! 

-

r'; n ­ ':.-.' ..!... r --.- ..--. rO ; -'-.-~ Y""\
 o LG~ L~	 ~J ..J:_ i~L..:....l.

DEPARTMENT OF ENVIRONMENTAL QUALITY .lI _.~ • .:2 DIVISION OF AIR QUALITY 

Michael O. Leaviul	 150 Nonh 1950 WeSI 

P.O. Sox 144820 

Dianne R. Nielson~ 2 Salt Lake City. UIAh 84114-4820 

~Du-.r~ (SOl) 536-4000 

RUAell	 A. Robens (SOl) 536-4099 Fax
 

(SOl) 538-4414 T.D.D.
 

October 18. 1994	 DAQE-915-94 

James R. Van Orman
 

Director, Environmental Management Office
 

Deparunent of the Air Force
 

Headquaners Ogden Air Logistics Center (AFLC)
 

Hill Air Force Base, Utah 84056
 

Re: Change of Jet Fuel from JP-4 to JP-8 

Dear Mr. Van Orman: 

The Division has received your letter dated August 8. 1994, requesting approval for the use of lP-8 

instead of lP-4 as currently specified in your Approval Order (DAQE-167-92 dated October 13, 1992). 

It is our understanding that the true vapor pressure of JP-8 is significantly lower than that of JP-4 and 

that emissions associated with handling and storage of this fuel will result in lower emissions than 

previously reviewed in your present AO. It is also our understanding that no physical changes will occur 

such as tank sizes or the addition of new tanks emission control equipment etc.. 

Since no new equipment will be added and because there will be no change (or a decrease) in emissions, 

no change is necessary to your existing Approval Order. However. if this is a permanent change and you 

wish to receive emission credit for the emission reductions that may have occurred, you will need to 

submit a Notice of intem for a modification to your AO. In addition. if there are other conditions that 

need to be changed such as condition #4 (fuel use limitations etc.) a NOI should be submitted and the AO 

will be modified. 

Thank you for keeping us informed of the changes that are being made to operations at your facility. If 

you have further questions regarding requirements for an AO modification please don't hesitate to call 

me at 536-4096. 

Sincerely, 

,/1 /7 1/)). / 

~X / i J:7~CG\0-- .­

~-eynn R. Menlove, Manager
 

New Source Review Section
 

Utah Division of Air Quality
 

LRM:DC:aj 

4.2.4-415 
/ 

RECEIVED 

DEPARTMENT OF THE AIR FORCE _: AUG 10 1994 

HEADQUARTERS OGDEN AIR LOGISTICS CENTER (AFMC) 

HILL AIR FORCE BASE. UTAH Air QuaP-­

08 August 1994 

OO-ALCIEM 

7274 Wardleigh Road 

Hill AFB UT 84056-5137 

Mr. Russell A. Roberts 

State of Utah 

Division of Air Quality 

P.O. Box 144820 

Salt Lake City Ut 84114-4820 

Re:	 Approval Order DAQE-167-92 for lP-4 Tank Throughput 

Limitations 

Dear Mr. Roberts 

Hill AFB will change from JP-4 to JP-8 in October 1995. The storage 

tank approval order allows a JP-4 throughput of 1,260,000 barrels 

per 12-month period. Since the vapor pressure of lP-8 (0.0085 psia) 

is much lower than JP-4 (1.3 psia), HC-emissions are less than 2% of 

JP-4 emissions. Calculations of the HC-emissions based on 1993 

throughput are included at Attachment 1. AP-42 emission factors for 

the floating and fixed roof tanks and a simplified distribution 

schematic were used to compare JP-4 and JP-8 emissions. 

EdWards AFB, located in California, has changed to JP-8, but 

California does not regulate JP-8 vapor emissions. How will Utah 

4.2.4-416 
<- handle JP-8 vapor emISSIOns and should the Approval Order be 

modified because of the change? 

If you have any questions. please call Mr. Andreas Zekorn at 777­

0359. 

