REPORT - DTICouuUSAFOEHL REPORT 89-010EQ0178BEF COMPLIANCE TESTING OF HOT WATER AND STEAM BOILERS,...

ouuUSAFOEHL REPORT

89-010EQ0178BEF

COMPLIANCE TESTING OF HOT WATERAND STEAM BOILERS, SHAW AFB SC

JAMES A. GARRISON, Major, USAF, BSC

"DTICFebruary 1989 ELECTE

JUN0 11989 UFinal Report

Distribution is unlimited; approved for public release

USAF Occupational and Environmental Health LaboratoryHuman Systems Division (AFSC)

Brooks Air Force Base, Texas 78235-5501

89 6 01 053

NOTICES

When Government drawings, specifications, or other data are used for any purpose other than adefinitely related Government procurement operation, the Government incurs no responsibility orany obligation whatsoever. Tile fact that the Government may have fomiulated, or in any waysupplied the drawing. specifications, or other data, is not to be regarded by implication, orotherwise, as in any manner licensing the holder or any other person or corporation: or conveyingany rights or permission to manufacture, use, or sell any patented invention that may in any way berelated thereto.

The mention of trade names or commercial products in this publication is for illustration purposesand doe"C; ,'o, Un1.,,U. cndorsement or recommendation for use by the United Sta,:s Air Force.

The Public Affairs Office has reviewed this report, and it is releasable to the National ITechnicalInformation Service, where it will be available to the general public, including foreign nations.

This report has been reviewed and is approved for publication.

a, q-9v. nc L4T7%/

AMES A. GARRISON, Maj, USAF, BSC 'S.. ELTON R. BIRCI, Colonel, USAF, BSC

Chief, Air Quality Function Chief, Consultant Services Division

Air Force installations may direct requests for copies of this report to: USAF Occupational andEnvironmental Health Laboratory (USAFOEHL) Library, Brooks AFB TX 78235-5501.

Other Government agencies and their contractors registered with the DTIC should direct requestsfor copies of this report to: Defense Technical Information Center (DTIC), Cameron Station,Alexandria VA 22304-6145.

Non-Government agencies may purchase copies of this report from: National TechnicalInformation Service (NTIS), 5285 Port Royal Road, Springfield VA 22161

JAMES C. ROCK, Colonel, USAF, BSCCommander

DISCLAIMER NOTICE

THIS DOCUMENT IS BEST QUALITYPRACTICABLE. THE COPY FURNISHEDTO DTIC CONTAINED A SIGNIFICANTNUMBER OF PAGES WHICH DO NOTREPRODUCE LEGIBLY.

UNCLASSIFIEDSECLOOITY CLASSIFICATION OF TRiS PA'

Form 4ppiovedREPORT DOCUMENTATION PAGE oMS No o704-e1

I RLPORT .S (fURJTY CLASSIFICATION lb RESTRICTIVE MARKINGSun ass fled,ECURITY CLASSIFICATION AUTHORITY 3, DISTRIBUTION/AVAILABILITY OF REPORT

Distribution is unlimited.2b. DECLASSIFICATION/DOWNGRADING SCHEDULE Approved for public release.N/A4. PERFORMING ORGANIZATION REPORT NUMBER(S) S MONITORING ORGANIZATION REPORT NUMBER(S)

USAFOEHL Report 89-OOEQO178BEF

6a. NAME OF PERFORMING ORGANIZATION 6b OFFICE SYMBOL 7a. NAME OF MONITORING ORGANIZATION

USAF Occupational and Environ- (if applicable)mental Health Laboratory EC(_6c ADDRESS (City, State, and ZIP Code) 7b ADDRESS (City, State, and ZIP Code)

Brooks AFB TX 78235-5501

8.. NAME OF FUNDINGISPONSORING Bb OFFICE SYMBOL 9 PROCUREMENT INSTRUMENT IDENTIFICATION NUMBERORGANIZAT!ON (if applicable)

Same as 6aS. ADDRESS (City, State, and ZIP Code) 10 SOURCE OF FUNDING NUMBERS

PROGRAM PROJECT TASK WORK UNITSame as 6c ELEMENT NO NO NO ACCESSION NO

II TITLE (Inxlude Security Clas.ification)

Compliance Testing of Hot Water and Steam Boilers, Shaw AFB SC12. PERSONAL AUTHOR(S)

Mai James A. Garrison'13a. TYPE OF REPORT 13b. TIME COVERED 14. DATE OF REPORT (YearMonthOay) IS. PAGE COUNT,Fi nalO

FROM TO -I Februry 199 16216 SUPPLEMENTARY NOTATION

17. COSATI COOES IS SUBJECT TERMS (Continue on reverse if necesary and identify by block number)FIELD GROUP SU-GROUP ' Boiler-- Staw Emission Testing, a r,

Steam. Stack Sampling. Velocity,Hot Water Source Tepting , Mni turp..

19 ABSTRACT (Continue on reverie if necessary and identify by block number)

k'

iAt the request of HQ TAC/DEEV, personnel of the USAFOEHL Air Quality Functionconducted source testing of eighteen small hot water and steam boilers todetermine stack gas moisture content and velocity. The data obtained duringthe survey was necessary for boiler operating permit application. '

Final results were determined on-site and provided to 363 CES/DEEV personnelso that permit application could be initiated immediately.

20,.ISTRIBuTION/AVAILABILITY OF ABSTRACT 21 ABSTRACT SECURITY CLASSIFi(ATIONUNC .ASSjEDjNLiMITEU C] SAME AS RVT Li Dic uskki( 'r-c], eJ

22a NAME OF RESPONSiSLE INOiVIDUAL 122b TELEPHONE (Include Area Code) 22c OFFICE SYMBOLJames A. Garrison, Maj, USAF, BSC (512) 536-2891 ECQ

DO Form 1473, JUN 86 Pevous edition% ate obsolete SECURITY CLASSIFICATION OF THIS PAGE

UNCLASSIFIED

CONTENTSPage

DD Form 1473 iIllustrations iv

1. INTRODUCTION 1

II. DISCUSSION

III. CONCLUSIONS 2

References 14

Appendix

A Personnel Information 15B Permit Applications 19C State Regulations 37D Building 403, Steam Boilers 2, 3 & 5 Field Data 49E Building 611, Steam Boiler Field Data 63F Building 922, Hot Water and Steam Boiler Field Data 69G Building 1046, Hot Water Boiler Field Data 79H Building 1102, Hot Water Boiler Field Data 85I Building 1130, Steam Boiler Field Data 91J Building 1200, Steam Boilers 1, 2 & 3 Field Data 97K Building 1206, Steam Boiler Field Data 109L Building 1402, Hot Water Boiler Field Data 115M Building 1422, Hot Water Boiler Field Data 121N Building 1604, Hot Water Boiler Field Data 1270 Building 1614, Steam Boiler Field Data 133P Calibration Data 143Q Exhaust Gas Moisture Content and Velocity Calculations 151

Distribution List Accesion For 159

NTIS MA&lC,TiC TAB Li

J,, bh ati,,: .. ........... . .

]~ ~ ~ ~Y .... ................. ..

,,.A , " "

ior

111 ~ v~

Illustrations

Figure Title Page

I Heat Plant Steam Boiler 32 Bldg 1102 Hot Water Boiler 43 Bldg 611 Test Site 54 Bldg 922 Test Site 65 Hldg 1046 Test Site 76 Bldg 1130 Test Site 87 Bldg 12(X) Test Site 98 Bldg 1206 Test Site 109 ORSAT Sampling Train I

10 ORSAT Apparatus 1211 Moisture Sampling Train 12

Table

Test Results 13

iv

1. INTRODUCTION

On 8-24 Aug 1988, a stationary source emission survey was conducted at Shaw AFB bypersonnel of the Air Quality Function. USAF Occupational and Environmental Health Laboratory(USAFOEHL) to determine stack exhaust gas moisture content and velocity for 18 small oil and gasfired boilers. This survey was requested by HQ TAC/DEEV to assist Shaw AFB in obtaining thenecessary boiler operating permits required by the State of South Carolina. Personnel involved withon-site testing are listed in Appendix A.

If. DISCUSSION

A. Background

Shaw AFB received a consent order from the South Carolina Department of Health andEnvironmental Control, Bureau of Air Quality Control for not having obtained operating permits for1 9 boilers located on the base. Permit applications were then filed, but were returned due to lack ofdata on moisture content and velocity. USAFOEHL was requested to provide this information sothat the base could obtain the necessary operating permits and demonstrate and maintain compliancewith all provisions under the South Carolina Department of Health and Environmental Control:Regulation 61-62 - Air Pollution Control Regulations and Standards.

B. Site Description

The 18 boilers tested ranged in size from 1.05 x 106 to 8.4 x 106 BTU/hr input and werelocated in 13 separate buildings. The primary purpose of the boilers is to provide steam heat or hotwater at the particular location. The location and operating parameters of each boiler are found onthe permit applications piovided in Appendix B. Typical boilers tested are shown in Figures 1 and2. Typical stacks and test sites are pictured in Figures 3-8.

C. Applicable Standards

Permit procedures are defined under Regulation No. 62. 1. Air Pollution Control, Sectioni. Permit Requirements. Emission Standards are defined under Regulation No. 62,5, Air PollutionControl Standards, Standard No. 1, Emissions From Fuel Burning Operations. These regulations areprovided in Appendix C.

D. Sampling Methods and Procedures

All stack tests were conducted in accordance with the procedures and analysis methodsspecified in Chapter 40. Code of Federal Regulations, Part 60 (40 CFR 60), Appendix A, Methods1-4. Therefore. test methods, equipment, sample train preparations. sampling and recovery,calibration requirements and quality assurance were done in accordance with the methods andprocedures outlined in 40 CFR 60, Appendix A.

Sampling ports were installed in the exhaust stack or ducting and traverse pointsdetermined for each site in accordance with Method 1.

Exhaust gas moisture content and velocity were determined simulta- neously using thesampling train pictured in Figure 9. The train consisted of a button-hook probe nozzle, heatedglass probe, heated glass filter, impingers and pumping and metering device. Flue gas velocitypressure was measured at the nozzle tip using a Type-S pitot tube connected to a 10 inchinclined-verticle manometer. Where stack/duct diameters were less than 12 inches, a detachedpitot tube was used so as not to significantly block the duct cross section. A 1-inch inclinedmanometer was used where gas velocity pressure was less than 0.05 inches of water. Type Kthermocouples were used to measure flue gas as well as sampling train temperatures. The probewas heated to minimize moisture condensation. The heated filter was used to remove particulatematerials. The impingr train (first, third and fourth impingers; modified Greenburg-Smith type:second impinger; standard Greenburg-Smith design) was used as a condenser to collect stack gasmoisture. The pumping and metering system was used to control and monitor the sample gas flowrate. Equipment calibration data is presented in Appendix P.

The sampling time and sample rate for each test run was selected to provide theminimum 21 standard cu ft sample volume and 0.75 cu ft per minute sample rate required byMethod 4.

During initial sample runs, flue gas samples for orsat analysis (measures oxygen andcarbon dioxide for stack gas molecular weight determination) were taken. Molecular weightsdetermined from these samples averaged about 29.6. This value was assumed for all subsequentcalculations. Orsat sampling and analysis equipment are shown in Figures 10 and 11.

Moisture and velocity calculations were done using "Source Test Calculation and CheckPrograms for Hewlett-Packard 41 Calculators" (EPA-340/ 1-85-018) developed by the EPA Officeof Air Quality Planning and Standards, Research Triangle Park NC. This is our standard methodfor calculating emissions data. Moisture and velocity calculations are found in Appendix 0.

Ill. CONCLUSIONS AND RECOMMENDATIONS

Table 1 provides the survey results for all boilers tested. In some cases, modifications to thestack were made to accommodate the sampling ports. Duct diameters shown were obtainedwhere the ports were installed. Where the inside stack or duct diameter measured during testingwas different from that on the permit application, the velocity was corrected to the diameter listedon the application. These results were determined on site and provided to 363 CES/DEEVpersonnel so that permit application could be initiated immediately.

The USAFOEHL will continue to support Shaw AFB as necessary in this project withconsultative and testing assistance.

2

is

Figure 1. Heat Plant Steam Boiler

3

Figure 2. Building 1102, Hot Water Boiler

4

A5

Figure 3. Building 611, Test Site

5

Irw


6

-AL,


7


8


9


10

UU

U.5wD w

LLI-

I- 0Cw>

wU <

'LCI

0x to M cccr. C CL -

Lo1

PROBE FLXBETBN

TO0 ANALYZER

Figure 10. ORSAT Sampling Train

.Crl' VALVA IC CC msIPETI

1MA7 VALVE TO a2PIPITIE

/1,117 VALVE TO C0 PIPETTE

ISATy

102

TABLE 1

SMOISTURE AND VELOCITY TEST RESULTS

DUCT**TYPE* DIAMETER YLLOCITY***

BLOC NO. BOILER % MOISTURE BY VOLUME (ft) (fps)

403 02, ST 15.26 I.D0.00) 30.0

#3, ST 14.73 1.02(1.00) 27.0

#5, ST 15.54 1.31(1.66) 26.0(16.0)

611 ST 11.28 1.15(0.66) 26.0(77.0)

922 HW 7.58 0.66(0.66) 3.0

ST 19.94 0.81(0.66) 11.0(17.0)

1046 HW 12.55 1.25(0.66) 15.0(55.0)

1102 HW 9.90 0.81(c.66) 15.0(23.0)

1130 ST 9.C2 0.83(0.66) 28.0(45.0)

1200 #1l, ST 9.01 0.78(1.0) 22.0(14.0)

#2, ST 12.42 0.78(1.0) 11.0(7.0)

f3, ST 10.88 0.78(1.0) 20.0(13.0)

1206 ST - 10.54 1.16(0.66) 8.0(24.0)

1402 HW 9.50 0.90(0.66) 11.0(20.0)

1422 HW 12.27 1.46(0.66) 9.0(45.0)

1604 HW 10.56 0.63(0.66) 22.0(20.)

1614 fl. ST 10.65 1.33(1.0) 12.0(21.0)

f2 ST 9.41 1.33(1.0) 12.0(21.0)

* ST - Steam boilerHW a Hot water boiler

Duct diameter measured during testing. ()indicates

duct diameter listed on permit.

'Velocity for duct diame-ter measured during testing.()indicates stack velocity corrected to stack

diameter listed on permit.

13

REFERENCES

1. "Standards of Performance for New Stationary Sources," Title 40, Part60, Code of Federal Regulations, July 1, 1987.

2. Quality Assurance Handbook for Air Pollution Measurement Systems -Volume Ill, Stationary Source Specific Methods, U.S. EnvironmentalProtection Agency, EPA-600/4-77-027-b, Research Triangle Park, NorthCarolina, December 1984.

3. Source Test Calculation and Check Programs for Hewlett-Packard 41Calculators. U.S. Environmental Protection Agency, EPA-340/1-85-018,Research Triangle Park, North Carolina, May 1987.

14

APPENDIX A

Personnel Information

15

(This page left blank)

16

Personnel Information

1. USAFOEHL Test Team

Maj James Garrison, Chief, Air Quality FunctionCapt Paul T. Scott, Consultant, Air Resources MeteorologistSSgt Shelley Schelin, Bioenvironmental Engineering TechnicianSSgt Pietro LaPorta, Bioenvironmental Engineering Technician

USAFOEHL/ECQBrooks AFB TX 78235-5501

Phone: AUTOVON 240-2891Commercial (512) 536-2891

2. Shaw AFB on-site representatives

Capt Michael Rusden, 363 Medical Group (TAC)/SGPBSSgt Edward Meltz, 363 Medical Group (TAC)/SGPBSSgt Deral Freysinger, 363 Medical Group (TAC)/ SGPBKarl Chandler, 363 CES/DEEVPenny Spell, 363 CES/DEEVJoe Bartlett, 363 CES/DEMMHTSgt Paul Trageser, 363 CES/DEMMH

17


18

APPENDIX B

Permit Applications

19


20

C 5MFAW AFB -Date:20 Apr 8877~ Steam Boiler Hea wg /3c L~r 96*

Heat Pl ant 8iollers &2 :3

71. Suoerior Aztec ___ c>: 5-5-402- A.......-a.:Ln-tuit 2.76 x 101D BTU,/hr Rated C"Lout x IO'D 3TU

L. s tf se amr,"I . and ____P S8

-. .-.. -~' Su~or Ash~ Conisumntion

7' 1 .17

k, .- 3cV Ls

T"CO or d Ptrrn, i

oc V42 D&-'

N/A

21

-- Nc .

