Document n9kyGDqZDZRoQ3xrgXZDg5y2m
P. O. BOX 471, TEXAS CITV, TEXAS 77S90
June 9, 1977
Mr. Dennis Haverlah Permits Section Texas Air Control Board _ 8520 Shoal Creek Boulevard Austin, TX 78758
*
Dear Mr. Haverlah:
Subject: TACB Construction Permit Application - Fuel Conversion, No. 2
% Powerhouse - Boiler No. ^3
*
Per our April 12th meeting, attached for your preliminary evaluation is a
General Application Form PI-1, Table 4 (Combustion Units), and Table 6 (Boilers and Heaters) covering our proposed fuel conversion project which would allow us to burn up to 0.7X Sulfur content fuel oil at our No, 2 Powerhouse Boiler No. 23. As discussed, the results of your preliminary evaluation with regard to the presently proposed revisions to TACB Regula tion II will be conveyed to us sp that we may thoroughly examine any pro ject changes, if any, which might be needed to obtain TACB Construction Permit approval.
In brief, Boiler 23 will be converted to oil burning capabilities by burner revisions, soot blower additions, opacity monitoring equipment and Instru ment additions. Oil handling facilities will Include a day tank, heat
exchangers, pumping facilities, and Interconnecting piping. All facilities will be heat traced and insulated. Additional information will be submitted
to your office as soon as specific engineering data becomes available regarding this project. If you should require any additional information, please feel free to contact me.
jrs very trul
RE0:ir
Attachments cc: Clark Benson
Lloyd Stewart
BCC Note
UCC
050416
bcc: Mr. J . F. Erdmann/Mr. J. B. Leverton/ As recommended by J. D. Martin and R. L,
Mr. F. S. Provenzano/P. M. Files Wright, this application is being sub
Mr. G . R. Halter
mitted prior to DOF issuance in order to
Mr. L . E. Kibbee- 511
avoid complications with possible future
Mr. J . D. Martin- 510
regulations. In addition, certain supple
Mr. A . W. McCloy
mental information to complete this per
Mr. J . V. Murray - 501
mit application will be required for sub
Mr. R . L. Wright- 510
mittal to TACB before the construction is
Mr. L . D. Pell
completed and an operating permit can be
Mr. C . 0. Steinmetz Mr. R . Van Mynen
applied for. We will Be advised by the TACB what they will require in this ins
Mr. V . F. Villani - 511
tance, Attached is a copy of the pro
posed revisions to TACB Regulation II.
TEXAS AIR CONTROL BOARD FORM PI-1, GENERAL APPLICATION (Read Instructions Before Completing.)
I. PERMIT TO BE ISSUED TO; UNION CARBIDE CORPORATION. Chemicals and Plattlrs
(Corporation, Company. Government Agency, Firm, etc.)
Mailing address
P. 0. Box 471, Texas City. Texas 77590_________________
Individual authorized to act for applicant: Name- Robert 0 BrYflP
.Title: Process Engineer
Address; p- 0. Box 471, Texas Citv. T&xas_7759Q ______
.Telephone: (713) 945-7411 ext.
1362
II. LOCATION OP PERMIT UNITS (Latitude and Longitude must be to nearest second): Name of plant or site: Texas Cjt/_Pla_ntstreet address (if available): 3301 - 5th Avenue South_____________
Nearest city: TeXd$ City County:-- GalvestOfl
Latitude. .29?
Longitude: -34-- 56*
S'*
III. TYPE OF OPERATION OR PROCESS OF PERMIT UNIT;.
A. Name of operation or prooesa of permit unit: Fuel Conversion, No. 2 POwerhOUSe
B. Permit unit identification number:_____________________________ 5____________________________________
C. Type (check one):
08 Permanent
D Portable
D Operating schedule: Houri/day -24.---------- Days/week
7 ----- ---------------Weeks/year .....,52-
IV. PERMIT\lNIT CLASSIFICATION (Check applicable blocks)*
Boiler No. 23
A. etn B. a C, 1----- 1 D. CTT] E. (=7)
New Permit Unit. Proposed start of construction Modification of Permit Unit Change in Location Change in Ownership Permit Unit Now Operating Under Permit Number
(Date) R-
.Start of operation 4th ..QtF 1373. (Date)
V. If Items IV.A, B, or C were checked, submit the - following information under either A or B:
A. Data requested in Bl, B2 and B3 has been previoualy submitted under Permit No.
B.l. Submit three copies of an area map to approximate scale showing the location of the property, the land use designations for adjacent and nearby lands which may be affected by the emission, geographical features such as highways, roads, streams and sqptificant landmarks, distance to the center of nearest city or town if located outside an incorporated municipality. If the property is located within a town or city, a city map may be used to preaent this information, and if outside a town or city, a county high way map may be used. County highway maps may be ordered either through the Texas Highway Department, Austin, Texas or through the State District Highway Engineer for the county.