Sincerely 

J~R.~~ JAMES R. VAN ORMAN 

Director of Environmental Management 

Attachment 

He-Emissions calculations 

4.2.4-417
 
Tank #10885 Floating Roof: 

Tank #10873 Floating Roof 

Tank #10861 Floating Roof 

Tank #10862 Floating Roof 

Tank #37 Fixed Roof 

Tank #38 Fixed Roof 

Tank #39 Fixed Roof 

Tank UO Fixed Roof 

Total 

DilTerence 

JP-4
 

2373.5 Ib/yr
 

800.6 Ib/yr 

152.4 lb/yr 

193.5 Ib/yr
 

972.6Ib/yr
 

972.6Ib/yr
 

8991.8 Ib/yr
 

8991.8 Ib/yr
 

23448.7 lb/yr 

11.7 tons/yr 

22951.0 Ib/yr 

11.5 tonslyr 

lP-8 

69.2Ib/yr 

65.0Ib/yr 

3.01b/yr 

10.9 Ib/yr
 

44.8Ib/yr
 

44.8 Ib/yr 

13O.0Ib/yr 

130.0 Ib/yr 

J,rn.7 Ib/yr 

0.2 tonslyr 

-

4.2.4-418
 

- 1 ­
) 

Simplified JP-4 ulstribution Schematic 

I 12483270 gal Distribution 

Fill Stand 

1,2,3 

I 22948680 gal ~--.. -­ Floating Roof Tanks Fixed Roof Tanks

356::;:~' g;rrrY---~.,.J1'-2-3-1-83-2-2-0"'~-a, Fixed Roof Tanks 

1#10861
 

/#10862
 

1110873
 

1110885
 ---~ ...... 234540 gal 

#37 

#38 

tv 

1 

...... 

I.D 

#39 

#40 

- 1a ­
-


External Floating Roof Tanks 

Tank #lQ88S-EmissjoDS with Dual Seal System 

LT=LR+LW+LF+LD 

LT =totalloss(1b/yr) 

LR =rim seal loss 

LW =withdrawal loss 

LF= deck finings loss 

LD =deck seam loss 

LR=KS VN p* 0 MV KC 

LR= rim seal loss Obslyr)
 

KS= table 4.3-4.AP-42. for welded tank with liquid mounted resilient seal
 

and rim mounted secondary seal) 

n= table 4.3-2 ­ D= tank diameter In ft 

MV= molecular weight (Table 4.3-2) 

KC= product factor 

V= average wind speed 

P= true vapor pressure 

PA= average atmospheric pressure at tank locauon 

P*= vapor pressure function 

lP-4 lP·8 

KS= 1.6 

n= o 

MY= 80 lbt1bmole 130 Ibllbmole 

KC= 1 

V= 8 mph 

D= 93 ft 

P*=(PIPA)/( 1+( I-PIPA)"O.5)"2 

PA= 12.4 PSlA 12.4 PSlA 

P= 1.3 PSlA 0.0085 PSlA 

P*= 0.027680768 P*= 0.00017143 

LR= 329.5 Ib/yr LR= 3.3 Ib/yr 

4.2.4-420 

- 2 ­
LW= 0.943 Q C WL ( 1 + (NC FC/D) ) / D 

LW== 

Q= 

C= 

'M..= 

D= 

NC= 

FC= 

Q= 

C= 

'M..= 

D= 

NC= 

FC= 

LW= 

LF=FF p* ~v KC 

LF=
 

FF=
 

P*.MV.KC=
 

P*=
 

MV=
 

KC=
 

FF=
 

LF=
 

withdrawal loss (lb/yr) 

througput (bbUyr) 

shell clingage factor (bbl/lOOO ft"2) 

average organic liquid density (Ib/gal) 

tank diameter (ft) 

number of columns 

effective column diameter 1ft) 