Fj EL 5:NU PERlET IPPL:CIT:,CN

SHAW AF -. . .*~~ ~ 20 Acor 88'712 3:eafF ;lBrnina Oporat --n: tenoler Heating 5~P693

Des Heat Plant oiler #I5

Kewanee Model 3C~C- -- i,:):. uae TCuti.V ,0 31 BT,hr Rated u p uG Lou 'h

x___ : ic- _,b-30- of s e,.-/,Ir Or0 an-* ___ S__

Fuel BT S ulf ur 7'Ash Cons umc ionem .,n 2.:. ' wea h b,; wei '-j: ra~ad caOUcIz.

.. J L ?,, :ue 0-.~ ? :r ze 0 .avelin; Gra7te

se i2~.,.veU ___

L73' 'rt.u$ f Ga- %'-'locity ft/sec

-- .? r & eprtr OFLo-. ion C," or Lact'Lc-;

nC ) Control method of Estimating~ ev ic e 3Ei 0i1 s

C ~: . .2,1 .4) AP 42 0ec 84

S. . Ha a i.. as 'i w

- . . . -.. .,,~n.:C,.;nrol equipment be of ~

22

*l- c.... :"%. C -R...RTTO h. ~ AND CC' iQMETA C RLBUR~EAU OF AIR QUALITY C'oNTROL I .D"c

FLEL BRNGPERMIT APPLICATTCN 9a-:

PART IJA R.Lvk&!ue- Byg:

comoa:v Name::..SHAijW AFa .<.. Date: 20 A pr 88 *.T fue Iur nin Q'. Ge ra t i 0n: Sen e a Eoi Ie r Neati no

Unit Dsfgna ~ 9n: 611 eoilpr

- -- 2. Make: .Soencar - modol: '4F-360-50-5ca: a c i Ratei4 lnouz t . x I C 3K/',h r Rated Out~uc x 100 BTU/hr

x__3_1,:x ls o,: steam/h ?ad___P:

3. Fue I D a a U.ia al un it s)

- 37" Sulfur % As h CdnSUMpt~on.r ne Corueuntent by weighlt by weight @rated capacit:y

Nar.ra C-s :, IThJ/pt 3 NI1L N IL 2913 F:t3/HR

o I 1 rnl*) P u 1% e- , zt,, Traveling Grate.7:zcer ~(specif,;) __________________

? I2 ze,-2 :-! 13 to begive rainjection.____

croDvc Desc-fp'- r,

~ it boe rcund d~ft Gas Velocityl ft/sec

:n Si D ia-.e t er to emperature- o-- I~___ ocation (,*-T'M or Lat/,Long) Thb-!j ol

7 .s~R.:s u raeU a-rai~v(Lbhr)B 0 r,- A cte rc ntrIol )-,! Cnro i Method of Estinmat4-ng

___Dev.ice Emissions

'.' I.; ,Q /V

.::7,-pr II, q1 C~I I pmtn t be J 1,ps:; of

23D HE F)

OF HE..',L. R -C

BUREAU OF A7R QUALITY CTN'R3L i..cFUEL BU R-, G PER,'11IT APD11'CA F~i

PAR T A .dS:

.- .Ccm)nv Name-- -SHAW AFB Date; 20 ADr 88Type off FelJ Burning Operation: Hot Water BoilerUnfz' Designation: Bldg 922 H/W 2O Ier

2..~k:A.0. Sinit' h Model:_ 3T 2A-n916- a~~iv:Rated input 1.7085 x Lou BTU/hqr Rdted outnur x ij'uMUh

______x1C3 lbs of: 0~a/rO ni____SI

3. D~ Da ta (idat all u ni4- t

F,- - - - BTU Si Sufu r Ash Consumocion

2n: G4 i Content b w ve igh :"LNa:.1ra, "as 1H2 STU/t iU I. h

7'.. e r (sprezlf-) ___________________

S- - n s. Z: 7e: r 1s .3 -'so 2 give 3rl'-c:n

__ ~-r~lDe,.ice Descrio:ion: _________________

6. Stack Data:r.egtAbove Grcound f ft Gas 7", ocity____s__

-,sii-e Diamne!tor 7emerat-ire

* ntn tro tro Meth-Iod of Estimating,

--r r;:i..

24

E

'Y 1 c: dr.", N 'm~ _SHAW AFB -Da.e 20ApE'~~n1 0i c -o~n: Steam Boile atn

* zn: Dts iga icn. Bldg 922 Boiler for Heat

2 . ~A .. MC~P ~ 615-N-51-2 NP

_________ L 'FS~ ____u and ?_S_ PC;

r As~iConsiumotion

~~....cq - -' 0 t OC 37,' - , - ___

A': ound ~Sft Gas .LCV rte

~e:2r ~ft Tciiie rdc.tre____

Conta. onrr2. c~hcdof £stiimacing~

25

6F

. .e iV ' B. , .

-..... ...Nae: SHAW AFT Date: 20Apr88

T'.'c '6b f 1 3,lln g Ocr a~i' Hct Water Boiler Heating -~- ~ ~De... . Sdq 10Ri6 OF Te -r

-Peerles ______ MrL:- 0714-PO-W -

17 .7117 x 3- Ku

F-e 3T Sulfur Ash Co n s 7, t o n

.';a-ural, iza IS2 3 TU/t 1~: _____ _ 17/ 'F

..............-..r..,.. 17.

7 . ..e

::" 2 D.i:..; -Pe rs ., oen: O-71-ur-W_..._-

-..7. __: 1.21 a' " 5,',:.r h at 'Lo e< biGO 1046

FCeiT -L " t f Metiod of Estimating

AP 42 Dec 4

. ... . .. . . ... :. . e ..... .( ;0C __:~ ______e ____ _____ ____

J-,

26 :..Q 1,. .

Be fo q Afte

26n .LC)n,) 'Ithdo s~m tn

U'J~C*'KL A P I >~T C I2UH A 0 EJV IR,30{TA E CNT CLBUREAU OF AIR QUALITY CONTROL '*

FUEL BURN:N'.G pERMIDmT "PPLECATICN

PART 1' TA~z~:~

SCo mSiA ABa -a- Date: 20 Apr 88 _

ay, o _; 3urning Operation- Hot Water BoilerUniz Dos;_.nar-on:_ Bldgl 1102 H/W BoilIer

--------- ~--M~~ Cnen-r~ot's ... ~ModeI CB H186-SOCa:: c4: -Rated Inc:ut 1.95 -x 10 BTU/hr -iKared Output ::100 T/~

_________ L ls or sIa/h F and____SI

3. --,el Daora (indi-catie all units):

- BTJ~~ Sulfur %AshCnucro.E an 2r" i Con-.ranv by ~ei4g dt by, weighc a~lztc:42 Oil -,'P . 00 BTUI/Ca ______7 N IL ..-

-. . oa . ?ulver~ze-d Travelin2 Groit2

act... r bC e r ,:e c______

z.Ai ?cL.i:' Co a ,, cL De-.-izc: Dos.-ipion:______________________

-6. Stack Dorta:Fei, nt (,ov round X2ft Gas Velocity f ft/sec

lnc~e~~:r .6,- ft Temperature_____Es C ! 1 r - Location (U4or Lar./'Loac.;) 2

. E:>~. a.>t a r Lrad c a Da c y (/r,

Cn rao C c nrr I. ~ !t d 4fEt ra

_______ ,wi ce Device Emissiocii

7.- 0-- -

27

.I "A_ _ A-7,T "'E' F .-IEAL 7TiT FL CC NTROL5URE.UI CF A:R ,UP<..7r C'.,NTROL

FJK E'J6RN G P E.RNMIT A P~ C Tvat-,r Ra.veAed By:

..- i Coinuanv Nae: -. SHAW AFB Sem-Date:-20 Apr 88iY7t2 0"' Fual Burn ing operation: Sta oiler HeaTinc________Uni: Designation: Bldg 1130 Bciler _______________

.M2ke: - -Kewa --- r_______ Model:_______________Caraaitv: Rate inuz x 100 BT,'hr Rarod . Outnut x 100 B TUh

____x 10-) lbs off t.. Fad___PI

3. Data (iaoall units)

rjC ~, As. iConsumo-tion-. atid Cra~a Contenr -w we ig by wein @ ratad,_ caoacit.;

NJatural Gas 1035 eTU/Ft3 Ndl NIL275F,/)

-~~ ~ -- e n (oiieLsn. C-Lerzc rvelin rt

7-- -- -**-Z5 C . ' 3 s~

6.~~ stc c ta

Height" Above cround 25 ft Gas ."alocitv _ft/secr~ioDiamet~er .66 ift Temperature___

c r. Locat ion (UT! or har

,..,'1 s 3 L R Rat at ritac 2p a ctv Lb

Ce r -l A nri ehdof tntn

L~~ncon 1e,:e DeL1 .riioflIn.. . . . D-., E., . S = ot

<'4 --.

28

BUg~~JO A' R I .QUL'Y CCNTROL -i.V.

-FUE ~L.~G rR~T PPLICATION

LAR Rev ~evd By:

C. n.Cc - Iam e. -SHAW AF3 20ApI ac -,;o' 73. Bu rnin g 0 pe r atioc Steam Boiler Heting ..-

Uni: Des3 a Lo n:I B.ldg200 Poilers 4t1 # ~2

----2 Ma -e.- -'Kewan ee ModeL: _______________

SCaaz::.: --Ratil Innuz 2.wjY x 160 WU'h/'r Rated Output x 106 BTU /-nr

_______ 1: ls af s a am Ir 0- and____PI

3. 1uo 4 (fi, a t e al uis

- BTVSlu Ash Consumption

-- ~ bve:t b er. racca capacit."

,Natural Gds 10,:; 1 L41 _____ '1 i'-

:±~ld e 3 gi:'?ul'.erized Travelin; Ort5-~ t""' Oth r (S ec4-v)__ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _

-n 2c r cr. ::2 used, reinj ect'_on.

z.A : i D ::n .. n tro c e'.vc D es Cr4r . o n:

He Dh ,b; rounc f Gas Velocity ft/secov

D _me ____L_ TeMer a ture_______. octo (UTMi or Lat/Long) !2 2'

n: -_r Cont-ol Method of EstimacringZviDevice Dn i 3S 1 i S

CO P9 4? 'ec 84

S. C.i(m ., n

3 1 n n ' t e 1 j, 1

3 - .. --- ' - '-. - ..29

_S> u-xKZ C. ' E.2.T>T 3F 1- E _'I7> CCNTRCL Nap' 0cUEA.U 0F AI:; u12L:T ID.2~ No.:

PA7T V.A R~evieCwed By:

i.&.~avName: SHAW AFB -Date: 20 ADr 88me f Fu oL Burning Operat cn: Steam 1cflar Heatinc

:n I' Desigain Bldg 1200 Sol er /Z

- . 2 Vke: Kewanee .Mdl _________________

C a ac it Rarcei Input ;2.05 x 100 BT~r Rtdoutput x 130 372j/hr______x 2~lb s o f s0a'r____~ and4 _____SG

alData a!-'cr all nitS)

Fu-el BTU %Sk'97- ir % Ash ConsumD tion

e nd ar a--' Con tent w e.':~ e,~: ra:e_7 zap-,i

-~ tau~r Utno:.a z; rent>.- tO ~e USEu ,I §:

a. Stack Data:ie~tAbove ',Ijuza ft Gas Veoct ft/sec

nsie iamte W~t emoerature

7. . . . . . . .' _-n 7 2

Beff,-ru _

ccn ro L C ontroL Methnod at Estimating

30

BUPE.4U1 OF AIR QUALrT'( CO.NTROL

FUEL BURNING PERMIT APPLICATIONI

PART I !A 37y-ae~~:

~'~§ oman m. am;=e: SHAW AFB.A77 Date: 20 Aor .38~Type -o: Fuel. 3urning Op erat ion: StamBolr HeatirioUnit Des 4--naton Bdo 1206 Heating Boiler

- .Mk: Ycrk 'ShiDlev -Model SPHW.V25-2-12 17-- -Capacl ty: Rated Input 1.05 x 100 BTU,'hr -Rated Output- x 100 5TU/hr-

x 107 Albs o-. staa/hr 'j 0 T and ___

3. 7uel' Dat-a (ini~eall units)

- -F',-,-BTU %Sulfur -- % Ash Consump tion

7,7e -.nd 4rd Content by: weight by weigo: .z rar:ed zaoac4:t:

Burner (-; 1o (cid fueLs cnly:Puve±e

f~ys- :-.....s to o e used, z4.,e .re injection.____

5. Air ?luinCtr Device Description: Ce

-- 6. Stack Data:- ne4ig'n Above G'round :t Gas Velocity ft/sec

I nsid Dametcer .5 0 t 0eprtre___

.~:. 1; tar ______ Locationr (UT., or Lar-T Lang) : ________

Be f-r:! A torControi Control Met'hod of E.stimntiz

Sri

io -,: z c

31DhEr

... .. . ...... . . . .. . - ~ T L. CCNTKCL

EBUREAU 9' ,. R .... I CCT-LF __ O .' o :

S L. Ce SHAW AFB Date: 20 Acr 3C- 'pe oFu6 n4r::rn Operaticn: Hot Water Boiler Heat"noU'n: Desig::a:i:;: Bld 1402 Boiler :1

... e:-uoerior Pawnee :'l e: C2-20-20A-Cs.c v -'Ra:eu r:.pur _ij :< t'' B''- r Rated6 Ou~ut x ID° BT,r

:< jC e.: 1:71 t , ': 0, e and -?Sill" ... . . . . .

As r n

n . . .A . C o n s ,-'I w eW e

1;u*ural Gas 1J35 .}T. _____ 4JL __ iZL. _ ,______,_, ___,' ___,

" -. .\ T : -uio --. , O" 2e -_- - -. ._."L ~ - .:

6. Stack- Data:Hei,-ir Above 7rcun Erf ;s "'--c t t'~

7nsi Diame-er.'r C____, _

.s I. ".:oi, ,11r , _ _1___ '__:___, -

T. J~. j~J.1 - - - --- l rt :_ "-- -- i - :

-') . . - . . ,.-, - -, P " , I L" ( p [' i['',

- .'.. .. - .•. .3-

32

Ji . Z :'oa.

SURE.AU OF . . U.'L:T> CCJiRVL ID No.:FJE. BURN'I' O - 7E>~ ,P2U : CA:C% an

A RV'-L:,'A Sy--

-.cnyn Nae .A :A-SFAW AJFB Date: 2'1 Apr 887y~~iw -- 2 urning Operacion: Hot Water Boiler Heatina

:2~i n~nano:- Bldgi 1422 biller

2.- iw Soencar- -i.c.. .modeo. 4F-45O-50WCayasny: Rawz2d Enaut 3.015 x loo 3Uhr Rated Output____ x 10D 37,hr

x sea,;h ~ OFZ and PSXJ

-... Ash osm c n

an. ~ ~ 301 cotn:b ein b ej:rc1zpci..

lex'ce Dec ±ptin: :

6.S 1- D naHy -n Atcv Ground 1 Ac Ga Velocity__ AMC_

* .~.. . r - -f ' e a~r0

- ~ : . e:- t-. rt- OF~.: .. _______

33

.~.'I A2 -'4L TY CON77?-L : N .

PART I1 I &A

c.. -,r Hot Water Boiler Heatinn ~ -

D. 31do 16C4 Boiler

',I ___ r L ~ ii!9,J/hr -.--.Rated OU:Dut x I ) h'L :-

-~', S~I~r %Ash - Cn'r~

________3_3 YTU f 1.17 _____

~ Ac;~ fr-hr. ~Gas VeL_"c:ityv 0~b~-.-i~:- ~ T e:i ~.r ar___ 7-

.~..

34'

>>CARC0VL D EPA R7MV 17 nF HE AL TH AND ENVIR~ONMENTAL CONTR L . Pu.cBUREAU OF AIR QUALITY CONTROL

.. FUEL BURNIN~G PERMIT APPLICATION .az

2i~L~ii -. ~: -. PAR7T IA -- Reviziuz-i By:

* . cn ~ -. SfIAW--AF" -Apr 88 ~4.:n ~ :'iBurning Operation: Steam Boiler HeatingUn?~i2~aion: Bldg 1614 Boilers (2)

2.:ak Newanlee Moldei:__________________

~ ~ Lnu: 100xIc BTU/hr Rated Output x 100 BTU/hr

_____x 10.' lbs of s~eam/hr - OF and ____PSIG

- .. -~ a!'. unjto.):

3 T S . 1 u r Asn Cons'.uocica

Conzent: by w eigh t by we i g,- c ratedl cac)aci::______ ~ ~ -____ 15 BT'/ I -1L I32 /R

- ue-s c-ilv, Pulverized ____ raveling. "rate

Z)K~ k&~ e .. (speci-Fv) _________________

-,:-n -5 to) De us e.1 , -ve % reinjection.____

,,rntrol Dev.'ce Description: ___________________

- lrud30 ft Gas Velocity ft/sec

~ e7nr e r at u re OF

r L. c~ a Lc : (U-, or Lat Lc)ng n A-.

