GB1429331A - Process for the production of synthesis gas and clean fuels - Google Patents
Process for the production of synthesis gas and clean fuelsInfo
- Publication number
- GB1429331A GB1429331A GB1246873A GB1246873A GB1429331A GB 1429331 A GB1429331 A GB 1429331A GB 1246873 A GB1246873 A GB 1246873A GB 1246873 A GB1246873 A GB 1246873A GB 1429331 A GB1429331 A GB 1429331A
- Authority
- GB
- United Kingdom
- Prior art keywords
- fraction
- produce
- effluent
- synthesis gas
- oil
- 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.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS 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
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
-
- 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
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/007—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 in the presence of hydrogen from a special source or of a special composition or having been purified by a special treatment
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS 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
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
1429331 Synthesis gas; fuel oil PULLMAN Inc 15 March 1973 [7 Nov 1972] 12468/73 Heading C5E Synthesis gas is produced by (a) introducing a hydrocarbon feedstock into a catalytic cracking zone in the presence of cracking catalyst, e.g. zeolite under fluid cracking conditions to produce an effluent which is then fractionated to produce a cracked naphtha fraction, (b) hydrogenating this fraction with hydrogen to saturate olefins and aromatics at least partially and produce a more saturated cracked naphtha fraction, and (c) introducing this so treated fraction and steam to a catalytic steam reforming unit to produce an effluent containing synthesis gas. The effluent from (c) may be CH 4 -enriched by adding a CH 4 containing fraction or by hydrogasification, methanation or CO 2 removal. The hydrocarbon feedstock, e.g. crude oil, topped petroleum or a heavy hydrocarbon fraction may be distilled to produce a virgin naphtha fraction, a light gas oil fraction and a heavy bottoms fraction wherein the heavy bottoms fraction is fed to the catalytic cracking zone, the virgin naphtha is blended with the more saturated cracked naphtha fraction from (b) and the light gas oil fraction is blended with part of the heavy bottoms fraction to produce a fuel oil. The fluid cracking catalyst is regenerated in a regeneration zone, producing steam as by-product for the steam reforming stage. A H 2 -rich gas is obtained from fractionation of the catalytic cracking effluent and this is used in the hydrogenation step.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US304508A US3862899A (en) | 1972-11-07 | 1972-11-07 | Process for the production of synthesis gas and clean fuels |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1429331A true GB1429331A (en) | 1976-03-24 |
Family
ID=23176825
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1246873A Expired GB1429331A (en) | 1972-11-07 | 1973-03-15 | Process for the production of synthesis gas and clean fuels |
Country Status (14)
Country | Link |
---|---|
US (1) | US3862899A (en) |
AR (1) | AR217610A1 (en) |
AU (1) | AU468086B2 (en) |
BE (1) | BE798011A (en) |
BR (1) | BR7307588D0 (en) |
CA (1) | CA983718A (en) |
DE (1) | DE2317674A1 (en) |
ES (1) | ES413603A1 (en) |
FR (1) | FR2205567B1 (en) |
GB (1) | GB1429331A (en) |
IN (1) | IN142078B (en) |
IT (1) | IT980838B (en) |
NL (1) | NL7304918A (en) |
ZA (1) | ZA738380B (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3929430A (en) * | 1973-05-14 | 1975-12-30 | Phillips Petroleum Co | Process for making synthetic fuel gas from crude oil |
DE10118248A1 (en) * | 2000-08-18 | 2002-10-17 | Aral Ag & Co Kg | Process for the production of high-purity hydrogen gas with a membrane reactor and a pretreatment step |