18029375 gal 

~29279.42 bbl 

0.0015 bbUlOOO ft"2 

6.4 Ibs/gal 7 Ibs/gal 

93 ft 

o 

1 

41.81bslyr LW= 45.7 Ibslyr 

fining loss llb/yr) 

total deck fittmg loss factor Ob-mole/yr) 

see above 

0.027680768 P*== 0.00017143 

80 Ib/lbmoJe MY= 130 lbJ1bmole 

1 

316 Ibs Mole/yr 

699.8 Ibslyr LF= 7.0lbslyr 

-


4.2.4-421 

- 3 ­
LD= K.D SD D"2 p* MV KC 

LD= 

KD= 

SD= 

D.P*.~1V.KC=

KD= 

D= 

P*= 

MV= 

KC= 

SD= 

LD= 

deck seam losses (Ib/yr J
 

deck seam loss per unit seam length factor llb-mole/ft yr)
 

deck seam length factor I ftlft"2)
 

see above
 

0.34	 Ib mole / ft yr
 

93 ft
 

0.027680768 0.00017143
 

80	 Ibl1bmoie 130 Ibl1bmole 

J 

0.2 ftlft":! 

1302.4 Ib/yr LD=	 13.1 Ib/yr 

J.P-8 

-. 

4.2.4-422
 
Tank #10873-Emissions with Dual Seal Svstem 

LR=KS V~ p* D \I\" KC 

lP·4 lP-8 

KS= 1.6
 

n= o
 

MV= 80 Ibllbmoie 130 Ibllbmole
 

KC= 1
 

v= 8 mph
 

D=
 63 ft 

P*=(PIPA)I( 1+( I-PIPA)'\0.51"2 

PA= 12.4 PSlA 12.4 PSlA
 

P= 1.3 PSlA
 0.0085 PSIA 

0.027680768 0.00017143 

LR= 223.2 Ib/yr LR= 2.2 Ib/yr 

LW= 0.943 Q C WL ( 1 + rNC FClDl)/ D 

Q= 15368388 gal 

365921 bbl
 

C= 0.0015 bbVI0Q0 ft"2
 

WL= 6.4 Ibslgal \VL=
 7 lbslgal D= 63 ft
 

NC=
 0
 

FC=
 1 

LW= 52.6lbslyr LW= 57.5 Ibslyr 

LF=FF p* ~V KC 

P-= 0.027680768 p-= 0.00017143 

!vfV= 80 Ibllbmole MV= 130 lbllbmole KC= 1 

FF= 237 lbs MoleJyr 

LF= 524.8 Ibslyr LF= 5.3 Ibslyr 

4.2.4-423 

5 ­
KD= 

D= 

P*= 

\1V= 

KC= 

SD= 

LD= 

o Ib mole I f( yr 

63 ft 

0.027680768 

80 Ib/lbmole 

1 

O.~ ftJftA~

0.0 Ib/yr 

P*= 

~1V=

LD= 

0.00017143 

130 Ib/lbmoie 

O.Olb/yr 

4.2.4-424
 

- 6­
Tank #10861·EmjssjoDS with Dual Seal SXStem 

LR=KS V~ p* D MV KC 

KS= 

n= 

MY= 

KC= 

Y= 

D= 

JP-4 

0.7 

0.4 

80 Ibl1bmole 

1 

8 mph 

42.417 ft 

JP·8 

130 Ibl1bmole 

P*=(PIPA)/( 1+( I-PIPA)"O.5)"'2 

PA= 

P= 

12.4 PSlA 

1.3 PSlA 

12.4 PSlA 

0.0085 PSlA 

P*= 0.027680768 P*= 0.00017143 

LR= 151.1 Ib/yr LR';' 1.5 Ib/yr 

/_. LW= 0.943 Q C WL ( 1 + (NC FClD» I D 

Q= 

C= 

WL= 

D= 

NC= 

FC= 

273527 gal 

6513 bbl 

0.0015 bbVlOOO ft'"'2 

6.4 Ibs/gal 

42.417 ft 

0 

1 

WL== 7 Ibs/gaJ 

LW= 1.41bs/yr LW= 1.5 Ibs/yr 