:i r a c pa ci1: : (ln/r

? Lyr~ .v97 GU46,____ AP 42 Dec ~

- I r. .v -Nov

I. w 1.4; -.. i -er~ r r,)- proc ,ss anin, control equlirMenc be .;pc' of'

35


36

I I I Ii i

APPENDIX C

State Regulations

37


38

b06:0501

SOUTH CAROLINA AIR POLLUTION CONTROL REGULATIONS

(South Carolina Department of Health and Entironmental Control; Regulation 61-62 - Air Pollution Control Regulations and Standards; Adopted July 26, 1972; Asamended through MaN 28, 1981; December 16, 1982; April 22. 1983; June 24, 1983;MaN 24. 1985; May 23, 1986)

CONTENTS 5. Applcazon - Means a form provided b, the De-Reoiilaln No 62 I -- Air Pollution Control partment which is prescribed to provide the informationRegulation No 602 - Prohibition of Open Burning required to grant approval to construct and operate aRegulation \o 62.3 -Air Pollution Episodes ,ource or an incinerator: or to report an existing in-Regulatin No 62 4 - Hazardous Air Pollution Condo- 'nerator.

iion, 6. Board - Board means Board of Health and En-Regultion No 62 5 - -ir Pollution Control Standard, irunmental Control.

tSee paec 506. 10(xO 7. Commissioner - Commissioner means the Com-Reeu!,ti,7 \t t, 2 f - Control of Fl:ugiti Partnculate missioner of the Department of Health and Environmen-

%Mtttcr tal Control.Regulation No. 62 7 - Good Engineering Practice 8. Department - Department means the DepartmentStack Height of Health and Environmental Control.

9. Emission Data - The definition contained in 40CFR 2.301(a)(2). July 1, 1982, is incorporated by

RE(;I LATION NO. 62.1 reference.10. Emission Limitation (and emission standard) - A

AIR POLL'TION CONTROL requirement established by the State or by the Adminis-trator of the Environmental Protection AgencN which

Section I - Definitions limits the quantity, rate, or concentration of emissions ofThe follo.ing %ords and phrases %hen used in the air pollutants on a continuous basis, including anN re-

Ree uIatons and Standards shall for the purpose of these quirements which limit the level of opacity, prescribereualions have the meanings respectivel, asribed to equipment, set fuel specifications. or prescribe operation'hc,- ir thi, section. un!ess a different meaning is clearlI or maintenance procedures for a source to assure con-indicated. This section augments Section 1 of the South tinuous emission reduction.Carolna Pollution Control Act. 11. Fuel Burning Operation - Use of furnace, boiler,

I. Acid Mist - Mist or droplets of sulfuric or other device or mechanism used principally but not exclusive-strong acids Sulfuric acid mist includes sulfur trioxide 1',, to burn an% fuel for the purpose of indirect heating in(SO, and sulfuric acid vapor as well as liquid mist. %hich the material being heated is not contacted by and

2. Add - Additions to a process which will increase adds no substance to the products of combustion.size. scope or emissions from such process. 12. Fugitive Dust - A type of particulate emission

3 Alter - Alter means modification or change in a that becomes airborne by forces of wind, man's activityprocess or processes. %hich gould affect emis.ions to the or both. including but not limited to, construction sites,,it-,,sphere tilled land. materials storage piles. and materials

4 .4mbien 4ir Quait., Standard - That standard handlingfor the qualit% of ambient air at or beyond a property 13 Fugitive Emissions - Air contaminants whichline on shich a source of pollution is emitting, escape to the atr not through an exhaust system. but

9-5-86 Published by THE BUREAU OF NATIONAL AFFAIRS INC Wash-iglon D C 20037 51

39

502 STATE AIR LAWS

through other means, including but not limited to. win- shall be treated as part of its design onl) if the limitationdows. vents, doors, ill-fitting closures or poorl main- or the effect it would have on emissions is federalytained equipment enforceable. Secondary emissions do not count in deter-

14 Garbage - Animal and vegetable waste resulting mining the potential to emit of a plantfrom the handling, preparation. cooking and serving of 25 Prucess Jndustrt - An% source engaged in thefoods manufacture, processing. handling, treatment, forming.

15 Ha:ardous Air Pollutant - A pollutant which is storing or an) other action upon materials except fuel-the subject of National Emission Standards for Hazard- burning operationsous Air Pollu.ants promu!g_-'ed bN the United States 26 Process Weight - The total weight of all materi-Environmental Protection Agenc) by publication in the als introduced into a source operation, including air andFedera! Register water where these materials become an integral part of

16 Incinerator - An engineered apparatus and all the product. and solids used as fuels but excludingappurtenances thereto, designed to reduce combustible liquids and gases used solelN as fuelssolid, semi-solid, liquid, or 2aseous waste bN high tem- 27. Process Weight Rate - A rate established asperature burning folloh s:

I - Araft pulp rmll" - Anx stationar source which (a) For continuou!, or long-run stead%-state sourceproducc, pulp from ood by cooking (digesting) v ood operations. the total process weight for the entire period

chips in a water solution of sodium h~droxide and of continuous operation or for a typical portion thereof.

sodum sulfide ( hite liquor) at a high temperature and di,ided by the number o: hours of such period or portion

rressurc Regeneration of the cooking chemicals through thereof.a recoery process is also considered part of the kraft (b) For cyclical or batch unit operations, or unitpulp mill processes, the total process weight for a period thatIp Major Plant Excep as otherwise provided, this covers a complete operation or an integral number of

term refers to an\ plant vhich directl) emits, or has the cycles, divided b the hours of actual prcess operationpotential to emit, one hundred tons per year or more of during such a period

Where the nature of an, process or operation or theany rMlate aiount Th ehdscharg design of an equipment is such as to permit more than19 Mass Envmi'on Rarc - The \height discharged one interpretation of this definition, the interpretation

per unit of time that results in the minimum value for allovable emission20 Opacitv - The degree to , hich emissions reuce shall apply.

the transmission of light and obscure the view of an 28. Refuse--Garbage. rubbish and/or trade waste.object in the background. 29. Rubbish - Solid wastes from residences and

2i Open Burning -An,, fire or smoke-producing daellings, commercial establishments, and institutionsprocess which is not conducted in any boiler plant, 30. Salvage Operations - An, operation of a busi-furnace. high-temperatture processing unit, incineratc: n iflare, or in an) other such equipment primarily designed ness, trade, or industry engaged in whole or in part infor the combustion of fuel or waste material salvaging or reclaiming any product or material, includ-

22. Particulate Matter - Any material, except un- ing, but not limited to. metals. chemicals. shipping

combined water. that exists in a finel\ divided form as a containers, drums or automobilesliquid or solid at standard conditionsSecondar Emissions - Emissions hich wouldoccur a., a result of the construction or operation of a

23 Plant - Except as otherwise provided, any sta- major plant or major modification. but do not come fromtionar', source or corrbination of stationar sources, the m.,jor plant or major modification itself. Secondarywhich is iocated on one or more contiguous or adjacent emissions must be specific. well defined, quantifiable.properties and owned or operated b) the same person(s) and must impact the same general area as the plant orunder common control modification which causes the secondary emissions Sec-

24 Potential to Emit - The maximum capacity of a ondar) emissions may include, but are not limited to.plant to emit a regulated pollutant under its physical and (a) emissions from ships or trains moving to or fromoperatnonal design Any ph.ysica; or operational limita- the new or modified planttion on the capacity of the plant to emit a regulated (b) emissions from any offsite support facility oper-pollutant. including air pollution control equipment and ation which would not otherwise be constructed or in-restrictions on hour, of operation or on the type or crease Its emissions as a result of the construction oramount of material combusted. stored, or processed. operation of the major plant or major modification

Environmewi AKIxwoer 52

40

S-29SOUTH CAROLINA AIR POLLUTION RULES 506:0503

32. Smoke - Small gas-bornc and airborne particles 20 carbonic acidarising from a process of combustion in sufficient num- 21. ammonium carbonateber to be observable b) a person of normal vision under 22 metalhc carbides or carbonatesnormal conditions.

33 Solid Fuel- A fuel which is fired as a solid suchas coal. lignite and wood SECTION II - PERMIT REQUIREMENTS

34. Stack - AnN flue. conduit, duct, chimneN. or A. Construction Permitopening arranged to conduct an effluent into the open I. Applicabilitair AnN person who plans to construct, alter or add to a

35. Stack Height - The vertical distance measured in source of air contaminants, including installation of an.feet between the point of discharge from the stack or device for the control of air contaminant discharges,chimnex into the outdoor atmosphere and the elevation shall first obtain a construction permit from the Depart-of the land thereunder. ment. The Department may grant permission to proceed

36. Standard Conditions - 760 millimeters of mer- %Aith minor alterations or additions %kithout issuance of acur, at 25 degrees Centigrade. permit %hen the Department determines that the alter-

37 StationarI Source - Any building. structure. ation or addition %ill not increase the quantitN and Iillinstallation or process %,hich emits or may emit an air not alter the character of the source's emissionspollutant sub)ect to regulation by any, national or state 2 Permit Applicationstandard 1, se of the term "source" is to be construed to Construction permit app,,cations shall be revievedmean "stationary source" and signed by a professiona, engineer registered to prac-

38 "Total reduced sulfur (TRS)'" means the sum of tice in the State of South Carolina and shall provide, asthe sulfur compounds hydrogen sulfide, methyl mercap- a minimum, the following information.tan. dimethxl sulfide, and dimethyl disulfide. that are a. The name and location of the plant and its plannedreleased during the kraft pulping operation and mea- operating schedules:sured b% Federal Reference Method 16. b Sufficient description including phxsical and chemi-

39. Trade 4aste - All solid, liquid, or gaseous mat- cal properties of materials and processes necessary forerial or rubbish resulting from construction, building the Department to determine actual and potentialoperations. or the prosecution of an. business, trade or emissions;industr% including, but not limited to, plastic products. c Identification of all emission points;cartons, paint, grease, oil and other petroleum products. d. A description, including physical and chemicalLhemials and cinders, properties of all emissions.

40 Volatile Organic Compound (VOC) - any, chemi- e. A complete descriptior including engineering designcal compound containing carbon which has a vapor and operating characteristics of an, air pollution controlpressure greater than one-tenth (0.1) mmHg at standard device or system that is to be installed: andconditions excluding: f. Source information and calculations to demonstrate

I methane compliance with "Good Engineering Practice Stack2. ethane Height" rules: and3 1.1.1-trichloroethane (methyl chloroform)4 benzene g Other information as may be necessar for proper

acetonitrile e%aluation of the proposed Nourc 4s determined by the6 chloroform Department7. carbon tetrachloride Package-t.pe incinerators of 750 pounds, hr rated ca-8 ethylene dichloride pacity or smaller uhich burn type, 0 and I %astes as9 eih 1ene dibromide defined b) the Incinerator Institute of America and10 methylene chloride package-type boilers of 100 ,' l0 BTU/hr input capaci-II trichlorofluoromethane (CFC-1 I I I or smaller which burn natural gas or oil as fuel are12 dichlorodifluoromethane (CFC-12) exempt from the requirement that the construction per-13 chlurodifluoromethane (CFC-22) mit applications be prepared and submitted by a regis-14 trifluoromethane (FC-23) tcred professional engineer provided the proposed unit is15 trichlorotrifluoroethane (CFR-1 13) identical to a proto-type model %hich has been previous-16 dichlorotetrafluoroethane (CFC-1141 1\ dc,,igned or othermise certified by a professionalI' choropcntafluoroethane (CFC-1 5) engineer1 carbon monoxide B Operating Permit19 carbo, dioxide I Original

9-5-46 Pubitshed by THE BUREAU OF NATI _i:L AFFAIRS INC Wash"nglor DC 2' 3 53

-004 STATE AIR LAWS

A ,4ritten request to obtain an operating permit shall cable, in a manner consistent *ith good practice forbe submitted to the Department no later than fifteen minimizing emissions(15) days prior to placing an\ neA, increased or altered 4. Source, required to have continuous emission moni-source into operation tors will make quarterl) reports as specified in applica-

2 Renewal ble parts 6' the RegulationsPrior to the expiration date of a source's operating D. Exceptions

permit. the source Aill be inspected b, the Department I Upon request. the Department may alter operatingin order to decide vhether to renew the permit T' nast permits. compliance schedules, or other restrictions onrecord of compliance and future probabilit, of c npli- operation of a source provided that resulting ambient airance will be given appropriate Aeight in making the concentration levels will not exceed an\ national or statedecision regarding renewal ambient air qualitN standard. Factors to be considered

An\ special condition in a permit should be verified b) the Department may include, but are not limited to,during the inspection and specificall. mentioned in the technolog . economics. national energy polic\. and exist-report Any additional 'PO% s'ons that the inspector be- tng air qualit\. The request by the source must also showlie~es Aarrants inclu-sion r, ;h1 renewed permit are to be the followAing

clear!\ and corcisel\ stated in the inspection report, a Good faith efforts hase been made to compl\ withC Standard Permit Conditions the state requirements.All permits shall contain, in addition to such special b The source is unable to comply %,ith the state

cend:tion, a, the Department find, appropriate, the requirements because the necesa_\ techn.agyor otherfo!low.;ng standard condition5 alterntise methods of contro, are not rea5onabl\ aail-

able. or have not been available for a sufficient period ofI No applicable la .. regulation or standard A.ll] be ti econtraxened time.2ontravened lec Anx available operating procedures. or control mea-2 A ll o ff c ia l c o r r e s r vr d e n c e , p la n s .p e r m it a p p li c a -s r s e u i g t e i p c o h o r e o m i n i

tions and ritten statemeni, are an integral part of the sures. reducing the impact of the source or ambient airpermit concentrations. ha%e been implementedd The request is submitted in a timely, manner.

3 For sources not required to have continuous emis-

sion monitors, an\ malfunction of air pollution control 2. The provisions of this paragraph shall no, apply toequipment or system. process upset or other equipment mass emission limits which are imposed upon any sourcefailure which results in discharges of air contaminants by the follo,ing requirementslasting for one hour or more and which are greater than a. Federal New Source Performance Standards:those discharges described for normal operation in the b. National Emission Standards for Hazardous Airpermit application shall be reported to the Department Pollutants:within twenty-four hours after the beginning of the c. Federal or State Prevention of Significant Deterio-occurrence and a wkritten report submitted to the Depart- ration Regulations. or,ment within thirty (30) days. The written report shall d. Non-attainment requirements.include as a minimum, the followAing 3. "Where a permanent increase in the , isb'e emission

a The identit) of the stack and/or emission point limitation for a source is requested. the source must%%here the excess emissions occurred. demonstrate that it will remain in compliance with the

b The magnitude of the excess emissions expressed in applicable particular emission standard

the units of the applicable emission limitation and the 4 Any alternative compliance schedule shall provideoperating d;:ta and caculation, used in determining the for compl:ance \,ith the ap'icable reguz::_- a, expedi-excess emissions tiousl) as practicable. based on a plan submitted with

c. The tirne a id duration of the excess emissions the request for the alternatise compliance schedule.d. The identitx of the equipment causing the excess 5. An\ request under this section wili be subjected to

emissions. public notice and opportunit. for a public hearing. Upone The nature and cause of such excess emissions. approval b\ the Board. the recommendations of thisf The steps taken to remed\ the malfunction and the Department shall be sent to the Administrazor of the

steps taken or planned to prevent the recurrence of such Environmental Protection Agenc\. or his de.:gnated re-malfunction presentative. for approval or disapprova

g The steps taken to limit the excess emissions 6 Where alternative compliance schedule provisionsh. Documentation that the air pollution control equip- are contained elex here in the air so:lu10 control

ment proce-s equ!prr en:. or prc)csses were at all times regulations, those pro\isions shall supersede the require-

maintained and opera'ed, to the maximum extent pract- ments in this section

Enwronment Reporter

42

5-10

SOUTH CAROLINA AIR POLLUTION RULES 506-005

E Transfer of Ownership/Operation The emissions inventorN for all major plants .'Wkheneer the ownership/operation of a source has re'ie'ed annually Information required for this rr. tA

been transferred, the Bureau shall be notified by the new will include, but is not limited to, the followingowner/operator within thirty (30) days of the transac- A Information on fuel burning equipment.tion A transfer of the operation or construction permit B Types and quantities of fuel used;%kill be effective upon written approval by the C Fuel analysis;Department D Exhaust parameters:

F Exemptions F Ra-A process materials and quantities used.I No permits shall be required for the following G Design and normal process rates:

sources constructed prior to Februar II. 1971: H Hours of operation,a. Natural gas boilers. I. Significant emission generating poiits or proccs.esb Oil-fired boilers of 50 X 106 BTU/HR rated input J. AnN desired information listed in 40 CFR 51,

capacitN or smaller Appendix E (July 1, 1982)c Coal-fired boilers of 20 x 10, BTL'/HR rated input Ever even calendar year a ne, updated err:s- :,n

capaci% or smaller in'entorN %ill be completed bN the plant All app. -e2 No permits shall be required for the following information will be recorded on the current for.- >-r

sources reporting emission data.a Bolers and space heaters of less than 1.5 Y 10' Ir the intervening calendar ,ears. an\ ch -. : in

