) 

PM 

co 

voc 

NOx 

-S02 

HF 

28.4 

0.6 

7.3 

1.2 

0.2 

3.5 

0.6 

0.3 

68.9 

2.5 

32.0 

5.2 

o.s 

15.5 

2.7 

1.4 

Emission point identification - either specific equipment designation or emission point number from plot plan. Specific point source name. 

VOC - volatile organic compounds as defined in General Rule 101.1 NOx - total oxides of nitrogen S02 - sulfur dioxide 

PM - particulate matter as defined in General Rule 101.1 co - carbon monoxide 

Hourly rates derive from highest one-hour emission rate measured; annual rates derive from average of three one-hour emission rate measurements. 

Emission rates are based on and the facilities are limited by the following maximum operating schedule: 

Hrsjday~2~4 ______ Daysjweek._.7 ______ weeksfyear __ s~2--__ or Hrs/year ____ ~s~7~6~o __ __ 

IJ:BAFT 

10 \~ 
I. 

Company Name. __ ..;;.;A;.;;.cme.;;;;.;;......;B;;;.;r;..;i;..;c;...k;.._ ________ TACB Account No. _________ _ 

Ci ty __ Se_a_l4

Y __________ county Austin TACB Region ___ ? ____ _ 

Testing required by: ___ T_~_CB __________________________ __ 

TACB Penni t No. R 9540 PSD Penni t No ·------...:NSPS SUbpart ______ _ 

(INCLUDE A COPY OF PERMIT SPECIAL PROVISIONS) 

Source Tested Kiln Exhaust Stack TACB E. I. Point No. 1 ------- Stack Height ____ ~7~2....;f~t~·;..._ __________ ___:Stack Diameter ____ ,_·_~4..;;.;7...:i=n=ch==e=s ___ ___ 

SAMPLING PORTS LOCATION: 

Downstream Distance to Obstruct:i.on:--_....;1;...9_f_t_. _ Upstream Distance to Obstruction 22. 5 ft. 

Checked for cyclonic flow?_x_Yes __ No Cyclonic flow present? __ Yes...x__No 

(INCLUDE A DRAWING OF 5rACK SHOW!ro SAMPLING PORTS & MEASURn1ENTS) 

Design Operating Rate:---------------...:Maximum Operating Rate 16 cars/day 

Normal Operating Rate Operating Schedule 8760 hrs/day 

TACB Test Observer ___ ~Mi='=ke~V~an==ce~-------------

11 
I. 

Company Name. _ ___;;A:.;..cm_e_B_r_ic_k __________ TACB Account No. __________ _ 

City Sealy County ___ A.;..u_s~t~i~n _____ TACB Region.-~7~------

Testing required by: ___ T_A:_CB _________________________ __ 

TACB Permit No. R 9540 PSD Permit No. _______ ..,:NSPS Subpart ______ _ 

(INCLUDE A COPY OF PERMIT SPECIAL PROVISIONS) 

Source Tested. __ ....;;D;.;;ry~er.;;.....;R;;.;.oo;...;;.;;m__;;Exha;;...__us_t _________ TACB E. I. Point No._2 _____ _ 

Stack Height~ ____ 65_f_t_. ________ ~Stack Diameter ___ 6_0_in_c_h_e_s ____ _ 

SAMPLING PORTS LOCATION: 

Downstream Distance to Obstruction 23 ft. Upstream Distance to Obstruction 40 ft • 

Checked for cyclonic flow?~Yes __ No Cyclonic flow present? __ Yes_x_No 

(INCLUDE A DRAWING OF STACK SHOWIN; SAMPLING PORTS & MEASUREMENTS) 

Design Operating Rate~---------~Maximum Operating Rate 16 cars/day 

Normal Operating Rate Operating Schedule 8760 hrs/year 

TACB Test Observer_~Mi-·~k~e_V.;..an~ce~----------

12 
a. 

FIGURE I 

.C7" 

0 

13 

22.5' 

1!r 

ACME BRICK 

KILN EXHAUST 

17 
I. 

FIGURE II 

AQ.AE BRICK 

DRYER STACK 

6011 

0 

23' 

14 
a. 

) ' 

1 

·j 

., 

Pollutant Sampled: .PM· KILN Exhaust --------~~~~~-------------------------

Run No. Run No. · Run No. Run No. ,. Results 

Date Sampled 6/18/91 6/18/91 . 6/18/91 >< 

No. 

Time 

of Points Sampled 

-~~ 

24 

0:59an: ~ 

24 

5p 

I 

• 

I 

~ 

24 

lQpm 

I 

I 

I 

~ 

_,.,-

~ ~ --.......... 

Operating/Feed Rate 16 cars/day 16 cars/day 16 cars/day! 16 cars/day 

! 

~ Operating Rate (Maximum) 100 100 100 i 100 

Stack Temperature 281.2 282.5 281.3 281.7 

Stack Flow Rate (DSCFM) 31391 31225 31527 31381 

Percent Moisture 8.142 7.705 7.770 7.872 

Percent Oxygen 18 18 18.5 ' 18.17 

Percent Carbon Dioxide I 3 4 3 3.333 

Percent Isokinetic 97.33 97.68 97.72 I 97.577 

Excess Air 630.3 694.4 831.3 718.8 

Pollutant Concentration9f'cf I 

0.0153 0.0158 . 0.0181 i 0.0164 I ' Mass I Emission Rate, ·Lbs/hr 4.107 4.241 1 

t 4.903 , 4.417 I 

i 

Emissions (NSPS Units) -- ----- ------1 - I 

. I ------

TACB Permit Allowable Rate 7.3 lbs/hr g.3 lbs/hr 7.3 lbs/hr' I 7.3 lbs/hr 

-· 

NSPS Allowable Emissions - ---- ----1 ------

Regulation Allowable Rate ---- ------ ------- ------

TACB Regulation No. ------ ------- -------- -------

Pre Date Post 

. Dry Gas Meter Calibrated 6/11/91 6/19/91 

Pitot Tube Calibrated 6/19/91 

Nozzle Calibrated 6/18/91 

' 

15 ;q 
I 

., 

., 

I 

·, 

Pollutant Sampled: . HF KILN EXHAUST 

Run No. Run No. · Run No. 

Date Sampled 6/18/91 6/18/91 6/18/91 

Time _ 

9.~ 0:25am ~ m ~ 3_E!1 

No. of Points Sampled 1 1 I 1 I I • I 

Operating/Feed Rate 16 cars/day 16 cars/day 16 cars/day f 

~ Operating Rate (Maximum} 100 100 

Stack Temperature 281.2 282.5 

Stack Flow Rate (DSCFM) 31291 31225 

Percent Moisture 8.142 7.705 

Percent Oxygen 18 18 

Percent Carbon Dioxide I 3 4 

Percent Isokinetic ---- --- Excess Air 630.3 694.4 

Pollutant Concentration, p~ 0.6934 0.7869 

Mass Emission Rate,-Lbs/hr 0.0675 0.0762 

Emissions (NSPS Units) ----- -----. 

TACB Permit Allowable Rate 0.6 0.6 

-· 

NSPS Allowable Emissions -- ------

Regulation Allowable Rate ---- ------

TACB Regulation No. ----- -------

Pre Date 

. Dry Gas Meter Calibrated 6/13/91 

Pitot Tube Calibrated 6/19/91 

Nozzle Calibrated 6/18/91 

16 

! 

100 1 

281.3 

31527 

7.770 

18.5 ' 

3 

I -----

831.8 I 

,0.8650 j I l I 

f0.0846 f 

·---~ 

0.6 , 

----1 

-----

------

Post 

6/19/91 

Run No. ,. 

~ 

Results 

_,_.,- --........... 

~ >< 

>< 

16 cars/day 

100 

281.7 

31381 

7.872 

18.17 

3.333 

------

718.8 

0.7816 

I 1 o.o761 

'------- I 

I o.6 

------

--------

-------
£!. 

I 

-~ 

Pollutant Sampled: .S02· 

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

KILN EXHAUST 

Run No. Run No. · Run No. Run No. ,. Results 

Date Sampled 

~~ 

6/18/91 

11 

6/18/91 

:4?::>m ___. 

~ 

6/18/91 ~ 

">< Time _ 0:59am ~45PJ ~- Op~ 

No. of Points Sampled I 24 24 I • 24 t 

I _...,..,-

~ -............. 

Operating/Feed Rate 16 cars/day 16 cars/day 16 cars/day! 16 cars/day 

! 

~ Operating Rate (Maximum) 100 100 100 i 100 

Stack Temperature 281.2 282.5 281.3 281.7 

Stack Flow Rate (DSCFM) 31391 31225 31527 31381 

Percent Moisture 8!h42·:- 7:.76s~= 1~~Tf6C 1 :.81ii ·-· 

Percent Oxygen 18 18 18.5 18.17 

Percent Carbon Dioxide I 3 4 3 3.333 

Percent Isokinetic 97.33 97.68 97.72 I 97.577 

Excess Air 630.3 694.4 831.8 718.8 

Pollutant Concentration, PPM 38.94 10.49 39.81 i ' 39.75 ! 

I ' Mass Emission Rate,·Lbs/hr I 12.14 12.56 i 12.47 ; I 12.37 

i 

Emissions (NSPS Units) I 

' ----- ---- ------ --

TACB Permit Allowable Rate 28.4 28.4 28.4 

' I 28.4 

-- NSPS Allowable Emissions ---- ----- ---- I ------

Regulation Allowable Rate ------ ---- -------- -------

TACB Regulation No. ------ ------ ------- -------

Pre Date Post 

· Dry Gas Meter Calibrated 6/11/91 

-------------------- 6/19/91 

Pitot Tube Calibrated 6/19/91 

Nozzle Calibrated 6/18/91 

17 

cJ-1 
Pollut~nt Sampled: DRYER STACK so~ 

Run No. Run No. Run No. . Run No. .. 

Date Sampled 6/18/91 6/18/91 6/18/91 . 

Time ..,.. ~ 9:20am ~ am ~~ 1:25am 

! I No. of Points Sampled 16 16 1 16 1 

I 

Operating/Feed Rate 16 cars/da} 16 cars/day i 

16 cars/dayj 

~ Operating Rate (Maximum) 100 100 

Stack Temperature 105.8 108.5 

Stack Flow Rate (DSCFM) 59860 58696 

Percent Moisture 5.292 4.544 

Percent Oxygen I 21 21 

Percent Carbon Dioxide I 0 0 

Percent Isokinetic ---- - --

Excess Air ---- -------

Pollutant Concentration,PPM 0.7167 0.7625 

Mass Emission Rate, ·Lb6/hr 0.4261 0.4445 

Emissions (NSPS Units) --- -------

TACB Permit Allowable Rate 0.6 0.6 

·- NSPS Allowable Emissions --- I -----

Regulation Allowable Rate ---- -----

TACB Regulation No. ----- -------

Pre Date 

- Dry Gas Meter Calibrated 6/11/91 

Pitot Tube Calibrated 6/19/91 

Nozzle Calibrated 6/18/91 

18 

! 

100 i 

108.5 

57914 

' 6.748 I 

21 I 

0 

. I ------

-------

. o. 8938 ! I I i 0.5140 I 

! 

i 

--------~ 

0.6 

----- I 

I -------

----------

Post 

6/19.91 

I 

i 

I 

1 

l 

Results 

~ 

>< 

>< 

16 cars/day 

100 

107.6 

58823 

5.528 

21 

0 

-----

--------

{) 7Ql 

0.4615 

----------

0.6 I 

----------

---------

----------
I. 

Run No. Run No. Run No. . Run No. " Results 

Date Sampled 6/18/91 6/18/91 :::><: 

nme -~~ ~q~?n~m ~ ·?":l~m 1 

~· ;::.m ~ >-<:::::: 

! i No. of Points Sampled 16 16 i 16 I . I 

i Operating/Feed Rate 16 cars/da' 16 cars/day 16 cars/davi 

! 

~ Operating Rate (Maximum) 100 100 100 ; 

Stack Temperature 105.8 108.5 108.5 

Stack Flow Rate (OSCFM) 59860 58696 57914 

f 

Percent Moisture 5.292 4.544 6.748 I 

Percent Oxygen 21 21 21 J 

Percent Carbon Dioxide f 0 0 0 

Percent Isokinetic . I - --- - - --- t 

Excess Air ----- -------- ------1 

Pollutant Concentration,PPM <.0.0579 ~0.0622 

Mass Emission Rate, LbS/hr <0.0107 ~.0113 

. Emissions (NSPS Units) ---- -----

TACB Permit Allowable Rate 0.3 0.3 

-· 

NSPS Allowable Emissions - --

Regulation Allowable Rate ------

TACB Regulation No. ----- -----

Pre 

. Dry Gas Meter Calibrated 6/10/91 

Pitot Tube Calibrated 

Nozzle Calibrated 

19 

Date 

6/19/91 

6/18/91 

l · ko.o744 ! 

i i 

I j(0.0134 ! 

I ( -------

0.3 

----- I 

: ------

-----

Post 

6/19/91 

>< 

1 F. ,-.::~rc::: /t'!=!v 

100 

107.6 

58823 

5.528 

I 21 

0 

------

--------

(0.065 

I 

i<0.0118 

I -------

I 0.3 I 

------

--------

---------
I. 

III. PROCEDURES 

The procedure for emissions sampling followed USEPA test methods 

as detailed in Title 40: Code of Federal Regulations. The 

following methods were used: 

Method 

1 

2 

3 

4 

5 

Title 

Sample and Velocity Traverses from Stationary Sources 

Determination of Stack Gas Velocity and Volumetric 

Flow {Type S Pitot) 

Gas Analysis for C02, 02, Excess Air and Dry Molecular 

Weight 

Determination of Moisture Content in Stack Gas 

Determination of Particulate Emissions from Stationary 

Sources 

6 Determination of Sulfur Dioxide Emissions from Stationary 

Sources 

9 Visual Determination of the Opacity of Emissions from 

Stationary Sources 

C02 and 02 were determined using a Fyrite analyzer 

Hydrogen Fluoride was determined following Method 13 ; Flouride 

in Stack Gases in the Texas Air Control Board's Laboratory 

Methods Manual. 

S02 and particulate testing was conducted on the Kiln exhaust 

stack for 2.5 minutes at each of 24 points, 12 points per 

traverse using a 60 inch glass lined sampling probe with a 0.1883 

inch ID stainless steel nozzle and a NaPP Model 31 Method 5 

sampling train. Hydrogen Fluoride was conducted on the Kiln 

exhaust using a seperate sampling train with a 36 inch stainless 

steel probe with a 0.5 inch stainless steel nozzle positioned in 

the middle of the stack pulling at a constant rate for 30 minutes. 

Hydrogen flouride and S02 sampling was conducted on the Dryer 

Room exhaust stack using two seperate sampling trains pulling at 

a constant rate for 30 minutes. A five foot stainless steel 

sampling probe with a 0.4375 inch ID nozzle was used for HF 

sampling and a five foot glass lined probe with a 0.5 inch ID 

sampling nozzle was used for S02 sampling. A 16 point velocity 

traverse was taken prior to each test run. 

20 
I. 

APPENDIX A 
fJ. 

ACME BRICK 

KILN EX. 

6118191 

Repetition # 1 

SAMPLE VOLUME, STANDARD CUBIC FEET 

(((HI13.6) I TM) * Y * VM * 17.64 = 29.36731 

VOLUME OF WATER VAPOR, STANDARD CUBIC FEET 

VLC * 0.04707 = 2.602971 

FRACTIONAL MOISTURE CONTENT 

VWSTD I {VMSTD + VWSTD) = 8.141846E-02 

PARTICULATE CONCENTRATION, GRISCF DB 

{MNIVMSTD) * 0.01543 = 1.525803E-02 

PARTICULATE CONCENTRATION, LBSISCF DB 

(MNIVMSTD) * 2.205~-06 = 2.180425E-06 

MOLECULAR WEIGHT OF STACK GAS, DRY BASIS 

(C02 * .44) + ( 02 * .32} + ( ( N2 + CO} * .28} = 29.2 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS 

(MD * (1- BWS}} + (18 * BWS} = 28.28811 

STACK PRESSURE, INCHES OF MERCURY 

(SP I 13.6} + PBAR = 29.8603 

STACK GAS VELOCITY, FPS 

(SQR(((TS + 460} I MS} IPS}) * CP * DP * 85.49 = 66.4077 

STACK GAS VOLUME, ACFM 

V * AS * 60 = 48004.8 

STACK GAS VOLUME, SCFH 

(((528*PBAR}I(TS+460}129.92)) *AS*V*(1-BWS) * 3600 = 1883483 

PARTICULATE EMISSIONS, LBSIHR 

CS * QS = 4.106793 

ISOKINETIC RATIO, % 

((VMSTDI17.64}+(.002669*VLC)}IANIVIPSIT*(TS+460)*1.667 = 97.32756 

EXCESS AIR = 630.2523 

21 
I. 

ACME BRICK 

KILN EX. 

6/18/91 

Repetition # 1 

PRESSURE DROP ACROSS ORIFICE, H = .8745 

METER CO-EFFICIENT, Y = .968129 

METER TEMPERATURE, TM = 100.77 

BAROMETRIC PRESSURE, PBAR = 29.9 

GAS METER VOLUME, VM = 32.182 

LIQUID COLLECTED, VLC = 55.3 

PARTICULATE SAMPLE WEIGHT, MN = 29.04 

STATIC PRESSURE, SP = -.54 

STACK TEMPERATURE, TS = 281.2 

PITOT CO-EFFICIENT, CP = .84 

SQUARE ROOT OF DELTA P; DP = .9872 

AREA OF STACK, AS = 12.048 

TEST DURATION, T = 60 

AREA OF NOZZLE, AN = 1.933872E-04 

C02 % = 3 

02 % = 18 

co % = 0 

22 ;)7 
C. 

,. 

ACME BRICK 

KILN EX. 

6118191 

Repetition # 2 

SAMPLE VOLUME, STANDARD CUBIC FEET 

(((HI13.6) I TM) * Y * VM * 17.64 = 29.31967 

VOLUME OF WATER VAPOR, STANDARD CUBIC FEET 

VLC * 0.04707 = 2.44764 

FRACTIONAL MOISTURE CONTENT 

VWSTD I (VMSTD + VWSTD} = 7.704903E-02 

PARTICULATE CONCENTRATION, GRISCF DB 

(MNIVMSTD} * 0.01543 =· 1.584067E-02 

PARTICULATE CONCENTRATION, LBSISCF DB 

(MNIVMSTD} * 2.205A-06 = 2.263686E-06 

MOLECULAR WEIGHT OF STACK GAS, DRY BASIS 

{C02 * .44} + { 02 * .32) + { { N2 + CO} * .28} = 29.36 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS 

{MD* {1- BWS}) + {18 * BWS) = 28.48473 

STACK PRESSURE, INCHES OF MERCURY 

{SP I 13.6} + PBAR = 29.86287 

STACK GAS VELOCITY, FPS 

{SQR{ ( {TS + 460} I MS} I PS}) * CP * DP * 85.49 = 65.85755 

STACK GAS VOLUME, ACFM 

V * AS * 60 = 47607.11 

STACK GAS VOLUME, SCFH 

{({528*PBAR)I(TS+460)129.92)} *AS*V*{l-BWS) * 3600 = 1873479 

PARTICULATE EMISSIONS, LBSIHR 

CS * QS = 4.240967 

ISOKINETIC RATIO, % 

{(VMSTDI17.64}+{.002669*VLC))IANIVIPSIT*(TS+460}*1.667 = 97.68002 

EXCESS AIR = 694.4447 

23 
I. 

ACME BRICK 

KILN EX. 