LF=FF p* ~fV KC 

P*= 

MV= 

KC= 

0.027680768 

80 Ibl1bmole 

1 

P*= 

MY= 

0.00017143 

130 Ibl1bmole 

FF= oIbs Molelyr 

LF= 0.0 Ibs/yr LF= O.Olbs/yr 

4.2.4-425 

r _ 
LD= KD SD D"2 p. MY KC 

KD= 

D= 

P*= 

MV= 

KC= 

SD= 

oIb mole I ft yr 

42.417 ft 

0.027680768 

80 IbIlbmole 

1 

0.2 ftlft"2 

P*= 

MY= 

0.00017143 

130 Ibllbmole 

LD= O.Olblyr LD= O.O.lblyr 

4.2.4-426 

- 8 ­
Tapk #10862·EmissioN with Dual Seal SySl4:ID 

LR=KS VN p. DMV KC 

K.S= 

n= 

MV= 

KC= 

v= 

D= 

JP-4 

0.7 

0.4 

80 Ibllbmole 

1 

8 mph 

52 ft 

JP-8 

130 Ibllbmole 

P*=(PIPA)/( 1+( I-PIPA)"O.5)"2 

PA= 

P= 

12.4 PSIA 

1.3 PSIA 

12.4 PSIA 

0.0085 PSIA 

P*= 0.027680768 p*= 0.00017143 

LR= 185.2 Ib/yr LR= 1.9 Ib/yr 

- LW= 0.943 Q CWL (1 + (NC FC/D)) / D 

Q= 

C= 

WL= 

D= 

NC= 

FC= 

1995239 gal 

47507 bbl 

0.0015 bbVlooo ftl\2 

6.4 Ibslgal 

52 ft 

0 

1 

WL= 7lbslgal 

LW= 8.3 Ibslyr LW= 9.01bslyr 

LF=FF P'" 1\1V KC 

P*= 

MV= 

KC= 

0.027680768 

80 Ibllbmole 

1 

p*= 

MV= 

0.00017143 

130 Ibllbmole 

FF= oIbs MoleJyr 

LF= 0.0 Ibslyr LF= 0.0 Ibslyr 

4.2.4-427 

·9· 
-
 LD= KD SD D A 2 p* MV KC 

KD= 

D= 

p*= 

MY= 

KC= 

SD= 

oIb mole / ft yr 

52 ft 

0.027680768 

80 Ibllbmole 

) 

0.2 ftjft A 2 

p*= 

MV= 

0.00017143 

130 lbllbmole 

LD= O.Olblyr LD= O.Olb/yr 

-


4.2.4-428
 

- 10­
Fixed Roof Tanks 

Tank #37-EmissioDS with Fixed Roof 

LB=2.26E·2 MV (P/(PA·P»"O.68 D"1.73 H"0.51 dT"0.50 FP C KC 

LB= breathing loss 

MV= molecular Weight (Table 4.3-2) 

PA= average atmospheric pressure at tank locatIon 

P= true vapor pressure 

D= tank diameter 

H= average vapor space height. including roof volume correction 

dT= average ambient diurnal temperature chnage 

FP= paint factor 

C= adjustment factor for small diameter tanks 

KC= product factor 

JP-4 JP-8 

MV= 80 lb/lbmole MV= 130 Ib/lbmoJe 

PA= 12.4 pSIa PA= 12.4 psia 

P= 1.3 psia P= - 0.0085 psia 

D= 16 ft 

H= 20 ft 

dT= 10 

FP= 1.2 

C= 1 

KC= 1 

LB= 89O.61b/yr LB= 43.91blyr 

4.2.4-429
 

• 11 ­
LW=2.40E-S MV P V N KN KC -


LW= 

MV= 

p= 

V= 

N= 

KN= 

KC= 

MV= 

P= 

V= 

Throughput: 

