GB2015027A - Reforming process - Google Patents
Reforming processInfo
- Publication number
- GB2015027A GB2015027A GB7903753A GB7903753A GB2015027A GB 2015027 A GB2015027 A GB 2015027A GB 7903753 A GB7903753 A GB 7903753A GB 7903753 A GB7903753 A GB 7903753A GB 2015027 A GB2015027 A GB 2015027A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reactor
- ratio
- calculated
- reforming process
- feed gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title abstract 2
- 238000002407 reforming Methods 0.000 title abstract 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 abstract 3
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 abstract 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 abstract 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract 1
- 239000005864 Sulphur Substances 0.000 abstract 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 239000003054 catalyst Substances 0.000 abstract 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 150000002430 hydrocarbons Chemical class 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 229910052750 molybdenum Inorganic materials 0.000 abstract 1
- 239000011733 molybdenum Substances 0.000 abstract 1
- 229910052759 nickel Inorganic materials 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/40—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts characterised by the catalyst
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1047—Group VIII metal catalysts
- C01B2203/1052—Nickel or cobalt catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
Abstract
The invention relates to a reforming process the object of which is to give a reducing gas having a high reduction potential from a feedstock rich in methane and generally containing 0.5-10% v/v of higher hydrocarbons, yet avoiding carbon formation. This is achieved by having a sulphur content in the feed gas introduced into the reactor of 2-10 ppm by vol., calculated as H2S; by using in the colder parts of the reactor a catalyst containing 2-20% w/w of nickel and molybdenum, calculated as oxides, the atomic ratio Mo:Ni being 1:1-4:1, supported on a carrier consisting of 70-80 w/w of alumina and 30-20% w/s of zirconia; and by having an O/C ratio of 0.8-1.3 and an H2O/C ratio of below 0.4 in the feed gas mixture fed into the reactor.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB7903753A GB2015027B (en) | 1978-02-03 | 1979-02-02 | Reforming process |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB447278 | 1978-02-03 | ||
GB7903753A GB2015027B (en) | 1978-02-03 | 1979-02-02 | Reforming process |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2015027A true GB2015027A (en) | 1979-09-05 |
GB2015027B GB2015027B (en) | 1982-06-23 |
Family
ID=26239148
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB7903753A Expired GB2015027B (en) | 1978-02-03 | 1979-02-02 | Reforming process |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB2015027B (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4631182A (en) * | 1984-02-01 | 1986-12-23 | Haldor Topsoe A/S | Process for preparation of a reducing gas |
EP0303438A2 (en) * | 1987-08-14 | 1989-02-15 | DAVY McKEE CORPORATION | Production of synthesis gas from hydrocarbonaceous feedstock |
EP0320979A2 (en) * | 1987-12-17 | 1989-06-21 | Osaka Gas Co., Ltd | A process for steam reforming of hydrocarbons |
EP0398251A1 (en) * | 1989-05-15 | 1990-11-22 | Osaka Gas Co., Ltd. | A process for steam reforming of hydrocarbons |
US5685890A (en) * | 1987-12-17 | 1997-11-11 | Osaka Gas Company Limited | Process for steam reforming of hydrocarbons |
US5997835A (en) * | 1997-06-10 | 1999-12-07 | Haldor Topsoe A/S | Process for steam reforming of hydrocarbons |
EP2969923A1 (en) * | 2013-03-15 | 2016-01-20 | LG Fuel Cell Systems Inc. | Catalysts for hydrocarbon reforming |
CN109721027A (en) * | 2017-10-27 | 2019-05-07 | 中国石油化工股份有限公司 | The method of methane hydrogen sulfide reforming reaction hydrogen manufacturing |
-
1979
- 1979-02-02 GB GB7903753A patent/GB2015027B/en not_active Expired
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4631182A (en) * | 1984-02-01 | 1986-12-23 | Haldor Topsoe A/S | Process for preparation of a reducing gas |
EP0303438A2 (en) * | 1987-08-14 | 1989-02-15 | DAVY McKEE CORPORATION | Production of synthesis gas from hydrocarbonaceous feedstock |
EP0303438A3 (en) * | 1987-08-14 | 1989-12-27 | DAVY McKEE CORPORATION | Production of synthesis gas from hydrocarbonaceous feedstock |
EP0320979A2 (en) * | 1987-12-17 | 1989-06-21 | Osaka Gas Co., Ltd | A process for steam reforming of hydrocarbons |
EP0320979A3 (en) * | 1987-12-17 | 1989-11-15 | Osaka Gas Co., Ltd | A process for steam reforming of hydrocarbons |
US5685890A (en) * | 1987-12-17 | 1997-11-11 | Osaka Gas Company Limited | Process for steam reforming of hydrocarbons |
US5124140A (en) * | 1989-05-15 | 1992-06-23 | Osaka Gas Company Limited | Process for steam reforming of hydrocarbons |
EP0398251A1 (en) * | 1989-05-15 | 1990-11-22 | Osaka Gas Co., Ltd. | A process for steam reforming of hydrocarbons |
US5997835A (en) * | 1997-06-10 | 1999-12-07 | Haldor Topsoe A/S | Process for steam reforming of hydrocarbons |
EP2969923A1 (en) * | 2013-03-15 | 2016-01-20 | LG Fuel Cell Systems Inc. | Catalysts for hydrocarbon reforming |
EP2969923B1 (en) * | 2013-03-15 | 2022-06-22 | LG Fuel Cell Systems Inc. | Catalysts for hydrocarbon reforming |
CN109721027A (en) * | 2017-10-27 | 2019-05-07 | 中国石油化工股份有限公司 | The method of methane hydrogen sulfide reforming reaction hydrogen manufacturing |
CN109721027B (en) * | 2017-10-27 | 2020-07-03 | 中国石油化工股份有限公司 | Method for producing hydrogen by reforming reaction of methane and hydrogen sulfide |
Also Published As
Publication number | Publication date |
---|---|
GB2015027B (en) | 1982-06-23 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
746 | Register noted 'licences of right' (sect. 46/1977) | ||
PE20 | Patent expired after termination of 20 years |
Effective date: 19990201 |