b 2 Give a legal deicription of the tract of land upon which the plant or facility is located. The term "legal description" means either a metes
and bounds description, or the block and lot number of a platted subdivision which would be suitable to effectuate the transfer of title to teal property. e.3 Submit a plot plan of the property, to scale, showing the boundaries, plant bench mark (latitude-longitude), the location of all emiSBon points of any air contaminants on the property, the distance from each emission point to the nearest boundary tine, prevailing wind di rection. true north direction, a scale and any other information deemed relevant by the applicant. Identify the emission points by num bers; use the same numbers for those emission points in this permit that win be assigned in the flow diagram and which will be used in present or future emissions inventory questionnaires.
VI. If Item IVJE is not checked, submit the following information:
A. Process Flow Diagram. Prepare and attach a flow diagram identifying significant individual processes and/or operations. Identify (by num ber) points where taw materials, chemicals, and fuels are introduced, where gaseous emissions and/or airborne particulates may be dis charged including intermediate release! where finished products are obtained, and location of pollution control devices. Description of Process. Prepare and attach a written description of each process and of the function of the equipment in the process. (Identify items of equipment by numbers corresponding to flow diagram numbers.) The description must be in suffleient detail to deter mine the general operation of the process. Particular attention must be given to explaining all stages In the process where there is or may be a discharge of any solid, liquid, or gaseous materials) into the atmosphere. Estimate number and type of air pollution abatement de vices to be used such as 1 electrostatic precipitator, 2 cyclones, 1 incinerator, 2 bughouses, etc.
VII. A copy of the application is being sent to the Regional office of TACB?
BYes
NoD
A copy of the application is being sent to local city or county Air Pollution Control Program? a Yes
VIII. I.
Robert E. O'Bryan
Process EngT nee r
(Name)
(Title)
No
state that I have knowledge of the facts herein set forth and that the same a, 1 '`urther state that to the best of my knowledge and belief, the project for M-von of the Texas Clean Air Act. Article 4477-5, Vernon's Texas Civil Texas Air Control Board or any local governmental ordinance or resolutioi
xue and correct to the best of my knowledge and belief. Ipplication is made wilLnot in any way violate any pro-
pnde^ot at^ Cle rules and regulations of the Tin H Inn Air Act.
datf 9 June 1977--
____ SIGNATURES
ucc 050417
FORM PI-2 (72-9)
TABLE 4 COMBUSTION UNITS
OPERATIONAL DATA
Number from flow diagram Name of device: Boiler No. ?3
Model Number (if available): Bypass - H Manufacturer: Babcock & Wilcox
CHARACTERISTICS OF INPUT
1
ii________ *
tii Material
Chemical Composition
Min. Value Expected ! Ib/hr
Ave. Value Expected lb/hr
li
L. L Ethanol t Reside___
0__
600
1 2. Isopnopanol ReSid.
i 3.
1
0
150<f
! 4.
!
!
! Design Maximum Ib/hr
; 1200
i 3000 i |
! 5.
JGross Heating Value
of Vsaste Material (Wet basts if applicable) |
Btu/lb 12000
i1
1 Minimum
Air Supplied fot . SCFM (70F A 14.7 psia)
Waste Material |
4000
| Maximum
j SCFM (70<F & 14 7 psia) j 8000
Contaminated Gas
t Total Flow Rate 1 Inlet Temperature
lb/hr
op
1 Mirimum Expected
Design Maximum
j
Minimum Expected
| Design Maximum 1
1 Material
Chemical Composition
Mm Value Expected lb/itr
xve. Value Expected Ib/hr
1
Design Maximum Ib/hr
f uel
i #4 Fuel Oil ;
8,ooo
12,000
13,000
;
<3. t ; 4.
