P.1 

OAR Box 1770 

Prepped by Keeia Richards 

Document Number: 

38) XII-D-8 

Docket Number: 

A-79-15 

Printed 1072872008 10:20:29 AM Sheet 38 of 93 
P.2 

Utl/. "i l yVIIU U 10

 ; 0 - N&H BUilUlN UUI\L i/vi\r ILLi- 1 "UilUUJUt l 

7 Docket No. A-79-15 

Item No. XII-D-8 

New Boston Coke Corp 

600 River Avenue • Phone (740) 456-4154 

P.O. Box 3128 • Fax (740) 456-5644 

New Boston, Ohio 45662 

DATE /Z'21-M 

FACSIMILE NO. 10 3' 13*7-31 HO 

PLEASE DELIVER THE FOLLOWING PAGE(S) TO 

NAME: k)Mt t 7k/#*V T KA#>J ff;nrr\ 

COMPANY: ^F~C' F jflrtSo/fi^e, 

EPA AIR DOCKET 

DEPARTMENT: 

CITY AND STATE 

FROM: -?Mr#€ /yieA^'/dJich 

REGARDING: -/W$V /?** \)<L5f<?&j 

MESSAGE: 

A TOTAL OF 63 ? PAGE(S) ARE BEING TRANSMITTED (INCLUDING 

THIS COVER LETTER) . IF YOU DO NOT RECEIVE ALL PAGE(S) OR 

COPY IS NOT LEGIBLE, PLEASE CALL (740) 4S6-4154 AND ASK 

FOR 

THANK YOU. 

************************************* * **************** ! 

PAXOOVBRXTR 
P.3 

I) tU. -21 yyilUt J ID: 00 Ntn BUilUN UUKt ouivr ILL - 1 '4U4000U4 4 I . I.H.M 

New Boston Coke Corp, 

600 River Avenue • Phone (740) 456-4154 

P.O. Box 3128 • Fax (740) 456-5644 

New Boston, Ohio 45662 

PARAMETER VALUE 

Number of ovens for battery #2 70 

Height of Battery - Pad to Roof 26" 11' 

Lenqhth of Battery 273' 

Width of Battery 39' 

Height of oven - Floor to Roof 13' 

Length of oven - Between Doors 36'2" 

Length of oven - Face to Face Brickwork 38' 9" 

Width of oven - Average 17" 

Diameter of offtakes - Inside 13" 

Offtake height - Induding Goose Neck 7'8" 

Charging average 1998 6.51 

Percent Leaking Doors 1998 2.55 

Percent Leaking Lids 1998 0.11 

Percent Leaking Offtakes 1998 1.22 

Pushing % Opacity Average 1998 10.39 
P.4 

JHIN V~> " KJB IO'J l I T It r WJINOUl. I 1 l"IU 

.. 15:33 m BOSTON COKE CORF 

I U ^IHUwt J I I J. I I U I -/ I t CJJ.' U l 

TEL: 17404565644 r\ 00! 

New Boston Coke Corp. 

600 River Avenue • Phone (740) 456-4154 

P.O. Box 3128 • Pax (740) 456-5644 

New Boston, Ohio 45662 

|Map 

Ref. 

Na 

- 1 

- 2 

- 3 

4 

5 

6 

7 

e 

s 

10 

11 

12 

13 

14 

15 

16 

1 7 

Fadlity Unit 

Quench Station 

No. 2 Coke Oven Battery 

Combustion Stack 

Weak Ammonia Uquor Storage Tanks 

Secondary Light Oil Separator 

Wastewater Pump Tank 

Primary Light Oil Separator 

Liqht Oil Storage Tank 

Wash Oil Circulation Tank 

Wash Oil Decanter 

Tar Storage TanK 

Tar Intercepting Sump 

Tar Dewatering Tank 

Flushing Liquor Circulation Tank 

Excess Ammonia Liquor Tank 

Tar Decanter 

Light Oil Condenser Vent 

No. of 

Units 

3 

2 

unit 

Height 

m 

50 

24 

210 

30 

7.76 

6.75 

7.75 

25 

17 

9 

35 

8 

27 

18 

,

 1 5 

1Z5 

6 

Unit Diameter or 

LangthArVMlh (ft) 

45LX15W 

273Lx39W 

NA 

31.5 

5.5 

5.5 

5.5 

10 

10 

30Lx8W 

32 

8 

10 

10 

6 

48LX14W 

1 

Unit 

Orientation 

(HorizrVert) 

V 

H 

V 

V 

V 

V 

V 

H 

H 

H 

V 

V 

H 

H 

H 

H 

V 

7o: JiZfJNlPBrX GlBZDhl 

fo: (h)S) 557-7177 

^M: j(fh5/k £IA/C,3 

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1 

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- m AA MA 1 A A n 111V M niiK t i " .. • A a n 
UNITED STATES 

DEPARTMENT OF THE INTERIOR 

GEOLOGICAL SURVEY 

Qoon/ V * CHILLICOTHE 45 Ml. 