BTL HR rated input capacit\. emis-.on data %ill be recorded on the annual conr.._-ceb Comfort air-conditioning or ventilation systems inspection report.c Motor vehicles. The above requirements notskithstanding, an em:.nd Laboratory hoods. inxentorN ma\ be required at any time in ord- " toe Emergencx posker generators of less than 150 KW" de-erminc the compliance status of an\ plant

rated capacit,f Sources emitting only steam, air, nitrogen, oxygen. REGLLATION NO. 62.2

carbon dioxide, or an\ physical combination of these.g Sources Aith an uncontrolled particulate emission PROHIBITION OF OPEN BUiRNING

rate of less than 1 lb/hr and/or uncontrolled VOCemission rate of less than 1000 lbs/mo may not require Open burning is prohibited except as provided be;:-permits However. source information needs to be sub- A. Open burning of leat es. tree branches or 'ardmitted to the Department and a determination on the mings originating on the premises of private reside-esneed for permits %%ill be made. This determination %%ill and burned on those premises.take into consideration, but will not be limited to, the and bur o n oe premises.nature and amount of the pollutants, location, proximit) B Open burning in connection with the prepara::-to residences and commercial establishments, etc.C food for immediate consumption.

h Sources Ahose only emissions are fugitive must C Campfires and Fires used scel> forrecreation --

submit source information, and the need fo, permit(s) poses. ceremonial occasions, or human warmth

\kill be made b\ the Department on a case by case basis. D Fires purpose set to fored: lands for specific -:This determination will take into consideration, but will ma'aeement purposes in accordance with pr2..not be limited to. the nature and amount of the pollu- accep'able to the Department and as administere -"tants. 1.,cation. proxirnity to residences and commercial the South Carolina Forestr. Commission Such r-_-establishments. etc. men t practices shall include.

i Prescribed burning under existing standard- 7

SE("ION III - EMISSIONS INVENTORY various management objectives, and

Emissions nventor\ is a stud) or compilation of pollu- ' Site preparation burning for purposes of clear. -are.; for regeneration.

tant emissions. Emissions inventories are designed to E Fires purposel) set for agricultural contro; -.locate air pollution sources, to define the type and size of eases. weeds. pests and other specific agricultura .-sources, to define the type and amount of emissions from pose, in accordance "ith practices acceptable i.. -- eeach source, to determine pollutant frequency and dura- D--tmenr oi Health and En- ironmental (ontvtion. to determine the relative contributions to air pollu- F. Open burning of trees. brush, grass and c:- rtion problem, of classes of sources and of individual vegetable matter for game management purpo-e- 'nsources and to determine the adequacN of regulations accordance with practices acceptable to the Depar-:.-,and standards of Health and Environmental Control

11-29-85 PublIshed by THE BUREAU OF NATIONA, ArrAr-t INC Was,'wgior DC 203-43

506:1001

SOUTH CAROLINA AMBIENT AIR QUALITY STANDARDS

(South Carolina Department of Health and Environmental Control; Regulation 61-

62.5 - Air Pollution Control Standards; As last amended April 25, 1984; May 24, 1985;January 23, 1986)

CONTENTS may be exceeded for soot blowing: but SECTION II - PARTICULATEshall in no case exceed an opacity of sixty EMISSIONS

Standard No. I - Emissions from Fuel (60) percent. A. Allowable DischargeBurning OperationsStandard No 2 - Ambient Air Qualitv B. New Sources The allowable discharge of particulateStandards No one shall discharge to the ambient matter resulting from fuel burning

Standard No. 3 - Er:ssions from In- air from any source constructed on or after operations shall be limited to the values

cinerators February I'I, 1971, smoke which exceeds obtained by use of Figure l and/or Part B.

Standard No 4 - Emissions from Process an opacity of twenty (20) percent. For a (For the purpose of determining heat in-Industries total of six (6) minutes in one hour or put. total equipment capacity refers toStandard No. 5 - VolatileOrganicCom- twenty-four (24) minutes in a twenty-four total equipment capacity discharging

S r othrough each stack. If a boiler has morepounds (24) hour period, twenty (20) percent than one (1) stack the total rated capacity

opacity may be exceeded for soot blowing; will be the boiler rated capacity discharg-

REGULATION NO. 62.5 but shall in no case exceed an opacity of gAIR POLLUTION CONTROL STAN- sixty (60) percent. ig o ue burn eration of

DARDS Figure I for fuel burning operations of

C. Special Provisions 1300 million BTU per hour heat input andSTANDARD No. I The opacity standards set forth above do larger shall be accomplished by use of the

EMISSIONS FROM FUEL BURNING not apply during startup or shutdown, equation:OPERATIONS Owners and operators shall, to the extent E = 57.84 P-'"'

SECTION I - VISIBLE EMISSIONS practicable, maintain and operate an) where E =the allowable emission rate insource including associated air pollution pounds per million BTU heat input,

A. Existing Sources control equipment in a manner consistent and P = million BTU heat input per hour

No one shall discharge to the ambient with good air pollution control practices

air from any existing source constructed for minimizing emissions. In addition, the B. Special Provisions

prior to February I1, 1971. smoke which owner or operator shall maintain a log of All fuel burning operations of 10 million

exceeds an opacity of forty (40) percent. the time, magnitude, duration and any BTU per hour heat input and smaller con-

For a total of six (6) minutes in one hour or other pertinent information to determine structed prior to February I1, 1971 shall

t,Aent-four (24) minutes in a twentN-four periods of startup and shutdown and make be allowed 0.8 pounds per million BTU in-

124) hour period, forty (40) percent opacity a%ailable to the Department upon request. put.

FIGURE I1.5 - ___----__.

- 1 .0

.. 6

.. 5

.3 - .1

I5 . 00 500 1000 5000

TOTAL EQUIPMENT CAPACITY RATING (FUEL INPUT ONLY)MILLION BTU PER HOUR INPLT

4-18-88 PubliShOd Dy THE BUREAU OF NATIONAL AFFAIRS. INC, Washington. D C 20037 5544

506.1002 STATE AIR LAWS

SL(TION III - S L- R DIOXIDE .- , -, ,, i phan,, ith an_, applicable state air pollu-E\IISSO% S "iam,, , _ . i .... tion coliro! regulations and standards

P,. 0 S -111 S, L .' Ib SO. r ..:n 9 TL - 1I a boi 'c is fired on m ore than one

,A. General Al ... ... . .... . 3 . li hc t tal capacity will determine theThe maximum allowable discharge of ofabove requirement,

sulfur dioxide (SO i from fuel burning 1). Special Pro,,isionsoperations shall he in accordance Aith a ifit can bedemonstrated to th ,aisfa('-ent ir an . (":Uminuous Opacity Monitor ReportingSstemr of priorities as specified hereinafter tion of the Board that amlient air - Requirementsin paragraph B The classifications shall be dards 4i1 not be contravened b, a source. Reui rofdelineated on a count% basis. The max- alone or in combination xith other [hi ,xncr or operator of an) fossilimum alloable discharge for the various sources, a greater allowance for sulfur fiu-nrcd stcam generator subject to the

classes is specified in paragraph C of this dioxide discharges may be made on a promoris of Paragraph A of this Section

Sect ion case by case basis- shall submit a written continuous OpacityMonitor report to the Department at least

B. ('lassificatio, SECTION IV - OPACITY MO.NlTOR- quiv.crJ%, or more often if requested All

I The class into Ahich a given count, ING REQUIREMENTS q.,irtls, reports must be postmarked byfalls has been determined by mathematical the 30th da.s following the end of eachatmospheric diffusion models and other A. Applicable Sources calenddr quarter.methods which esaluate those factors I. Fossil Fuel Fired Boiler s The owsner The report shall include the followingwhich necessitate limits on sulfur dioxide or operator of any fossil fuel-hrcd steam minimum information.emissions These factors included but were generator ol more than 250 million BT( a A]l integrated six mnute opacit.no! limted to. (I) total sulfur dioxide per hour heat input capacit., shall install. mea.surements for periods during Ahichemissi)ns, (2) spatial di-trbution of sulfur calibrate. operatc. and maintain no later the applicable provisions of Section 1 havedioxide sources. i3) effect, of single. large than June 14, 1978. continuou, monitor- bee, exceeded. together with their naturesources. (41 existing. measured air qualits: ing system(s) for the measurement 01' and cause.(5) iopoeriPhical features of the counts: opacit\ which meets the performance b For periods of monitoring system(61 .,ntrminuions to bakground levels due specilications of Paragraph [) of this See- malf in.t:itnto .oure, outside the county being con- tion ex,.cpt "here: (0) The date and time identifsing eachsidtred. iC population densits. a. Gaseous fuel is the onl% fuel burned, period during which the monitoring s,-

2 The assigned cladsifications will be b. Oil or a mixture of gas and oil arc the tern oas inoperative, except for zero andre' ,-Ned periodicall % at intervals not to ex- only fuels burned and the steam generator span check,,.ceed three \ears. and changes will be made is able to comply with the provisions of (ii) The nature of monitoring systemas required When a counts is assigned to a Sections I and 11 of this Standard without repairs cr adjustments.more restrictive class, individual com- utilization of particulate matter collection (iiii Proof of opacity monitoring systemphance schedules wll he established in equipment, and where the steam generator performance may be required by the De-,.uch a "a% that reasonable time will be has never been found, through an) ad- partment Ahenever repairs or adjustmentsallowed for the source to make necessary ministrative or judicial proceedings, to be have been made.changes in equipment and/or fuel con- in violation of Section I of this Standard. c. boiler system repairs or adjustmentstracts c. The steam generator operates with an made to correct violations of the provisions

3 The following classifications arc annual average capacity factor of 30 per- of Section IAssigned cent or less, as reported to the Federal If no reportable incidents occur during

Class I - Charleston County Power Commission for calendar year 1974 a quarter, a report is also required indicat-Class II - Aiken County -Anderson or otherwkise adequately demonstrated to ing as such.

( ount\ the Department and has not subsequentl. 2 Alternative data reporting proceduresClass Ill - All ithers increased this factor to more than 30 ma be allowed if the owner or operator

C. Allowable Discharges percent show,, to the satisfaction of the Depart-

Sulfur dioxide emissions from fuel burn- 2. Vioodwaste Boilers The owner or ment, that these procedures are at least as

ing sources located in various counties operator of an) woodssaste boiler, not accurate as those describedwill not exceed the following limits: equipped with a sct scrubber, will be 3. The owner or operator shall maintain

(ICour:,e, .Id, I required to install, calibrate, operate and a file of all information contained in the

,, um AIlouabie Emision, dmaintain continuous monitoring system(s) quarter;, reports, calibration data for theRaied Snurce Szt li O- m on BTL nput approved by this Department for the me- opacty monitoring sstem(s). relevant re-

p , aB ncd , ,' , BTI hr 3 surement of opaeity, if it meets one or cords of anriustments and maintenance,-e-tie-'"m:! ..- Bmore of the following criteria performed on such system(sY and all other

a. Any woodwaste hoiler of at least data generated by the continuous opacity

,iaruo, . TLI5'u., 60.00) lb steam,'hr rated output monitorng s,tem(s), for a minimum of-:, ,-. b. An\ woodwastc boiler. regardles, of to e ars from the date of submission of

o . size. that has been operating in non-com- such rcpo-ts cr collection of such data

Environment Reporter 56

45

s9-I9

SOUTH CAROLINA AIR QUALITY STANDARDS 506 1003

The information contained on file must be V. Monitor tocation B ( owl-fired boilers greater than 50made available for res e% b, e)partment 'Ahen the effluents from t,,o or more I'(1 BT, hr rated inputpersonnel upon request affected steayn generators of sim;lar design (. A odwa,te. or combination wood-

C. Exemption from Reporting and operating characteristics are combined waste boilers greater thin 20 > 10'

Requirements before being released to the atmosphere. HBt 'hr iarcd npui

A temporarN exemption from the opa i- the opact, monitoring s ,si ,tc ii.j , l -, E -O \ 1 -- SO! R (E TEST

ts monitorng and reporting requirements installed on the combined effluent When

of thisSection ma, be granted duringan the affected steam generators are not of REQ-IREMEN I-SA. The owner or operator required to

period of monitoring srstem( l malfunc- similar des g r and operating comply with Section VI above shall con-tion. provided the owner or operator ohaactests o enthe eento duct such tests as required bs the Depart-sho,. t, the sat-sfaction of the Depart- one affected steam generatoris releasedto ment in order to demonstrate compliancement, that the malfunction "as un- the atmosphere through more than one with this Standard EPA test methods orasoidahle and is being repaired as ex- point, the owner or operator shall apply such alternative methods as approved bypeditousl. as posihle for an alternate prucedure to compls Aith the Department prior to testing

the requirements of this Section Tests shall be conducted while theD. Eluipment Pe rformance Sicifictions F. Exemption's from Monitoring source is operating at the expected maxi-

The continuous opacit, monitoring Requirements mum production rate or other productionsystenis) required by Paragraph AI of %khenorer the requirements for ,-:inuous rate or operating conditions which wouldthis Section for fossil fuel fired steam opacit,, monitoring cannot be im- result in the highest emissions An, pro-generators shall conform with the per- plemented b the owner or operator due to duction rate less than rated capacity mayformance specifications set forth in 40 physical plant limitations, extreme result in production limitations on theCFR. part 60. Appendix B. Performance economic burden. or infrequen: steam permits.Specification I which is incorporated b, generator operation of less than 30 days All tests shall be made b%. or under thereference as a part of this Standard except per year. or when the specified monitoring direction of. a person qualified by trainingthat where the term "Administrator is procedure would not provide accurate and 'or experience in the field of air pollu-used the term "Department" shall be sub- opacit. determinations. alternate monitor- lion testingstituted In addition, the opacit, monitoring and reporting requirements ma% be B An\ soure om nor or operator pro-Inc s,tem(s) shall complete a minimum aprosed on a case-by-case basis provided posing to conduct tests in accordance withof one cycle of operation for each succes- the owner or operator submits a written paragraph A ab,,e shall notif\ the De-sive 10-second period: be installed such reque.st to the Department whic- inJudes, pariment in the manner set forth below ofthat representative measurements of opac- but not limited to the intent to test, not less than two weksit from the affected steam generator are I The basis of reason(s) tha: alternate before the proposed initiation of the testsobtained: and have an instrument span of requirements are necessars. so the Department ma, observe the test ifapproximately 80 percent opacity 2 A proposal of the alternate monitor- it desires to do so

The owner or operator shall record the ing and reporting requirements. and Notification shall include the followingzero and span drift in accordance w\ith the 3 Any other information needed by the minimum information'method prescribed h the manufacturer of Department to make a determination that I the purpose of the proposed test.such opacit\ monitoring s.stem(s); sub- the alternate requirements are adequate to 2 a description of the source to beject the s.stem(s) to the manufacturer's meet the intent of this Section testedrecommended ero and spai check at least SECTION V - EXEMPTIONS 3 a descriptior, ol the test procedures.once dai e unless the manufacturer ha, The following sources shall be exempt equipment. and s .mpling sitesrecommended adustments at shorter n - from the provisions of this standard. 4 a timetablc. setting forth the dates ontorsall, in which case soch re.cimenda- A Residences of four families or less. which the tetine will be started andions hall hec folloed. adiust the zer', and B Ocean-going sessels actuali. engaged concluded

span '.,,honorer the 24-hour ier,. drt~i or n the physical process of nationa! or inter- ( The finaltes results must be submit-24-ho,,ur c,fid'ri, drit limit,, 4i(C|FR. national trade or defense ted no later than 30 days after completionPart 6). -\ppendix B. Performance Speci-fic.ion I are exceeded: adjus, the opa,:' 'F(1 ION \I - PFRIODI( TESTING of the on-site testing, containing as a mini-monitoring si.stem(s) purchased prior to Scheduled periodi, tests for par:iculatcs mum, the followingSeptember II. 1974 A.heneer the 24-hour Aill be required of the sources listed below I process \eAight rates Ib hr)zero drift or 24-hour calibrati,,n drift ex- escr', two years. or as required b,% permit 2 process design and load rates atceeds 4 percent opacit' for those genera- conditons to demonstrate compliance w ith which the test wa#. conductedtors construoted prior t, F-ehraars, I. thi- Standard Compliance Ait sulfur 3 procedure used for determining pro-19-1 and 2 percent opacits for those dioxide will be b, ource testin ontnu- cess weight raite,general,,rs ,,nstructed after F ehrars, ou, minitorine. or fuel anal.,I, as re- 4 calculation, udcd to determine pro-I 1. 19-I quited by the permit condition, ces, weight rate,

The monitoring systems must be ap- A (il-tired boiicrs greater th.:- 250 .1 signiturc responsible compan.procd h. thi, agenc prior iti installation 1i) BTI hr rated ;nput ,lihl

4-18-80 Publ,00e1 by T-4E B REAU Or NATOI AL AFFAIRS IN Waslngtor' D C 20037 57

46

506:1004 STATE AIR LAWS

D. The o'~ner or operator proposing a dures or requirements maN be grounds for minutes in an'. one hour or twentN-foursource test under the prossons of this not accepting the tests (24) rninUIC' In ai isents-1our hour PerFodsccion shall be responsible for pros iding STANDARD NO. 2 C Odors from the incinerator shall he

I sampling ports. pipes, lines, or appur- AMBIENT AIR QUALITY STAN- reduced to such a level as not to create anicnanccs for the collection of samples and I)ARI)S undesirable leveldlita required b\ the lesit procedure The follow~ing table constitutes the am- D. Emissions shall not contain in-

, safe acces;s to the sample and data bient air quality standards for the State of wulpries hchaeufcit%collection losations South Carolina. The analytical methods to laree as, to he visible a-, individual particle's

Ilight. clectrici!s. and other utilities be used wAill be those applicable Federal a eeiso on raeo uhszrequired for sample and data collection Reference Methods published in 40 CFR an aueisio oin r arel of siuchf s

51. Appendices A-F. In the case of incandescent particle,- This, reqUirrmentE Any proposed deviations from the fluorides either the double paper tape shall onl% applh if particles fall on real

pricedures ind requirements stated abos e sampler methods (ASTMD-3266.73T) or proper[% ot .her .than tha! of the personmiust be thkoriughl\ explained and mut be the sodium bicarbonate-coated glass tube -ern befrieeiso.ipprosed In this Decpartment prior to test- and particulate filter methods IASTM- epnil frteeisoIn_, Failure 1, o~bserse an\ of these proce- 3268-'!T) mas he used TNDR NO4

EMISSIONS FROM PRO( E55 IN-MEASt*RING MICROGRAMS CUBIC METER D( S-1 Rlll -

POL'T-NT INTERVAL (1)(2) SECTION I - GENERAL.