Gross Heating Value of Fuel
i
J | 1
Btu/lb 16.500
!. i\
_________ I .. .. '
_ _____
1 ..
Air Supplied for Fucl ,
^ Minimum | SCFM (70<'F & 14.7 psia) ; ISjQQCI.
! Maximum ! SCFM (70op & 14.7 psia)
I 7a*HQQ_
Describe how waste material is introduced into combustion unit on an attached sheet. Supply drawings, dimensioned and to scale to show- clearly the design and operation of the unit
i ICC
0SQ41&
-------- ^ I ORM PI 2 (72 V)
1 AIM I (.
BOILERS A NO HEATERS
Type hi ik wiv Boiler No.. 23
..Manufacturer _Babcock 4 W_11 cox_
_Number Irmn llnw di.ijgr.im
. Mode) NimilnTj..
Type Fm*l
#4 Fuel Oil i
____ OiARAtIRJSTKintjNPi)L
Chemical Composition
Inlet Air Temp WF
CJt b\ Weight)
(after preheat 1
C-
11 SASH -
87.95%
11.25% .70% .10%
800 F
Gross Heating Value of Fuel (specify units)
Average
Fill- Flow Rate (scf m or lb/hr)
Design Maximum
12,000
13,000
Average
Total Air Supplied fsefm*)
Design Maximu n
16,665 BTU/Lb 79,200
79,200
Type Transfer Medium (Kau*r, ml.iu l
HEAT TRANSFER MEDIUM
Temperature F
Input
Output
Pressure (psia)
Inpul
Output
Flow Rate (specify units)
Avc.
Design Max.
Water
300 830
1100 1000
310,000 lb/hr
350,000 lb/hr
Avc Foe Hox lcmp at max tiring rate
OPERATING CHARACTERISTICS
Fire Box Volume (ft.^),
Gas Velocity in Fire Box
(from drawing)
(ft/soc) at max Firing rate
Residence Time in F ire Box
at max firing rate (sec)
2,200F
MUxjcuL - .
Hue Gas
CHARACTERISTICS OF OUTPUT Chemical Composition of Exit Gas Released 17c bv Volume)
co2 12.1% h2o 10.6%
$0,, 0.036%
N,
74.5% 2.8%
Attach an explanation on how temperature, air flow rate, excess air or other operating variables are controlled.
Also suppK an assembly drawing, dimensioned and to scale, in plan elevation, and as many sections as are needed to show clearly the operation of the combustion unit. Show interior dimensions and features of the equipment necessary to calculate its perfor mance.
Standard Conditions: 70PF. 14.7 psia
t. ICC
050419
- ijT tr
TABLE 4 . COMBUSTION UNITS
FORM PI-2 (72-9)
received
JUN 8 \$n
R.E.O'B
OPERATIONAL DATA
Number from flow diagram:
Model Number (if available): ...
Name of device: t/ezi %o/l.
Manufacturer:
CHARACTERISTICS OF INPUT
____ (L * UfiLc.cc
Chemical Composition
*
Waste Material*
Material
st+a hoc Z !$***A!*L * 3. 4.
Min. Value Expected Ib/hr
c
a
Ave. Value Expected Ib/hr
6 CO
\ TOC
Design Maximum Ib/hr
/ZOO
*5 ooo
5.
Gross Heating Value of Waste Material
(Wet basis if applicable)
Btu/lb
/&
Air Supplied for Waste Material
Minimum
SCFM (70F & 14.7 psia)
COOP
Maximum SCFM (70F & 14.7 psia)
M*CL
Waste Material or Contaminated Gas
Total Flow Rate Ib/hr
Minimum Expected
Design Maximum
Inlet Temperature
of
Minimum Expected
Design Maximum
Chemical Composition
Fuel
Material
I. to 4-&5L 2. 3. 4.
Min. Value Expected Ib/hr
ff. oeo /
Ave. Value Expected Ib/hr
Design Maximum Ib/hr
rz /
etc --------------
------ /?
votrPi---------------
Gross Heating Value of Fuel
Btu/lb
Air Supplied for Fuel
Minimum SCFM (70OF & 14.7 psia)
Maximum
SCFM (70F & 14.7 psia) 7&Ao_
Describe how waste material is introduced into combustion unit on an attached sheet. Supply drawings, dimensioned and to scale to show clearly the design and operation of the unit.
ucc
050420
i Aim (i
BOILERS AND HEATERS
I ORM PI-2 (7'.9) RECEIVED
JUN 8 1977
R.E.O'B
Tyin- nl I Vviio.