N= 

KN= 

KC= 

LW= 

working loss 

molecular weight 

true vapor pressure 

tank capacIty 

number of turnovers per year 

turnover factor 

product factor 

JP--4 

80lbl1bmole 

1.3 pSla 

50000 gal 

117270 gal 

2.3454 

0.28 

1 

82.01b/yr 

m.2l lll:1v 

~~ lUp 

~~ a'bl7Ir 

JP-8 

MY= 130 Ibl1bmole 

P= 0.0085 pSla 

LW= 0.9lb/yr 

4.2.4-430
 

- 12·
 
Iank #38-EmissioDS wjth Fixed Roof 

LB=2.26E-2 MV (P/(PA-P))AO.68 DA1.73 HAO.Sl dIAO.SO FP C KC 

LB=Breathing loss 

MV= 

PA= 

P= 

D= 

H= 

dI= 

FP= 

C= 

KC= 

JP-4 

80 Ibllbmo1e 

12.4 psia 

1.3 psia 

16 ft 

20 ft 

10 

1.2 

MV= 

PA= 

p= 

JP-8 

130 Ibllbmole 

12.4 pSla 

0.0085 psia 

LB= 89O.6Ib/yr LB= 43.91b1yr 

LW=2.40E·5 MV PV N KN KC 

,,­

LW=Working loss 

MV= 

P= 

V= 

lbroughput: 

N= 

KN= 

KC= 

JP-4 

80 Ibllbmo1e 

1.3 psia 

50000 gal 

117270 gal 

2.3454 

0.28 

1 

MV= 

p= 

JP-8 

130 lbllbmole 

0.0085 psia 

LW= 82.0 Ib/yr LW= 0.9Ib/yr 

"1'iW Et :E~~:pm;I'Mi §~

JP" JP·8 

U­

!LW. 

~~ll~

~f) n~

~~~ n~

Us 

!.WI!I 

~~

fl~

oo.~

JfJIT! 

J:bI7:r 

]~

]»H1u;!D~; ~~.?

4.2.4-43 I
 

- 13 ­
Tank #39·Emjssjons wjth Fixed Roor 

LB=2.26E·2 MV (P/<PA·P))"'O.68 0"'1.73 8"'0.51 dT"'0.50 FP C KC 

LB=Breathing loss 

MV= 

PA= 

P= 

D= 

H= 

dT= 

FP= 

C= 

KC= 

JP-4 

80 Ibflbmole 

12.4 pSla 

1.3 psia 

16 ft 

20 ft 

10 

1.2 

1 

I 

MV= 

PA= 

P= 

JP-8 

130 Ibllbmole 

12.4 psia 

0.0085 psia 

LB= 89O.61b/yr LB= 43.9 lb/yr 

LW=2.40E-5 MV P V N KN KC 

LW=Working loss 

MV= 

P= 

V= 

'Throughput: 

N= 

KN= 

KC= 

JP-4 

80 Ibllbmole 

1.3 pSla 

50000 gal 

11591610 gal 

231.8322 

0.28 

1 

MV= 

p= 

JP-8 

130 Ibllbmole 

0.0085 psia 

.-" 

LW= 8101.1 lblyr 

!It;smR)!l); A!lIlJ "1) 

LW= 86.1 lb/yr 

JP-4 JP-8 

JLl). 

lLW. 

~,

~n~n.:l

~ll.~

J~

]l/r.r 

a~

U. 

:LW-, 

~~

~ll

1~.~

3~

J~

J~

DmR'lM'!i ~1S~ nat. 

4.2.4-432 

• 14 ­
Tank #4O-EmissiQDS with Fixed Roof 

LB=2.26E-2 MV (P/(PA-P))"O.68 D"1.73 H"0.51 dT"0.50 FP C KC 

LB=BreathlOg loss 

JP-4 

MY= 80 Ibllbmole MV= 

PA= 12.4 psia PA= 

p= 1.3 psia P= 

D= 16 ft 

H= 20 ft 

dT= 10 

FP= 1.2 

C= 1 

KC= 1 

LB= 89O.61b/yr LB= 

LW=2.40E·5 MV P V KN KC 

LW=Working loss 

JP-4 

MY= 80 Ibllbmole MY= 

P= 1.3 psia p= 

V= 50000 gal 

Throughput: 11591610 gal 

N= 231.8322 

KN= 0.28 

KC= 1 

LW= 8101.1 lb/yr LW= 

JP·8. 

130 Ibllbmole 

12.4 psia 

0.0085 psia 

43.9 Ib/yr 

JP-8 

130 Ibllbmole 

0.0085 pSla 

86.1 lb/yr 

1P-8 

~.1i a~ U­ ~.J) ltl7J' 

~1l~:J..1l n~ !LW. M.l ~~

WJ)1l.~ n~ 1l~.:D a~

mJ.tl 

4.2.4-433 

- 15 ­