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HomeMy WebLinkAbout912011.tiff mE •„ t 'f -I t•a- i . ._ To Keith Shuett Date Au gu st 79, 7997 C(i RATA From Wes Po t v' o Subject: Hamilton Energy Corporation The staff has reviewed the proposal from Hamilton Energy Corporation to process Ethylene Glycol water mixture in Weld County. It is my understanding that the process involves handling a mixture of water and glycol that is recovered from de-icing of airplanes and distilled to reconstitute the ethylene glycol in a usable fashion. This process is conducted through a standard oil field heater- treater and would be sited at an existing gas processing facility in Weld County. This process seems to be compatible with the existing natural gas processing operations as they exist in Weld County. If this operation is conducted in conjunction with an existing facility, the staff does not find that this would be a significant departure from a normally defined gas processing operation. The applicant should be advised to provide documentation with regard to the total volumes of materials to be handled and any emissions which may be produced in the operation. The applicant should also submit a letter from the State Air Pollution Control Division certifying that there is not a need for an additional air pollution emissions permit. The applicant should request permission to develop this process with an existing facility, and the Division would request an opportunity to review the final proposal as submitted to the Department of Planning Services prior to formal approval from Weld County. WP/lam-336 AUG 2 0 1991 1,41',!-! Se-y.11 9 a..e.c.. rj l Zo t� 1flEff1ORAflDU1fl Keith Schuett, Planning August 16, 1991 To Date Drew Scheltinga, County Engineer COLORADO From } Hamilton Energy Corp. , SUP-264 Subject: I have reviewed the letter dated August 7, 1991 by J.M. Hamilton regarding collecting and concentrating de-icing fluids at their existing natural gas processing plant. Since this proposal would add one 5,000 to 7,000 gallon truck per day, there will be no significant impact on Weld County roads. Also, if the distillation unit and associated tanks are contained within a perimeter dike, there will be no impact on drainage. DS/mw:pr.mrw cc: Commissioner Harbert Planning Referral File - Hamilton Energy Corp. , SUP-264 ' • i APPLICATION FOR AIR POLLUTION EMISSION PERMIT OR PERMIT MODIFICATION This application must be filled out completely except for #14 & #15; otherwise, application will be considered incomplete - SEE INSTRUCTIONS ON REVERSE SIDE. Mail completed application, APENs, and filing fee to: Stationary Sources Program, Air Pollution Control Division, Colorado Department of Health, 4210 East 11th Avenue, Denver, Colorado 80220. 1. PERMIT TO BE ISSUED TO: Hamilton Energy Corporation ,ni ; 2. MAILING ADDRESS: "' " 1 4514 W 68th Ave. Westminster State:ZIP CODE:: 80030-00 - mm Ai�-- 1, i -I,: l 3. AGENT FOR SERVICE (See No. 3 on reverse) ; N/A 4a. GENERAL NATURE OF BUSINESS: Production and processing of 4b. SIC Code: natural gas , Reconcentration of Ethlyene Glycol 5a. AIR POLLUTION SOURCE DESCRIPTION: 5b. Days per year • source will operate Natural Gas fired process heater 330 6a. SOURCE LOCATION ADDRESS: Check if map included: 6b. UTM Coordinates (in km) : SWa Sec. 32 T1S R66W COUNTY ADAMS . _ H _ _ _ _ _V j 7. ESTIMATED COSTS: - Air Pollution Control Procedures or Equipment: 7a. Source, Process Equipment or Project: 7b. Capital Cost: $ Annualized:$ Cap. Cost•$ Annualized:$ 7c. Operating Cost $ /yr. 8a. STATUS • ® New Air Pollution Source [] Existing Source Change (Control equipment added, process change, etc.) : ❑ Other: Projected .Dates for Construction to: Projected Source Startup Date: 8b. Beain: 8/20/91 8c. End: 9/1/91 8d. q/9/q1 9. Enclose check to cover APEN FILING FEES. One APEN should be filed for each emission point: 1 APENs @ $60.0G per APEN a $ hn np 10. S ' TORE OF LEGALLY AU ORIZED PERSON (NOT vendor lla. DATE SIGNED: 1lb. TELEPHONE NO. : •r e� j ' manufac (303) 427-007n 12. T 1•e or print name and official title of person signing item 10. Agency Use Only 14. DATE RECEIVED J.M.Hamilton III President 13. Check appropriate box if you want: a. ❑ Copy of preliminary analysis conducted by Division b. ❑ To review a draft of the permit prior to issuance? NOTE: Checking either item could result in increased fees 15.. PERMIT NUMBER or processing time. See Reverse. APCD:SSP:200C (Rev. 1/84) - - r---- ------- . i .0 APC-200A(10/88) vmmummimmo. ., ,-0 zf w - r,Of nt. to o- 0 0 g 3 I m n m V ' A fro' g m 44 en n own F. O m , ,.- 1:';' n m it N [� 0. ,_�2 A 0 R "� x 2 . r z o :. a x" ~' a "a F z g a 2r a ..g •. •• m r m r o n z p, (D n r (J) nn I�m.n v O i C!• n n H o 0 o y o f, pi o,-, F v 9 Cl Fi 0 o m - a w „ 0 z n 0 o•r n n n N . a •o Z ~ o z N M O ^ C m Ny• .A p y n ru REIM n a z h!y�y oy L.O gj hi O F-� y ? m •d O Hel 47 • dcri ; n-g H O R y I I-f• L�. C Z (Ji hh: 4 R.U O to I . 