SlurDi'ie3 hour l300 (4) A The miehod Ashih is, apprk'.ed b%.24 hours 365 (4) the Department for determining. comnpi-annual 80 ance w~ith opacits limitations under ithis

_______________________________________________________________Standard is ! PA Reference Mvethod 9 (40Suspended Particulates 24 hours 2503 CFR fi0. Appendix A. al revised July 1,

annual G.M. (3) 60 1984) *Xternate methods m."s be utilizedon)N it apoeinavnt Nthe Depart-

Carbori 'slriside 1hour 40 mg per cubic meter -en approvte Einrdoncena Prtcto8 hour 10 mg per cubic meter Agene'. .

B This standard %% ill not supersede anNOzo ne I hour 0. 12 ppm (5) requirements, imposed by Federal Ness

______________________________________________________________Source Performance Standards, NationalGaseous Fluorides 12 hr. avg 3.7 Emission Standards for Hazardous Air

(as H F- 24 hr. avg 219 Pollutants. Federal or Statn Prevention ofI wsk avg. 1 .6 Significant Deterioration Regulations, norI mo. avg. 0 8 special permit conditions, unless this

Standard would impose a more restrictiveNitrogen Dioyide annual 100 emission limit.

____________________________________________SECION 11 - SULFURIC ACID

.cad Calendar Quairterl% 1.5 MANUFACTURING

Me an A. The rate of emissions of sulfur diox-ide from sulfuric acid manufacturing shaltbe limited to no more than 4 pounds of

I ) Arithmectic .-\s~erage except in ease of suspended particulates sulfur dioxide per tori of 100'r- sulfuric(21 At 25 C and -60 mm Hg. acid -roduced and emissions of acid mistI.; Geometric Mean 1 0. pounds of sulfuric acid per ton ot(4) Not to be exceeded more than once a year 0?acdpoue

15) Not to be exceeded more than one day per year B. The maximum allowsable stack outlet

SrANDARD NO. 3 pounds per million BTt of heat input to, opacit, from an,, source under this eate-

EMISSIONS FROM INCINERATORS the incinerator, excluding auxiliar) fuel gorN in 20'SECTION Ill - KRAFT PVLP AND

All incinerators shall operate within the IPAPFR MANUiFACTI. RINGfollow~ing emission limitations- B Emissions shall not produce smoke The rate of emission,, from kraft pulp

A. Particulates in the flue gas discharg. w~hich exceeds twenty (201 percent opacit ' and paper manufacturing shaill be limiteded into the atmospherc shall not exceed 0.5 for an aggregate of more than ,iN 16) to the follossinr.

Maximum Maximum allowable emni-.-ion otallowable particulates in poundsiequisaleni toni

Stack Qpi9j! of air dried. unbleachedjrulfprrodu.cd

RecoserN furnace 40% 2 75Dissolving Tank 207 ) 0l ime Kiln 207r 1 0

Environment Retporte. S

47


48

APPENDIX D

Building 403, Steam Boilers 2, 3 and 5 Field Data

49


5o

4 Iz

-rz2

-J Li

W W

H I

I- I!<K-i-

- .- S.,

z 'A10 cc

Luo

cr

Li m

Z I F,z ei___ 2- W

- u51-

PRELIMINARY SURVEY DATA SHEET NO. 2(Velocity and Temperature Traverse)

BASE DATE

BOILER NUMBE

INSIDE STACK DIAMETER

/Z InchesSTATION PRESSURE

STACK STATIC PRESSURE

iIn H20SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN H2D ' -/Ci-;IC STACK TEMPERATURE (OF)

_________3_ 7>S2L

AVERAGE

OEHL FORM 16 5I ~P 78 52 II I~ ••[ llI

AIR POLLUTION PARTICULATE ANALYTICAL DATA

BASE DATE RUN NUMBER

BUILDING NUMBER SOURCE NUMBER

PARTICULATES

ITEM FINAL WEIC.HT INITIAL WEIGHT WEIGHT PARTICLES(am) " (A) (am)

FILTER NUMBER

ACETONE WASHINGS (Probe, Front

Half Filter)

BACK HALF (it needed)

Total Weight of Paticulates Collected

II. WATER

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT WATER

(wg")(MPIN)ER 1(7120) .I

IMPINGER 3 (Dry),M INGR ,2 ,,,20 ,) 0 0 .- 2 0 , o

IMPINGER 4 (Sillca Get)

Total Weight of Water Collectedam

Ill. GASES (Dr-y)

ITEM ANALYSIS ANALYSIS ANALYSIS ANALYSIS1 2 3 4 AVERAGE

VOL % 02

VOL % CO

VOL % N2

V1% N2 = (100% % CO 2 . % 02 % CO)

OEHL FORM' 20MAY 78 53

0 c- -

CI. - 0

02I- cr JXC

w I- 0 xo

0 w

m m< 0 -

x IL 0, z 0 0~

wul 4--.

I

AW W

N 4''j 2-70 I N.<

- - - - - -

uj 0x: t

I- 5-,

o _/-------------------------------------------------------------------------------4u~ IiL

~2 0 w~~

J

'Cl w

>

I --__ - - -

allI

-~u

f-c0

®r- i I

04U

2 32£ w -. 51. -- 0 - -z~~ z zI u

z < 0

'UO

540

PRELIMINARY SURVEY DATA SHEET NO. 2(Velocity and Temperature Traverse) "O°')

BASE DAT

BOILER NUM, ~ 6 ~3

INSIDE STACK DIAMETE

J2, 5_ 5' InchesSTATION PRESSURE

'3 2 In HgSTACK STATIC PRESSURE

In H20SAMPLING TEAMcE'g L ,_ 2

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN H2 0 , STACK TEMPERATURE (OF)

__ __ _ ___ ____ _ ,,_. _5 55

AVERAGE

OEHL FORM 655APR '78

... . .. ... ma i n n _ _Iun mlm m_ l ll I 3 II

PRELIMINARY SURVEY DATA SHEET NO. 1

(Stack Geometry)

BASE PLANT

,594Wu93 B t- 1 9 0DATE SAMPLING TEAM

SOURCE TYPE AND MAKE

SOURCE NUMBER INSIDE STAC DIAMETERI /if Inches

RELATED CAPACITY 1T PE FUEL

DISTANC5 FROM OUTSIDE OF NIPPLE TO INSIDE DIAMETER

3 Y/ InchesNUMBE OF TRAVERSES NUMBER OF POINTS/TRAVERSE-

LOCATION OF SAMPLING POINTS ALONG TRAVERSE

PERCENT OF DISTANCE FROM TOTAL DISTANCE FROM OUTSIDE

POINT DIAMETER INSIDE WALL OF NIPPLE TO SAMPLING POINT(Inches) (Inches)

1 0 ," 41 .

2 // , / 3.

OELFORM I

0ELAPP70 1 56

/IIo m_ _iil_ l_ _I

e _ _ _ __im_ _ l _




PARTICULATES

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLES(a#m) (am) (wi)

FILTER NUMBER

ACETONE WASHINGS (Probe, FrontHalf Filter)

BACK HALF (It needed)

Total Weight of Particulates Collected

II. WATER

ITEM FINAL WEIGHT INITIAL WEIGHT [ WEIGHT WATER

(a) (am) (9-)

IMPINGER 1 ff12fO) -

IMPINGER 2 (H-20) 2qZ

IMPINGER 3 (Dry)

IMPINGER 4 (Silica Get) 29

Total W*Ight of Water Collected "7

Ill, GASES (Dry)

ITEM ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVERAGE1 2 3 4

VOL 2. 7,2- 7,2 7 t 7, L

VOL CO

VOL N 2 I

Vol % N2 = (100% - % C%2 . % 02 .% CO)

OEHL FOR" 20MAY 76 57

7! -

In f _

InI M

'o -C

-z w w -

U 0c- c'0 c

w

> -4S

ww U,

1U 0

00In 00a.

CI

j cir-K

C~ 0 .I4I0 0. - 2

-~~ ~~~~~ ! - - - - - - -- - - - - -

>58

PRELIMINARY SURVEY DATA SHEET NO. I(Stack Geometry)

BASE PLAN (t

DATE SAMPLING EA

SOURCE A D M

A\

S EU ER TNsD-) S CK DAMEE

- -- InchesRELATED CAPACITY TYPE FUEL

DISTANCE FROM OUTSIDE OF NIPPLE 0 INSIDE 'IAMETER

I C-7 C 11InchesNUMBERNUMBER OF OINTSTRAVERSE


PERCENT OF DISTANCE FROM TOTAL DISTANCE FROM OUTSIDEPOINT DIAMETER INSIDE WALL OF NIPPLE TO SAMPLING POINT

(In c es) (Inches)

_ _1,( 4_3"3, , 97,2

Is

OEHL FoRmM 15A PR 1= 59


aASE DATE

BOILER NUMBER

INSIDE STACK ETER

STATION PRESSURE

In HgSTACK STATIC PRESSURE

- In H-20SAMPLING TEAM

TRAVERSE POINT\NUMBER VELOCITY HEAD, Vp IN H2D V STACK TEMPERATURE (OF)

AVERAGE

OEHL AORM 16 60AP 78 6

AIR POLLUTION PARTICULATE ANALYTICAL DATABASE DATE RUN NUMBER

dUILDING NUMBER - SOURCE NUMBER

I ( I PARTICULATES , _

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLES(gu?) (grn) (0r.)

FILTER NUMBER


BACK HALF (If needed)

Total Weight of Partlculates Collecteda

WATER

ITE. FINAL WEIGHT INITIAL WEIGHT WEIGHT WATER(81m) (am) (gr)

III (H20) S47 2D0 0IMPINGER 2 (H.R0)

AG 12

IMPINGER 3 (Drn

IMPINGER 4 (SitIce Get)

Total Weight of Water Collected ~7

I II. ~~~~GASES (Dry') _________

ITMANALYS!S ANALYSIS ANALYSIS ANALYSIi AVERAGE1 2 3 4

VOL '- CO 2

VOL" 0 2

VOL % CO

VOL % NZ

Vol% N2 m(100%.CCO2 . % 0 2 . % CO)

DFORM 65AMD Eee 4 651 REPLACES OEHL 20, MAY 78, WHICH IS OBSOI.ETE

61


62

APPENDIX E

Building 611, Steam Boiler Field Data

63


64

-L*-

.:~~~ 21 r 1 7~-

a. a. 2* u

Il -" 'Al 0C Ic-

2I~~1u____

a .Lo

00

-0,

LL D

Lfl < 0 - -r

d IU

A 0W C~L~

WUi I J -zU <

JJ

-

CL 0.65


BASE PLANT

DATE MLNG.

SOURCE TYPE iD MAKE

SO RCE NUMBER INSIDE STACK DIAMETER

I i 21) C Inches

RELA'E0 CAPACITY YPE FUEL ~

DISTANCE FROM OUTSIDE OF NIPPLE TO INSIDE DIMETER .

NUMBER OF TRAVERSES NUMBER OF POINTS/TRVERSE



(Inches) (Inches)

2 _ ___ __123 15'(0? !2~1,3 /;

OEHL FOR M 15APR 76

66


B ASE DATE

BOILER NUMBER (6 - f. JINSIDE STACK DIAMETEI c

Inches

STATION PRESSURE

In Hg


• In H20

SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN H20 04 STACK TEMPERATURE (OF)

I 2_

AVERAGE

OEHL FORM 16 67APR 78



BUILDING NUMBER SOURCE NrBER

PARTICULATES

ITMFINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLESITM(9m) (901) (aml)

FILTER NUMBER


II. WA TERf

ITMFINAL WEIGHT INITIAL WEIGHT WEIGHT WATERIT M(00) (400) (1110)

IMPINGER I (1120) 2o .2c ic9

IMPINGER 2 (H120) ()4

IMPINGER 3 (Dry) i

IMPINGER 4 (Silica Gel) o

Total Weight of Water Collected

Ill. GASES (Dry) __________ _________

ITEM ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVERAGEI2 3 4

VOL % CO 2

VOL % 02

VOL % CO

VOL %. N2

Vol % N2 R (100% CO 2 01O . CO)

ADFEB64, 651 REPLACES OEHL 20. MAY 76. WHICH IS OBSOLETE,

68

APPENDIX F

Building 922, Hot Water and Steam Boiler Field Data

69

(this page left blank)

70

10 .

Li 0 - 0 I

F.. I AX1I 4

0~ 14X-f-i

4 v~ ~N

0

CN

w<

in z ____ V

_L U.LL0 U

4r I

z i

4 ~ I. L - -- - --- ----


BASE APLANT

zsL4w o W,~DATE SAMPLING TEAM

SOURCE TYP F A QJMAKE . .. '.

SOURCE NUMBER [INS IDE STACK DIAMETER

1 91Inches

RELATED CAPACITY TYPE FELiDISTANCE FROM OUTSIDE OF NIPPLE TO IN E DIAMETER

-"

17 PInchesNUMBER OF TRAVERSES NUMER OF POINTSITRAVERSE



POINT DIAMETER INSIDE WALL OF NIPPLE TO SAMPLING POINT

(Inch es) (In ch e a)

I __ _ ,5

4 __ __ _,__ __ __7,5'

OEHL FORM 15APR 76 72


BASE OATE

B3OILER NUMBER


Inches

STA ION PRESSURE


In H2OSAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN H20 STACK TEMPERATURE (OF)

C)

AVERAGE

OEHL FORM 16 73OELAPR 78 1




PARTICULATES

FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLESI T E M ( ) (g) ()

FILTER NUMBER

ACETONE WASHINGS (Probe. Front

Hall Filter)



11. WATER


IMPINGER I (H20) Z ,0 2

z 7,IMPINGER 2 (H20) 2-0i?).

IMPINGER 3 (Dry) 9IMPINGER 4 (Silica Gel) zo0

Total Weight of Water Collect.d

Ill. GASES (Dry)

ITEM ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVERAGE2 3 4

VOL % CO 2

VOL % 02

VOL % CO

VOL % N2

Vel % N2 a (100% .C0 2 . %0 2 .% CO)

AMD SM4 651 REPLACES OEHL 20, MAY 78. WHICH IS OBSOLETE.

74

0. -I-dZ .