6/18/91 

Repetition # 2 

PRESSURE DROP ACROSS ORIFICE, H = .8829 

METER CO-EFFICIENT, Y = .968129 

METER TEMPERATURE, TM = 104.66 

BAROMETRIC PRESSURE, PBAR = 29.9 

GAS METER VOLUME, VM = 32.352 

LIQUID COLLECTED, VLC = 52 

PARTICULATE SAMPLE WEIGHT, MN = 30.1 

STATIC PRESSURE, SP = -.505 

STACK TEMPERATURE, TS = 282.5 

PITOT CO-EFFICIENT, CP = .84 

SQUARE ROOT OF DELTA P, DP = .9816 

AREA OF STACK, AS = 12.048 

TEST DURATION, T = 60 

AREA OF NOZZLE, AN = 1.933872E-04 

C02 % = 4 

02 % = 18 

co % = 0 

24 
I. 

ACME BRICK 

KILN EX. 

6118191 

Repetition # 3 

SAMPLE VOLUME, STANDARD CUBIC FEET 

(((HI13.6) I TM) * Y * VM * 17.64 = 29.61394 

VOLUME OF WATER VAPOR, STANDARD· CUBIC FEET 

VLC * 0.04707 = 2.49471 

FRACTIONAL MOISTURE CONTENT 

VWSTD I (VMSTD + VWSTD) = 7.769588E-02 

PARTICULATE CONCENTRATION, GRISCF DB 

(MNIVMSTD) * 0.01543 = 1.813735E-02 

PARTICULATE CONCENTRATION, LBSISCF DB 

(MNIVMSTD) * 2.205A-06 = 2.591889E-06 

MOLECULAR WEIGHT OF STACK GAS, DRY BASIS 

(C02 * .44) + ( 02 * .32) + ( ( N2 + CO) * .28) = 29.22 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS 

(MD* (1- BWS)) + (18 * BWS) = 28.34825 

STACK PRESSURE, INCHES OF MERCURY 

(SP I 13.6) + PBAR = 29.86176 

STACK GAS VELOCITY, FPS 

(SQR(((TS + 460) I MS) IPS)) * CP * DP * 85.49 = 66.43415 

STACK GAS VOLUME, ACFM 

V * AS * 60 = 48023.92 

STACK GAS VOLUME, SCFH 

(((528*PBAR)I(TS+460)129.92)) *AS*V*(1-BWS) * 3600 = 1891614 

PARTICULATE EMISSIONS, LBSIHR 

CS * QS = 4.902853 

ISOKINETIC RATIO, % 

((VMSTDI17.64)+(.002669*VLC))IANIVIPSIT*(TS+460)*1.667 = 97.7182 

EXCESS AIR = 831.8349 

25 
D. 

ACME BRICK 

KILN EX. 

6/18/91 

Repetition # 3 

PRESSURE DROP ACROSS ORIFICE, H = .9071 

METER CO-EFFICIENT, Y = .968129 

METER TEMPERATURE, TM = 102.4 

BAROMETRIC PRESSURE, PBAR = 29.9 

GAS METER VOLUME, VM = 32.544 

LIQUID COLLECTED, VLC = 53 

PARTICULATE SAMPLE WEIGHT, MN = 34.81 

STATIC PRESSURE, SP = -.52 

STACK TEMPERATURE, TS = 281.3 

PITOT CO-EFFICIENT, CP = .84 

SQUARE ROOT OF DELTA P, DP = .9886 

AREA OF STACK, AS = 12.048 

TEST DURATION, T = 60 

AREA OF NOZZLE, AN = 1.933872E-04 

C02 % = 3 

02 % = 18.5 

co % = 0 

26 3/ 
I. 

ACME BRICK 

DRYER STACK 

REPETION # 1 

6/18/91 

MOLECULAR WEIGHT OF STACK GAS, DRY BASIS, MD 

(.44 * %C02) + (.32 *% 02) + (.28 * (N2 +CO))= 28.84 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS, MS 

MD * (1 - BWS) + (18 * BWS) = 28.2664 

STACK GAS PRESSURE, IN HG, PS 

PBAR + (STATIC/13.6) = 29.81177 

STACK GAS VELOCITY, FPS 

85.49 * CP * (SQR P(TS I (PS * MS))) = 57.7135 

VOLUME FLOW RATE, ACFM 

60 * AS * VS = 67974.95 

VOLUME FLOW RATE, SCFH 

3600 * (1- BWS) * VS *AS* ((528 * PBAR) I (TS * 29.92)) = 3591585 

%C02 = 0 

%02 = 21 

%CO = 0 

%N2 = 79 

STACK TEMPERATURE, F = 105.8 

SQUARE ROOT OF DELTA P = .9808 

STATIC PRESSURE, IN H20 = -1.2 

BAROMETRIC PRESSURE, IN HG = 29.9 

PERCENT WATER VAPOR (BWS * 100) = 5.2915 

AREA OF STACK, SQUARE FT. = 19.63 

PITOT CO-EFFICIENT, CP = .84 

27 
£!. 

ACME BRICK 

DRYER STACK 

REPETION # 2 

6118191 

MOLECULAR WEIGHT OF STACK GAS, DRY BASIS, MD 

(.44 * %C02) + (.32 *% 02) + (.28 * (N2 +CO)) = 28.84 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS, MS 

MD * (1 - BWS) + (18 * BWS) = 28.34748 

STACK GAS PRESSURE, IN HG, PS 

PBAR + (STATICI13.6) = 29.82647 

STACK GAS VELOCITY, FPS 

85.49 * CP * (SQR P(TS I (PS * MS))) = 56.38788 

VOLUME FLOW RATE, ACFM 

60 * AS * VS = 66413.65 

VOLUME FLOW RATE, SCFH 

3600 * (1- BWS) * VS *AS * ((528 * PBAR) I (TS * 29.92)) = 3521744 

%C02 = 0 

.%02 = 21 

%CO = 0 

%N2 = 79 

STACK TEMPERATURE, F = 108.5 

SQUARE ROOT OF DELTA P = .9576 

STATIC PRESSURE, IN H20 = -1 

BAROMETRIC PRESSURE, IN HG = 29.9 

PERCENT WATER VAPOR (BWS * 100) = 4.5435 

AREA OF STACK, SQUARE FT. = 19.63 

PITOT CO-EFFICIENT, CP = .84 

28 
a. 

ACME BRICK 

DRYER STACK 

REPETION # 3 

6/18/91 

MOLECULAR WEIGHT OF STACK GAS, DRY BASIS, MD 

(.44 * %C02) + (.32 * % 02) + (.28 * (N2 + CO)) = 28.84 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS, MS 

MD * (1 - BWS) + (18 * BWS) = 28.10852 

STACK GAS PRESSURE, IN HG, PS 

PBAR + (STATIC/13.6) = 29.82647 

STACK GAS VELOCITY, FPS 

85.49 * CP * (SQR P(TS I CPS* MS))) = 56.95231 

VOLUME FLOW RATE, ACFM 

60 * AS * VS = 67078.43 

VOLUME FLOW RATE, SCFH 

3600 * (1- BWS) * VS *AS * ((528 * PBAR) I (TS * 29.92)) = 3474850 

%C02 = 0 

%02 = 21 . %CO = 0 

%N2 = 79 

STACK TEMPERATURE, F = 108.5 

SQUARE ROOT OF DELTA P = .9631 

STATIC PRESSURE, IN H20 = -1 

BAROMETRIC PRESSURE, IN HG = 29.9 

PERCENT WATER VAPOR (BWS * 100) = 6.748 

AREA OF STACK, SQUARE FT. = 19.63 

PITOT CO-EFFICIENT, CP = .84 

29 
I. 

APPENDIX B 
C. 

S02 Data Reduction 

ACME BRICK 

KILN EX. 

6118191 

Repetition 1 

Volume of sample, VM STD 

(((HI 13.6) + .PBAR) I (TM + 460) * Y * VM * 17.64 = 29.36731 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = 2.602971 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 8.141846 % 

S02 concentration, lbslscf 

(MN I VMSTD) * 2.205 ~ 10-6 = 6.475201E-06 LBSISCF 

S02 Concentration, ppm 

(385.2 I MW) * LBSISCF = 38.93611 PPM 

Delta H, H = .8745 Inches H20 

Meter Temperature = 100.77 F 

Barometric Pressure, PBAR = 29.9 inches HG 

Meter Volume, VM = 32.182 CU. FT. 

Meter Co-efficient, Y = .968129 

Liquid collected, VLC = 55.3 MLS 

Sample weight, MN = 86.24 MG 

S02 Molecular Weight = 64.06 

30 
C. 

HF Data Reduction 

ACME BRICK 

KILN EX. 

6118191 

Repetition 1 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 15.13946 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = .9978841 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 6.183695 % 

HF concentration, lbslscf 

(MN I VMSTD} * 2.205 A 10-6 = 3.600366E-08 LBSISCF 

HF Concentration, ppm 

(385.2 I MW) * LBSISCF = .6934305 PPM 

Delta H, H = 1 Inches H20 

Meter Temperature = 95.67 F 

Barometric Pressure, PBAR = 29.9 inches HG 

Meter Volume, VM = 16.409 CU. FT. 

Meter Co-efficient, Y = .969636 

Liquid collected, VLC = 21.2 MLS 

Sample weight, MN = .2472 MG 

HF Molecular Weight = 20 

~1 37 
a. 

S02 Data Reduction 

ACME BRICK 

KILN EX. 

6118191 

Repetition 2 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 29.31967 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = 2.44764 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 7.704903 % 

S02 concentration, lbslscf 

(MN I VMSTD) * 2.205 A 10-6 = 6.733149E-06 LBSISCF 

S02 Concentration, ppm 

(385.2 I MW) * LBSISCF = 40.48718 PPM 

Delta H, H = .8829 Inches H20 

Meter Temperature = 104.66 F 

Barometric Pressure, PBAR = 29.9 inches HG 

Meter Volume, VM = 32.352 CU. FT. 

Meter Co-efficient, Y = .968129 

Liquid collected, VLC = 52 MLS 

Sample weight, MN = 89.53 MG 

S02 Molecular Weight = 64.06 

32 
1 .. 

HF Data Reduction 

ACME BRICK 

KILN EX. 

6118191 

Repetition 2 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 14.97613 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = 1.275597 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 7.848991 % 

HF concentration, lbslscf 

(MN I VMSTD) * 2.205 A 10-6 = 4.085751E-08 LBSISCF 

HF Concentration, ppm 

(385.2 I MW) * LBSISCF = .7869156 PPM 

Delta H, H = 1 Inches H20 

Meter Temperature = 108.2 F 

Barometric Pressure, PBAR = 29.9 inches HG 

Meter Volume, VM = 16.598 CU. FT. 

Meter Co-efficient, Y = .969636 

Liquid collected, VLC = 27.1 MLS 

Sample weight, MN = .2775 MG 

HF Molecular Weight = 20 

33 39 
I. 

S02 Data Reduction 

ACME BRICK 

KILN EX. 

6118191 

Repetition 3 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 29.63291 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = 2.49471 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 7.765 % 

S02 concentration, lbslscf 

(MN I VMSTD) * 2.205 A 10-6 = 6.621047E-06 LBSISCF 

S02 Concentration, ppm 

(385.2 I MW) * LBSISCF = 39.8131 PPM 

Delta H, H = .9071 Inches H20 

Meter Temperature = 102.04 F 

Barometric Pressure, PBAR = 29.9 inches HG 

Meter Volume, VM = 32.544 CU. FT. 

Meter Co-efficient, Y = .968129 

Liquid collected, VLC = 53 MLS 

Sample weight, MN = 88.98001 MG 

S02 Molecular Weight = 64.06 

34 
HF Data Reduction 

ACME BRICK 

KILN EX. 

6118191 

Repetition 3 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 14.5132 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = 1.073196 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 6.885466 % 

HF concentration, lbslscf 

(MN I VMSTD) * 2.205 ~ 10-6 = 4.491071E-08 LBSISCF 

HF Concentration, ppm 

(385.2 I MW) * LBSISCF = .8649802 PPM 

Delta H, H = 1 Inches H20 

Meter Temperature = 112.83 F 

Barometric Pressure, PBAR = 29.9 inches HG 

Meter Volume, VM = 16.216 cu. FT. 

Meter Co-efficient, Y = .969636 

Liquid collected, VLC = 22.8 MLS 

Sample weight, MN = .2956 MG 

HF Molecular Weight = 20 

35 
a. 

S02 Data Reduction 

ACME BRICK 

DRYER STACK 

6118191 

Repetition 2 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 14.32813 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = .513063 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 3.45702 % 

S02 concentration, lbslscf 

(MN I VMSTD) * 2.205 A 10-6 = 1.268079E-07 LBSISCF 

S02 Concentration, ppm 

(385.2 I MW) * LBSISCF = .7625103 PPM 

Delta H, H = .8333 Inches H20 

Meter Temperature = 113.2 F 

Barometric Pressure, PBAR = 29.5 inches HG 

Meter Volume, VM = 15.6 cu. FT. 

Meter Co-efficient, Y = 1.0096 

Liquid collected, VLC = 10.9 MLS 

Sample weight, MN = .824 MG 

S02 Molecular Weight = 64.06 
a. 

HF Data Reduction 

ACME BRICK 

DRYER STACK 

6118191 

Repetition 1 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 15.54716 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = .795483 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 4.867531 % 

HF concentration, lbslscf 

(MN I VMSTD) * 2.205 A 10-6 = 3.006724E-09 LBSISCF 

HF.Concentration, ppm 

(385.2 I MW) * LBSISCF = (5.790949E-02 PPM 

Delta H, H = 1 Inches H20 

Meter Temperature = 112.8 F 

Barometric Pressure, PBAR = 29.5 inches HG 

Meter Volume, VM = 16.885 CU. FT. 

Meter Co-efficient, Y = 1.011 

Liquid collected, VLC = 16.9 MLS 

Sample weight, MN = (.0212 MG 

HF Molecular Weight = 20 

(. o!G1 !~hv 

37 
~. 

S02 Data Reduction 

ACME BRICK 

DRYER STACK 

6118191 

Repetition 1 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 15.24389 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = .9366929 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 5.788995 % 

S02 concentration, lbslscf 

(MN I VMSTD) * 2.205 A 10-6 = 1.191901E-07 LBSISCF 

S02 Concentration, ppm 

(385.2 I MW) * LBSISCF = .7167033 PPM 

Delta H, H = .85 Inches H20 

Meter Temperature = 105.9 F . Barometric Pressure, PBAR = 29.5 inches HG 

Meter Volume, VM = 16.385 CU. FT. 

Meter Co-efficient, Y = 1.0096 

Liquid collected, VLC = 19.9 MLS 

Sample weight, MN = .824 MG 

S02 Molecular Weight = 64.06 

38 
C .. 

HF Data Reduction 

ACME BRICK 

DRYER STACK 

6118191 

Repetition 2 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 14.54473 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = .875502 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 5.677621 % 

HF concentration, lbslscf 

(MN I VMSTD) * 2.205 A 10-6 = 3.229109E-09 LBSISCF 

HF Concentration, ppm 

(385.2 I MW) * LBSISCF = 6.219264E-02 PPM 

Delta H, H = .95 Inches H20 

Meter Temperature = 118.7 F 

Barometric Pressure, PBAR = 29.5 inches HG 

Meter Volume, VM = 15.961 CU. FT. 

Meter Co-efficient, Y = 1.011 

Liquid collected, VLC = 18.6 MLS 

Sample weight, MN = .0213 MG 

HF Molecular Weight = 20 

39 
C. 

S02 Data Reduction 

ACME BRICK 

DRYER STACK 

6118191 

Repetition 3 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 12.22401 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = .866088 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD .+ VWSTD) = 6.616358 % 

S02 concentration, lbslscf 

(MN I VMSTD) * 2.205 ~ 10-6 = 1.486353E-07 LBSISCF 

S02 Concentration, ppm 

(385.2 I MW) * LBSISCF = .8937609 PPM 

Delta H, H = .8667 Inches H20 

Meter Temperature = 124.7 F 

Barometric Pressure, PBAR = 29.5 inches HG 

Meter Volume, VM = 13.575 CU. FT. 

Meter Co-efficient, Y = 1.0096 

Liquid collected, VLC = 18.4 MLS 

Sample weight, MN = .824 MG 

S02 Molecular Weight = 64.06 

40 
l 

HF Data Reduction 

ACME BRICK 

DRYER STACK 

6118191 

Repetition 3 

Volume of sample, VM STD 

(((HI 13.6) + PBAR) I (TM + 460) * Y * VM * 17.64 = 12.32624 DSCF 

Volume of water vapor, VWSTD 

VLC * 0.04707 = .922572 SCFH 

Fractional moisture content, % 

VWSTD I (VMSTD + VWSTD) = 6.963431 % 

HF concentration, lbslscf 

(MN I VMSTD) * 2.205 A 10-6 = 3.863951E-08 LBSISCF 

HF Concentration, ppm 

(385.2 I MW) * LBSISCF = .744197 PPM 

Delta H, H = .9667 Inches H20 

Meter Temperature = 128.8 F 

Barometric Pressure, PBAR = 29.5 inches HG 

Meter Volume, VM = 13.762 CU. FT. 

Meter Co-efficient, Y = 1.011 

Liquid collected, VLC = 19.6 MLS 

Sample weight, MN = .216 MG 

HF Molecular Weight = 20 

41 47 
I. PARTICULATE 

company ,/fw. &cf' 

ANALYTICAL OATA FOR~ 

Location: 1(/t,/11 CX 

Date: 6" /j'g /. <=t/ I 

Run Number: _ ___;· ~-----&.~_tJ __ _ 

Dens i t y ( ? a ) : --:'-.;.1.-.¥_{_)_a-. __ 

Liquid Level Mprked7_-=V";..._ __ 

Blank Concentration(Ca). ~ 

Rinse Volume(Vaw) ~~ ~ 

Residue in Rinse (Wa) = Ca·Vaw.Pa -----

Date of Weighing b /1{/'11 

Date of Weighing. 6/2o/'1 f 

. Average 

Grass W t._CJ~9_7.;....:· /L~..J;;;..; 2 ·;_(_. __ _ 

Gross W t._1.:....4...:.......;.9~/t~~~~....~.l __ _ 

Gross W t. _9...:.....;..\j....:.Cf...:.FJ-_~~* ..:....} ----

Less Blank Residue (Wa) c:) ------------ Tare wt. '14'} 0 f ,.s-~ . 

Weight of Particulate in Acetone Rinse 0(1,~ . 

Date of Weighing~///;·,/ 

·oate of Weighing ~-:2,0-9/ 

Gross Filter Weight #-ZJ,. 02. 