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IV N'rl I'mto a ° n U) m y C m X m I . v\ J� P 1) C IJJ hS < m W 4. O.1 H ). A N X n O m C . N L O o N o ti F-` n o -p A • I (n " m V' R}�1 P O M . M H I O ...• O 1.J.� .0.070 ' Z Z ra ...m inm tJ n :3:, v n nn O. - ar GS • '0_ v w c a •� ' r 0..=== ▪t^ OH r O c Nv Z n a n a c a z • n '9. • -.- AUGUST 7,1991 STACK EMISSION CALCULATIONS AP 42 FUEL: NATURAL GAS BURNER CAPACITY, MMBTU/HR 1.8 OPERATING TIME,HR/DAY 24 OPERATING TIME, DAY/WK. 7 OPERATING TIME, WK/YR. 48 NOMINAL BTU OF FUEL,BTU/SCF 1000 FUEL USED, MMSCFD/YR 14.5152 EMISSIONS FOR BURNERS PER AP 42, #EMMISION/MM SCF FUEL #/YEAR TON/YEAR NOX 100 1451.52 0.73 CO 20 290.30 , 0.15 SO2 0.6 8.71 0.00 PARTICULATES 1 TO 5 (USE 2) 29.03 0.01 VOLATILES 5.3 76.93 0.04 METHANE 2.7 39.19 0.02 TOTALS 1895.69 0.95 _ VESSELS GAS PROCESSING, LTD. August 22, 1991 Mr. Jim Hamilton Hamilton Energy t,,, ,/ 4514 West 68th Ave. Westminster, CO 80030 RE: Proposed Ethylene Glycol Reconcentration Project Space City Plant Site, Weld County, Colorado Dear Jim: For the benefit of any concerned third parties, the referenced project involves a process that is completely consistent with our normal operations. In any of our plants or remote compressor stations where the dehydration of gas is accomplished, we consider the reconcentration of the glycol used for this purpose to be perhaps the simplest and least hazardous of our functions. Should you require any additional information or confirmation, please do not hesitate to contact us accordingly. Very truly yours, VESSELS GAS PROCESSING,LTD. Ja A. Workman General Manager cc: K.S. Ramsey JAW:dla SUITE 2000 PRUDENTIAL PLAZA•1050 SEVENTEENTH STREET•DENVER,COLORADO B0265 • 303 025-3500 • HAMILTON ENERGY CORPORATION 4514 W. 68th. Ave Westminster, Co. 80030 ( 303 ) 427-0020 Lm I7R AUG 0 8 1991 August 7, 1991 `' Weld County Planning Mr. Keith Schuett 915 10th St . Room 342 Greeley, Co. 80631 Dear Mr Schuett : Pursuant to our conversations, this letter is to furnish information to you concerning a proposed land use within Weld County. The proposed site is an existing natural gas processing plant located at NE1 /4 Sec 31 T1N R65W Weld County. Hamilton Energy Corp. and its partner , Silco Distributing of Denver have formed a joint venture for the purpose of collecting and concentrating the de- icing fluids from the Denver Stapleton Airport . The collection facilities are in place and operating for the last year of more. The second phase of the operation is to install our own concentration facilities to produce a concentrated ethylene glycol /water mixture. Fig. 1 is a flow sheet of the distillation unit , which uses existing technology, an oil field heater treater, modified slightly to perform the distillation process. Referring to Fig. 1 , the product feed is pumped at low pressure ( less than 15 psig) through heat exchangers to the heater treater where heat is applied to drive off the water. Concentrated glycol flows from the bottom of the heater treater through heatexchange to storage. Overhead steam is directed through heat exchange to condense the effluent water stream and is collected in storage, to be returned to the airport de- icing pond. The unit is designed for a throughput of 5000 to 7500 gallons per day based on a feed composition of 15 to 25% ethylene glycol and 85 to 75% water . (Approximately one truck load per day ) Fig. 2 shows a proposed unit layout with feed and product tankage along with the treater unit . It is our intention to locate this unit at the site of existing natural gas processing plant for the following reasons : A. A reasonable supply of natural gas fuel (25 to 50 MCFD required) . B. Normal gas processing operations are consistent with this process. (The dehydration of natural gas is commonly done using ethylene glycol to absorb the water from the gas and the glycol reconcentrated by boiling the absorbed water ) . C. Most of the necessary offsites and infrastructure is in place. From my conversations with various planning and environmental persons it seems that this operation does not fit in the standard processes you are used to dealing with on a specific basis, mainly because this operation is incorporated in a total plant precess or falls under oil and gas production equipment classifications . From my investigations the regulations define this material and process as non hazardous , the material is bio-degradable, and the unit will be exempt from air quality emissions (products of combustion ) because of its small size. Once you have had a chance to review this letter I would like to meet with you to discuss any questions you might have. Sincerely, H milton E ergy C . 44 '4/ , M. Hamilton III President Hti > HM I-3 P4 Sao tzi r d roro 7 t e � ro � x c ro CI 111 En 7d H trJN • ro > o r Hr o H H g• Di x °z > r� HIV 11J N rLri > H O M ITJ CJ ij-3i / ii ztf, 1 . 1 b 1 J rr W 1 a d r(1;1) H O i > 0 H �_ 1 z 0P I trJ ( Tri".... tri I tri ' '-3 d d tli ro Z 0 It o rx) CD11 r 0 I-3 { .. � \ 1 „/".0.20wiern__no .,.,.... ..� .a_e..�.lins. .._m..�. ... .� . - zi/f//';') 7-'/ Hello