KR930000658A - Manufacturing method of high calorific city gas - Google Patents

Manufacturing method of high calorific city gas Download PDF

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Publication number
KR930000658A
KR930000658A KR1019920009888A KR920009888A KR930000658A KR 930000658 A KR930000658 A KR 930000658A KR 1019920009888 A KR1019920009888 A KR 1019920009888A KR 920009888 A KR920009888 A KR 920009888A KR 930000658 A KR930000658 A KR 930000658A
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KR
South Korea
Prior art keywords
reaction
gas
hydrodesulfurization
catalyst
hydrogen
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Application number
KR1019920009888A
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Korean (ko)
Inventor
토시히사 카나마루
쇼오지 우라노
나쯔오 키노시타
케이 오오타
슌지 카오사키
치카시 니시노
Original Assignee
삭가 타다시
사이부 가스 카부시키가이샤
호리 토시오
미쯔비시 유카 엔지니어링 카부시키가이샤
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Application filed by 삭가 타다시, 사이부 가스 카부시키가이샤, 호리 토시오, 미쯔비시 유카 엔지니어링 카부시키가이샤 filed Critical 삭가 타다시
Publication of KR930000658A publication Critical patent/KR930000658A/en

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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Catalysts (AREA)
  • Superconductors And Manufacturing Methods Therefor (AREA)

Abstract

In the process of producing high calorie SNG type city gas from hydrocarbonic crude gas, e.g., butane, propane, naphtha etc., an elementary feed gas is produced by using hydrodesulfurization as a first step, and then secondly further methanizing the product in a column. The hydrodesulfurization uses a nimox catalyst and a zinc oxide adsorbent. The desulfurized feed gas is further methanized on an alumina group carrier supported by nickel to obtain methane-rich gas, i.e. the elementary feed gas in a combined use type column. The necessary hydrogen to be fed into the hydrodesulfurization is obtained from a methanol/water mixture. This hydrogenizing reaction tube is combined within the same column above. Inorganic salt is used as a heat transfer medium heat-sourced in an external furnace and the heat transfer medium temperature branched into two system-flows are controlled by a three-way flow rate control valve simultaneously. The above reaction temperature is about 320<o>C.

Description

고열량 도시가스의 제조방법Manufacturing method of high calorific city gas

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

제1도는, 본 발명 SNG소 원료가스의 제조방법 공정도.1 is a process chart of the production method of SNG cattle source gas of the present invention.

제2도는, 탈유탑구조의 개략을 표시하는 도면.2 is a diagram showing an outline of a deoiling tower structure.

제3도는, 반응탑구조의 개략을 표시하는 도면.3 is a diagram showing an outline of a reaction column structure.

Claims (2)