Gross F'il ter Weight:l /;&.I 0 

Aver age Gross W t. __ _..;.'I_?~J~· 0_..;.1 _____ _ 

f i 1 te r Tare W t. _4~{...:.~..:..--~{..;;..S ____ _ 

~eight of Particulate on filter _ _.~,'j;.:.·-.·..:..(j....;.f/ _______ _ 

Total Weight pf Particulate d, '7. 0'1 ttl~· 

42 
... PARTICULATE ANALYTICAL OATA FORM 

Company: .,..;k ___ ~..;.-Me.--.._____.&=---'-'-'..;../(____ Run Number: L . f;J 

Location: &~ a Oensity(Pa): , 71)9-

0ate: 6 /;g- /il 

Liquid Level.Mprked? ~ 

Blank Concentration(Ca) ------ Rinse Volume(Vaw) 

Residue in Rinse (Wa) = Ca·Vaw-Pa ----- Date of Weighing @7 ,/yj 

Date of Weighing 6-~o- Cf/ 

Gross Wt. 9 7 2 ~ ~ 5 

Gross Wt. 9 7.2 3 ,8. 5:: 

Average Gross Wt. -------------------- Less Blank Residue (Wa) c:? ----~=-------------

Tare W t. ~Cf:.....o_ 7....;;;;../L_· ..__/ 7_;,.....::~:~~'1'¥'~-_ 

Weight of Particulate in Acetone Rinse_----"""'~ ... 0 .... ,,_7"------------

-Date of Weighing ~/11!__1/ Gross F'il ter Weight t/?5;" 1'8 

·oate of Weighing G_· :ZO- ~/ Gross Filter Weight 1../7). L{C 

Average Gross Wt. '17s-, 'i i 

filter Tare w t. L/66.0 7 

~eight of Particulate on filter CJ. t/ 

Total Weight pf Particulate 

43 
I. PARTICULATE ANALYTICAL DATA FORM · 

Company: 4:.w,e ~. tk 

Location:f!l~tl c~ 

Run Number: __ 3,L-----.~./1_JJ_,~ __ _ 

Density(Pa): ,;z_g-:)2___ 

Oa te: 6/· If- ./'1 I 

Liquid Level Mprked'?--"~---

Blank Concentration(Ca) _____ _ 

Rinse Volume(Vaw) 

Residue in Rinse (Wa) = Ca·Vaw.Pa 

Date of Weighing &lir/'11 Gross Wt. 

Date of Weighing 6- 2-CJ- 9/ Gross Wt. 

Average Gross w t. 10:1615:' 

Less Blank Residue (Wa) c:) ------------- Tare W t·~..:...~ 0_.~...;:..5_~~6.~# ..=...( __ 

Weight of Particulate in Acetone Rinse __ -""[A.l..l<g~,~£'--------

Date of Weighing 6 /; '7 /7/ Gross Filter Weight 1.-/?0?--J 

·oate of Weighing 6 -z<; .. ,f Gross Filter Weight L(?{).). 3 

Average Gross Wt. '1?0~)...5 

Filter Tare W t. ---~..;..·....;~~3_7.;......;..:2-...;;;;._ ___ _ 

~eight of Particulate on Filter ___ ....;;~;;....:..~ ~3;...;./ _____ _ 

Total Weight pf Particulate >3 t:i xI 

44 
I. --· 

ACETONE BLANK ANALYTICAL DATA FORM 

PLANT: /kwte. ~(,A:_. 

S.llMA..E LOCATION: I(;~ F>< 

LIQUID LEVa MARKED'? v 

BLAI'I< VOLUME (Pa): jd:; ~ 

DATE OF WEIGHING t(' ); i /9/ 

DATE OF WEIGHING 6-,2..0- 9/ 

GROSS WEIGHT I 0 I '} ~ 7 ,S 

GROSS WEIGHT / () 11 d--1 b L 

AVERAGE GROSS WEIGHT ___ -::or-~~---::=---

TARE WEIGHT I 0 11~ 7, 5:"4 

WEIGHT OF BLANK (ma) ___ ___::.0~----=-0_ ma Ca = Va Pa = 0 mg/g 

Note: In. no case should a blank residue greater than 0.01 mg/g or 0.001% of 

the blank weight be subtracted from the sample weight. 

45 

6/ 
a. /)cm6 

5,c,cv:+ Ct::l l-vciCHTJ 

' 

_----- __ --:_ --~-~~=-'l;]~--_(ji-_ -~P.;ril~~-~l~le -~-- s~~~:fiALt.Q_-_~-~---~---- -~-· ~--------~ -_---~----~-=-- _-· 

--- -···-- --- ----------~------ --~ ''-~ 3 ------------·- ··-----· --·-·--------------·---··-· . --- -·-· -- . . . tv e:<o~~o 

---_ .... -=-~~~=~=-··-t3:~:- -----~9 -~;Q~~= -----=-=---=-=~~=-~-=-----·~--~-~~~---- ~-~=-~---- . -~---· ·:· .• _---- . 

----~-~=-~~~=~-----i!Y!-- .. E ~---=ii_F- 7idllv_ ___________ ·:~-==:~-===~-~~---~ ---~~·--~---~- ------- .---- --·------~ 1- -- ---fgf~f ------ ----------------··------ - --~_fL_3~Qd~~------------- -==~--~ 

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

. n . :J.-.. L -- .. · (u- f~i -·----- 1 1~-------- -~1- ,c;?J,£ ·- -----------· -~-_f..,c__ __ _ 

-~-- ----------·-·--

------· _· ~~ f/...6 3~' 

----------- -----------------·-·------

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

·-- -- --------------------------------------------- -------- ----------------------------·------- ------- --

46 
I. /lc tY?F g,l cl::_ 

1 :-51" r:_,..e:-: t~ -~; J-/~~ AtvlrL /5/S 

_____________ __ src~~c;_. .• ,z. D ____________ 1u:L _ __g£~c1'r- _____ ________ _ _ _ _ _ _ __________ _ 

-___________ W,!VI< _______ {h_O~------------ -- ------- .. _______ ---------- --

1 J-0 J -- .J._g~ 3 ··- -------- -6---' .· ! J ~----- ------- ----------·----·---------- ·- --------

-- }~;1 -;~~~----- um - -- U --- U - m U mU -

---------- r ·------- ---- --· ------- -- ------- ----- ----- ----------- -----

- 1- ·~.f -ft;J;J_ -- ------ . -·---- ----~t_ ____ . -------------------· .. --·-'- ---- ----- ------------ ---· ---- ·-· --------· . -· ·-

-----'W~t/4 --7~ ----------------------------- --------- ~ c;_c,..a:.! /fii.V--~4/e _vq(~f~ e _ ,.,¥,v· ______ ~~--_____ rt(; ( ~ ___ _ 

r;:_,_~cx 1-__!_r-:- g; c _______ [;ff _____ ~t.z ______________ O~d4:.; £) _ z, :E ,_, !/CO 2c0 0 0 ______ _ _ _ 

~vr, ~ J63 l._ls-________ O~d.??_~---

--~'-I'k P\co 119 0 ~: .cJ __ _ 

''tl :r;, J, I{ I ~I' L3s': O.J...']:)b 

10/ 1qa --~ · 6 -.·o : 

I. 

:7~-l rz., trJ _ _ ..1. ~ 

--~---------------- ! ---- ·---------

--~!~__:...._.J, 2.__L1__ I i7 ~4_L ______________ <:~az._LL·- __ 

-----'---"~ .k_ 2 CJ6 J~ __ <·C) r _, Q _____ _ 

-~~11 t?\{3 11)"--__ <J___ (,0~/3 ___ • 

---~Lrz... J__o---=7_=----~---11::-..ci=---__ <_ .. --o ---~: __ . Q_~_:_ ___ _ __ __,_g.~ ) 1----'-1--~~'------------(~ q_?--)f ____ '--

--- _________ 'g-L);~ Z co Lo-o ___ .o '0 ~----------------- ........ ---------- --

~- - -------~--------

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

_____________ _____.P'l ~A.O --

47 
a. 9 ___ _ 

8 ___ _ 

7 ___ _ 

6 __ _ 

5 ___ _ 

4 ___ _ 

3 ___ _ 

2 ___ _ 

t_ __ 

9_ 

s __ 

u 7 __ 

- 6_ 0 

·o 

~ 

s_ 

.. 

3_ 

s_ 

... 

... 

c 

< 3 __ ... ~ 

...J=> 

uz 

>: 

!i .z 

ci 

2 __ 

~(.) 

:I: a: ...... 

-Ul 

.. Ul 

.. "' ., 

'...J ...... ... L- :E:5 -9. "'"' ::.: .a_ 

A.l -7 

:i: • 6_ 

. s_ 

·4_ 

• 3_ 

2-
L. oco he>.;] ----- --

~jVI Ex 

J) 

J) 

5/!ptfC.E 

. I ;) ;I. SC;,; 

:6c...;.:. /.J K 

y;_rcf<_ 

..::;, :7 ez7 -': ... ·. ._~_,. ... o, 0, .<J 

.. . _}7-l__ ·-· -- ·-· 

0 

0,0103 

SAI"'ft.C - 7/lZ~- Av<!.. - V.l < _VeL..._ - F ,I ~ 1 ,#s- ~ L . . 5": (15-:0} {; 0_ ~.OJ) .zso . -~ -·. . --- . .;;:J .• '1 ' c I' "':: . 

/ Ob•.;;-.--

Ktbr. ... ___ .. "'...,.d._,~~- _ .J.. .. ___ 2:~ __ s: __ ____ 3.3.1t .. 

.f.:r.-.!1 .. . _ -~-s-:r,. s-..z./ .sf . 5:!37 ... ~.rc: ···- .. _("___ ____ _ 'l~.51 7 ~i.~3 

11J.£s. ______ _______ !_t.3.f.!2___ . .3. ..... ;~----<=-------··- _. '~·1r.tf__ 

____ 7

' ___ ..... 1-:m:. I1. ..... _ .... __ ;;e;,_~J,_£j __ _ -~~3) ___ ~l" __ r_ ____ ·-- .. . Yfi'/. / g?. 72 

--~~- __ --~IJL _______ -~~·-"~-) ,_j_ __ _._3_~(1__.v:o !-" -----~·_o15 _____ ... _ 

1/: 2'6;1-:-·- -------- --.-- -------· -.. ---·· ---------------- ... ·--- ----·- - -·-..... .1!1. --·- ··-. -

JJ~j-tf.._~AC/f. :tL :rt ~ o~ -·-~'=i--~or" • ~ J..t:~ ~ __ ~./$.. ~ y__ ··r-= 

-------- _j.,Jlr___ __ Q~I ~PI ·· ~_l._[D _____ ~------- ·-· 9 ___ ·· ... 

______ ______ .. kiJ_ ____ .!..o.r .or; .Dr _____ ._a_~--~rc _____ r _______ d. coR.!.(_ 

---------- .... -~'If rz ___ - o,..._p, __ ~-- ____ Q_. -~rc __ r- -- . _(?_ __ . . ·- . 

_____________ g_l1J..tL _ .• _or; ~-~f--.ar:.__ ____ ~C l.~ r- _______ o!~A'/ ___ ····--

-------·-··· ----'~.I1I-... --~rt:>_/ _o ______ c;_ _ _ z.~ c_______ c 

A II ;;' :;_ /j. ?;<'/ 

---- ,_, __ ··----··---·-·--·--··--- . 

----- ... 

Nc'lt!".?f..~ ,.f_ 13<-._[c tp •. iJ.l.. : __ val 'J.'" so~ x Nou·-4fo fl-z.Soc1 

.... ________ .... .. Vel ~-[~LGJ:w. ____ . 

-

/. . I 32 'X Vo/_, 
APPENDIX C 
I. .rl" PARTICULATE FIELD DATA 

PLANT= Ac/'·''i'"'=-- . DATE:-~ 1~ h· · 

REPETITION: 1 

LOCATION: (('tLJV eX._ 

OPERATOR: "R.T" 

STACK #: ? '•t.. 

SAMPLE BOX #: 5:::-_,z... ·t ·' -,./"" -

METER BOX #: 6 

AMBIENT TEMPERATURE: 

ASSUMED MOISTURE: ~4 .,m 

,.. 

BAROMETRIC PRESSURE:l~. ~ a 

PROBE LENGHT :~" .o- · -,. 1... t. 

NOZZLE DIAMETER :lZs0 l'i# .I~~" .ottA 1.7 I 

STACK DIAMETER:~; 

METER H : I ~a-yo '(·? 

C FACTOR:_~<.: . . 

METER CO-EFFICIENT: .j~'g./: i 

FILTER TARE: 

PRE-TEST LEAK'CHECK 

Meter: a-=1 Cu. ft .IS" in. HG 

Pitots: y- in. H20 

t--"' 

IMPINGERS 

Initial 

#l = J-r:JQ ~ .(7 II () #2 =~ov ~ ~~ -v 

#3: 

#4:)..~~ 56 

#5: 0 

COMMENTS: 

POST-TEST LEAK CHECK 

Meter:o.-aos-"cu. ft./~ 

Pitots ~ 

Final 

"1 

"'' 

J;_t 

~J/.3 -

55:3 

in. HG 

in. H20 

' ~ e r~~ J~ 1 ~? 1 VA? I ~H I F~.rr I,JL~ ~~~~~ ~WI~~~ J 75.) I L.((S I I I I , i _wg ... fi} 70! 9/ I 7 I I .2. ''n I 7 If' I ~ 

~ 1/ ,v I I LD 1/Y,~ I '5s- I 70 l..i<'f"O I ?s- I I 

] 

15fl- 11 /') . .t jg:,'") I o5 1'1t IH-.S"'/ I--:~- I L 

I 1 _']6 I ].sr")t:;"' ."'1 1~'1 I JI03 1'77 IL1 u 'J{ I ? 

IJ-.1~ I 1 t-- 1.! !)(,.~ 11!1_"5 111 I rl.S I 7{ I ) 

I "1 .... ~1 U_. J I, 1- 3~ . .3 1/_Q_( I 9 '1 I a ~ I 'II I 3 

·' 

L~.c; 1 f.6t: 1 1 14tL~ 11/U 1/f)/ ItA~~ JC I 4 · 

~x>L- I • ') I I"' '1f'J,') I !I I I (i'].; I,?.__)~. (4 I ) 

I~/ I ~ . j ~~~~ II f I /D1.J 1)-~L I '14 I 1 

I J 1 m, ""-11.-·f ;f I I I 

Av 

50 
PARTICULATE FIELD DATA. 

,.:==~ ., 

, r I 

! 

PLANT: /- :. · : .:_-

DATE:~ ;_.,.:: 

REPETITION: i.J 

LOCATION: :-: // j!;<' 

OPERATOR:·,:-~ 

I 1 II 

! 

rl 

i 

- IMPINGERS 

~--

STl\CK #:- 1. 

SAMPLE BOX #:_$0l- .r fc;¥f1L 

a -:o Initial 

#1: J_cC· ~ __ / -, C·, METER BOX #:6 , 

AMBIENT TEMPERATURE:'"X> : . .J/1·-

; 

~2. • &-, .. " 1t" • _e-.:; 

#3:-

BAROMETRIC PRESSURE: L. '7. 7 1 

ASSUMED MOISTURE: '?~ ( 

PROBE LENGHT: ~" - . 

NOZZLE DIAMETER:. 1:tt #!OJ, I~ STACK DIAMETER:~1~ 

METER H :/.6"8o/CJ~7 

C FACTOR:. '<.' 

METER CO-EFFICIENT: ;9r6/Z.(LI i 

I. 

FILTER TARE: 

PRE-TEST LEAK CHECK 

Meter : 0 ~a c.> j- Cu . f t .. d.- in . HG 

,.._ 

1 

Pi tots: Ill"" in. H20 

v ( 

' 

#4: /ue., ..- / ~ /-' 0 

·1~ .. ·#5: c 

COMMENTS: 

-~ ~ ~OST-TEST LEAK CHECK 

;_ ~Meter :o...o:> Cu. ft .L"" 

'. Pi tots ;:;/ . in. HG 

in. H20 

I _, e 'lsr.PRE~Sld. JFs I 6 '? .I- VF:P I ~ H I v T I T m I Tm I OVEN L.'!YfLE:riVACUJR ,.. 1.1 . F'i.~ INLET lcun-£r TEMP. ~EMP. CIN H,.S) 

J I//N2 I-Z¥v I/ .. I· I I I . 1:{5/.aaa I 'i~ I /J I~SO I J~ I J 

::s 1 ~ ! 1,. t- 1 11, 1 1 s-.J. 9 ! 7 7 1 '1J k;i?__r-o 1 ?.? · 1 t.... ~ I Z-8:;) I/,/ I I I 15"'5-"''f 1/dlJ I '7o/' vx JO I 7E.- I 2... 

? ._~5:1 I <-K3 II I I l<c .. o 1.14 '-/ 17 r- I~ r-7 I ?fl/ 1.3 . 

1-1 ! 2 zrr 1 ~ ss 1 1 , ~ 1 r, 1. o 1 t of. 1 4"''7 1 _d.f:tl '7 v 1 t...-

'l- I ~ ~ '- I f , I I I I 6 7. 5"' I I tS I q ~ ·1 z ~-/ I I' :..-· I L I 

i 

'-· I A ~ 'i I /, 1..---- I I f. ' 'l i . ~ I I 0 lJ I '1 t, I OlS_ I / 1'1-- I 7 I 

,- -.5 I ?.-1'2, I 1.-v I I I r!JJ,I.J. I Jr.'l I 'T~ I fJ..JO 'h I "L 

!, 1 :,...,3 1- 1 1,, /."V 1 14,4 'c/1- 1 c;~ Lz.._n 1 ;y 1 z.._.-.. : 

1 I ~ ~ J I 1. I 5"' I /. C I 16: C I I o 7 I I ~ I ~s 0 I /} 3 I -1-- I 

I /) ""l I I G' I f1'1. ~ I ' r r· '7 I tr'[. I I~ /l ;, I '- I ~ 1--.,:· I 1 ' r - , (]\. 

"" ._, I ;Z ~ 3 I I Cf,/ I ' <D <"(6. < I /'6 'b I q ~ I ~ )'/ ) ) I v . I 

I -z 't Ll ,. --:~ .r-1 . ' ou' ' _Lc:; ~ I -, ,- 7~ 7 J I "2 - . ! 

51 
PARTICULATE FIELD DATA 

PLANT :.A{';:·,:_:-· 

DATE: 61 /<3 -

-z REPETITION: j 

LOCATION: t".:.>~ C;l_· OPERATOR:~ 

STACK #: . 

SAMPLE BOX #: :~.;. ... :-·~,__ ,.1_~. 

METER BOX#:,! 

AMBIENT TEMPERATURE: ~ )"' 

BAROMETRIC PRESSURE:L~~rASSUMED MOISTURE: ? ~ 

PROBE LENGHT: .:,-' - "'" 

NOZZLE DIAMETER~/~3 

STACK DIAMETER: ~ 7 

METER H : 1 -~ <6Yc£/ ;7 

C FACTOR: -~._,. 

METER CO-EFFICIENT: • <f~/L/~/ 

FILTER TARE: 

PRE-TEST LEAK CHECK 

IMPINGERS 

Initial 

COMMENTS: 

POST-TEST LEAK CHECK 

Final 

t'fZ.. 

f}_Ob 

~J 

"-~ 

Meter: o ·....., cu. ft./Gn. HG 

Pitots: ~ in. H20 

Meter:O··ft Cu. ft. s . \/ P~tots ~ 

in. HG 

in. H20 

c.-

I ' e /STAT!~ is 

I I WY/ I vm / Tm lcJ:rm /OVEN ~p .,VACUJ~ ~.= ~H T -T K 

- PRES. OF Fi. 3 I NLEi . L£i TEMP. 1

·Ek@. CIN H,S) 

/ }. "<::;) -K ~~~ 1/.-/ I I I k(sf.!f(' I /)it 17~ I~SZ' I 1~ I ---z;:..:: 

2- IP:<t? ......-I /,3 I II~ J I(/!: t 1/~ 1~¢" I C..t""v I/<! ld:. 

3 I IZ'i?-"2..--· ! / 3 I I~.,_ 15?1, '-- 17~1 ~~_9' IZJ<J I '> };- I 2....--

'I li_<V I ,,-~ I I},~ 17~ I /Ov 1'1~ LA.f'l 1/~ I -ts- Itt--'6 7..,t f'J...-3 I /,"1.....- po, 5 lft,41 I '1!""' I~ I A?.,... I v 

.,;;' - • .s-z.-1 7 Kt....-- I /. 3 I/. /1 17'~~ I J6r- 17_.... I ~.f1 /""t.-- I <...... 