2 I t Ixp I

CL. a. a

LU~~ 7n 01OIj -'I >'

I- !

z CL

Cy- -- I __ _ _

ui Q-~I~LaJ~

-j0 x

i w(L xV j co .24.K. - - --- -- 4-]-F7F- irT75


B ASE PLANT

DATE SAMPLING TEAM

SOURCE TYPE AND AK

S CEUMBE STACK DAMER

~s97c ,,o,, ,. q.5 InchesRELATED CAPACITY

T Y' ;

DISTANCE FROM OUTSIDE OF NIPPLE TO INSIO DIA;ZT

NUMBER OF TRAVERSES NUMBER OF POINTS/TRAVERS



(Inches) (Inches)

z ,2 '--t5, 7

___ 15_76

OEHL F'. 15 76


3AS (Velocity and Temperature Traverse)

!n UI'-(INSICE STACK DIAME E P , - 5I

c e

S.7ION PREL3RE 77 e3 -

jTACK Z7A-IC PRESSURE

SAMPLING TEAAI

2

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN H20 C STACK TEMPERATURE (OF)

_ _ _- - _ - _ -_ - _ ----------------

71

__ _ _ _ _ _ _ __ _ _ _ _ _ _ _ __ _ _ _ _ _ _ __ _ _- -v _ _ __ _ _ _ _ _ _

-- -- - - - -. - ..... .. . .. .... ..... ..... .... ... -- - - - --

-_______ .... ... . ... _____________________ _______________ ..... ... . ... .... . .... .

- _'- - -__i- -- - -

-- _--.--------- --- _-.- _ -_-----------------t------ ------------- -- --

_________ -- AVERAGE I--------------------------OEHL 'P 16 , ,i



BUILDING NUMBER dy~ SOURCE NUMBER

I. PARTICULATES

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLES

iLTEq NuMBER

AZETONE *ASHINGS 'Probe, Front.Lalf Filter)

SACK HA..F (It needed)

Totul Weight of Particulatet Collectedalm

WATER

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT WATER(gin) (9,,) (gra)

.MP!NGEP I (H20?%c

U,.,,,, G, ER 21 ,0) -- ,

:mpiNGER 3 'DI-;

IMPIN' ,ER 4 (Silica Gel) I~i-ij)LL.Total Weoght of Water Collected))

II. GASES (Dry)

! ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVERAGE1 2 3

'C___________ ____-- I

V.5 .. C2 I

i'D. '. CO

2I

Val % N 2 = (100%. % CO 2 . % O - % CO)

MD FES Ba 651 RFPI-ACES OEHL 20. MAY 76. W-ICH IS OBSOLETE

78

APPENDIX G

Building 1046, Hot Water Boiler Field Data

79


80

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PRELIMINARY SURVEY DATA SHEET NO. 1(Stack Geometry)

BASEPLN

OA IE SAMPLING TEAM

--7SOURCE .PE AND I E

SOURCE NUMB3ER INSD SACK DAMER

RELATED CAPACITY I TYPFIUhL

DISTANCE FROM OUTSIDE OF NIPPLE TO INS4OE OIAMETE

75- k°, ee(- I" o I .OA,. ,75 InchesNUMBE A OFTAESESNUBRO ITSRAEE



(tnches) (Inches)

(.,(a -3._ _ _ _ _ _ _ _ _T-3

OEHL '-0 RM 1AIR 7l 82

I L I __ __ _ __ _ __ 0


BASE D / AT

E


1 5" dInchesSTATION PRESSURE


-, 06-51In H20SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN H20 /Vp STACK TEMPERATURE (OF)

5 _ _ _ _,

14 6

AVERAGE


AR POLLUTION PARTICULATE ANALYTICAL DATA


BUILDI NG NUMBER U SOURCE NUMBER

PARTICULATES


(a-n) (Ur) (a1)

FILTER NUMBER


BACK HALF (if needed)


II. WATER

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT WATER(en) (s"n) (urn)

IMPINGER I (H,20) zf0 5s, 2

IMPINGER 2 (H20) C)o.

lURING ER 3 (Dry)

IMPINGER 4 (Silica Ge)7


II1. GASES (Dry)

ITEM ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVERAGEI 2 3 4

VOL % CO 2

VOL % 02

VOL % CO

VOL % N2

Val %N 2 z (100%. %C0 2 % 02.% CO)

AMD Fm,, 651 REPLACES OEHL 20. MAY 70, WHICH IS OBSOLETE.

84

APPENDIX H


85

, n , m ,n I II I


86

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DATE SAMPLING TE&"

Z3 __ __ _ __ __F__ __ _ __ __ _

SOURCE TYPE J A K

SOURCE NUMBER INSIDE STACK DIAMETER

1 975-InchesRELATED CAPACITY YP FUEL,

DISTANCE FROM OUTSIDE O( NIPPLE TO INSIDE DIAMETER

ON 2- Inches

NUMBER OF TRAVERSES ' NUMBER OF POINTS/TRAVERSE




(In ch ee) (Inchea)

0EHL Fogm 15 8APRI 88

II__ I _ _ _ __ _ _ _ _ _


(Velocityv and Temperature Traverse)I

BOILER NUMBER

T6INSIOE STACK DIA '!E ER

IceSTATION PRESSURE


- I In H20SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN 1420 STACK TEMPERATURE (F

2 35

_ 15

AVERAGE

' OEHL FOM 16 89APR78



BILDING NUMBER SOURCE NUMBER

7. PARTICULATES

I FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLEST(g ) (gin) (am,)

FILTER NUMBER



Total Weight of Porticulates Collected

11. WATER


(am) (071) (ga)

IMPINGER I (H20)

IMPINGER 2 (H20 P,14-,) , 4-

IMPINGER 3 (Dry) C

IMIG R4 (5m~ca e) Zo o ' -Total Weight of Water Collected

Il. GASES (Dry)

ITEM ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVFRAGE1 2 3 4

VOL % CO2

VOL 0 2

VOL % CO

VOL %N 2

Val MN2 a (100%. 1 CO 2 . ,02 . C3)

AMD Ft 651 REPLACES OEHL 20. MAY 78. WHICH IS OBSOLETE.

90 ..

APPENDIX I


91


92

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SOURCE NUMBER INSIDE STACK DIAMETER

RELATED CAPACITY TYPE FUEL

DISTANCE FROM OUTSIDE OF NIPPLE TO INSIDE DIAMETER

0 Iches

NUMBER OW TRAVIt-S N"UJER OF hOINTS/TRAeERSE



(In c ea) (In cd es)

4 3.__ L_ __ 3,__ __2-__

OEHL Fo" 15 94APR 711


BASE IDATE

BOILER NUMBER


t .Inches

STATION PRESSURE


In H20

SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD. Vp IN H20 STACK TEMPERATURE (4)

5 2_. . ... _

(7~6

AVERAGE

OEHL FORM 16 95APR7




1. PARTICULATES

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLES(9-) (gui) (gu)

FILTER NUMBER

ACETONE WASHINGS (Probe, FrontHall Filter)


II. WATER

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT WATER(901) (am) (am)

IMPINGER 1 a120)o 23a .3oo9 ,IMPINGER 2 (H20) oc~ Q0~ f

IMPINGER 3 (Dry)

IMPINGER 4 (Silica Gel) 2 -c

Total Weight of Water Collected (II. GASES (Dry)

ITEM ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVERAGEt 2 3 4

VOL % CO 2

VOL % 02

VOL % CO

VOL % N 2

Vol % N 2 " (100%- S CO 2 . %0 CO)

AD FEB 94 651 REPLACES OEHL 20. MAY 78, WHICH IS OSSOLETF.

96

APPENDIX J

Building 1200, Steam Boilers 1, 2 and 3 Field Data

97


98

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BASE Dtk)jATE

BOILER NUMBER


A.3 InchesSATION PRESSURE

__ _ __ _ __ _ __ _ __ _ -I _ _ __ _ _ _ In Hg

S§TACK( STATIC PRESSURE

- " 0iIn H20

SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN H2p (I ? STACK TEMPERATURE (OF)

!, ,. .. -17 C

(a 3 ____3_ L

'"I 43c(

_________ _______ ,_,t.- /0 _ _ _ _ _

AVERAGE




SI)uz ,fl / 2 '9&-) F"7BUILD'-4G NUMBER SOURCE NUMBER

* 3L DC-/ 2ooPARTICULATES


FILTER NUMBER


Half Filter)


Total WeIght of Partlculates Collected

II. WATER

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT WATER(8im) (am) (am)

IMPINGER 1ITJ120) 2-00 0

IMPINGER 2 2 (,20) 2-O,

IMPINGER 3 (Dry)/ /

IMPINGER 4 (SIc Get) -

Total Weight of Water Collected sS *Ill. GASES (Dry,)

ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVERAGE1 2 3 4

VOL ' C02 (,S ' z__ __ _ _ __ __ __

VOL %02 / cy/ 'L'VOL " CO

VOL N2 _2 _/

Vol % N 2 (100%. % CO 2 . %02. % CO)

OEHL RMY 20 101

I-i

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BASE DATE

BOILER NUMBER U3

AVN0 VP


Ice

*ATION PRESSURE

).-q, 4 SIn HgSTACK< STATIC PRESSURE

,W 1 In H20SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN M2 -- STACK TEMPERATURE (OF)

AVERAGE

OEHL FO 6 - L16

03



.D4I ..(ki*-F--Lz j /BUILDING NUMBER SOURCE NUMBER

I. PARTICULATESITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLES

ITM(di"e) (gn) (ci)

FILTER NUMBER


Hall Filter)

BACK HALF (ifneeded)

Total Weight of Particulates Collectedgm

II. WATER


IMPINGER (120) 1 22=0 62,D

IMPINGER 2(0 20 .ZoO2

IMPINGER 3 "5 0"Dry"

IMPINGER 4 (Silica 0et)2.6


IIl. GASES (Dry)


VOL % CO 2

VOL % 02

VOL % CO

VOL % N2

Vol %N 2 a (100%.%CO2 . %0 2 . %C0)

OEHL FORM 20 104MA Y 71

zz

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PRELIMINARY SURVEY DATA SHEET NO.. 1(Stack Geometry)

BASE PLANT

DATE SAMPLING TEAM

SOURCETYRE AN MAkq

SORCE NUMBER INSIDE STACK DIAMET

Iq - 1AR.0) Inches


DISTANCE FROM OUTSIDE OF NIPPLE T INSIDE DIAMETER

3 f(3.q \ nchesNUMBE A OS POINTS/TRAVmum


PNPERCENT OF DISTANCE FROM TOTAL DISTANCE FROM OUTSIDEPOINT DIAMETER INSIDE WALL OF NIPPLE TO SAMPLING POINT

(in ch ee) (lnches)

S-3

'-( 3,( 0,57.____ __ ,9

7 '112 ,57

OEHL FORM 516I ~P m76l 106 I~ III III

""m


BASE DATE

BOILER NUMBER

INSIDE STACK 0eI&ETER

STATION PRESSURE' nhe

Z,4_l In HgSTACK STATIC PRESSURE

0 In H20SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN H20 STACK T!:,P'!RATURE (OF)

2-t5 2053 125 -37

5 _-__ _ _ _ _ _-

& . .,1 1 33g

,03 15 )3o_,o1-3 305

AVERAGE

OEHL FORM 16APR s --107.



BUILOING NUMBER IJOURCE NUMBER

PARTICULATES

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLES(gom) (lm)

FILTER NUMBER


BACK HALF (I needed)


II. WATER

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT WATERITM(9011) (AM) (am)

IMPINGER I (7120)

"MP°GE 2 (H20) 20 0,0 C

IM G R3 (Dry) 1 6

Io , ,4 (Silica 0 2G0el 0

Total Weight of Water Collected:. am

Ill. GASES (Dry)


VOL % CO 2

VOL % 02

VOL % CO

VOL % N2

Vol %N 2 (100%- %CO2 .%02 . % CO)

OEHL FOm8 20 108MA Y -

APPENDIX K


109


110

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01


(Stack Geometry)

BASE PLANT

DATE SAMPLING TEAM


SOUCENUBE INSIDE STACK DIAMETER

SO CE NUMER SA AM3x Inches


DISTANCEFOM OUTSIDE OF NIPPI-TOENSE DIAMETE

i IN I Inches-NUMBER OF TRAVERSES NUMBER OF POINTS/TRAVERSE



(Inches) (In ches)

z_1,5 4,7

2 2. 7,7

5 12,_ 1246

OEHL FoRn 1511APR 70 112 ,


BASE DATE

BOILER NUMBER

INSIC;E STACK CIAMETf :R

STATION PRESSURE


- ,005 In H20

SAMPLING TEAM


0A0

5 .01_ _ __ _ _

AVERAGE

OEHL FORM 16APR 78 113


BASE *Jr ~RNNMBER

BUILOING NUMBER SOURCE NUMBER

PARTIUAE

ITMFINAL. WEIGHT INITIAL WEIGHT WEIGHT PARTICLES

FILTER NUMBER


Hall Filler)

BACK HALF (it needed)

Total Weight of Particulates Collected'am

II. WATER

ITEM FINAL WEIGHT I INITIAL WEIGHT WEIGHT WATER(amn) (a-) (1110)

IMPINGER I (7120) ? 0 O ,,LS4

IMPINGER 2 (H120) 3-00 Vr\LS

IMPINGER 3 (D ry) 0

IUPINGER 4 (Silica Oel) 2 ,oSc- o~ c

-- Total Weight of Water Collected

Ill.________________GASES (Dry)

ITE ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVERAGEITM12 3 4

VOL % CO 2

VOL % 02

VOL % CO

VOL % Na

Vol % N2 (100% - % CO2 . 02O % CO)

OEHL FOR ' 2014MAY76 11

APPENDIX L


115


116

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B ASE PLANT

DATE SAMPLING TEA

SOURCE TYP AJ E(, L--6 y

SOURCE NUMBER INISACKDAEE

RELATED CAPACITY 10 [5 TYVPEFUEL

DISTANCE FROM OUTSID OF NIPPLE 0 INSIDE DIAMETER

/ Z26 21che5NUMBER OF TRAVERSES

NUMBER OF POT STW A M 1ERSE

LOCATION OF SAMPLING POINTS ALONG TRAVIRSE


(Inches) (Inches)

.2o

OEHL FORM 1 1APR 79 1 18


BASE DATE

BOILER NUMBER . , .,

INSIDE STACK DIAMETER 1

STATION PRESSURE

- - 1 In HgSTA K STATIC PRESSURE

In H20SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD. Vp IN H20 C1. , STACK TEMPERATURE (OF)

2-I__ _ __ I2L ,_ _ _

3 __.

AVERAGE

OEHL FOM 16 119




PARTICULATES

FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLESTEM(gi) (dlmJ (il')

FILTER NUMBER



Total Weight of Particulotes Collected

II. WATER


(e-) (a) (901)

IMPINGER (1o20) ?o ) z

IM IG R2 (1420) -'-T

IMPINGER 3 (D~ry)

F

IMPINGER 4 (Silica Oel)


Ill. GASES (Dry)

ITEM ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVERAGEI 2 3 4

VOL % CO 2

VOL% 0 2

VOL % CO

VOL % N2

Ve % N2 u (100%- % CO2 . %02. CO)

~AMDFE ,, 651 REPLACES OEHL 20, MAY 78, WHICH IS OBI ETE.

APPENDIX M


121


122

0 w

0 CLC o -J

rM J

M __ -J

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w w w

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c CL CL z a o ~ '

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Nuz PO

V) w.

w Vzx w

£ 0 a CL 0

123

PRELIMINARY SURVEY DATA SHEET NO. I(Stack Gemeory)

BASE PLANT

DATE SAMPLING TEAM

SOURCE TYPE AND A E

SOURCE NUMBER ,NSROE §TACK DIAMETER o 3 0I n, Inches


10DISTANCE FROM OUTSIDE OF NIPPLE TO INSIO 7 DIAM TER i

a-o. 5 E . InchesNUMBER OF TRAVERSES 1NUMBER OF POINTI/TRAVIERSE




(Inches) (In cheo )

I3 ,__ __ __-3

1 :, ,

OEHL APR7 15

t.


BASE DATE

BOILER NUMBER

13 X, 13L-co6 fq-Z.LINSIDE STACK DIAMETER

/?I SInchesST TAT ION P RESSUR E

- . '- >In HgSTACK STATIC PRESSURE

--,0/ In H20SAMPLING TEAM


2. /

7 /0

AVERAGE

OEHL FORM 16 125. ,H F I m , tI I



I F17 4L)6 T'BUILDING NUMBER SORENUMBER

7P AR TICUL ATES

ITMFINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLES

FILTER NUMBER

ACETONE WASHINGS (Probe. FrontHall Filter)

B AC K H A LF (it needed)

Total Weight of Particulates Collectedgm


(902) (am) (901)

IMPINGER 1 (H20) -a 0c

IMPINGER 2 (Hf20) 0 -oo:~I

IMPINGER 3 (Dry)(D

IMPINGER 4 (Silica Gel) C


ill. ~~~~~~~~~~GASES (Dry)_____________________

ITEM ANALYSIS 1 ANALYSIS ANALYSIS ANALYSIS AVERAGEI I2 34

VOL % CO 2

VOL %0

VOL % CO

VOL % N2

Val S M2 a (100%. - CO2 . % 02 CC

AMD FE:6 651 REPLACES OEHL 20, MAY 78. WHICH IS 0O! YL ETE.