부탄, 프로판, 나프타등의 탄화수소원료를 수첨탈황으로 유황분을 제거하여, 수증기개질(메탄화반응)을 하여서 소원료가스를 발생시키고, 다음에 탈탄소, 탈수하여 정제한 후, 탄화수소가스로 열량조정을 하는 고열량 도시가스(대전천연가스)의 제조공정에 있어서, ① 수첨탈황을 하는데에, 니목스(Nimox)촉매와 산화아연을 충전한 반응관을 보유하는 1체형열교환방식 U자형 유로(流路)의 탈황탑을 사용하여 동체측의 열매순환에 의하여 350℃정도의 온도를 유지하면서 수소혼합원료를 왕로의 니목스층에서 수소와 원료중의 비활성유 황화합물과 반응토록 하여 황화수소(활성유황 화합물)로 바꾸어서, 그 다음에 복로의 ZnO 층에서 ZnS로 하여 원료중에서 유황분을 제거하고, ② 수증기재질을 하는데에, 알루미나계담체에 니켈을 담지시킨 메탄화촉매를 충전한 반응관을 보유하는 열교환방식 셀튜브형 반응탑을 사용하여 동체측의 열매순환에 의하여 320℃정도의 온도를 유지하면서 탈황된 원료와, 수증기의 혼합물을 촉매를 통하여 1탑으로 1단계의 특정한 반응조건하에서 동온반응시켜 부(富)메탄함유가스를 직접발생시키며, ③ 수첨탈황용수소를 얻기 위해서는, 상기 ②의 반응탑의 일부인 튜브를 수소화촉매를 충전하여 반응관으로서 별도 유로로 사용하고, 메타놀과 물의 혼합물을 같은 온도에서 촉매에 의해 1단계의 특정한 반응조건하에서 등온반응시켜서 부(富) 수소함유가스를 직접발생시켜, ④ 수첨 탈황과 수증기개질의 각각의 최적인 반응온도를 유지하기 위하여 열이동속도가 큰 무기염계의 열매체를 사용하여 순환하고, 발열반응의 열을 흡수하여 흡열반응의 열을 공급하는 동시에 임의의 온도로 조절할 수 있는 2계통의 열매순환계로 실시하는 것을 특징으로 하는 고열량 도시가스의 제조방법.Hydrocarbons such as butane, propane and naphtha are removed by hydrodesulfurization to remove sulfur and steam reforming (methanation reaction) to generate small raw gas, followed by decarbonization, dehydration and purification, followed by calorific adjustment with hydrocarbon gas. In the manufacturing process of high calorific city gas (Daejeon Natural Gas), 1-type heat exchange type U-shaped flow path having a reaction tube filled with Nimox catalyst and zinc oxide, while hydrodesulfurization is carried out. Using a desulfurization tower of), the hydrogen mixture is reacted with hydrogen and an inert sulfur compound in the raw material in the Nimox layer of the royal road while maintaining the temperature of about 350 ° C by the fruit circulation on the fuselage side. Then, sulfur content is removed from the raw material by ZnS in the ZnO layer of the double path, and ② a material of steam is filled with a methanation catalyst having nickel supported on an alumina carrier. The reaction of desulfurized raw materials and water vapor in one step through a catalyst was carried out using a heat exchange cell tube type reaction column having a reaction tube while maintaining a temperature of about 320 ° C. by the fruit circulation on the body side. Under the conditions, the reaction mixture is heated to generate a rich methane-containing gas directly. ③ To obtain hydrogen desulfurization hydrogen, a tube which is part of the reaction column of ② is charged with a hydrogenation catalyst and used as a separate flow path as a reaction tube. Isothermally reacted with a catalyst at the same temperature under specific reaction conditions in one step to directly generate a rich hydrogen-containing gas, ④ heat to maintain the optimum reaction temperature for each of hydrodesulfurization and steam reforming. It circulates using an inorganic salt heating medium with a high moving speed, absorbs heat of exothermic reaction, supplies heat of endothermic reaction, Method of producing a high-calorie city gas, characterized in that to carry the fruit circles of the two systems can be adjusted to. 소원료가스의 정제로서 탈탄산, 탈수를 하는데에 연속류 PSA 방식을 사용하는 것을 특징으로 하는 청구항1기재의 고열량도시가스의 제조방법.A method for producing a high calorific city gas according to claim 1, wherein a continuous flow PSA method is used to decarbonize and dehydrate the small raw material gas. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019920009888A 1991-06-14 1992-06-08 Manufacturing method of high calorific city gas KR930000658A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP3142903A JPH0686598B2 (en) 1991-06-14 1991-06-14 High calorific city gas production method
JP91-142903 1991-06-14

Publications (1)

Publication Number Publication Date
KR930000658A true KR930000658A (en) 1993-01-15

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Country Status (7)

Country Link
EP (1) EP0518269B1 (en)
JP (1) JPH0686598B2 (en)
KR (1) KR930000658A (en)
CN (1) CN1068357A (en)
AT (1) ATE127146T1 (en)
DE (1) DE69204361T2 (en)
TW (1) TW197467B (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU6799996A (en) * 1996-05-29 1997-12-04 Sunkyong Industries Co., Ltd. Gaseous compositions containing a bittering agent
FR2788839B1 (en) 1999-01-22 2001-04-20 Saint Gobain Vitrage METHOD AND DEVICE FOR REGULATING A GAS FUEL CURRENT
KR101256288B1 (en) * 2008-09-19 2013-04-23 그레이트포인트 에너지, 인크. Processes for gasification of a carbonaceous feedstock
CN102583593B (en) * 2012-02-21 2015-12-16 北京纬纶华业环保科技股份有限公司 A kind of method and apparatus processing high concentrated organic wastewater production methane gas
CN106560505A (en) * 2015-09-25 2017-04-12 新地能源工程技术有限公司 Process and apparatus for removing water from synthetic natural gas by using low temperature methanol solution
JP6707049B2 (en) 2017-03-23 2020-06-10 大阪瓦斯株式会社 Method of operating fuel gas production system
CN114110736B (en) * 2021-11-25 2023-02-28 广西电网有限责任公司电力科学研究院 Non-contact heat exchange steam supply method for extracting steam at different steam temperatures

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1544245A (en) * 1976-05-21 1979-04-19 British Gas Corp Production of substitute natural gas
NL7908283A (en) * 1979-11-13 1981-06-01 Veg Gasinstituut Nv PROCESS FOR THE PRODUCTION OF SYNTHETIC NATURAL GAS FROM HYDROCARBONS.
GB2154600A (en) * 1984-02-23 1985-09-11 British Gas Corp Producing and purifying methane

Also Published As

Publication number Publication date
ATE127146T1 (en) 1995-09-15
EP0518269A3 (en) 1993-05-12
EP0518269A2 (en) 1992-12-16
JPH04366200A (en) 1992-12-18
DE69204361T2 (en) 1996-03-21
DE69204361D1 (en) 1995-10-05
EP0518269B1 (en) 1995-08-30
JPH0686598B2 (en) 1994-11-02
CN1068357A (en) 1993-01-27
TW197467B (en) 1993-01-01

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