~ 17 R"t lid I I9'LYs-l ICC I '7" I t:.f/ I /2.. I (_ 

~ lr? ?L· I# y(""' .~ M:"~ I I r;·{ I -: t? 12-i/' 1"71- I 1 ... ..-' 

q l?}..t}- I , "13 .'7 '76, I I ! _.,I I s~: I~~ I 'l"L 1---

.. 76 I 02--<lv I ' <. ,s- I '11.; I I(; 1 iii : rlk'c.l '")1_ I ~ J/ ~~~:v 1,-J~ I .~ I J't ~..- I I o '1 I i'1 I L<'l 1 \.... I "\_,. ... 

J]/ !~7~ 1 4s I I .~ I o·-,I... I I v'6 I (/JO 1 lAn 117 I LJ !Cb-"IS 1.. 1t~ I I ,cr IJC0 ) l."'T I ,o.~ I 1/JiJ I iJ._{J. I "1 'l..-' I v 

2.- 1...._<?-:... I frf I I I I-, I T nS" I~~ I~~ '. "\.....- I I . :; R.'%Z.... 11.1- I I ~ .. t I U)( I I OJ I 'J..S"/ 171/ I Z-

,, I /l..7"'1 II r 1....- I I, 'f,t. I 'ffJ 1 1 qer 18~ 7-:c I L._ 

<;" f-, s"""v ~~~q I 

'I~ I ,, 1.--- I ( ,/ 170~ I ;t:D lA_ <;-o I z...::- 1 '\....... I 

/ ~~~OL I I,,_ I r,j I i7t1 lot? .1/CO 17\~ I '77 _, I L I 

I ~.Sd T Ll I I q,q.._ I I(. i 17 llj I ~JO I '!1 I ... - I 

f 13- !11 I I I I ,'T I (C, 7i I : :: "i I leG I ::1..~' ·13 I 7 - I ~ 

~~6 I , 9 'I I I' '~~(> I /01 I 7 t; I (}..) t ·; ~ 12.. I !.,. I ~1{ Is "j l ,'1 '}. 3 /f)tfj 1161 I ~.(-I ·•f;,....- TJ/ . I 

l~')"b 1,7:3= , b /u, [. /0'1 I 10/ I~ c-. I 1"'v I , I 

!2 la--l~ I . $'"'"-6 I ,; l~.r; liD I I o i l~l I 1-v I I I 

T ... ".15'1 I. I I I I . I I ( 

!).v 10.~1.3 I ,,qqu, I ,loH ''J ., fl.l. "- I ' (X.. I j ' 1/CJ;,L. Ci..!! ; 

52 .\ 

\ ~ ( '\ 
··~ PARTICULATE FIELD DATA 

I 

.. 

fPLANT : 1\:_ rY\ { · . 

DATE: ·G-/3- "'JJ 

REPETITION: f 

LOCATION: fy.. l'c. ·\.S + k_;l I\. 

OPERATOR: 3 ~ 

STl\CK #: ""'" 

SAMPLE BOX #: "2. 

METER BOX #: "'3 

AMBIENT TEMPERATURE: 1' ~ 

BAROMETRIC PRESSURE: fot~ 

ASSUMED MOISTURE:~ok 

PROBE LENGHT: ; rl 

NOZZLE DIAMETER: 1

1 '' 

STACK DIAMETER: '-/( ' 1 

METER H : I • 6 (j "314 

C FACTOR: , :;, Lf 

METER CO-EFFICIENT: ·, q 1Jl6 36 

FILTER TARE: P ~(U t 

PRE-TEST LEAK CHECK 

Meter: e .o~ Cu. ft. IS in. HG 

Pi tots:· v in. H20 

e ~TATI~ is 

I I \It:? I ' 

RES. OF D.? ~H 

-

I Gf ;,-'1 l~f I I I 

'· 0 -z.. I ? Q-z,.l I , . 'J 

~ I -:1 ~o I I /.~ 

'-1 I~ l<'f I I I f,O 

5· I -:;)...9/ I I 1. u 

·'- I :Je?l I I. o 

I 

I I 

I I 

I I 

I I I I 

I 

. I I I 

I I I 

I I I 

I I 

I 

I 

I 

I 

I I I 

I I I 

I I 

I I 

I I I 

I I I I 

Av I I I I 

53 

IMPINGERS 

-Initial 

#1 : 2;:)~ N A 0 ;t 

#2 : 2_;:J ~ f'J A .) }-1, 

#3: -

COMMENTS: 

POST-TEST LEAK CHECK 

Meter: Cu. ft. 

Pi tots 

I vm I Tm ~ IovEN Fi. 3 INLET . t:'i iEMP. 

1Ls7'.V3'11 99 I <XL I - I 

I!~~.-~ 

''#o. 'lI 

I I 

I 

o 

05 

1 I <it I - I 8 ~ I - lt.t17S,J I I o5 I qo I - I 6 '11- q I I o 1 I tfb I - I/,~"'. 1- I I 0 '1 I 113 I - I !5"J,q !.fZ I /I'- ...I. 

\ "" 

1----.... I I I <f.( 6"'7 I / ,,,~1 \ I .. -. I 

./I --· I 

~ I I . 't- I I I 

I I I I 

I I I 

I I I I 

I I I 

I I I 

I I I I 

I I ' I I 

I I I I 

I I I I 

I I I 

I 1 I 

I I I 

I I I 

I I I 

i I I 

Final 

;).It 

2.vD 

J-_o). -L 

JJ, "-' 

in. HG 

in. H20 

~p r -r IVACUJ-K E~ CIN H5) 

I ;; o I Lj 

lt-.o I 4 

I -b u I ·y 

I LO I t/ 

l~o I 4 

I ~0 I 4 

I I 

I I 

I I 

I I 

I I 

I I 

I I 

I I - I I 

I ! 

I I 

I I 

I' I I 

I I I 

I I I 

I I . I 

I I I 

I I I 

I l ( 

I i 
tl.t" PARTICULATE ~ 

~ ' I ' 

PLANT: IJ.c. '1';\ .e 

DATE: ~-~~~41 

REPETITION: 1-

LOCATION: \~.It\,. 6frho-wA 

OPERATOR: 3~ 

STl\CK #: 

SAMPLE BOX #: 2-

METER BOX #: 3 

AMBIENT TEMPERATURE:$0' 

BAROMETRIC PRESSURE: J<>J 1.} 

ASSUMED MOISTURE:8~ 

PROBE LENGHT: 1 ' 

NOZZLE DIAMETER :Yz.. 1

' 

STACK DIAMETER:41~ 

METER H : I. 6f~ ~ 

C FACTOR: , '-'1 

METER CO-EFFICIENT:.~,qb)' 

FILTER TARE: 

PRE-TEST LEAK CHECK 

' Meter: Cu. ft. in. HG 

Pi tots: in. H20 

I ' e STATI~ Ts I - PRES. °F ~? I vMJ I ~H I /J;'tl-r-- I 2-<iO I I I /.o 

- /' 2. / I~-., I I l_~__o 

~ I '2.Sif I I _1_, 0 

y I "'2.~....,...1 I I J. o 

s I 2~ 1 I I Jo 

6 I 2-~:vl I I ,o 

I I 

I I 

I I 

I l I 

I I I I 

I 

. I I I 

I I I· I 

I I 

I I ~, I 

I I I 

I I 

I I I 

I I I I 

~ I I I 

I I I 

I I 

I I 

I I I 

~v i I I I 

54 

FIELD DATA 

IMPINGERS 

Initial 

#1 : Z,v<> ,,.J ~ f\),., (; • 

#2: '7 - "'"" -'- • N ,.. , c -1 "" 

#3: -

#4: :::~., 5 .. ; 

#5: -

COMMENTS: 

POST-TEST LEAK CHECK 

Meter: Cu. ft. 

Pi tots 

I vm I Tm [ Tm IovEN 

Fi.3 INLET ·.~'UTL...Ei iEMP. 

lbS"~.V~I lO'L I '1-=f I - 16?~'·' I Ill I 1P I - I 6b '/, .;tl )/!-, I Jo3 I - l~h. '1 I I I 9, 1 ;os I - ,-,4. /, I /d.-.0 I /rJI{ I - 10 ::z~.1-l (}q I 'o ~ I - 16":i(, oocj ,,-1 ~1. 

I I I 1/DS.cl. ~ 

1/£,!1~ I \ I ./"~' 

I I ---r--·· I 

I I I I 

I I I I 

I I I 

I I I 

I I l 

I I I 

I I I I 

I ' I I 

I I I I 

I I I I 

I . I I . I I 

I I 

I I 

I I I 

i I I 

I 

Final 

in. HG 

in. H20 

~p IVACUJP. ;~LET <IN He) MP. e.~ 

I ~o I 3 

I A 0 I 3 

I 6 ° 13 

I ~c) 13 

I J.O I 3 

I oo l:.j 

I I 

I I 

I I 

I 

I 

I 

I I 

I 

I . ' I 

I 

I I 

I I 

I 

I 

I 

I I 

I I 

I I I 

i 
I 

.. 

PARTICULATE FIELD DATA 

PLANT: Ac..:.-v• ~ (3 ,,de__ 

DATE:tjtffJ"'il 

REPETITION:3 

LOCATION: K· (h E;t.. 

OPERATOR:0s 

STACK #: 

SAMPLE BOX #: tfP 

METER BOX #: 2 

AMBIENT TEMPERATURE:~o 

BAROMETRIC PRESSURE: .t..,.r' 

ASSUMED MOISTURE: ~t 

PROBE LENGHT: !J 1 

NOZZLE DIAMETER:.;-

STACK DIAMETER: '17'' 

METER H : /, t 'fi?, 

C FACTOR: • )~/ 

METER CO-EFFICIENT:J/(rtJf 

FILTER TARE: 

PRE-TEST LEAK CHECK 

Meter:o~oQ Cu. ft. /~in. HG 

Pitots: v in. H20 . t/ 

' e ISTATI~ Ts I 1 vrr I AH PRES. CF A? --

~ I ,'o,l I '2..~3 I I I /, 0 

2 I ? ~~ I I . ,,\;) 

"3 I 'i.~C I I /.0 

't I .., a. J..-1 I I 1,0 

J I ~o I I '; o 

.(,. I "'1A I I I /,o 

I I 

I I 

I I I 

I I 

I I I I 

I I I I ' 

I I I 

I I I 

I I 

I 

I I 

I I 

I I 

I .... ~:~ I 

I - I I 

I I 

I 

I I I 

I I I I 

Av I I I I 

55 

IMPINGERS 

Initial 

#1 : 1.. {rr) .,..J._ p . : ,... >t 

#2: ;._cA:J -

#3: 

#4 : ).. cru 0 56 

#5: 

COMMENTS: 

POST-TEST LEAK CHECK 

Meter: tJ. oa Cu. ft. ,o 

Pitots V 

I vm I Tm lcJrm IovEN 

FT. 5 INLET . l.£T TEMP. 

f6~~ ~~~~I /.10 ·I JOf> I 

I'~·" I JJ't, I ;o-:;. I 

I t re, :; .. ! _1_ "2...0 f ~ ()6 I 

I t:~ ~ . ~ I "2, I I fo S' I 

IAgf,q I 11--'L- 1 lor 1 

~.--:::; I , '-"Z- I /or I 

~i1.3'1t I l I 

(11/.t,V I ) 

II t. Ll( I r I 

I I i I 

' I I I I 

I I I I 

I I 

I I I 

I I 

I I I 

I I I I 

I ' I I 

I I I I I 

I I I I 

I . I I 

T I 

I I I 

I I I 

I I I I 

j I I 

Final 

in. HG 

in. H20 

Prp- IVACUJF ~~T CIN H5J 

I (. u I 'l 

I ~o I '3 

I· '() 13 

I r-.o I~ 

I ~ c;, I' 6C::~ Is 

I I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

i 
D.· PARTICULATE FlELD DATA 

2, 

,.... '' 

i•.J .. " 

.... 

'/'. 

3 

L•• 

-.. 

< L 

~ 

PLAI\lT : '¢1-.c. w-. e... t $ l! "" \ "i . DATE: f,p) f S ( '? I 

REPETITION: I 

LOCATION: D (':'=..-< 

OPERATOR: -r~. . - I 

STACK ~: {tF ~ _. r I, ~ · ~ ./' ~ · r 

SA."!PLE BOX =i*: I cHETER BOX #: If AMBIE.~TT TEMPERATURE: ~ 1... 

BAROMETRIC PRESSURE: 7PJ, 0, 

ASSUMED MOISTURE: ?;,0

/o 

PROBE LENGTH: Q>~ ~~ 

NOZZLE IDN-IETER: /(f, 

STACK DLZl.i.'1ETER: 6 0'1 13 . .)AIV•f(Jle 

METER E : l • b'-''1 

C FACTOR: -g '-1 

METER CO-EFFICIENT: } ,() 1/ 

FILTER TARE: Nft 

PRE-TEST LE..~\ CHECI\ 

· Heter: ~ ·0 1 cu. ft. l.h 

?itots: ~ 

in.· HG 

in. H20 

/ 

I p e STATIC Ts VKP :;:::; PRES. OF l:J.P 

t IS: S"''2.. ~r.'"'J., toz- .g~ 

,., I 99 .. 8S 

~ I ;o.J ~~S 

Lf I I !D~ , 8.\ ~I i . 

.... ID fa .. as- ~I ' I -roVr .R~ 

i 

I 9.;~~ /0'1, .'? 

7- i !Dr 9 1 ' 

3 I I/!)~ ;'q 

y I ! ' /Of ,! 

~~ I 

l 10 ~ .. 8 

"' ' I I o "! ,,., I 

I It ~SS" !O'i-. ,'} 

l I I'PJ • 

q 

3 I jt;CJ ,q 

\../ I 11 0.,. ' Cf 

..s I IO"+- I ~ 

"fD /II .. 2 It;;,~ 

6H 

1·0 

/,D 

/, \) 

), 0 

/,(:> 

!,_;;> 

1 f.D "'. 

·~ 

/.D 

/. 0 

(, D 

, .::: 

," 

, _'i 

rr90 

1/0 

I, f) 

I,() 

1, D 

o., ~-

IMPINGERS 

Initial 

#1: ~o /V ..... o~ 

#2: ).4:>= A).,.o~ 

~3: 0 

:;:;:.4 : '2. 00 s &--

#5: 

D., '-

fZ. 1 't::> "2..1 

r< z. o z., 

K 0 Zt . 3 

POST-TEST LE.l\1\ C:-IECK 

Heter: cu.::t. 

Pi tots: 

I vm Tm Tm OVEN 

FT.3 INLET jOLJTLET TEMP. 

1188.3/iO /07 104 -~' '57; I I 1-=f /0.3 ~'fh 

196. 6- tJ.o -+ ;oS ~'/~ 

CJ-d, r _L_J3 I i_OS ol'/'1 lf~,s 1 I). r, I I£)_;. :2lfi 

18~ f. (_~-:;- ~ ii '-15' 

b:>oc .. ~ i .,,z;~ :; 

/ . r<s:- . ' :,;:. -- r-:za~~ )/D /07 25't:l 

tf.-r !21 - ;or-.... ~.S?J 

-r.,.s- 1~1· I /10 ~!Lr I r) I ~.., 'LJL .i II'•( -~'i'-1 

ld,S"_ I 13_r I It~ ~!1_3 

~~.o -!.l_'i J..J.:r ~'1-;;. 

~at.JrS i ,,q,, -r ) 

r5.Cf61'J 

~.rr, 16;; /). 0 J;<o ~ Ll;) 

Z./.5' /33 /~I :;. '/-:;..-

~lf. a. ) 31" f,}_f <7~"/ 

d-e ... q /3q ta;;. _;)'{ 0 

~9 .. -r 13't /.)..0 d'/;' 

I) ~-'t.. . 32, ~1 j'-(U I~ 1-- .J Lj 0 

· . ~c . ~ l v....--

1"------. /';, 1~1- I !J 'l., 'I 1 

\ v -

~~I ((:;2_ {:-.;. 

,· .... ,( 

Final 

212_ ;;21~ . ~ 

2'-:::: 

2oD ,;i:)()_ 2CC: 

0 G c ~Ql.f. 7 ;..o:.6 J.'?f ...... ;.. ") 

/(. 1 h-6 I"':,& 

. I 

L.~~ '<:.. (' 1.... .? • ''-

.n ..-. ,, 1C 0 · ::J ~ c '1 

-Rt... o.]iJ ~"2. ~ 

ir... HG 

in. P..20 

IMP VACU.JR IOQTLET (IN H!J) TEMP. 

~( ~-o 

~;2 .;;; .. o t.~ d). u 

.&3 I ~-Q 

I f,-3 ~-0 

{ct.( c;)_ () 

62- 2.0 

/.Z .;;;. .. u 

b3 ~-(') 

b '/ ,;.u 

h¥ ~ .. D 

/,.5' ;; .. o 

:,3 ;J.() 

0 !../ ~- ~ 

c. '/ ;.,Q 

h'-1 r:J ... u 

;;.s- ;;:; -() 

:h) ;}.CJ 

~~A~v~I __ -J--~----~--~----~~~~----~--~----~--~----~~-~ h~ 
I.~ PARTICULATE FIELD DATA 

PLANT: Ac:..Y'-'1 ( 

DATE:{.,-)'-~ 1 

REPETITION: J 

LOCATION: f.\C..v4f 1 ~e"" ;J'-:-X 

OPERATOR: t.w, TfA. 

STl\CK #:1)..-v~v 

SAMPLE BOX /#: (p 

METER BOX #: I 

AMBIENT TEMPERATURE:q2 

BAROMETRIC PRESSURE: Z'\,0, 1 ... ~~,,·-~ • 

ASSUMED MOISTURE: sYo 5:.2]/<""" 

PROBE LENGHT: S 1 

NozzLE DIAMETER= rz." ···---- So'-

sTAcK DIAMETER: (J;'' \";~, " 

~E~i~T~R ~ ~ Ji~ ?>++ 

METER CO-EFFICIENT: 1 .. ~c~00 

FILTER TARE:, 4/., ·u ~ 

· PRE-TEST LEAK CHECK 

Meter: .. OIC'• Cu. ft. ;g 

Pitots: :::;:.--

in. HG 

in. H20 

!j(I..Wtf\ 

IMPINGERS 

Initial 

#1: 2.Dt:>, ... ,.\.~ b% J.lL..Cz. 

#2: zoo""\-' 1..% Hz6t-

#3:-

#4: zoo J .... s C:s-

#5: 

COMMENTS: 

-

POST-TEST LEAK CHECK 

Meter: o,()f~> Cu. ft. /S' 

Pitots ._.., 

--

Final 

;;21"3 

).03 

in. 

in. 

HG 

H20 

I ' 8 sTATI~ Ts r~,ot.~~~ I vm I Tm bJrm IovEN ~P lvACUJr 

PRES. OF 6H FT. 3 INLET . l.E:T TEMP. ;~~T C IN He:· - MP. -..!. -

~I r;so -i. -z.-.1 to~ I J./0 IIOl.f,.SSI gs ,,s.,..2%1 rr 1 fS I ~"to I '~ I Co2. Q 

v I IO"g I f.t! · 1/ol 1~&5'1 .&5 I S?-.1 I tOT- I ~ fr I :u.s I 'b I .;;.1) 

3 I lot I /, u.Y Ito 'I I .. ~1 /iS I r,o, ~ I /13 I fit I ~~~ ' 

,s- I :2. i:) 

4 I I of I /,D~ ~otf,Srl , l,c;- I ~ . ~ I It r I {cro I .J.bf I 's I d>- l:) 

~ I lo'l I .~< l!ot h l-.q ,k~ IJ.S, c I t/ if I /()I I elslf I ~.~- I .;;.6 

fn I Jo9 I .~7 .... f/)1/.B~ I ,s-{ I t,K, 'I I /e2'1 I t ~ 'f I ~s-~ '" I .;;.o ...., I tof I ,.,~ l"otO, /,;lSi I I I I 

i' I ltfi I .It,~ I I I I I I 

I I I I I I I - ~ ( I lo& I .'1V I I i ...1. I 

'2.1 I tO?, I .rv 1 I I I I I I 

~ ! Loa# I ·WI I I I I I I 

L( I LocJ I lto~ I I I I I I I ..... I tD~ I I .oo I I I I I I 

(o ' I to~ I l&o~ I I I L 

"1 I to~ l l.tO I I I . I I 

~ I tor I I rO I I I I I I 

I I I I I ' I I I I 

I 1 I I I I I I 

I I I I I I I I _l 

I I I I I I I I 

1- I I I I l 

I I I I I I 

I I I I I 

I I I I I I I I 

~v 116S"·i I • I 11,()~ I -z4)' i JC~<t<r 11o5".Cf! i 

57 
I ' 

PARTICULATE FIELD DATA 

PLANT:~,....... 