APPENDIX N

Steam Boiler Field Data

127


128

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129


BASE PLANT1511- , F/ cf-..- / oDATE SAMPLING TEAM


SOURCE NUMBER INSIDE AK TAMER

Inches


DISTANCE FROM OUTSLE OF NIPPLE TO INSIDE DIAMETER

/ 0 's Inches

NUMBER OF TRAVERSES NUMBER OF POINTS/TRAVERSE



(Inches) (Inch- )

/ / ,___ ___,5

3

6 U.s __ _ _ __ _ _ __ _ _ _

OEL 157 0

OEHL APo111 1513


B A S E 7 -5 A T IE

BOILER NU -MSE

INSIDE STACK D1Pj.ETER I

STATION PRESSURE


- 17 In H20

SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD Vp IN 20 STACK TEMPERATURE (OF)

13 A

L .13,5 _ ,_.I45 ,45 z.-__.1

D,- F} .P) r f,

AVERAGE

OEHL FORM 16 11m i

APR 7913 7-lll______l__nnil____II

AIR POLLUTION PARTICULATE ANALYTICAL DATABASE DATE RUN NUMBER

S14t 74BUILDING NUMBER SOURCE NUMBER

I. PARTICULATES

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLES(l)•(Il1) j(a")

FILTER NUMBER

ACETONE WASHINGS (Probe, FrontHall Filter)

BACK HALF (It needed)

Total Weight of Partilculates Collected

II. WATER

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT WATER(lm) (am) (m

IMPINGER 1 (1120) oo-

IMPINGER 2 (H20) e

IMPINGER 3 (De7) /

IMPINGER 4 (Sties Get)

.....• ......... . ."Totl, Wight Water Coll~cted

III.GASES (Dry)

ITMANALYSIS ANALYSIS ANALYSIS ANALYSISAVRGITEM AVERAGE12 3 4

VOL % C0 2

VOL % 0 2

VOL % CO

VOL %i N 2

Vl 1N 2 2 (100%- % CO 2 . % 02 . % CO)

_AMD P ;'1tq 4 651 REPLACES OENL 20, MAY 7,. WHICH IS OISOLETE.

W .. , .. ..

APPENDIX 0


133


134

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135

PRELIMINARY SURVEY DATA SHEET NO. 1(Stack G,.ometrt,

BASE PLANT

3,h&- -P /-N/ &DATE SAMPLING TEAM


C/1- FI EfD &1E 4~/SOURCE NUMBER INSIDE STACK DIAMETER



/9? InchesNUMBER OF TAVERSES . .STRAVERSE

LOCATION Of SAMPLING POINTS ALONG TRAVERSE


(Inches) (In ch es)

2- 7______ /Z 7D3 __ _ __ _ 2,V __ _ _ _ _ __ _ _ _ _ _

__ _ __ _iq.9 /7,9j

0 FOM iii10ELAPR 79 1 136


BASE DATE

BOILER NUMBER

INSIDE STACK DIAMETER I c e/'{ JInches

STATION PRESSURE

In H&STACK STATIC PRESSURE

- In H20SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD, Vp IN H20 STACK TEMPERATURE (OF

_ _ _ _ _ _ _ _5'

AVERAGE

OEHL FOAM 16 137APR 78.. . ,, .' ," w,,"t "" ' .l i P.'- , - "




PARICUILATES __________

FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLESITE(M () (

FILTER NUMBER



Ttal Weight of Particulates Collected

II. WATER


(am) (am) (90)

IMPINGER I (H120) b fr343 4-.D 044

IMPINGER 2((H2O) OI o

IMPINGER 3 (Dry,)

IMPINGER 4 (Silica Go,) Zoo,

Total Weight .f Water Collected '7

Ill, _GASES (Dry)

ITEM ANALYSIS ANALYSIS ANALYSIS ANALYSIS AVERAGE

1 2 3 4

VOL % CO 2

VOL % 02

VOL % CO

VOL % N2

Vol S N2 " (100% . 1 CO2 . % 02 % CO)

AMD .O10 651 REPLACES OEHL 20, MAY 70, WHICH IS OBSOLETE.

138

0 4 u

w~ ~~~~ oi J-

N0

4 0 0 w -

4n 0

I £

(%4~J 0 I

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'139


BASPL ANT

DATE SAMPLING TEAM


SOURCE NUMBER I SIDE STACK DIAMETER

W-2-____________ Lches

RELATED CAPACITY T FUEL


/ I LJP L 3"If ) InchesNUMBER OF TRAVERSE NUMBER OF POINTSITRAVERSE

LOCATION OF SAMPL !NG POINTS ALONG TRAVERSE

PERCENT OF DISTANCE FROM TAL DISTANCE FROM OUTSIDEPOINT DIAMETER INSIOE WALL OF NIPPLE TO SAMPLING POINT

(In che ) (In ch es)

/ _ _, /__ _ _.Id

'4,12. _ _ _ _O 7,0

, 3 12, Is-,o_ _-_ _ _ _ _,_ _ 7 .ci

OEHlL FOM 151-AP.

.140


BASE DATE

BOILER NUMBER

INSIDE %TACK DIAMETER

16 Inches

STATION PRESSURE

-Z In HgSTACK STATIC PRESSURE

.. In H20

SAMPLING TEAM

TRAVERSE POINT NUMBER VELOCITY HEAD. Vp 04 M20 O STACK TEMPERATURE (OF)

3 10

AVERAGE

OEHL APR 16 141



S/-+, ,'-*w -4,3 3,v -, Y -


PARTICULATES

ITEM FINAL WEIGHT INITIAL WEIGHT WEIGHT PARTICLES(&'m) (em) (Lir)

FILTER NUMBER

ACETONE WASHINGS (Probe, FrontHalt Filter)

BACK HALF (IIneeded)

Total Weight of Porticulates Collectedjm

II. WATER


(am) (am) (g01)

IMPINGER I (H120) D ' ( 1LbQ 0i~C

IMPINGER 2 (H120) b9L 1 0 C)

iMrIGER A ...ry, 0

IMPINGER 4 (Silica Gel) 1 00 C

Total Weight of Water Collected 5-2.3Ill. GASES (Dry)


VOL % CO 2

VOL% 0 2

VOL % CO

VOL % N2

Vol N 2 z (100%. % C0 2 - 0 2 . % CO)

AMD a" 651 REPLACES OENL 20, MAY 7S, WHICH IS OBSOLETE.

142

APPENDIX P

Calibration Data

143


144

METER BOX CALIBRATION DATA AND CALCULATION FORM

(English units)

Date 12- jkA 8 Meter box number ;0i0 fi[R

Barometric pressure, Pb = in. Hg Calibrated by

Gas volume TemperatureOrifice Wet test Dry gas Wet test Dry tas meter

manometer meter meter meter Inlet Outlet Avg- Time

setting (VW), (Vd), (t), (td (td ), (td), (a),(i), a " Y.

Sin. H 20 ft3 ft3 Dr t/iA rjPk 1JP, min in 1.__- _____- _'_______ -- -

0.5 5 3S , 53S 9 3, 1.07d 0 0

1.0 5 532(. 7S JQ3.O

1.5 10 4.30 731 53 -9 5?,5 1. 3 , . .o00

_ _ f 38 o0,553 5q1 51.5 15,5 _. 2- - V

71 qo& 917M 2.0 10 TL155 20 53q5 (o 55. 10A 553-5 a35 I/.0o7o0 3 7

3.0 10 ____~976 5 ' .5 1 .5 9'555 55?,23. /,8I 2.1074.0 10.1

A .077 2.070

AH, H d w Pb(td + 460) 0.0317 AH (t + 460) 0 2

in. 13 y.6 = 1 Ai VH20 . (P + .6 ) (tw + 460) Pb (td + 460) V

0.5 0.0368 .3 L(-/ 3- 4JI/ ' /.1,... 3T,2 .... .

1.0 0.0737 , (i I: ) C3&, ) ' _I

1.5 0.11D ('C 3 3&(2J/J 3 '1~~~#i (~)

aIf there is only one thermometer on the dry gas meter, record the temperature

145

'71 , 1, 1 t I I I

14ETER BOX CALIBRATION DATA AND CALCULATION FORM

(English units)

Date L S 2S Meter box number

Barometric pressure, Pb in. HS Calibrated by T fti tv E f=

Gas volume TemperatureOrifice Wet test Dry gas Wet test Dry Ras metermanometer meter meter meter Inlet Outlet Avg Timesetting (Vp), (Vd), (tw), (td.), (td , (td). (a),(AH),03 3 1 a. A

in. HO2 ft ft * ?A I~ k~ min in. 1

0.5 5 4,71Z- '7 53 Z5" ,72 -57 !Ag,)5 12,p /,081/l.!2

1.0 5Pz 0,40 2K 53T.5 10 0&.5 ,53 55Z,7 ."o g i~ /- 0,56

d 1.5 10 7I It_ _ _.__O is 1 535 1,3S 1 Rq542.5 57.L5 15.0 /.0 75I908

2.0 10 q,5-; i' 53,5 105 V31~ - 55~j~5566.,S 13 -a 1,087 l/703

3.0 10 q, 6 554753 5 63. 0 -7 /.oP .

4. 0 10 9/, 53/A v / , o I /. 7 3

AH, V Pb(td + 460) 0(t + 460) e

H20 13.6 ( +_ AH t = .0 P 7(t + 460)d(Pb 13.6 (t/+ 460) bd 0

0.5 0.0368 - 9'1, 7X ( 3?__Y__ 7' .J2 21% 3I1f /11-3 , .523

1.0 0.0737 - Z )(.c I. /5-,i 735- CilJ . i1.5 0.110 (16 2/3131-)

Z.

____A__cfTi ,/1. *TJ 3~ 13 ,1 7,5

3.0 0.1 - t : ,-. L [ I,-6' .6,ff .) -1 lu L,_ :4.0 0.29 , 2 ,, -X ./3/ \ ! - ,

aIf there is only one thermometer on the dry gas meter, record the temperature

under td.

Quality Assurance Handbook M4-2.3A (front side)

146

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APPENDIX Q

Exhaust Gas Moisture Content and Velocity Calculations

151


152

* XROM 'METH 5' XROM 'METH 5^ XROM "METH 5^

RUH NUMBER RUN NUMBER RUN HUMBER

BLDG 483, BOILER 2 BLDG 483, BOILER 3 BLDG 403, BOILER 5RUN RUN RUN

METER BOX Y? METER BOX'Y? METER BOX Y?

1.8778 RUN 1.8778 RUN 1.8778 RUN

DELTA H! rELTA H? DELTA H?

2,8808 RUN 1.9880 RUH 1.4808 RUN

BAR PRESS I BAR PRESS ? BAR PRESS ?

29.8688 RUN 29.8680 RUN 29.6850 RUN

METER VOL ? METER VOL ? METER VOL ?27.0848 RUH ,25.89I0 RUN 22.9918 RUN

MTR TEMP F1 MTR TEMP F? MTR TEMP F?

128.208 RUN 115.3080 RUh 120.7888 RUN

% OTHER GAS % OTHER GAS % OTHER GAS

REMOVED BEFORE REMOVED BEFORE REMOVED BEFORE

DRY GAS METER ' DRY GAS METER ? DRY GAS METER ?RUN RUN RUN

STATIC HON IN ? STATIC HON IN ? STATIC HON IN?-.8808 RUH -. 0808 RUH -.0458 PUN

STACK TEMP. STACK TEMP. STACK TEMP.

578.9008 RUN 582.5888 RUN 333.8008 RUN

ML. WATER I ML. WATER ? ML. WATER ?188.5088 RUN 94.2008 RUN 87.4888 PUN

IMP. % NON = 15.3 IMP. 4 HON = 14.7 IMP. % HON 15.5

* HO=15.3 % HOH=14.7 NONl1",'"

E.988 RUK1 8.088 RUN 8.8088 PUN

988Z. R OXYGEN? P OXYGEN?.908 RUN 7.2808 RUN 8.8888 RUN

CO P .Co? % CO ?PIUlN RUN RUN

MOL WT OTHER? MOL WT OTHER? MOL WT OTHER?

PUN RUN RUN

MWd =29.42 MWd =29.57 MWd =29.68

%W WET:27,68 MW WET=27.86 MW WET=27.88

SORT PSTS 2 SQRT PSTS SORT PSTS11.8388 RUN 10.9672 RUN 10.3136 RUN

TIME MIN ) TIME MIN ? TIME MIN ?

40,0000 RUK 40.0008 RUN 40.0088 RUN

NOZZLE DIP ? lsImm. RUN .5008 RUN 1 RUN

STK DIP INCH ? STK DIA INCH ? STK DIA INCH ?

12.2580 RUll 12.2568 RUh 15.7588 RUN

VOL MR STD = 26.268 * VOL MTR STD 25.66@ VOL MT STE= 22.3"'SI" PRES ABS 29.85 STK PRES ABS = 29.85 STK PRES ABS = 29-.6

VOL HON GAS = 4.77 VOL HON GAS = 4.43 VOL NON GAS = 4.11

MOISTURE = 15.26 % MOISTURE = 14.73 % MOISTURE = 15.54

MOL DRY GAS =8.847 MOL DRY GAS =8.853 MOL DRY GAS =8.845

% NITROGEN = 85.28 % NITROGEN = 84.80 % NITROGEN = 84.-0

MOL WT DRY = 29.42 MOL WT DRY 29.57 MOL WT DRY = 29.68

MOL WT WET = 27.68 MOL WT WET 27.86 MOL WT WET = 27.8e

VELOCITY FPS = 29.58 VELOCITY FPS = 27.11 VELOCITY FPS = 25.P2

STACK AREA = 8.82 STACK AREA = @-82 STACK AREA = I .

STACK ACFM = 1,452. STACK ACF= .341. STACK ACFM = 2.896.

SSTACK DSCFM = 624. * STACK DSCF = 626. * STACK DSCF=

153

XROM "METH 5' XROM 'METH 5' XDOn METH 5"

RUN NUMBER RUN NUMBER RUH NUMBER

BLDG 611, BOILER I BLDG 922, HW BOILER BLDG 922, BOILER IRUN RUN BLG92 OLRI RUN

METER BOX Y? METER BOX Y?1.8778 RUN 1.8778 RUN 1.E77 RUN

808 RUN DDELTA H? 1. 4000 RUN1.4888 RUN 1.4888 RLUN DELTA HU

BAR PRESS I BAR PRESS ? BAR PRESS ?29.688 PUN 29.8158 RUN 29.635B PUS

METER VOL I METER VOL ? METER VOL ?22.2988 RUH 22.9068 RuN 2ETER VOL

MTR TEMP F? MTR TEMP F? MTR TEMP F?

95.6888 RUN 111.9888 RUN 95.7M8T RUN

% OTHER GAS % OTHER GAS 9 OTHER GASREMOVED BEFORE REMOVED BEFORE REOER GASDRY GAS METER ? DRY GAS METER - REMOVED BEFORE

RUN RUN DRY GAS METER ? RNSTATIC HOH IN STATIC HON IN ? STATIC HOH IN ?-.38 PlUN -.0050 RUN -.82@0 PUN


489.1888 RUN 253.6888 RUN 295.588 RUNML. WATER ? ML. WATER ? 295.5888RPU

61.2888 RUN 39.7888 RUN 126.2ML0 RAT

IMP. ' HOH = 11.3 IMP. 1 HOH 7.6 IMP. % OH= 19.9

' HOHzfl. % HOH=7.6 % HOH=9I.9

% C02? * Co2? % C02?7,8888 RUN IC3888-- RUN 8.0880 RUN

OXYGEN? % OXYGEN? % OXYGEN?

11.8888 RUN 8.8888 RUN 8.8888 RUHPUN % CO ?N % CO?PUN RUN PUN

MOL WT OTHER? MOL MT OTHERI MOL WT OTHER'PUN PUN PIJN

MWd =29.56 MWd =29.68 MWd =29.68

MW WET=28.26 MW WET=28.72 MM WET=27.29

SORT PSTS I SORT PSTS ) SQRT PSTS ?18.2839 RUN 1.4185 RUN 4.4233 RUN

TIME MIN ? TIME MIN ?

TIME MIN ?

48.888 RUN 48.8888 RUN 48.088 PUN

,tW PUN A RUN W RUN

STK DIP INCH ? STK DIA INCH ? STK DIA INCH ?

1Q.7588 PUN 8.8888 RUN 9.7588 RUN

, VOL MTR STD = 22.668 * VOL MTR STD = 22.774 * VOL MTR STD = 23.845

STK PRES ABS = 29.68 STK PRES ABS = 29.81 STK PRES ABS = 2967

VOL HON GAS = 2.88 VOL HON GAS = 1.87 VOL HON GAS = 5.94

% MOISTURE = 11.29 % MOISTURE = 7.58 % MOISTURE = 19.94

MOL DRY GAS = 8.867 MOL DRY GAS = 8.924 MOL DRY GAS = 8.881

% NITROGEN = 82.88 % NITROGEN = 84.88 % NITROGEN = 84.88

MOL WT DRY = 29.56 MOL WT DRY = 29.68 MOL WT DRY = 29.68

MOL WT WET = 28.26 MOL WT WET = 28.72 MOL MT WET = 27.29

VELOCITY FPS . 25.53 VELOCITY FPS = 3.46 VELOCITY FPS z I.!7

STACt$ AREA = 1.. : STACK AREA = e-35 STACK AREA 8.52'TACK ACFM = 1,588. STACK ACFM = 72. STACK ACFM = 348.