Number from Jlow diagram:
.. _
fjp Zgjt
Manufacturer _______________ _Model Number......___
AC.Q.utz. cr
ay
__ // ___________
Type Enel
f*sC OIL.
CHARACTERISTICS OF INPUT
Chemical Composition
Inlet Air Temp F
(% by Weight)
(after preheat)
c-
//5-
fr>6
// i r ' `7 '
eoo"r
Gross Heating Value of Fuel (specify units! /*, 66yi*
Fuel Flow Rate (sefni* or lb/ht)
Average
Design Maximum
it,, COO
1J, coo
Average
Total Air Supplied fscfm*!______
j Design Maximu n
19.
z-co
Type Transfer Medium (Water, oil. etc.)
Temperature F
Input
Output
Pressure (psia)
Input
Output
Flow Rate (specify units) Ave, Design Max.
t" Are/z.
Avc. Fire Box Temp, at max. firing rate
loo
1/06 /COO
OPERATING CHARACTERISTICS
Fire Box Volume (ft.^).
Gas Velocity in Fire Box
(from drawing)
(ft/sec) at max firing rate
-3 TOfoco<-^ _________
Residence Time in F ire Box
at max Firing rate (sec)
-Z7, GO /~
Stack Diameters
7f
Material ft V 5
a as
130 FFj/rec-
/. ^ sec,
Stack Height
/
STACK PARAMETERS
Stack Gas Vel.icjU (ft/secj_
Stack Gas Temp (` F)
(@'Ave. Fuel Flow Rate) (ftMax. Fuel Flow Rale)
*3. o
Ql.o
q-os V
CHARACTERISTICS OF OUTPUT
Chemical Composition of Exit Gas Released i% bv Volume!
co^
iL.f
A l4-.r %
$0*
>0 c.03%
z. 2. ez
Attach an explanation on how temperature, air flow rate, excess air or other operating variables are controlled.
Also supply an assembly drawing, dimensioned and to scale, in plan, elevation, and as many sections as are needed to show clearly the operation of the combustion unit. Show interior dimensions and features of the equipment necessary to calculate its perfor mance.
* Standard Conditions: 70^F. 14.7 psia
[
c^s Air Control Board
tgjiafcon II-- Control of'Sc^ Pollution from Sulfur Compounds!
, f'wdci-fi fConanttXLtu>n **'<??
i Ground Level Concentration.'t31:04-0.1*'<
or perpni^lu^.^
jTtv Texas Air Control Board is.proposing to amend* '; sulfur dioxide TnjttT a.j^ur^e or source* pules 131 (M 01 007- 009 to allow more flexibility for i property jor.'auiltiple^urcea operated Li/ft inoditicanon and growth in .Galveston, Harris, i . !.jprope<|iis*)^tp exceed tS$et ground levei coj*f--"' ^iciTermiii. and Orange Counties.Industrial sourcesare ' ^ O.S&^m^M'ereged d^er any 36:?tiioute ~l
ji'unvertnig from natural gas to either,a$l or coal due Jto.i ftfie decline of the natural gasrpeerves. -PRolesA
?i 04 01 007 and .008 presently require that the riet`i $,,wina level concentrations for all contiguous properV' iu>s pe limited to 0.28 ppm and
* ei>loaCfnjfattfm mTfe foreon *in Jeffijhon
eau#e,>aufrer, aliqw.of perpvit^j - -' W^r;.touri*a.ep nrwl.dpe^te
lP m, T -A* ,,
f,
11tUa-ievids specified in Rules"lSii^^ OOt Vnd.j^SS^
(tiground
?*&*> set effective March 5,19t2iio'jprt8ct the8e criiih^
s'asyja^-i
j'.ic*. /r.im deterioration of the arifbient'Jevelsbf sulfur^ |.,i..siile he\end the secondary arobient'eir quality stab-#
i4>W'd for svdrur dioxide. The hoardalspaHopted ildgula^ effective March 5, 197%qniiHSg all neafjon#;
iirtruouon nr modifications to obtairva.permit.