DATE: ~-I£ ·11 

REPETITION: d_ 

LOCATION: f-.../y; 1;' 

OPERATOR: 1-w; -r~ 

STACK #: V.,y~ ey 

SAMPLE BOX #: {.. 

METER BOX #: I 

AMBIENT TEMPERATURE: liJ'{ <:t) (""~~· BAROMETRIC PRESSURE: ..Lf.'t --~=--:-t_ 'I'\ 

ASSUMED MOISTURE: J.Yo '-/. :;-~ ]) ) 

PROBE LENGHT:t~~,. ~ ~ 

NOZZLE DIAMETER:Yz -

STACK DIAMETER: ~D~ 

METER H : /. 7-'f J9? 

C FACTOR: , i .,. 

METER CO-EFFICIENT: f, oo ~' o 

FILTER TARE: -5-. (?_ t 

PRE-TEST LEAK CHECK 

Meter: o.otJS cu. ft. 8' 

Pi tots: 

~ 

Ts 

in. HG 

in. ~20 

"'-II\ 2 

.O.H 

IMPINGERS 

Initial 

# 1 : ::2 oo ..... 15 G, 0 1~-:.;) l. 

#2: Joo ..... ~; G% !h ~,. 

#3:--

#4 : 2 o o "'',... S.C:s • 

#5: v 

COMMENTS: 

S!--

c 

Tr-.,.,~rH~ .. @, 9.'tf,sPOST-TEST LEAK CHECK 

Meter:D.~Oi Cu. ft. ~ 

Pi tots __. 

_,. 

Final 

;:Lo8-.... 1r 

'2. 0 0 

in. 

in. 

HG 

H20 

-

- e STATI~ PRES. OF 1~6.:~1 w;:p I Ts"J IJP I vm I Tm· ~ IovEN 

Fi. 3 INLET CT iEMP. ~p IVACUJP. ;~~T CIN H,5) . 

l+t '&f :.s:l. -/.o I lo~ I • 75:___ !toot I ,q I ~'I l~;z.S7ol 'i't I lo o lc:olb~ I "3 I .:l 

2 I !Dfl I .~_2 1117-/. q 1 .. 9 I -:;s. 2- II~ I /O I 1..2~.3 I {,J. I ~ 

1 I IC8. ! I g,s: I lOb~, i I ;a· 177-.. ~ ! ~~~ I t o3 1.;:17~ I ~3 I .:t .., I lo9 I c;~ ltoa/ .. 1 I .. ~ I~~-~ I I.?D ·I IDS I-.2S 7 I ~'i I .:Q 

·) I to<K I 1 , .3:»o l&"'r/,~ I ,~ eJ~ ~ 1 ;;;s I 108, l..21(i I InS' I ~ , c. I /O'a I _l_,z..o I to-r/. l? I ~ ~-~.!: '/ I /3.;1 I ID tt I.)S~ d:-5 I -<. 

? I 1-o£ I . "),r 1{,/f, II o I I I I 

"' g I IQ'1_ I .~:,r I l 

I I I - I I l I I 

I ffO I J. Jo I I i I I - '8 ( . 2 I 110 I /.I I I I I I I I 

2 I to'i I I I I I I I I I I . '( I Jo~ I I • 1:) I I I I I I I 

~ I tog I .,;;_~I I I I I I 

r, I toe; I 'U" I I I 

1' I ,~e; J .~ I I I I I 

~ I 1n~ I ,j__ I I I I 1 

I l I I . l I l 

I l I I I I I 

I I I I I I I 1 

I I I I I I I ,... 

I I I I 

I I I I I _1 

I I I I I 

I I I I I I I I 

Av j , {)<j 1 <)~ I .15"1' I , '631) i l~_b_ I 1/13.~! i 

58 
\ 

J( 

PARTICULATE FIELD DATA 

PLANT:fle~ 

DATE: b-t&-~ql 

REPETITION: 3 

LOCATION:<;c_..._\.._1 1 l)( 

OPERATOR: !_ w, "i'J:\ 

STl\CK #: Uv-y(A.. E"~' 

SAMPLE BOX #: (.p 

METER BOX #: I 

IMPINGERS 

Initial 

#1: 2ou .... ls [., ·< ltz6t 

#2: 2.oo .... Is loi- 2 D, 

#3:-

#4: 20<.) !i ... ~ !:r. 

#5: v 

AMBIENT TEMPERATURE: '\ Lf 

BAROMETRIC PRESSURE:21,~J 

ASSUMED MOISTURE: 3 fo /~ ~u<; . PROBE LENGHT: 1.. o., . • /7 ° 

NOZZLE DIAMETER: '!,.'' "",.__ ______ ,... ( 0 l- COMMENTS: 

(C"~-

STACK DIAMETER:~o~ 

METER H : I I 1''1 ~1-1-

c FACTOR: , ~'{ 

METER CO-EFFICIENT: 1-~0'f(,O 

FILTER TARE: ~- f'l- I 

PRE-TEST LEAK CHECK 

- 02.. 

D -

2( 

l..a.\leAet. ~ lo;.sc~ 

POST-TEST LEAK CHECK 

Final 

'2-l~ 

'l.O"L 

D 

'J-_6), y 

/1.· ~ 

Meter: fJ,OJl Cu. ft.IJ in. HG Meter: tJ. OtJ S" Cu. ft. 'f c· in. HG 

Pitots: ~ in. {&~ Pi tots ~~~ ~ in. H20 

I ' e STATI~ is ~~~~~~vs~ I vfi/iF I I vm I Tm.laJrm IovEN Prp- IVACUJi= 

PRES. OF AH FT.3 INLET l.£1 iEMP. ;~rT C IN Hc:J - T'(, AI MP. -' 

J'\1 Ito: 55'" 'r&/.0 l110_ I L 10 IJol? /.CJ I _; <;o I ~i~.s .z~1 1/f I '113 I~~~ I ''2.. I ~- D 

"Z.. ' I I 1o I (dO It~~/ ... '\ I #' 0 I '1'1 ... o I /.J., I IJ.S I ~ t.. '2. I .,3 I z.._ ~ 

3 II ', os- I 110 ! I " ~ ~ o_S_L, ~ I ... ~ ~0 I '13.'1 ! I 3'1 I 11s- I t2itJJ I 1-Y I ...2. C) 

'1 I ,, 0 I I f'j ltoq I ..-9 I ,~ 0· I Cf~,! I (.5_3 I II~ I J.Sfo I '" I ;;. D 

}( ~ If; IS I flo I .c;.<: (O'V I g I .iO q~.l I l'f 3 I II 8 I ~"fa I ~5 1 a, o ~ I. I. tO~ I . -~e:- JOT I, '8; I ,g-6 l~l. I I l!L o 1 rz.'f l..ttf.r t,s I ;l A:> 

1- ,,, :3_':1 I l?J1-L .7b I I I I I 

\"' 'g I lo C/ I , 70 I I I , t:o< I I I - I I I t~.J...l .7,( I I i I I -·- B t I __!._ 

2. I to7 I ,c:; I I I I I I 

3 I I o_l___ I I ,1) I I I I I I I . '-I I I Of I 't:,.<' I I I I I I I 

!:;" I Ji> l I l./0 I I I I I I 

(p I lh 511 (,o( I I . I I 

7 I I tl~ I -~ I I I I .. I 

~ I (o¥1 .t.o I I I I I I 

I I I I ' I I I 

I 'I I I I I I 

I I I I I I I I 

I I I I I I I 

I I I I I 

I I I I I I 

I I I I I I I 

I l I I I I I I 

Av il..t2~~1 I .lb)l I _<l,,l ; 13.c;'l.)i lr2t.J tt! i 

59 
rJ.' 

APPENDIX D 
£!. VISIBLE EMISSION OBSERVATION FORM 

No. [(, G I ,-

COMPANY NAME . 

A t/YI c 13 a_, cl<. 

STREEi AOORESS : 

--

.... - ..!;-&,;;L ; 

P c../.._,-- S ,c;.l\.lfe. i 1;;. e.• T2.. 'b 

CfrY I STATE 

<; ;: 4/ II lx ~~7+1f-- PHONE (KEY CONTACT) I SOURCi: 10 NUMBER - (4<X\- A As- 41.24- R- q_s--4-D- -. PROCESS EQUIPMENT 

K.. i~l /?y~ 'All~+ 

~PEFII\TING MODE 

~ 11 iMb -//, cllk..~ CONTnOL EQUIPMENT . I OPERATING MODE 

I H '.' ,.!(OQu} <:rrubb.u-. .f u/! (.ol' 1'.;. l DESC~ISE EMISSION POINT . 

::-~k .. 41 11 ~to h_;a~ ctf~y'E\;..~-:_ D; ~~-<.O r- . ! ,. .. 

HE!GHT ASOVE GMOUNO LEVEL I HEIGHT R~LATIVE TO OBSERVER 

'7tJI , Sta:~ "":10 End !---=-----

CtS7 I DIRECTION FROM 08SERVER ANCE FROM OBSERVER 

Sur:/~/) I E:'ld Start Dl c. V/td-. End 

DESCr.JSE EMISl:IONS 

Start ~ol..;t.·~; b\"t. G""~ss:~'J El"\0 

EMISSION CCLOR ·1IF WA TEA DROPLCf PLUME 

Start- End Anac.'llld 1.1 Oelac:ned C f--·----· 

?OINT IN THE PLUME AT WHICH OPACITY WAS DETERMINED 

start o fJ I!" !'\; i.!U iu Abo r c. End 

DESCRIBE PLUME BACKGROUND 

Star:-~ k Y::..-_____ _..,.E:;...nd.:;..._ _______ ---; 

SACKGriOUNO COLOR I SKY CONDITIONS 

,_s_ta_rt_""S=-1-u....;:c. ___ E._:"Id ____ ....,-s_ta_rtP_r_{lv Clc,uJ no 

I 

WINO S?E~!) WINO DIRECTION 

AMBIENT TEMP 

Start 'iC • End 

S!.JCX 

wun a:= ::-rume 

Sun + 

star: :Soil~ End I WET BULB TEMP I AH, perc;ont 

SOURCE LA YCUT SKETCH Craw Nol".n Arrow 

I OBSERVATION DATE 

t-Jtl-7! 

~-----_,...../ El~ TIME 

/0/30 

SEC 

0 15 COMMENTS 

() 

I(/ !o 

IO Ia ~ a I o I~ 

s o lu cIa 

1 o lc? IGJ lc7 

8 CICICI8 

s o· I c ~-~~-::---=-! -o--+-------

'

0 () IC I c:~ I 0 

12 

1

:J ~I fJ lc I o 

0 

15 (!} lo IO 16 tJ o I o 1 t7 

17 0 Ia o lo' 

18 o 10 16' lo 19.~ 6 I OT CJ=----+1=-c;--_ 4--------

zo r- I - 1- I :-

21 o lc? I a Ia 

22 o I o lo Ia 

:s" o t:J I o I o 

29 () 

:o () 10 

OSSERVER·s NAME (PAINT) 

MA1f" TAY L ott.. 

OSSERVER·s SIGNATURE 

-?Vfa}(;(- 1/- ·L 
a.· VISIBLE EMISSION OBSERVATION FOAM No. I< I /)(_ COMPANY NAME . OBSERVATION DATE I START TIME I ENO TIME ,t::} C:/YJ F 8 r.~ '(_)<._ ~ -/<j-9/ I&~ se> - I/. 0 :_--. STREEi AOORESS • 

~ 0 15 JO -45 COMMENTS N 

6d,2 J).r~l!f- .5 M Fd. · ~~ I~O~ I _11 {) 0 0 

I /J I CJ Cll"Y I STATE I z;74.74 

2 {) {) ! 

SeA-Ir/ rr 3 () I PHONE (KEY CONTACT) I SOURCe 10 NUMBER () 0 ID 

(1-cq,j ~y£5 4-124 · R-Cf~4o 4 0 0 f) lo 

PROCESS EQUIPMENT OPERATING MOOe 5 0 /) c9 lo K..-i/tJ C XIJA~~ f- ~ ;/CAtJifG· M 

CbNTROL EQUIPMENT 8 {) {) (!) C) OPERATING MODE 

t-.Jfi£"l3eK! SC!.fvbL.ar fu lf Lo 1f-l:::J 7 olo 0 o 

DESCRIBE EMISSION POINT 8 tJ CJI~ lo '?{!)' 1-h'&...h GrAY l51Aci<.. s '{-,l.d(._ 9 () L?> 0 le> 

10 .a Q [) 0 HEIGHT ABOVE GROUND LEVEL I HEIGHT RE!fTIVE TO OBSERVER 11 I) vlo lo -, 0 I Sr&n "7 C!J End - f..--·-----

a () 0 lo DISTANCE FROM OBSERVER I CIAECTION FROM OBSERVER 12 

Stan / ,;ztJ ' Stan \N End - End 1-- - () r, {216 1:3 '-.../ DESCRIBE EMISSIONS 

- 0 1-a {) ! _Q_ Sran- 14 E:-.o 

EMISSION COLOR · IF WATER DROPLET PLUME 15 

- - v I f) IO Ia Slat: End Al!acnec:ll.l - Oelacned [J 

POINT IN THE PLUME AT WHICH OPACITY WAS DETERMINE!) 16 0 _a_l_alo 

Stan (JaJ.JF ~ ~ l::::,J 14ft...,.J...,/'End 17 0 0 ol Ci 

DESCRIBE PLUME eACKGROUNO 

Sran 

18 () olo IQ End 

1

::!olo OIO BACKGROUND COLOR I SKY CONDITIONS 

Stan End Stan End 20 0 ltV ll' lo WINO I WINO DIRECTION SPEED 

Stat: E:'lC: End '0 lo loiV 21 Stan 

AMBIENT TEMP WET BULS TEMP I RH, perconl 22 () a I olo Stan End 

~lo olo 2:3 

suo SOURCE LAYOUT SKETCH Craw Nonn Atrcw 

"'''" 610 cc::. 

0 24 

Plume 0 6 

10 Sun + 25 t:J a 0 Wona -- () 0 () 16 26 

... 

X {) 10 27 0 0 . Emosaoon Pcont 

28 _{J_ 0 QIO 

29 tJ~ n olo 

:30 0 0 o1o . ~ 

OBSERVER'S NAME (PAINl) 

Ocs•rv•r·s Posotoon Mmt-"11\-v t.l)tL 

OBSERVER'S SIGNATURE IOATE 

__ . ____ J(_ _____ 

1VIrdk ~~A-· fa -'Y~ ~ I 

ORGANIZA TlON /;. 

Sun Loea n Lon• ~~~;[{~,.. 

CERTIFIED BY 0 

ADDITIONAL INFORMA TlON TAG~ k!TC -l'i- Cf; 

F ·-----

L-------------------61__..11 coNnNUEO oN veo FOAM NUMBER I I ~~I 
13. VISIBLE EMISSION OBSERVATION FORM 

OSSfRVATION OA~ I START TIWf 

)28'>/M 

I ENO TIUE 

I 

COMPANY NAME /JC/11 B 73r~·J<- STREET AOORESS • 

0 15 JO 45 COMMENTS 

.5C::..z Pckv--- S,:wFc:_J,· Pc-R._lJ 

CITY I STATE 

.s "'U4-t l/ (-,{ I ZIP7 ?"f 74- ~NE (KEY CONTAC~ I SOUACC ID NUMBER 

~f) <[i'"~ ~4 R-~~~ 

0 0 0 

2 0 lo 0 

3 0 Ia 4 ~ 

PROCESS EQUIPUENT I OPEAI\TING MODE /<;/ttl ~J( ;::,; If ~ 

CONTROL EQUIPUENT s. . I OPERATING MODE 

f.l...'//:)60/.~~ C-fvb fo~ k., I( 

0 

C) 

7 

DESCRIBE EMISSION POINT 8 

IC'~ ~lAde~ !Hf:...l< 

'.} 9 

10 

HEIGHT ASOVE GROUND LEVEL I HEiGHT RELATIVE TO OBSERVER I a; / Start :;.. 0 End f-------

DISTANCE _, FROM OBSERVER I CIAECiiON FROM 08SERVER 

Stan Stan N i:.- End - '7.,j End 

11 

12 

13 

DESCRIBE EMISSIONS 

Stan - Ena 

----- a 

EMISSION COLOR ·1 IF WATER DROPLET PLUME 

Start - End At:ae:led 1.1. - Oetaelled 0 

POINT IN THE PLUME AT WHICH OPACITY WAS DETERMINED 

s~n / ~~eJ,-rAiut~e:_end - 15 

16 C) 

17 

OESCRieE PLUME BACKGROUND 18 

s~r. 6k~------------~E~~----------------~ eAC~D CO!..OR I SKY coNDITIONS 1---!~--;.-::::---r-=::;._....;---.;::;.....+---------------- stan L v ~ End Stan ~il (Jo~ End 

19 

20 

WINO SFEEO I WINO DIRECTION 

S~r./ 0 IYI./)1"1- End Stan $, c;-

-'M61ENT TEMP I W;i 6UL6 TEMP 

s~n <f~"' End Y'1• 

Stacx 

woan a:= 

Plume 

Sun + 

SOURCE LAYOUT SKETCH 

· X E:nossoon Poonl 

End 

RH, pergnl 

Draw NorUI Arrow 

Observer's Posoloon 

21 

22 

43 

24 

25 

26 

::7 

28 

29 

:lO 

140"/ 

----s~~ ••• ;-L7,;"e ____ -- /Gj 

~================---=-=-=-=~.....~ 'CERTIFIED BY y 

~or~~=f~AMAOON I "fA L_{l [ -------------------------~E~.;:_~ CONTINUED ON VEO FOAM NUMBER 
FJ. VISIBLE EMISSION OBSERVATION FORM 

COMPANY NAME --= Br I STAAT TIME :r_j<._ OBSCRVATION DATT: At/!?6- I END TIME 

Z.'C?' STREEi AOOAESS • 

~ 0 15 30 45 COMMENTS .. 5 b~ fl4n._5AAr-T./,f)~- I fl_ () '(!) _{j 

(()10 ala CITY In: I ZIP7i'4?L 

2 . ::5.~/v PHONE (KEY CONTACT) I SOURCC 

3 C) IO 0 b 10 NUMBE4 +D '1 - <6 ~~-4;;24- .. R- 1r o 4 0 0 CJic? 

lo PROCESS EQUIPMENT OPER.\ TING MODe 5 CJ () cD ;<.,·;AI tX'IJnus+ F~tl ! 