UJ UU i 860 CMJO FEET (OHIOIIJWOSEMOIUNT-2.5 M/. 

°45 ' i nun—nl—4L*~U[ i -w dL ^ 

270 000 FEET 

(OHIO)" 
DEC. -21 " 99(TUEJ lo :

J -

" De c 3 0 9 9 11-27 a 

Ntfl bUbIUi\ GUI\L ^UKrWalte r I. Fridle a 

ILLA 1 /4U4000O4 4 

205-437-050 4 

P.7 

P- 2 • 

New Boston Coke 

Data Form for Coke. Byproducts Plant Emission Sources 

Facility Coke Production Rate: 353.091 tons/yr 1998 year 

40.31 tons/hr 

Source 

Light oil borage 

tank 

Tar tfeiinicr 

Naphthalene 

xepnrRliMii &• 

prouetcini; 

Caoling \c-tt, 

Ur-botlurii 

T»r intercepting 

2ump 

Tar dawaU-ring 

Link 

Tar storage lank 

Light oil 

coAiiaKer veni 

Li£tH oil muip 

B T X rtorogc 

Bcittcite Aorage 

Flushing liquor 

circulation Unk 

K.xcev ammonia 

. liquor uiik 

Wash oil 

decanter 

ft'uli oil 

cirsulolJoti laiit 

No. « r 

UuiU 1" 

1 

1 

M A 

N A 

1 

1 

j 

2 

N.A 

NA 

NA 

1 

1 

1 

1 

C u 

Blanketing 

(Vt-L.f.9) 

Y t t 

V c 

N A 

N A 

Yes 

Ves 

Ye* 

Y o 

NA 

N A 

N A 

Yes 

Ye* 

Y o 

Y o 

Source 

Hclcln 

(n) 

25 

12.5 

NA 

MA 

S 

27 

35 

(cadi bilk.) 

6 

NA 

NA 

NA 

IC 

15 

9 

1? 

Source Dta or 

Length/Width 

{•XT 

10 

48x1 4 

N.A 

N A 

8 

10 

32 

(aidl unk ; 

1 

NA 

N A 

NA 

10 

6 

Jf)x ? 

10 

Tiuik 

Orientation 

(Hor W 

Vert) 

II 

11 

NA 

N A 

V 

H 

V 

(each tank.) 

V 

N A 

N A 

NA 

II 

H 

H 

l i 

Calculated Benzene 

Emiaiioo.* 

(lUjrl 

J5.J 

nN.\ 

NA 

o.o 

1.2 

0«l 

(etfh uink) 

tiJJ.ti 

(each vail) 

NA 

NA 

NA 

O.O 

U(l 

53.0 

5.«.ll 

Mclhcdn f 

Cali-.W 

TANKS 

TANK S 

N A 

N A 

TANK S 

TANK S 

TANKS 

AP-JI; 

N A 

N A 

NA 

TANK S 

TANKS 

AP.*: 

AJM : 

(1) NA indicates source docs noi exist 

(2) Diameter if cylindrical lank; length and width if rectangular tank 

(3) TANKS indicates U.S. EPA TANKS3 program used to calculate benzene emissions: AP-42 indicates drall 

AP-12 Table 12.2-J3 used to calculate benzene emissions 
Lito. -n yyuuLj 10-00 i\m DUJIUI\ OUI\L ^iu 

'Dec 2Q 99 11:27a Walte r 1. Fridle a 

ILL• i /MU40UUU4 4 

205-437-0504 

P.8 

P- 3 

New Boston Coke 

Equipment Component Emissions for Components in Benzene Service 

Stream0' 

Light oil 

Light oil 

Light oil 

Light oil 

COG 

•......- . ' 

Benzene Mass 

FractionC) 

0.67 

0.67 

0.67 

0.67 

0.10 

Type of Equipment0' 

Valves 

Open-ended lines 

Flanges/connectors 

Pumps 

Pressure relief devices 

No. of 

Components 

122 

72 

848 

9 

8 

Benzene 

Emissions 

(Ib/yr) 

13.0 

4.1 

38.2 

21.2 

2.3 

(1) For process streams in benzene service (e.g., light oil liquid, light oil vapor, etc.) 

(2) Benzene stream composition (mass basis) 

(3) Types of equipment may include flanges, connectors, valves, pumps, exhausters, pressure 

relief valves, open-ended lines, etc. 

Sample Calculations: (emission factors based on COETF four-plant fugitive emissions study) 

Light oil valves: 

(122 components)(8.26 x IO"6kg/hr source)(8760 hr/yr)(2.205 lb/kg)(0.67 benzene) -13.0 lb/yr 

COG pressure relief devices: 

(8 components)(1.46 x 10"* kg/hr source)(8760 hr/yr)(2.205 lb/kg)(0.10 benzene) = 2.3 Ib/yr