~T&p$iSS$Z \permit emissions -of Xulfqr
irpsa operabed on a property Hon fcontiguous propertied tO^:
k -
^ *V
- #' x
|tbn V*I also protects the ambient-levels by -reqnfCingti
controls and emission jlrfitatidri? from ri*W dr' ^tidd'ed sources The secondaygf'^Vtlbrd fof^nmur/
:t$ other, th*n Bl+
^ - -!
Srm. ^Grange lEic^tia^ ** Pf...
dioxioe was issued on April 30,il&tl;arTd included thd*
following provisions: an annudl arithmetic meani-tqgi^ ;centrat ion of 60 micrograms jraJ^^etei^;j<MKj|L c|tyftep^i
or contiguous properties ix& -\
'mts of Rule 131.04.<n.00?T saionsourw is congtnkt^G
ppm); a maximum 24~hou*eonpentrat"ill'?? njicrograms per cubic metej^^^.'ppA^f,.not tAP
clyrt'wVty or"properties l ?fU^jroviding all of thef "
ceeded more than once per yi&i^n'dfc maximujfAl hour concentration of 1.3003incrogrn(nsmeter (0.5 ppmnot to be exctfalWre tosn once M
n and operation of the,n.s,-- e^on|^urce meets any applicable
year
c.^?'
-
SourCsRarformance Standard and utilised
fyja.-; 4^wjtfa^paifeiQontrot technology, with consideration to On September 14, 1973, the EhVirifi^pUi! PWl^VV^Wma^ySirt^^fahility andVcnnnmic reasanable-
Agency revoked the annual arithmetic mean a no t if
ofyedociByg or eliminating the emissions from the
maximum 24 hour portions of the;Standard Th i;i j^otlity. '' /'V\
--
ondary standard now consists of a maximum ,-LOi'nt .,.1- i2f^ThejMmstA^h^ and^iper^ion of the new hour concentration of 1,300 micrograrn^ per-cyh/1^ pr modif^^^^nisston souredt 4bes not Xause
t meter <0.5 ppm), not to be exceeded more titan ona.< u4r nribpt^^i^^^iditio^.such that either the"prithdT-W "7
year.
^
^ if^,thfemdary $uWf doriie a*r quality standards *re- :
The board has concluded that ppm net ground level conte^ien*?
i. * *?*?* "1
^
properties is more stringent than required i.o.pTo1j^^ff^<>r to tfaa effectlve date f,rUj^COD' ^
against violations of the secondary fstandatil `.'
OtMl tofcSfftl oomphance with Rule 131.04.01.009 otan ^
board is proposing that the 0.28 ppm and <tV2?]** ob^ained pur`Uant to
levels be applied to single propefU^s and ;f)-4`ppmr
, vi . .
ground ievel concentration be. spplj^d .tn'
properties in the alTected
eludes that these measuresg,. cw?jjinbwtniedo witnh P& tDWqjpj:^^'lTTTS2S5a8O0- Charles R. Barden. P.E. .'-^ ; ;T'
VI, will provide adequate .pn>|eiqh of tins-
i ; ^ V;
Executive Director
ambient air quality standards {dikrftfifijr diood" ;J'
1 *:-
Texas Air Control board
Public vited.
9:30 a
> ,IC^
"-b.fi
comment on the proposal^>niemtmvot'.
A public hearing will be heldNm -iune. 2'LJV
m , in the auditorium of the Texa- Air <'o*>,;?ofi
^
- * ' i'fbeotsdOstSblAdoption:
WittSn60dsys.rihublidhesrins-'A-yi
For kstnarMonratton. ptan csU45t 2) 45ts6?11 ,*xl.441.
Board, located at 8520 Shoal Creek Bouievani Av (in,
and on June 30, 1977, 1:30 p m., in the the City of Houston Health Department, i<> .;ih!
>,f ;> i
V/|,mr 2 Number 4.1 Afov .?/. 1977
North MacGregor, Houston, for the purp > ' j:v- <' :t 1 ' -
ing public testimony relative to the pr'.;i. t > .i .'-v ments. Interested persons are invited to o.;,mr.
SfcCfS7C
views, and recommendations on the .uniT.'i/u^nfs.
either orally or in writing. Written statement-, m.4v in-'
submitted prior to the hearing by maiiing 15 tor-nw 4;'
such statements to the Texas Air Control H i *
Shoa! Creek Boulevard, Austin. Texas ~P\
UCc
n S042-
w >/ vv/1
*+*
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UCC
050423