6 iL2 Ia CJ CONTROL EQUIPMENT () OPERATI( MOOE lfi_ V {:)( Ob'f:.tt..t S t.f ubb....r FUI 7" 0 ololo 

DESCRIBE EMISSION POINT a tJ n lo lo 

9 {)lo () IO 

10 0 u o-lo HEIGHT ASOVE GROUNO LEVEl. I HEIGHT RELATIVE TO oBSERVER 

In tO ole? 11 

Slalt • Encs f--·----- I CIAECTION FROM OBSERVER 0 CJio DISTANCE FMOM OBSERVER 12 0 Start El'od Star. End 0 0 0 Ia 1:l 

DESCRIBE EMISliiONS 

10 15 lc lc? 14 Star: Ena 

EMISSION COLOR -~IF WATER DROPLET PLUME 15 0 _C)_ 1:2 lo Start El'od Ar:at::~IICI 1.1 Oetacnea 0 0 0 ?;> 1--·---· 16 0 POINT IN THE PLUME AT WHICH OPACITY WAS DETERMINED 

Start El'od 17 (!) 0 () I D' 

DESCRIBE FLUME BACKGROUNO -- 18 0 in (f)IO Star. Ex 

o. 0 lo IO !--=-=----

SKY CONDITIONS BACKGROUNO COLOR 19 

Stan Enc Start End 20 Olo I DIO WINO SPEED I WINO DIRECTION 

Star: E:1d Start End 010 olo 21 

~M61ENT TEMP I wET euLe TEMP I RH, pen:ont 22 0 0 d IO Start End 

Ia 1 a lo I(") ::3 

Sucx SOURCE LAYOUT SKETCH Olllw Nonn Anew 

*"" ~ e:> OleJin 0 24 

Plume 

Sun + 25 0 0 CJ le> Wol'od ......... 

Cl. n Qld 26 

-.-

X E:nouoon Po.nt :!7 0 0 0 Q 

28 I() () IO IO 

29 0 IO 010 

:lO 0 C> 010 

OBSERVER'S NAME (PRINT) 

Ooset~ter·s Poslllon 

OBSERVER'S SIGNAT\JRE I DATE 

140./ 

ORGANIZATION 

-------------- Sun L.oeaaoon L.one 

CERTIFIED BY 

ADDITIONAl. INFORMATION I DATE 

-------

t L--------------------6____..311 CONnNUEO ON VEO FORM NUMBER II~ 
a. VISIBLE EMISSION OBSERVATION FOAM 

'7-. COMPANY NAME A . b/2 /~/L OSSCRVATION DATE I START TIME 1 ENO TIME urltr 

STREET AOORESS • 

~ 0 15 30 -46 COMMENTS N 

...6 i, ;;z_ ~ S4A.r-Fe..J .. ,cc;--H_o 1 t) .tJ 0 () 

{)/ Ia CITV ITY ,;.,+74 2 0 0 fJ~l/ [lHONE (KEY CONTACT) 3 0 a ~ lo I ARCC 10 NUMBeR 4oCf)- '616 ~ 41 ;z.4- -qs-4-n 4 0 0 C) Ia 

PROCESS EQUIPMENT OPER.\TING MODe 5 {) () CJ Ia K ·lltl Z.xh,::vs+ -Fu t'\ 1 

CONTROL EQUIPMENT OPERATING MOOE 

8 0 0 0 lo 

Hv D<"o &reA! Sc,u-u bb~ hll 7 f)_ Ia 16' lc::? 

DESCRIBE EMISSION POINT 8 c!J 0 tJ Ia 

9 0 CJ OlcJ 

10 0 0 010 1-ifiGHT ASOVE GROUND LEVEl. J HEIGHT AELA nve To OBSERVER 

1-------- Stat~ • End 

11 () olo I~ 

£) 0 0 12? DISTANCE FROM OBSERVER I DIRECTION FROM OBSERVER 12 

Stan End Sian End (!} IU' ~ t? 13 

DESCRIBE EMls:iiONS 

/'J a () 18 14 Sian Ena 

EMISSION COLOR -~IF WATER DROPLET PI..UME 15 12 CJ C?lo Stat~ End Anad'18CI 1.1 DetaChed 0 

POINT IN THE PLUME AT WHICH OPACITY WAS DETERMINED Q 0 OIQ 16 

Stan End 17 a C) CJIO' 

DESCRIBE PI..UME BACKGROUND 18 ~ IC' IC'IG Stan End 

BACKGROUND COLOR I SKY CONDITIONS noltJIO 19 

Stan End Sian End 

WINO SPEED 

20 () Qla Ia I WINO OIAECTION 

Stan End Sian End 21 Q t1 ~ IO 

AMBIENT TEMP I WET BULB TEMP I AH,I)Ife~nt 22 (() Q d lo Stan End 

Stacx SOURCE LAYOUT SKETCH Otaw North Arrow 

23 0 C) ~10 

6 h WI In a:::. 

0 24 

Plume 6 t:J 

Sun + Wona 

25 6 C) ~ ~ -- ~ cj Q_ I/! 26 

.. -

0 X Emosaoon Poont 27 0 ~ -CJ 

28 Q ~ ~ b 

29 0 b 0 I C) 

30 0 0 0 Ia 

OBSERVER'S NAME (PAINT) 

Otlsvver·s Pos111on mA-..,-r-rp v uR- ~~~NAT\J£ I DATE 

140"/ ..ttl(~ :.'.... ~-ly-f I 

ORGANIZA noN ();: 

-------------- Sun Loc:atoon Lone :l.-1.. tu .. :jA_;, ._o c- u, -

E L ___________________ 64 _ _.ll CONTINUED ON "0 FORM NUMBER 

CERTIFIED BY Ci 

ADDITIONAL IOATE INFORMA noN TAL'[;; 4 -!i ·/II 

··-----
... VISIBLE EMISSION OBSERVATION FOAM 

COMPANY NAME No. K.Z. Pc. ,_ . OBSCRVATION DATE I STAAT TIME 'I END TIME /JL/77 & 23 r ,· de 

STREc: I AOOAESS • 

t-1'1-f/ ll,~'h/Hn 

I~ 0 15 30 46 COMMENTS N 

< ~:z_ ~h.r 514fi F"e-l.iJ e !2-P I () CJ 0 () 

lo Cll"Y I STATE I ZIP7 7f74-

2 (!) 0 a ' 

~~ (-t( 

PHONE (KEY CONTACT) I SOURC.E 10 NUMBER 

3 0 (j cJio 

t4o9) q ~ .s - 4/..:;JJ T? qrltJ 4 0 0 0 n 

PROCESS EQUIPMENT I OPEAATJNG MODe 5 _(]_ a Q lo LLfN {"'Xj~~s+ ' I -.ru ?( · 8 () (J 0 In CONTROl EQUIPMENT . I OPERATING MOOE 

:: i/D(()6w su-." £ba-r Fvtl 7 0 0 () Q 

DESCRIBE EMISSION POINT 8 0 () 0 IIJ "R, ~ ts I~'- S-1-ll cl - 9 (!) a Olt1 

10 ((} CJ tJIO HEIGHT ASOVE GROUNO LEVEl. j HEIGHT AELA nve TO OBSERVER 

1---------

-,o I · Stan ":7 (,;) ' End 

11 _{)__ _{) 101~ _Q () rO ICJ DISTANCE FROM OBSERVER I CIRECTION FROM 08SERVER 12 

Sran /I) I)' End Sran N k/ End -

o1o 010 13 

DESCRIBE EMISSIONS 

D 0 CJIO 14 Sran 

- Ena 

EMISSION COLOR -~IF WA TEA OROPI.fT PLUME 15 () 0 0 10 Sran - E:ld Ar.ac:led 1.1 Oetacned CJ 0 0 OIO POINT IN THE PLUME AT WHICH OPACITY WAS OETERMINEO 16 

Sa.an/4J..aLk Dd ~ • .1-.£ End 

- 17 () () g 118' 

DESCRIBE PLUME BACKGROUND 18 0 (J _0 10 Sran S/Z{ Enc tJ 0 0 IO 1----rs: :Y CONDITIONS BACKGrlOUNO COLOR 19 

Sran E:ld ~ian fWly_C/ b~ 20 

WINO 0 '(J 010 S?EE!J I WINO DIRECTION Din OlD Sratt r E:-~d <;ran S~ End 21 

-'MBIENT TEMP I WET BULB TEMP I RH, ptrconl 22 () Sratt End tJ OIQ 

n () () lr> 23 

Sracx SOURCE LAYOUT SKETCH Craw Norm Arrow 

""''" n 0 0 10 a= 

0 24 Plume 

IV Ia Sun + 25 (j 0 w.na -- 0 0 0 10 21!1 ,_ 

X Em•ss•on Po1nt 27 0 0 0 CJ . 

28 0 Ia {) 10 

29 0 0 fl_ IO 

:JO n 0 0 VJ 

Ooserver·s Pos•••on M~YnntL 

~VER'S SIGNA0- . IOA2-/r-7,. 140"/ ~~~-

------------ ~ ~Nt Sun Locaa•on t.•ne -~- CERTIFIED BY 

ADDITIONAL INFORMA TlON I DATE ytt-c_J:s__ -4--!7-ti I 

F . ------

L-------------------65_..11 CONTINUED ON veo FORu NuuaeR 
£i. 

APPENDIX E 

\ 
rJ. 

,. 

Western Atlas 

International A Lmon!Ora!aer Company 

L A B 0 R A T 0 R Y T E S T S 

JOB NUMBER: 911502 

CLIENT I.D ••••••••• : DATE SAMPLED ••••••• : 02/25/91 

TIME SAMPLED ••••••• : 00:00 

CUSTOMER: Acme Brick 

UORK DESCRIPTION ••• : LPG 1-25-91 thru 2-25·91 

TEST DESCRIPTION FINAL RESULT 

Analysis of Natural Gas 

Carbon Dioxide 1.94 

Nitrogen 0.56 

Methane 92.52 

Ethane 3.67 

Propane 0.74 

lsobutane 0.13 

N-Butane 0.13 

Isopentane 0.07 

N-Pentane 0.05 

Hexanes Plus 0.18 

Total 100.00 

Ethane Plus 1.386 

Propane Plus 0.409 

Butane plus 0.207 

Specific Gravity 0.6110 

Gross Heating Value, Dry 1040 

Gross Heating Value, Wet 1022 

Pressure Base 14.65 

APPROVED BY: 

03/25/91 

LIMITS/*DILUTION 

*1 

0.01 

0.01 

0.01 

0.01 

0.01 

0.01 

0.01 

0.01 

0.01 

0.01 

0.01 

0.001 

0.0()1 

0.001 

0 

0 

0 

0 

PAGE: 1 

CORE LABORATORIES 

R E S U L T S 

ATTN: Ken Thompson 

LABORATORY J.D ••• : 911502-0001 

DATE RECEIVED •••• : 03/21/91 

TIME RECEIVED •••• : 13:24 

REMARKS •••••••••• : 

UNITS OF MEASURE TEST METHOD 

Mol % 

Mol % 

Mol % 

Mol % 

Mol % 

Mol % 

Mol % 

Mol % 

Mol % 

Mol % 

Mol % 

GPM 

GP:4 

GPM 

(Air = 1.000) 

BTU 

BTU 

psi a 

GC 

ASTM D-1945 

ASTM D-1945 

ASTM 0·1945 

ASTM D-1945 

ASTM D-1945 

ASTM D-1945 

ASTM D-1945 

ASTM D-1945 

ASTM D-1945 

ASTM D-1945 

ASTM D-3588 

ASTM D-3588 

ASTM D-3588 

P. 0. Box 34282 

Houston, TX 77234-4282 

(713) 943-9776 

DATE 

11/13/90 

TECHN 

~aoe 

Tr,e ana•yses. op•n•ons or •nterpretat•ons conta•neo ,, !n•s report are baseel upon ooservat•OJlS,jlnC -a:'.:'··a· s ... pc11e0 by the client tor wnose e:r.:: ~~ .e ana confrdent•at use tt'HS reporr has been The tnterpretar•ons or op•n•ons exoressea rec•esent !l"le oesr JUdgement ol Core Lat:Ct)or es :are ·_at)oratorres assumes no respons•O· ~. 3ra makes no warranty or representations express or •rnphea. as ro the oroouctlv•ty. proper operar•ons. or prolllacteness nowever of any 011 gas :ca• or c!r-er m1nera1. property. well or sa,.,c .. ::mnecuon w•th wn•ctl such report ·~ed.r-­ re1•eC o.;pon tor any reason wnatsoever / J 
""-;. ,. J ": ~ •• .... 

. ' 

:-· .. ( 

I) " I ,_C''\ ;/ 8C_IVJE ·aR I CK CDMPA.t::!.Y.. SEALY, TEXAS f ~ ....... ~ r.:,; 

T I ME : 12 I 50 I 54 IJATE1 &/18/91 

KET KEP UCP GO 61 62 63 64 GS 66 67 68 RC 

!:>ETPOINTa 170 (I" .1799 1730 1825 1920 197(1 2(1(1(1 20(15 2013 2013 1920 1460 

ACTUAL a 158 83" .1756 1723 1826 1919 1970 2001 2005 2010 2009 1921 1498 

DAMPER POSITIONSa KED DCD CAB HAS ECD MUB 

83" 70" 20" 99" 30" (I" 

) 

PUSH SCHEDULEa 301 0 FLASHa OFF FLASH NUMBERa 0 AUTO UPDATEa OFF 

CONTROL MODEl KED• AUTO KEDF• MAN. ECDa MAN. MUS• AUTO 

COMMENTS I •••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••

. . "' ....................................................................................................

-...) 

RECORDER • 1 READINGS *******************************************************************************************************

COMM ERROR WITH PEX 

CHANNEL NO. 1 1(16 [;HANNEL NO. 2 1(14 CHAI"N

CHANNEL NO. 4 (I CHANNEL NO. s 108 CHAN

CHANNEL NO. 7 12(1 CHANNEL NO. 8 133 CHANN

CHANNEL NO. 10 814 CHANNEL NO. 11 948 CHAN

CHANNEL NO. 13 1111 CHANNEL NO. 14 1200 LHANN

CHANNEL NO. 16 1433 CHANNEL Ntl. 17 6~1 CHAN

CHANNEL NO. 19 1470 CHANNEL NO. 20 1389 CHANI

CHANNEL NO. 22 1141 CHANNEL NO. 23 165 CHAN

CHANNEL NO. 25 228 LHANNEL NO. 26 153 CHANN

CHANNEL NO. 28 ~16 CHANNEL NO. 29 1'~6 CHAN

--=:> 

~ 
0'1 

co ~ ~ 

RECORDER • 2 READINGS ***************************************************************************************************

COMM ERROR WITH PEX CHANNEL NO. 1 154 CHANNt:L NO. 4 211 CHANNEL NO. 7 72 CHANNEL NO. 10 102 CHANNEL NO. 13 530 CHANNEL NO. 16 1987 CHANNEL NO. 19 2018 CHANNEL NO. 22 ~009 CHANNEL NO. 25 2035 CHANNEL NO. 28 2008 13a11a01DISTURBANCE MAKE-UP BURNER PILOT LIGHT OUT PREHEAT FLAI'IE OUT 13a11a55DISTURBANCE MAKE-UP BURNER PILOT LIGHT OUT MAKE-UP BURNER OVER-TEMP. CHANNEL NO. 2 191 CHANNEL NO. 5 240 CHANNEL NO. 8 24 CHANNEL NO. 11 1601 CHANNEL NO. 14 798 CHANNEL NO. 17 2008 CHANNEL NO. 20 1992 CHANNEL NO. 23 ~043 CHANNEL NO. 26 2030 CHANNEL NO. 29 1'350 
ti 

APPENDIX F 
,. 

~ETER BOX CALIBRATION SUMMARY 

METER BOX # 6 

6-11-91 

BAROMETRIC PRESSURE = 29.7 

DELTA H = .5 VW = 5 TW = 80.~ 

VD = 5.215 TD = 82.5 TIME = 11.083 TEST METER Y = .998 

METER BOX Y = .9592084 

METER BOX H = 1.412014 

DELTA H = 1 VW = 5 TW = 80.75 

VD = 5.262 TD = 87.25 TIME= 8.616999 TEST METER Y = 1.003 

METER BOX Y = .9621338 

METER BOX H = 1.693878 

DELTA H = 1.5 VW = 10 TW = 81 

VD = 10.648 TD = 92.5 TIME = 14.25 TEST METER Y = 1.003 

METER BOX Y = .958425 

METER BOX H = 1.72221 

DELTA H = 2 vw = 10 TW = 81.5 

VD = 10.475 TD = 97.25 TIME = 

METER BOX Y = .9795356 

METER BOX H = 1.736327 

DELTA H = 3 vw = 10 TW = 82.25 

VD = 10.484 TD = 99.25 TIME = 

METER BOX Y = .9735558 

METER BOX H = 1.757373 

DELTA H = 4 vw = 10 TW = 82.5 

VD = 10.441 TD = 100.5 TIME = 

METER BOX Y = .9759184 

METER BOX H = 1.782478 

AVERAGE Y = .9681294 

AVERAGE H = 1.684047 

12.433 TEST METER Y = 1.002 

10.217 TEST METER Y = .997 

8.917 TEST METER Y = .996 

69 
f.l. 

~et:: Ecx Calit:aticn 

Dry Gas Met:: D: ~ C.a.!.it:a t:c t:y: l}g Cat:: & --11- tt I . · 

5ar::net:ic F:assur:: ';2 ql 7 

Orifice Test Orf Gas i :!r.C '=:at~=~ ~'-i ~-tets: Met:: 

Volwrr.e Volune est 

v vd .et::. 

w T 

w 

(), {".0 

/,{ 

1./,(J \0, 

y = vw Fca: (id + A60) 

V (?b~- • ~ ) {T + AeJ) d =~ 13.6 w 

- c .a:n 7 Ill-' [ (T, . ., .. ~co) e J .. '2. 

- F < r .. ~eQ ) v tar ~ ~ 

,... 

r't:~- c.o. = Earome::ic Pr;ssw:e 

70 

Time 

s 
•-

D I( y G A.S /'tl E 7 E R -.jJ; : _ __;:b=::;..__ __ 

DA-TE.· ~-II -V- ./?j~, :/9.7 

!J.H vw Tw VD TDT TDo 470 -6-

- • s-(s~+3) : ~). ~.oo o q/ ~~D t;(~/1.~7~ go 7'1 

<I~~/\ i 

. 

' 

") ;q. 0 tJ (j 5{")', l.JUJ ({q ~ 

(', ()00 so ~ t; ?15 <?.C) I/, n<X ~ l 

: 

/. 0 (.51+3J. i ~ Jf!. "0() ~I I C,!J t:;"l (; I~~ ~t../ ~_3 

i 

::J~~.DDd c;,J /so {1..1(': ~7{ q7 <:s-

' <.D I 7S ~7 ?') <t. t~l I ' t:;'". IJDO ~ )(jd, 

' 

I 

/.5 (1o/-1' ; J.~q .Mo ') .;;l l~o ')7{, I 7~~ Cto ~7 

; ~:J4.tDl!J ~;)._ I ~o C)~LJ l<-"7 ) {)$ 9o 

I IJ DM Cj/ JO f4£J~ Jq;; C)' 14 .,~ 

2.o {!o.Pr) ' -:;¥q .ooo 4,)./ ~u '7 7> 7. '). ~c q7 ql 

:J<'f .Mo <15 /cp; ~1~.'7~) /07 qtj 

' c;,;,c; f().L/7') q7, ')c;- fQ,Qc)O I :J.LJJ? 

.3.0 (t61+ 3

) ' ':2 ~q4bO.tl ~~ /gt ~q 7 .1'-1'-/ 94 95. 