, STACK DSCFM 847. * STACK DSCFM = 49. * STACK DSCFM = !97.154

XROM -METH 5"

RUN NUMBER XROM METH 5 XROM 'METH 5 RUN NUMBER

BLDG 1846, BOILER I RUN NUMBER BLDG 113OL BOILER 1

RUNRUN MEER BOX Y? RUN

METER BOX Y? METER BOX Y? 1.770 RUN

DELTA H? 1.8778 RUH DELTA H?

1.410 RUN4 RUN BR PRESS ?7N

BAR PRESS ). BR PRESS ? 296358 U

29N 29.815 RUN METER VOL ?METER VOL ) RUN METER VOL ? 22.6260 RON

MTR TEM 22.576e RUN MTR TE2P F?96.T8PF MTR TEP MTR TEMPP FF 1.2808 pU'0

.OTHER GAS 87.7000 RUN % OTHER GAS

REMOVED BEFORE % OTHER GAS REMOVED BEFORE

DRY GAS METER ? REMOVED BEFORE DRY GAS METERPUN DRY GAS METER ? ?

STATIC HONSTTIC HO IN ?

-.8558 RU STATIC HOH IN ? -UN-55 RU-.gO RUN ST.C T 6EMP.'

STACK TEMP. -.e488 STACK TEMP.

358888 UNSTACK TEMP. 407.9808 PUN358ML.WA EUN 237.708 RUN ML. WATER ?

ML. WATER M I L, WATER ? 48.1880 PU71.008@ RUN 54.70 RUN IMP. V HON 9.8

IMP. NON 12.6 IMP. % HOH 9.9

H H 1 2. . % HOH=9.9 % HOH=9.

" C02? V.C02? %C2

CO-- 8.08 RUN 7.080 RUH8.P8 UN

OXGN

O OXYGEN' % OXYGEN? OXYGEN? RU.89 U8.0000 RUN 1U.0 0 @ e R U N % c o ?

V. CO ? V.COCO ? RUN

MOL WT OTHER? MOL 9T OTHER? RUN MOL WT OTHER' PUNRUN

NMWR 229.6 ~d =29,68 MWd =29.56

MM METN28.14 MW MET=28.45 "W WET:28.52

S~ORT PSTS ?SQRT PSTS ? SORT PSTS" 6098 UN11.3643 PUN

6. 1812 RUN 6.0948 RUN TIME MIN 1 4

TIME MIN ? TIME MIN ? 4e.0000 PUN

48.9898 RUN 40.8888 RUN

-,pivo RUH A RUN STK DIA INCH ?

STK DIP INCH I STK DIA INCH ? lP.000 PUN

15.8800 RU 9.?500 PUN1

* VOL MTP STD = 23.282 VOL MTR STD = 23,438 VOL MTR STD 22.2

TK PRES ABS = 29.82 STK PRES ABS = 29.81 STK PRES ABS 29.62

VOL HON GAS = 3.34 VOL HON GAS = 2.57 VOL HON GAS 2.21

VO MOISTURE 12.35 % MOISTURE = 9.90 % MOISTURE = 82MOL DRY GAS 0=874 5OL DRY GAS = 9.901 MOL DRY GAS 8.910

.NITROGEN = 84.8 % NITROGEN = 84.88 % NITROGEN = 82.8

ML NTRY 29.60 MOL WT DRY z 29.-6 MOL WT DRY = 29.56

MOL WT T = 28.14 MOL NT WET = 28.45 MOL WT WET = 22.52

VELOCITY FPS = 15.2 VELOCITY FPS = 15.03 VELOCITY FPS = 28.8

STACK AREA = 1.23 STACK AREA = ST0CK ARE =

STACK ACF 1,128. STACK ACFM = 468. STACK ACFM = 919.STACK DCF 6. * STACK DSCFM = 318. STACK DSCFM = 54.

.Toc RV.M = 315.155

XROM "METH 5" XROM 'METH '" XROM *METH 5"PUN NUMBER RUN NUMBER RUN NUMBER

BLDG 1208, BOILERfi BLDG 12e8, BOILER 2 BLDG 1280, BOILER/I/3

RUN RUN P RUN

METER BOX Y? METER BOX Y? METER BOX Y?

1.8778 RUN 1.8778 RUN 1.8770 RUNCTA H? DELTA H? DELTA H?

1.3700 RUN 1.5700 PUH 1.30089 RUN

BAR PRESS ? BAR PRESS ? BAR PRESS ?29.9450 PUN 29.9458 RUN 29.9298 RUNMETER VOL R METER VOL ? METER VOL ?26,928R RI.! 25.3229 RUN 25.4158 RUN

MT 2 TEMP F? MTR TEMP F? MTR TEMP Fl89.48T8 RUN 121.4888 PUN 107.5888 RUN94OTHER GAS % OTHER GAS % OTHER GASREMOVED BEFORE REMOVED BEFORE REMOVED BEFORERRY GES METER E DRY GAS METER ? DRY GAS METER ?

RUN RUN PUNSTATIC HON IN ? STATIC HOH IN ? STATIC HOH IN ?

-.8458 PUI -.0458 RUN -.8980 RUN


369.1888 RUN 266.2800 RUN 281.6088 RUN

ML. WATER ? ML. WATER I ML. WATER ?

58.9888 RUIN 75.888 RUN 66.3988 PUNIMP. % HOH = 9.0 IMP. % HOH = 12.4 IMP. % HON = 18.9

'O .8.."HOH=12.4 % HOH=10.9

C % C02? % C02)

6.8888 RUN 7.8880 RUN 8.8808 p:.'j% OXYGEN? 1 OXYGEN? 1 OXYGEN?

11. 4888 RUN 11. 8888 RUN 8.8888 RUN

%CO? U CO ? % CO ?PUN PUN U

MOL WT OTHER? MOL WTQTHER? MOL WT OTHER?

RUN PUN RUN

MWd =29.54 MWd =29.56 MWd =29.68

MW WET=28.58 MW WET=28.12 MN WET=28.34

SQPT PST: 'SORT PSTS ? SORT PSTS9.1134 RUN 4.6228 FUN 8.1518 PUN

TIME MIN ? TIME MIN ? TIME MIN ?

48.8888 RUN 48.8888 RIJN 48.888 RUN

RUN .11111111m RUN A RUN

STK DIP INCH ? STK DIP INCH ? STK DIR INCH ?

9.6388 RIJN 9.6380 RUN 9.6388 RUN

* VOL MTR STD = 27.9R9 s VOL MTR STD = 24.883 VOL MTR STD = 25.556

STK PRES ASS = 29.94 STK PRES ABS = 29.94 STK PRES ABS = 29.92VOL HOH GAS = 2.77 VOL HOH GAS = 3.53 VOL HON GAS = 3.12

% MOISTURE = 9.81 % MOISTURE = 12.42 % MOISTURE = 18.88MOL DRY GAS = 8.918 MOL DRY GAS : 0.876 MOL DRY GAS = 8.891

* NITROGEN = 81.88 % NITROGEN = 82.88 % NITROGEN = 84.08

MOL WT DRY = 29.54 MOL WT DRY= 29.56 MOL WT DRY= 29.68

MOL WT WET = 28.58 MOL WT MET = 28.12 MOL WT WET = 28.34

VELOCITY FPS = 22.4A VELOCITY FPS = 11.44 VELOCITY FPS m 28.18

STACK AREA : 8.51 STACK AREA = 6.51 STACK AREA = 851

STACK RCFM = 688. STACK ACFM = 347. STACK ACFM = 618.

* STACK DSCFM =94. * STACK DSCFM 221. STACK DSCFM 387.

156

XROM 'METH 5" XROM "METH 5' XROM 'METH 5"

RUN NUMBER RUN NUMBER RUN NUMBER

BLDG 1286, SMALL BOILER BLDG 1482, BOILER I BLDG 1422, BOILER IRUN RUN RUH

METER BOX Y? METER BOX Y? METER BOX Y?1.8778 RUN 1.8778 RUN 1.8778 RUN

DELTA H? DELTA H? DELTA H?1.2588 RUN 1.4088 RUN 1.4888 RUN

BAR PRESS ? BAR PRESS ? BAR PRESS ?

29.8480 RUN 29.8508 RUN 29.8588 RUN

METER VOL ? METER VOL ? METER VOL ?

25.6368 RUN 22.3048 PUN 21.6736 P.N

MTR TEMP F? MTR TEMP F1 MTR TEMP F?

98.2588 RUN 88.9888 RUN 93.9888 PUN

% OTHER GAS % OTHER GAS - % OTHER GAS

REMOVED BEFORE REMOVED BEFORE REMOVED BEFORE

DRY GAS METER ? DRY GAS METER ? DRY GAS METER ?RUN RUNI PUN,

STATIC HOH IN ? STATIC NON IN ? STATIC HOH IN ?-. 8858 PRjil -.8188 RUtH -. 8188 PL.

STACK TEMP. STACK TEMP. .

STACK TEMP.

238.!q 8 RUN 255.188 RUN 241.6886 PUN

ML. WATER " ML, WATER ? ML. WATER65.4888 PUN 51.6888 RUN 66.8808 PU

IMP. ;' HOP = 18.5 IMP. % HON = 9.5 IMP. % HON =12.3

HOH= 1.5 : HOP=N.5 % HOH=12.3

% C02? % C02? , C02?7.8088 RUN 7.088 RU" 7.088 RUN

% OXYGEN, % OXYGEN? % OXYGEN?11.8888 RUN 11.8888 RUN 11.8888 RUH

%CO ? % CO ? R CO IRUN RUN RUN

MOL WT OTHER? MOL WT OTHER? MOL WT OTHER?RUN RUN RUN

Mkd :29.5A MWd =29.56 MWd :29.56TMH UT-7.)34 MW WET=28.46 MW WET=28.14

SORT POTS 1 SORT PSTS ? SORT PSTS ?3.1988 RUN 4.3536 PUN 3.7343 RUN

TIME MIN TIME MIH ? TIME MIN 1

48.8888 RUN 39.5888 PUN 48.0888 RUN

. P PUN PUN RUN

STK DIP INCH ? STK DIP INCH ' STK DIP INCH ?

13.8888 RUN 18.7588 RUN 17.508 RUN

* VOL MTR STD = 26.124 * VOL MTR STD = 23.132 * VOL MTR STP = 22.480

STK PRES ABS z 29.84 STK PRES ABS = 29.85 STK PRES PBS = 29.8R5

VOL HOH GAS = 3.88 VOL HON GAS = 2.43 VOL HON GAS = 3.14

*, MOISTURE = 18.54 % MOISTURE = 9.58 % MOISTURE : 12.17

MOL DRY GAS = 8.095 MOL DRY GAS = 8.985 MOL DRY GAS = 8.877

% NITROGEN = 82.88 % NITROGEN = 82.8 % NITROGEN = 82.88

MOL WT DRY = 29.56 MOL WT DRY = 29.56 MOL WT DRY= 29.56MOL WT WET = 28.34 MOL WT WET = 28.46 MOL WT WET = 28.14

VELOCITY FPS = 7.88 VELOCITY FPS = 18.73 VELOCITY FPS = 9.25STACK AREA = 1.05 STACK AREA = 8.63 STACK AREA = 1,67

STACK ACFM = 497. STACK ACFM = 486. STACK ACFM = 927.

* STACK DSCFM = 335. * STACK DSCFM = 278. * STACK DSCFM = 611

157

XROM METH 5' XROM "METH 5'

RUN NUMBER RUN NUMBER XRUN NUMBER

BLDG 164, BOILER I BLDG 1614, BOILER 2 RUN B ERRUN RUN BLDG 16S4, BOILER I U

METER BOX Y? METER BOX Y? METER BOX Yl1.87?8 RUN 1.8778 RUN 1.8778 RUN

DELTA H? DELTA H? DELTA H?1.40@ RUN 1.4880 RUN 1.4888 UN

BAR PRESS ? BAR PRESS ? BAR PRESSP29.8868 RUN 29.8068 PUN 29886 RUN

METER VOL I METER VOL ? METER VOL U

22.6458 PUN 22.8708 PUN 22.7580 P

MTR TEMP Fl MTR TEMP F? MTR TEMP F?184.5888 RUN 88.6b8b RU 1M7.6T0T RU

% OTHER GAS % OTHER GAS % OTHER GAS

REMOVED BEFORE REMOVED BEFORE OER GFR

DRY GAS METER ? DRY GAS METER R

RUN RUN DRY GAS METER PUN

STATIC HOH IN ? STATIC NON IN ) STATIC NON IN-.8799 PUN -.9198 PIN -.A8C1HN 8I ) LH

STACK TEMP. STACK TEMP.

STACK TEMP.

151.88008 RUN 268.308 RUN 272.50 RU

ML, WATER I ML. WATER ? ML. WATER ?57.208 PUN 52.3888 PLIN ML.7ATER ?

iMP. % HOH = 18.6 IMP. % HOH = 9.4 IMP. %HOH= 18.6

SHOH=10.6 HOH=9.4 HOHIO.6

C C 2 7 , " 1 C02? % C02?7 .08 PUM 7 8 @88 PUN 7 .8C8 2?

OXYGEN? R OXYGEN? OXYGEN'UN11.0888 PUN 11.8998 PUN 11.8880 RUN

% CO ) RIN CO ? PN% CO IURUN PUN U

MOL WT OTHER MOL WT OTHER? MOL WT OTHERL

RUN RUN RUN

MWd =29.56 MWd =29.56 MWd =29.56

MU WET=28.34 MW MET=28.47 MW WET=28. '3

S Q T P S T S 1 S R T P S T S ? S R T P S T S ?8.8416 PUN 4.8668 RUN 4.6759 PUN

TIME MIN ? TIME MIN ? TIME MIN )48.8889 RUN 49.9988 PUN 49.88 RUN

.M RUN m RUH m RUH

STK DIR INCH ? STK DIA INCH ? STK DIA INCH ?

7.5088 PUN 16.8890 PUN 16.8888 RUN

* VOL MTR STD = 22.883 * VOL MTR STD = 23.697 * OL MTR STD 22. 792

STK PRES ABS = 29.88 STK PRES ABS = 29.81 STK PPES APS 29,81VOL NON GAS = 2.69 VOL HOH GAS z 2.46 VOL HON GAS = 2.72

' MOISTURE = 18.56 % MOISTURE = 9.41 % MOISTURE = 10.65

MOL DRY GAS = 8.894 MOL DRY GAS 8.9e6 MOL DRY GAS = 8.894

% NITROGEN = 82.88 % NITROGEN = 82.88 % NITROGEN = 82.88MOL NT DRY = 29.56 MOL WT DRY = 29.56 MOL WT DRY = 29.56MOL WT WET = 2834 MOL WT WET OL T ET = 28.3

28R34 MWT WET =E 2828.4VELOCITY FPS = 21.85 VELOCITY FPS = 12.8 VELOCITY FPS = 11.56

STACK AREA = .I STACK AREA = 1.48 STACK AREA = 1.49

STACK ACFM = 482. STACK ACFM = 1.885. STACK QCFM = 968.

* STACK DSCFM = 389, * STACK DSCFM = 665. * STACK DSCFM = 621.

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DISTRIBUTION LIS r

Copies

HO AFSC'SGPB 1Andrews AFB DC 20334-5000

HO USAF'SGPA 1Boiling AFB DC 20332-6188

USAF Regional Medical Center Wiesbaden/SGB 1APO New York 09220-5300

OL AD, USAFOEHL 1APO San Francisco 96274-5000

USAFSAM/TSKIEDH 1 eaBrooks AFB TX 78235-5301

Defense Technical Information Center (DTIC) 2Cameron StationAlexandria VA 22304-6145

HSD/EV 1Brooks AFB TX 78235-5501

HO USAF/LEEV 1Boiling AFB DC 20330-5000

HQ AFESC/RDV 1Tyndall AFB FL 32403-6001

HO TAC/DE 1Langley AFB VA 23665-5578

HQ TAC/SGPB 1Langley AFB VA 23665-5578

363 Medical Group/SGPB 2Shaw AFB SC 29152-5300

363 CES/DEEV 2Shaw AFB SC 29152-5000

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r U S GOVERNMENT PRINTING . -..:- 1q8q-6 .O l 00005

REPORT - DTICouuUSAFOEHL REPORT 89-010EQ0178BEF COMPLIANCE TESTING OF HOT WATER AND STEAM BOILERS,...

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