' Jl.ft) ,/)[){) ~ "<:" I t:J.--;;_ t)~7 ,"JL,o J;u qs:_ 

' IO.aco C6:?, ~~ !{J. '-/QL{ qq ).~ ;CJ.'d/7 

1/-.o (lo/1 3

) . ~~q .ODD ~~~9,~ GD9 1~5 Jon q& 

:J c:::-q .DIJO Li ~ /7,? .;q11'-l'-1 !I() q& 

lO.at?ll <- -; t; (7.' ' I() . L.jl-1 \ 10()_,<; q q)/ 

7 PI 
a. 

MMMMETER BOX CALIBRATION SUMMARY 

METER B'OX # 1 

6/10/91 

BAROMETRIC PRESSURE = 29.7 

DELTA H = .5 VW = 5 

VD = 4.995 TD = 87.3 

METER BOXY= 1.00474 

METER BOX H = 1.606965 

TW = 

TIME 

83.5 

DELTA H = 1 VW = 5 

VD = 5.052 TD = 93.8 

METER BOX Y = 1.008063 

METER BOX H = 1.718886 

= 11.81 

TW = 84 

TIME = 8.68 

DELTA H = 1.5 VW = 10 TW = 84.5 

2 

TEST METER Y = .998 

TEST METER Y = 1.003 

VD = 10.196 TD = 100.8 TIME = 14.55 TEST METER Y = 1.003 

METER BOXY = 1.009419 

METER BOX H = 1.791876 

DELTA TW = 84.8 

VD = 

METER 

METER 

H = 2 

10.28 

BOX Y = 

BOX H = 

vw = 10 

TD = 106.8 

1.009072 

1.769043 

TIME = 12.58 

DELTA H = 3 

VD = 10.241 

METER BOX Y = 

METER BOX H = 

VW = 10 TW = 85 

TD = 110 TIME = 

1.010689 

10.36 

DELTA H = 4 

VD = 10.2 TD 

METER BOX Y = 

METER BOX H = 

1.79086 

vw = 10 

= 113.3 

1.015612 

1.784978 

· AVERAGE Y = 1. 009599 

AVERAGE H = 1.743768 

TW = 

TIME 

85.8 

= 8.97 

72 

TEST METER Y = 1.002 

TEST METER Y = .997 

TEST METER Y = .996 
ti 

~et:: e~x C~lib:~ticn 

Ori fica Test Dr/ Gas Te~c!:-:t•...!r: Time ~'-! ~eta: Met::- ~ ... y Volume Volune Test Orv Gas Met::: ~HZ 

v vd ~ete:. w T 

w 

rn1el ~utl•r ~ve Tdi I co I d 

~.s I s.~or;) I '-V'i~.S I ~J . .s ~~~!./ ~'i _,/'i-~ ~r.:>l II.~ I I . :Jav 

'·C) I (.o.;) a 

I I lq\ //ll~ ./1 I S' ~ 0 S" l. ~'-\. u _./'i 1\ .-/~a, 'i3. cg, g, t. B 1/.dt;'? I I 

r.s I \l).v.:JO 1/C,I~lo I g ~, S ro' _,/\i /1&~ ~ /l ..-qt. \oo.~ \1.\ ~SS ll.cJr)~ I 

2. i) l[£),ooo I I 1/C~ /'j'~S ~/1 I 1o.1~c H'i .. & /rz.s- _,.-fo• 1016._\ I2.S9 I ' /V :: I 

z,.o l,o,ooo Lc.2'11 l~s- .D l'o't/fiM . I I _/,-z'!l .--ID"i 11o.o lb. 3~ I (It, 7 I 

Lf" i) lp,'O~O (0, 2D~ . rns- / r·,~-/1 I ~S". 't ./!'3~ .~~-,~ b \13.3 ~.'it I (} ~ /, 

y = vw Fear (Td + 460) 

V (Pb + ~H ) (T + AcG) d a: 13.6 w 

c .0317 &~ [ <r,,., • ~cJ) e ] '2. = F ( i • ~eQ j _.;.;.....__" __ _ 

ta: ~ ~ 

A :0."'!'1 ... -

F~-- = Ea:~me::ic F:assure ~..~ 

73 
tl. 

DR..y GA.s /J7ETE.R. ~ .. ---=---

Dif-TE .· b-to-C}t · 

J'Li11H vw Tw VD TDT TDo 470 -e-

. ~{s~+') • 17~,0QO ~'i/~ 31'1. 2q5 ~3 '6_3 

: _l.~"'\·000 ~'1 jr :( J'1~, :SDO 

6 '6._) _l Cf9 6~ 

5.oDo '?J.S 1~'1 5" '1).3 1\ :'3' I 

' ' 

/. 0 (~+3J. : 11'1 ,. 0" ' , J ..... (~) /u YeY,~;.,-;... 9\ ~y 

I 

I '1'-\ • o ~ ~ ~s" /€ !.\ :q~.2'f~ \ I ' '6~ : 

: 5:. t>-G 0 ~y' i) $;,cSl. •lJ, X' ~. (.~ 

/.5 (1o/i' ' 

~cs /cew. : 

'f)'f, CW·o Y_li.\. stJ ID\ ~~ ' 

f1-9, 0 u 0 ~·~ J~\J Yo~ • .3'17" l\ ~ -~~ 

IO. c 01~ ~ u ~ 

6 '.~ \b.\C,L, ,r,3 ~~ .~s' ' 

2. o r ,o.,.rJ :1~9. oc. ~ 8S/~~ '12~,& 2.3 \ D ta '15 

I <t/~. o~ ~ 6S/~~ 11'~ .. s~; \ 2.5' to 1 

I(}. 00 D \'"I·~ U•· '-So lOb. 6 12. s ~ 

3.0 (!t;/+ 3

) ~·\9 - ,___,_ .) , '-' ..... 85 hlf ~3S. bb~i ·\0~ l~ 

\9~ ,o~·~ ~·~I~~ ~1t1-~i23 ~~ '< L~Y 

lo.o=>D ~s:.o ID, 1'11 l\o .. o /0.3G 

J/.. 0 ( ID .f.; 3

) ~1'1.~·::>,:) 8~ As LJqs, z ~'-i 1\_£ i 0 .l 

Joct. M -s ~· \.. ·I) I~.' :0 1"",... ,...., 'I 

.. b -~· ';I '-f !3D \0 (., 

'~j "' ·) ·) ~ ~' ~ It:>,· L Ch) 113.3 {. '1+ 

I 

I 

~ 
1.· 

METER BOX CALIBRATION SUMMARY 

METER BOX # 3 

6 13 91 

BAROMETRIC PRESSURE = 29.7 

DELTA H = .5 

VD = 5.44 TD 

METER BOX Y = 

METER BOX H = 

vw = 5 

= 98.5 

.9349788 

1.596815 

TW = 87.25 

TIME = 11.811 

DELTA H = 1 VW = 5 TW = 87.25 

TEST METER Y = .998 

VD = 5.375 TD = 103.5 TIME= 8.791001 TEST METER Y = 1.003 

METER BOX Y = .9583557 

METER BOX H = 1.753546 

DELTA H = 1.5 VW = 10 TW = 87.75 

VD = 10.65 TD = 107.75 TIME = 14.455 TEST METER Y = 1.003 

METER BOX Y = .9725598 

METER BOX H = 1.767819 

DELTA H = 2 VW = 10 TW = 88.5 

VD = 10.57 TD = 113.5 TIME = 12.18 TEST METER Y = 1.002 

METER BOX Y = .9862896 

METER BOX H = 1.661297 

DELTA H = 3 VW = 10 TW = 89.25 

VD = 10.501 

METER BOX Y = 

METER BOX H = 

TD = 113.5 TIME = 10.01 

.9840431 

DELTA H = 4 

VD = 10.445 

METER BOX Y = 

METER BOX H = 

1.687715 

VW = 10 TW = 89.5 

TD = 111.25 TIME = 

.9815892 

1.695547 

AVERAGE Y = .969636 

AVERAGE H = 1.69379 

8.668 

75 

TEST METER Y = .997 

TEST METER Y = .996 
£1. 

~ete: E:x C3lit:aticn 

Orifics iest Or/ Gas i::r.c~:-=t~r= i ime 

ilL.: . . ~4eta: Met:: 1:. 

.... 

Volume y Voll:me IT -c:. Drv Gas Met:!' 6rs 1:'- '-

v vd t.!e"·~~ Inlel Outle~ Ave . , .. --. 'N 

i 

idi Tdc r id w . 

,S ~~~~ ls.lf~ 1-rt-.=t:>l'%:.1~ 11i.s l11. '611 I ,q~~ I 

(,0 Is ~Oo" 15. 3=tsli7.;SI'%.1~1-Ito3,sl ~. ~~ ll.o.J3 I i" .s- Ito ,.a;,o Ito· bS !17.1-~ '% ~k~Y,~ ~I~ 1.15 JLf. Lf'55 I i. Oo3l 

."2,..~ I \O,o.;;o I fu.5'1 I 9,'/.S 1''~/ ;;;-,;...; 1·· :~.)fu ·,I U3.5-I J~.l~ I J • .jO J_ I 

;3,0 ,.. . I _... 1:~:,/ I to .o~~ I (o, :;,of I <El:f· ~ b /I I f 1

/r:,'1 · /?.;-2.1r~.s- t.:> .of I ,q'l-:r I 

lf,o ! t o.a~al,o.':'tf;lg,,£1. %~1'~"2-.~f'/·2>1 i.!.bz\ ~ q~t., 

y = v.~ F t:a: (I d + 460) 

Vd (Pb • ~H ) (i + AcJ) ar 13 _

6 v1 

- C .0317 ll.L.I [ ( iw + AeO) 

- F ( i + ~cG) v t:a: c ~·l 

76 
DR..y GA.s !I!E.TER.JJ:: __ 3__ _ DftTt: .· Co -13 _q ~ 

Fb~ ~9 / l4H vw Tw VD TOT TDo A. TO -6-

. s-{s;-;3) -~3?.oo~ ~~ ~1- 5" ~'Z. J 2.0 q-:p- ~0 

y~~- t"' ' , :)O 'l'i /96 58_~ .. hSC) I' 2- '15 I 

5 .Dut. g--=t-.~5 5.yy ..,.;::p '1~.S" 1/.rt// 

I 

/. 0 (j1+3J- i 

Lf '-/)...DO ~~ /<66 5q;,q 4f5 io-3 qj-

:Lf...,-, 

. ~ r.c"C< <t<ZI gf ~.g~.l '2.0 II Lf 9~ 

' ·5, occ 11--~5 ,... ...., _., ('8 

:~. ~ ~...J ~ to1 J 5 '~~-:hJ 

J.5 (lo/T' ; 

I 

'-t5;:J...D00 ~"'I z=r b () '-/, 1'15 I o-::;- t{5 

Yl/2. o j)Q 9~ /<6Z 5 &:f).~'f$ f -:2- y /oC: 

/6) 0 ~~ _ _.., .....,_ 'o, b s --7 I o-:t. =i-S 1'/. £jS5 r_ ...... i •. ---

2. a ( 1o1r) · 

LJ6 2, rJO~ gg ( ~g {;,jt.j, i-15 lib /61 

f{S'..z.o~ z,b t PJ o foOLf, JYS ;2t J)} -

Jo ,O<'v 'J3, 5 I 0. 5-:t ~· { 13.5 /:J,/'3 

:;.o (t~+ 3

) · 

'-11. 7 c-o" ' . ~" ~~ ( ~6 b';;.f. ~16 I /6 I o-z, 

'Jf-4o~ ;q / -;o b I t/ I i-1 5 /.Z ltj lo=;-

. I o. (Nt:>o Sit). 2 S" (0. so, ~ fl 3. 5 ;o. o; 

3) . J/...o (IDII · 

Lf,-,_/1 ,jo..~u (.-. ~'1 I 9o 6 35-, b~l II=!- /0?-

y- ..., "--' ... -r ""'. t.:r/14 G.)- S. 'J I 6 I '2- L/ JoZ. 

lC,c:;.C 1~.c;- /O.Lf~S ---7 (!I· ~5 g.t6S 

II rz 
I. 

METER BOX CALIBRATION SUMMARY 

METER BOX # 4 

6-11-91 

BAROMETRIC PRESSURE= 29.7 

DELTA H = .5 VW = 5 

VD = 5.049 TO = 88.5 

METER BOX Y = .9957156 

METER BOX H = 1.588929 

TW = 

TIME 

83.75 

= 11.751 

DELTA H = 1 VW = 5 TW = 84 

TEST METER Y = .998 

VD = 5.051 TD = 95.5 TIME = 8.467 TEST METER Y = 1.003 

METER BOXY = 1.011358 

METER BOX H = 1.630556 

DELTA H = 1.5 VW = 10 TW = 84 

VD = 10.17 TD = 101.5 TIME = 13.881 TEST METER Y = 1.003 METER BOX Y = 1.014194 

METER BOX H = 1.625862 

DELTA H = 2 vw = 10 TW = 84 

VD = 10.234 TD = 105.75 TIME = 12.165 . TEST METER Y = 1.002 METER BOX Y = 1.013218 

METER BOX H = 1.652457 

DELTA H = 3 vw = 10 TW = 84 

VD = 10.186 TD = 107.75 TIME = 10.065 TEST METER Y = .997 

METER BOX Y = 1.013996 

METER BOX H = 1.6908 

DELTA H = 4 vw = 10 TW = 84.25 

VD = 10.134 TD = 109.75 TIME = 8.383001 TEST METER Y = .996 

.METER BOX Y = 1.01879 

METER BOX H = 1.559819 

AVERAGE y = 1.011212 

AVERAGE H = 1.624737 

78 
£1.·-

~ets: Ecx C~lit:aticn 

Dr·, Gas Mets: II: L/ 

C= 1 ;;...,.- ~"=,.. t:y. A/) -----Q. ---- . .!.::> Oats: f.,-J1-C1f · 

Ea:onet:!c P::ssw:s: ?~.7 

Orifics Test Dr/ Gas T:!r.C~==t~r: I Time 

~'-: Met.:: Meta: 10: y .... 

Volurr.e Volune iT est D!'V Gas Met:: ~1-i'a 

v vd Met.::. 

w T Inlei Cutle~ Ave 

Tdi Teo r Td w . 

() ,<, - I ~ I< r-,uq I 1~1 43

I" 

~ ~. 7f !C"}. ~- -~~ _/ ~{~ .. s--1 ! ,,...., <"! I o qC(~ 

I.{) I ~ I ~.o<;;l I 4;4 I%G ~~~D; 11z;.~l ~ .'-1& 71/,0U~ I 

!.{ I I I) l,o 11ol ~4 ''·~~-~ I q

3 

qq ~ 1{), ~- ,.~ . ~s 1 I I , o o 3._ I 

'7!) rr, I II) l,b :~ <,L/ I ~d I ~ I q4 /I J I 1

_.-i,Cf ro':) la~.7 t~.l(a<)'" l.oo") I ~.D I 1/) lm , ~L.I ~4 l'o1 l'ou- I d I ~~o '"~ loi.i l (~, (;(.,~ 0. Or:, 7 I 

/...}. () I I!J I I . . rl' oa. I 10 

10 !"2..4 ~lf.)'>.·· ~ d ~ I 1"'1~ · rfl' ICq,/ ~.S~(, 0.0q0, 

y = Vw Ft:a: (T d + 460) 

Vd (Pb __ • ~ } (T + 460) c:.;. 13.6 .,, 

_ a .0317 ~ [ <r .. ., • l.:cO) 

- F ( i . + AeQ ) v Ca: c ':J 

Ft:-- = Ear:~c::ic F:sssu:e c. 

79 
DR..y GA.s /}JE.TE.R. ~ : __ 7 __ _ DA-TE .· b- I/- 0 /. (';;~./I ;. q 7 

11H vw Tw VD TOT TDo 4TO -6-

. s-{s~-;3) ~ )L/. I'Ll. y;j !<;-? I~ I. l61 ~~ ~) 

i . /.' ;~ . ~!t(.ooo I !: -:) ""·7 ~;..; ~--~ I).(,. I )O 'I 

.:::.!){"~ ,• ~ -.-... 

-..· -., -. t:: I) L/C, ~Q ~ I I. 75" I 

I 

/. () (~+3J. i -:. ~!) ·; "" .r- -.. ·., :. /.(_/ /:·t.j /' . 'IS (2, I,. c:_ ~lJ ?< ~~ .., .. : ..... J .. ; !• !J (.; (j,'lj.~.,, ..... ~-~· ..... ! IS/.7(/1 1 oct q:; 

(', r., ·:~.r- ,. '/ 

~l--SI Ct~. c; q. '-i(j 7 _,_ ''-1 

! 

/.5 (lo/-1' I 

;)~4.Qco ~u l~:.f I L/ /~ .Q Cl,f\ 9q cts 

·2,::i..Ct.cr:c c;c.!/ ~C/ I Z,.:, <:· )0 /I~ tiCt 

/() .oco t;'i IIi I 7() 10 I. C) J s <:: <;: I 

' 

2. o {!o.Pr) s t..fQ. {)C() /Lf 

~- J;L.! !)7, :t_:)L/ I 0 4 q~ 

~~Q,Doo (L/ I~:; fL.ILoCiC\0 1/q /()d. 

I{) rro 

'1..._, ~-·· ~·!l 10 I :J <t.J f(l '5":7 ~ 1). ! &') 

.3. 0 (It;/+ 3

) ·-, ·-q , .... •';-.. ...., ") ' ...;:._,,_ C,-'¥ /~y I~ I .L-ll o 10/ //![J 

'2, :..J Cl 1"1:~,..... . . . -- ·- ~~u I ~u ,(7,)-;~ } ") 0 fOLf 

1 :J ..... nu C64 /(). t~IJ /(Jl. 7t) IO,o&~ 

J/..o (lo/1 3

) 

I 

"2, . . LY. . C:/'1", _. '-' ~4 ~4 J 7 7. ~1-!l/ JOY ) 0::; 

-:2_ ~ 4 :]! '/) 4~1~'-1 tl,/,LJio ;']~ ;05' 

'·' ~- ~· ..... l_ ~ Ll 1 j') 10 1~4 IOf4.7~ cl.~~5 

80 qv 
,. ,~ 

-

-

Compe:ny Name: 

PITOT T~B~ !NS?!::CTICN DATA SiiE~T 

--.:....;~:.....~· {wl't't.~-:-:5:&,f.:.....:..r..::::"~.,.._:;;.,~f::;=;,...--~YL~J~,~ ? ~e- s amp 1 e 

-o / Date f:?- =t_q\ 

Post Samole 

Date 6 //9(1\ <l( 

KUrr •••car•• """" NIUia. 1011 JlfiMI81 .. e 

level? 

obstructions? 

damaged? 

-lao 

-lao 

-5~ 

-5~ 

< Ctt 

< Ctz 

< s1 

< Sz 

y 

e 

A 

< +10° 

< +1ao 

< +5~ 

< +50 

!' (. l z,t"" 

~i:OS'ot .n·r 

< Pa < 1 5 . 0•, lo . 

I l.as Dt < Pb < 1.5 o ... 

lo 

~n ~ I 3/16" ~ Dt '(: 3/S" 

0 

I o 

.5!3 

;/-I 

I 

I H~f •••UfiiiC :.t'tt.l. ~'':a,;. rcc :t!t ... ,., .. 

.. IY~ 2.~S"I A tan y <a.125" ,~, 771-f"l # "- - I 

, D f ~ ( I A tan e < a.03125" ,:)J'i/ 

\. 

~ I Pa = Pb ±. 0.063" 

Comments: 

Pitot tube/probe nrJrrtberrt-,t<Jr/tlts.l meets or excee all specifications 

criteria and/or app1icable"*design features* ~·kre~y_.,a~ss'L!'··-~d a 

pitot tube calibration factor of a.84. r 

Signature ~~~~----~------------~--------------

·~~'! ~J -.:.-"' :~. ·;a .. ~:.~c. ~0~. !-I!!'!!':OC: :. ,ler-if'l ::te :!t;ni~ 

Z ine~ se~:ae~ or :~e :~e~:e::.o:i! !ne ~~e ~inimum Jt: inc~ 

seo:ar1~:cn :!e~·-e!!'l ~!'le ~~ ::: ::.o:e !nC :.'le nc::ie u S/lawn at 

:!'le ::o of :!'lis '4~!. 

81 

0-25 

Date '-6 /7/,/ 

I 
ll. 

,. 

:· 

-

-

_ /j_ PITOT TUBE INSPECTION DAy SHEET 

Compe:ny Name: Arms.k~ &v!r~11¥t?.JP/ftsampl e Post sJ~olei 

I I 

~---· __.rz ••- ! () Date b;'/Sj'<i/- Date t".: !y/7; f-'( 

-=~===.;;;;; .. =~- '"" <) 

~~,.i I ,·· ~.,_ I 

l

r .I I tr~-:-;;; ... '\ j:! 1-.1011 .. ::u , _ _,~ \! . : ' 

lft:JU ••t(.l'fiiiC l.rt'(\. -o1ilftGII 

1"04 nTt•••••.;, T. :')e(• C ..... Ct.R.Afl .. f. tre~rr I .. ICATIIC LIW\. 

IIOIITIGII 108 .xf(MI•I .. e 

(' . == 0<-=·-:--ra -·--·~·--'-'--"'=- " .---==s ,; 

:lt~U t .. tUft.C 1.ML 

~~I Tl~ IGC :C:(MIIU .. 

. 

I 

,/ 

JU;A 

jf)O 

4(} 

JZ~ 

/ 

• I 

-30 

y~ 

/;; 

/-:1 • ' '6 

.311--~ 

~JJ'Z . -' ' 

V.Lt II 

level? 

obstructions? . damaged? 

-lao < Ctt <+lao 

-lao < Ct.z < +lao 

-so < St < +50 

-so < Sz < +50 

y 

e 

A 

LaS Dt < Pa < 1. 5 Dt I 

LaS Dt < pb < 1.5 Dt 

3/16"-<: Dt ~ 3/8" 

'A .Q36 tan y < 0.125" 

~A tan e < 0.03125" 

p a = pb ± 0.063" 

Comments: 

tec.-ct '••tnr-c L.IE'fl\. -an•• '" :C.!U•u•,_. ., .-.. '• 

Pi tot tube/ probe niJ!nl:>er .£ meets 

criteria and/or applicable design features* and i 

pitot tube calibration factor of 0.84. 

·~l!t! ~J ..:~-~ ~~. ·Joa . .;z. ~Ia. 10\;, ~!t;!'tOC Za Ver-ify the rn;ni:!Ur.! 

Z inc~ se~~ac~ of tne :~e~c:•:l! !n~ :ne ~inimum 3/: inc~ 

seo:a1'1:1c:n ile~-.. <!!!'1 ::'le ~i ::: ::o:e !nd :!'le !'IC:::le lS snown at 

:ne :op of ::'lis ja9e. 

82 

v I , A ·.I/ -'·A , I 

JVO I 

1-f I 

h.J I _, 

z· I ..... .. -;.-

_,.' I 

-'"' a I / -

z.. e. I . 6'66 I I ? c s- _; I I .. 3 'I! I -~ ,, . L/ I 

r: _.,IJ ~ · ... -' '-·-f' I 

,rs:<4 I ,_. j .· I 
POST METER BOX CALIBRATION SUMMARY 

6 /I ~n' 

METER BOX # 4 

BAROMETRIC PRESSURE = 29.7 

DELTA H 1 vw 

VD = 10.181 

METER BOX Y = 

METER BOX H = 

DELTA H 1 vw 

VD = 10.315 

METER BOX Y = 

HETER BOX H = 

DELTA H 1 VW 

VD = 10.375 

METER BOX Y = 

METER BOX H = 

= 10 TW = 

TD = 102.25 

1.004624 

1.68899 

= 10 TW = 

TD = 110.5 

1.006122 

1. 641353 

= 10 TW = 

TD = 114.5 

1.007317 

1.624187 

AVERAGE Y = 1.006021 

AVERAGE H = 1.65151 

90 

TIME 

90 

TIME = 

90 

TIME = 

= 17.15 TEST METER Y = 1.003 

17.03 TEST METER Y = 1.003 

17 TEST METER Y = 1.003 

83 
I. 

Post-Test 

Meter Box Calibration 

0 ry Gas Meter II: .a. 

! 

C a 1 i brat e d by :/'f>:;-

Oate:~-i~· q1 

Barometric Pressure:.;_~·1,~ 

Orifice 

6H 

/.() 

1.0 

/.0 

) 

6H® 

Test Dry Gas TPmn~T'::~i""T'"' 

Meter Meter 

Vol ume!Vo 1 urn e. Test Drv Gas Meter 

-leter Vw . vd ~n1et Jut1et Ave Tw ~ di T'" do T d 

1a l10. I Rl 9o ~'i 

~ ·;ro; v I· ·;.: ·' :~ .· IJ -- /0 1/0.31~ 'to ~~ 1.2{, ~/0.5 

/!J //).:3~!' tto ~ ..... "''1 '% /1. /:J I.~-~-

Vd (Pbar + 6H) (Tw + 460 

_0.0317 6H 13 • 6 t(Tw + 460) 

-pb ( Td + 460) v ar w 

Pbar = Barometric Pressure 

84 

Time 

8 

~}9.1~ 

11.0~ 

/9:tJO 

'( 6H® 

/.1)()3_ 

1.(){)3 

I OCJ.: 
a. /) /(_ y G A: s trl £ IE R. -=#- : _+...;,..,._ __ _ DA-7E: ~-/"f-9/ 

AH Vw -rw VD ID/ /DO Ll T.D -e1. o (torr-~) 5 ~I ~- 'Y'\ .._,. 70/cJo .:zs-t. ~II '1Cf c;; 5l~.OcD CJo/9~ ;?4&,.~3() I ;q Lt10 

IC qo 10. 1a 1 j();.~~ .. /7t/~ -

1. o (to# 3

) .-·'c; . ' ,, ··.- ., .• .;< '- • ' ' C?o/9:J ~t.~. q ..7 /, 1~1 1121 .J qo/t:Jt; /:2(, r..q "'"I "·''·-- ;l ~(,. /,// /t;? -' Cl • .J·-1.._; 

/0 q() ,, '>!S" I ltJ. :;- I 7. Z>.3 

/.o (;~t; 3) 11/0L \)~ Qo/Qn b:77?. ?61 I f I /0~ 

~o~ J...., ., ._. '"" . . ..) _, qn/4n .?~!, tf:l~ f;J.q /11 

IJ Q('J 1D,3~ /Jt/,1' I 7,oo 

I 

85 
r.l 

·~OST METER BOX CALIBRATION SUMMARY 

METER 1BO.X # 6 

6trtf'ft 

BAROMETRIC PRESSURE= 29.7 

DELTA H 1 VW = 10 TW = 87 

VD = 10.58 TD = 92.75 TIME = 16.83 TEST METER Y = 1.003 METER BOX Y = .9556146 

METER BOX H = 1.636503 

DELTA H 1 VW 

VD = 10.637 

METER BOX Y = 

METER BOX H = 

DELTA H 1 VW 

VD = 10.723 

METER BOX Y = 

METER BOX H = 

= 10 TW = 

TD = 99.75 

.9612129 

1.645603 

= 10 TW = 

TD = 104.25 

.9598551 

1.656314 

AVERAGE Y = .9588942 

AVERAGE H = 1.64614 

87.75 

TIME = 

88.5 

TIME = 

16.96 TEST METER Y = 1.003 

17.06 TEST METER Y = 1.003 

86 
t;· 

Post-Test 

Meter Box Calibration 

Dry Gas Meter #:& 

Cal ib rated by :fr"':i 

Date:tJ-19-9! 

Barometric Pressu=e :Z9. 9--

Orifice Test D=y Gas TPmnpr::~t-,,,..=-

6H Meter 1

Meter Test Drv Gas Met_e_r_ valumrolume. ~eter Vw vd ~nlet Putlet Ave Tw ~ di ~do T d 

lt?J 10 l;t, s--r ~+ ~ 4- % 92.~ 

/.() /0 l;a~.?~ ~·~?: r. ""' .% qt# 

~. ·R ., .J 99,~$ 

f.() /0 /(),'g.Z.3 1~·.s- ~ ~ ~ /!)4;! 

) =VwPba= (Td + 460) 

Time 

8 

(6,~3 

V6. if~ 

'71-.o~ 

Vd (F. + 6H) (Tw + 460 

car - 2 

0. 0317 6H 13 •

6 r_( T_w_+~46_0_) __ f?3 6H~ =p (- 4'0) b ld + b v 

ar w 

Pbar = Barometric Pressure 

87 

'( 6H(gl 

1.003 

/,JJO~ 

I. ~():i 

97 
ilH v'W -rw 4 VD -ro-r /DO Ll T.D -e1. o (torr- 3

. ) £2r2.XO '?7/y~ '7~ &-'!1 <69 <l~ 

lJ'!;?.CClO <tX'I g1- 9-..Z.C. 0 (p q /f)A "':L 

I o ,5'i I-" 

. /{) ~7 ~.7) !C..~~ 

~. 

/.0 (Jo# 3

) . .- ct>/rz 7 qj, q!f___ "'"'"::?·7 .·'l.:_Z r;;.s O.U'; -.1~&1'- ,./ _, 

. 

~ "7 -<' ............. , ~·--- ... '._1 ~Cf/fll 14-L~~ I I I 115 

f7,7;; I' 

!0 JP,&3 "+- 91, 7S, ~ 

I~ CjlJ, 

: 

/.o {tt; PI 3

) 'r942 . 'J{_,'.._ ... "·· ~(/ jycj 7Qo69 /0~ 99 

~3:z,cco <(f /ti 1.fl.~8k I I]- /t:Jv 

;a ~~~~ /(),1~3. ltJ4, -;.~- ......... J7,ot:, 

88 
a: 

POST METER BOX CALIBRATION SUMMARY 

METE" BpX # 3 c. /<7/9/ 

BAROMETRIC PRESSURE = 29.7 

DELTA H 1 vw = 10 TW = 

VD = 10.728 TD = 98.5 

METER BOX Y = .9504973 

METER BOX H = 1.892659 

DELTA H 1 vw = 10 TW = 

VD = 10.601 TD = 105.5 

METER BOX Y = .9730522 

METER BOX H = 1.841836 

DELTA H 1 vw = 10 TW = 

VD = 10.601 TD = 98.25 

METER BOX Y = .9583931 

METER BOX H = 1.863877 

AVERAGE Y = .9606476 

AVERAGE H = 1.866124 

88 

TIME = 

88.5 

TIME = 

89.75 

TIME = 

18.16 TEST METER Y = 1.003 

18.01 TEST METER Y = 1.003 

17.96 TEST METER Y = 1.003 

89 
D. 

Post-Test 

Meter Box Calibration 

Dry Gas Meter II: 3 

Calibrated by :ft\1 

Date: {,-/~-7i 

Barometric Fressu:-e: ~~.'1--

Orifice 

6H 

I. 

.() 

) 

6H® 

Test Dry Gas TF' JO>T":::li-111"' ... 

Meter Meter 

VolumeVo lume 

Vw vd 

10 

10 

Vd (Pbar + 6H) (Tw + 460 

_0.0317 6H 13 •

6 [<Tw + 460) 

-pb ( Td + 460) V 

ar w 

Pbar = Barometric Pressure 

90 

Time 

8 '( 6H® 

I~~~~.: 

v3 
1:. /JR. y G .4 s IYt £ 1£ K -::#- : _3 ___ _ 

DA-TE : t -1'1- 9 I 

..1.H Vw -rw VD -ro-r /DO AT.D -e1. o (toft-=) -f!:xJ. ~c\J ~q/<l4;' I?Bd,.;;;;_ 9+ <6~ 

04J.oco q({/r/ ~9~~ 4. ' ~I JJs 9& 

10 ~~ I ttJ.7;z$ c;a, 5- I~ ~I~ 

/. o (to# 3

) ~ .!::Jb;;,:;co ~({/fd qg 7:4c/ I t?1- ~L, 

-..5 ~ ~ 1', .. -y: '....., ._... __, 1<7'7 I r1 70~.19; /l'l /b~ . 

/6 <{({, ~ ~~-~~ _m£_f" /<{ ~~ t 

/.o (;~PI 3) £1c2.ooo 90/'17 /,<?,#q ql 11 

6/o~.ooo t::}?J/jJ 11 t. .~ ~');;' •· ;;s- qr; 

<6Cf,ls-" 16 t,c/ ~,),s- ~ Jt) 17,9~ 

I 

91 /01 
13. 

POST METER BOX CALIBRATION SUMMARY 

METER BOX # 1 

6/l '7/"1 I 

BAROMETRIC PRESSURE = 29.7 

DELTA H 1 VW = 10 TW = 90 

VD = 10.4 TD = 103 TI~E = 

METER BOX Y = .9847805 

17.76 TEST METER Y = 1. 003 

METER BOX H = 1.808863 

DELTA H 1 VW 

VD = 10.635 

METER BOX Y = 

METER BOX H = 

DELTA H 1 VW 

VD = 10.731 

METER BOX Y = 

METER BOX H = 

= 10 TW = 

TD = 115.5 

.9844014 

1.733886 

= 10 TW = 

TD = 118.5 

.9806805 

1.744574 

AVERAGE Y = .9832874 

AVERAGE H = 1.762441 

90 

TIME = 

90 

TIME = 

17.58 TEST METER Y = 1.003 

17.68 TEST METER Y = 1.003 

92 
Et 

Post-Test 

Meter Sox Calibration 

Dry Gas Meter II: I 

Calibrated by:(Yi'T" 

Oa te :~ -!'9- q_~ 

Barometric Pressu:-e ::...~. f':;.- . ' 

Orifice Test Dry Gas 

6H 

TF'mn.,.,..:::I-••T"co 

Meter Meter Test Drv Gas Mete-r valumrolume. 

/,/) 

/,!} 

/,0 

I 

) 

~eter Vw vd Inlet Put let Tw 

iJ" di ~do 

/0 I!D.4 'to I~ '12 ~ /() Ill' /-::. .. ~. ~-= 'iti ~ ~3.:2. ~ () 

10 /:}., 31 qo I~ 3 I~ ... 

Vd (Fbar + 6H) (Tw + 460 

_0.0317 6H 13 ·

6 [(Tw + 460) 

-pb ( Td + 460) V 

ar w 

Pbar = Barometric Pressure 

. 93 

Ave 

Td 

/OJ 

1/S:sllt..sTime 

8 '( 

It:~.% ~,t'o3 

11. s-t I /..&~ 3 

11'7. ~ ~ l.f1&3 

6H® 
tl. 

.. EA-r ~7.; 

AH Vw -rw VD ID/ /DO AT.P -e-

' 

1. o (torr=) tJO,:XD 90/9c 72I~ol 10/ ctO 

~aJ.~C() 't:jt) /7Z? 1 f I. D~ \ I z,z, e:rq 

/J 90 I o ,4- ld_3 17. ~~ 

/. o (Jo-H- 3

) c. 2<".1Cf 9~/~ 'J+2.J51 ~,i~ ltJ~ 

11-/S: CJ~) fl/~o /]6/,lZ( I ~;2._ II 0 

' 10, /,3£' ~ f- jC· f/J 115.5' ,-,.~a , 

/.o (!~Pi 3

) l&r3~tJU: ~O/f't) 15:<.89~ I ;z_l 10 i ~~~oo:l 'iO I ~o ?42.~ -

~.3 I I:L 

/~ tl~ 10.13--l 11~~ 17.torf 

94 
APPENDIX G 
El. 

fArmstrong 

~ Environmental, Inc. 

47471rving Boulevard, *204 .. Dallas, Texas 75247 • (214) 631·0021 • FAX (21 4) 905..Q634 

RESUME OF Richard Taylor 

EDUCATION Southwest Texas State University 

B.S. Environmental Studies 

San Marcos, Texas 

PROFESSIONAL EXPERIENCE : 

February, 1991 - Present 

April, 1988 - February, 1991 

January, 1988 - April, 1988 

September, 1987 - January, 1988 

95 

Project Manag.er Armstrong Environmental, Inc. 

Dallas, Texas 

Project Manager 

Turner Engineering, Inc. 

Dallas, Texas 

Assistant Manager 

Better Buys Sport Shoes 

Weatherford, Texas 

Substitute Teacher 

Cedar Hill I.S.D. 

Cedar Hill, Texas 
a. 

if Armstrong ~ Environmental, Inc. 

47471rving Boulevard, #204 • Dallas, Texas 75247 • (214) 631-0021 • FAX (214) 905-0634 

RESUME OF: Larry Whicher 

EDUCATION: 

B.S. Geology Western New Mexico University, Silver City, NM 

PROFESSIONAL EXPERIENCE: 

January, 1991 - Present 

April, 1988 - January, 1991 

February, 1987 - April 1988 

Project Manager 

Armstrong Environmental, Inc. 

Dallas, Texas 

Project Manager 

Turner Engineering, Inc. 

Da1las, Texas 

Electronic Distribution 

Lex Electronics 

Dallas, Texas 

February 1986 - November 1986 Office Manager 

Amerex Rent-A-Car 

Dallas, Texas 

96 
fArmstrong 

~ Environmental, Inc. 

47471rving Boulevard, #204 • Dallas, Texas 75247 • (214) 631-0021 • FAX {214) 905-0634 

RESUME OF Jerry Salinas 

EDUCATION Sunset High School, June 1988 

PROFESSIONAL EXPERIENCE : 

February, 1991 - Present 

August, 1988 - February, 1991 

March, 1984 - August, 1988 

97 

Technician 

Armstrong Environmental, Inc. 

Dallas, Texas 

Technician 

Turner Engineering, Inc. 

Dallas, Texas 

Service Assistant 

Stevens Park Golf Course 

Dallas, Texas 
1: 

if Armstrong ~ Environmental, Inc. 

47471rving Boulevard, #204 • Dallas, Texas 75247 • (214) 631·0021 • 

RESUME OF: Matthew A. Taylor 

EDUCATION: Cedar Hill High School 

PROFFESSIONAL EXPRIENCE: 

February, 1991 - Present 

August, 1990 - February, 1991 

November, 1988 - July, 1990 

Technician 

Armstrong Environmental, Inc. 

Dallas, Texas 

Technician 

Turner Engineering, Inc. 

Dallas, Texas 

Lab Technician 

Dixico, Inc. 

Dallas, Texas 

98 

FAX (214) 905.0634 
[' 

f=Arms.trong 

~ Envtronmental, Inc. 

47471rving Boulevard, 1204 • Dallas. Texas 75247 • (214) 631-0021 • FAX (214) 905-0634 

RESUME OF: Thomas Armstrong 

EDUCATION: 

College of Dupage, Glen Ellyn, Illinois 

PROFESSIONAL EXPERIENCE: 

February, 1991 - Present 

April, 1984 - February, 1991 

1976 - 1984 

1975 - 1976 

President 

Armstrong Environmental, Inc. 

Dallas, Texas 

Vice-President 

Turner Engineering, Inc. 

Dallas, TX 

Project Manager 

The Almega Corporation 

Bensenville, Illinois 

Environmental Specialist 

Particle Data Labs, Ltd. 

Elmhurst, Illinois 

Mr. Armstrong has 15 years experience in performing field and 

laboratory analysis of air pollutants. Mr. Armstrong has 

tested for air pollutants in a variety of industries, 

including chemical, steel food, power generation, 

pharmaceutical, ceramics, petrochemical, and cement. Mr. 

Armstrong has performed ambient and stack tests for 

particulate, SOx, NOx, hydrocarbons, TRS and others using 

virtually all current test methods and procedures. 

99 ;(D