US7318845B2 (en) * | 2002-07-10 | 2008-01-15 | Applied Research Associates, Inc. | Compact distillates fuel processor with effective sulfur removal process |
US7238846B2 (en) * | 2002-08-14 | 2007-07-03 | Exxonmobil Chemical Patents Inc. | Conversion process |
US7435760B2 (en) * | 2004-05-14 | 2008-10-14 | Battelle Memorial Institute | Method of generating hydrocarbon reagents from diesel, natural gas and other logistical fuels |
US7381320B2 (en) * | 2004-08-30 | 2008-06-03 | Kellogg Brown & Root Llc | Heavy oil and bitumen upgrading |
US20090007996A1 (en) * | 2005-05-12 | 2009-01-08 | Battelle Memorial Institute | Method for Vibrating a Substrate During Material Formation |
CA2531262A1 (en) * | 2005-12-21 | 2007-06-21 | Imperial Oil Resources Limited | Very low sulfur heavy crude oil and process for the production thereof |
JP5721327B2 (en) * | 2006-12-14 | 2015-05-20 | シェブロン ユー.エス.エー. インコーポレイテッド | Improved process for producing Fischer-Tropsch olefin naphtha and hydrogenated distillate |
US20080237090A1 (en) * | 2007-03-30 | 2008-10-02 | Nicholas Musich | Process and system for redcuing the olefin content of a hydrocarbon feed gas and production of a hydrogen-enriched gas therefrom |
BRPI0805566B1 (en) * | 2008-12-18 | 2018-02-14 | Petróleo Brasileiro S/A - Petrobras | INTEGRATED PROCESS FOR THE MANUFACTURE OF OLEFINES AND INTERMEDIARIES FOR THE PRODUCTION OF AMMONIA AND UREIA |
KR20120004449A (en) * | 2009-04-28 | 2012-01-12 | 유니버시티 오브 써던 캘리포니아 | Efficient and environmentally friendly processing of heavy oils to methanol and derived products |
CN104593041B (en) * | 2013-10-30 | 2016-05-25 | 中国石油化工股份有限公司 | A kind of modifying low-quality heavy oil and hydrogen manufacturing combined processing method |
EA039454B1 (en) * | 2016-09-19 | 2022-01-28 | Сабик Глобал Текнолоджис Б.В. | Steam reforming system and process |
KR20220109784A (en) * | 2021-01-29 | 2022-08-05 | 주식회사 엘지화학 | Method for preparing synthesis gas |
KR20220109780A (en) * | 2021-01-29 | 2022-08-05 | 주식회사 엘지화학 | Method for preparing synthesis gas |
KR20230000240A (en) * | 2021-06-24 | 2023-01-02 | 주식회사 엘지화학 | Method for preparing synthesis gas and aromatic hydrocarbon |
KR20230000227A (en) * | 2021-06-24 | 2023-01-02 | 주식회사 엘지화학 | Method for preparing synthesis gas and aromatic hydrocarbon |
FR3136374A1 (en) | 2022-06-09 | 2023-12-15 | Inserm (Institut National De La Sante Et De La Recherche Medicale) | Composition for the treatment of vitiligo |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3050457A (en) * | 1958-11-24 | 1962-08-21 | Phillips Petroleum Co | Hydrocarbon conversion with the hydrogenation of the cracked products |
US2998380A (en) * | 1959-02-27 | 1961-08-29 | Standard Oil Co | Catalytic cracking of reduced crudes |
US3329628A (en) * | 1963-04-19 | 1967-07-04 | Exxon Research Engineering Co | Synthetic zeolites |
US3607127A (en) * | 1968-04-05 | 1971-09-21 | Pullman Inc | Apparatus for conversion of hydrocarbons |
US3537977A (en) * | 1968-07-08 | 1970-11-03 | Chevron Res | Refinery utilizing hydrogen produced from a portion of the feed |
US3546109A (en) * | 1968-12-30 | 1970-12-08 | Texaco Inc | Method and apparatus for characterization of hydrocarbon mixtures |
US3671419A (en) * | 1970-02-27 | 1972-06-20 | Mobil Oil Corp | Upgrading of crude oil by combination processing |
US3712800A (en) * | 1970-09-04 | 1973-01-23 | Little Inc A | Method for converting residual oils into fuel gas |
US3671422A (en) * | 1970-11-13 | 1972-06-20 | Mobil Oil Corp | Water pollution abatement in a petroleum refinery |
US3726789A (en) * | 1971-04-05 | 1973-04-10 | Ashland Oil Inc | Hydrocarbon conversion process for the production of olefins and aromatics |
US3732085A (en) * | 1971-06-04 | 1973-05-08 | Gulf Research Development Co | Thermally efficient nonpolluting system for production of substitute natural gas |
-
1972
- 1972-11-07 US US304508A patent/US3862899A/en not_active Expired - Lifetime
-
1973
- 1973-02-09 AU AU52021/73A patent/AU468086B2/en not_active Expired
- 1973-03-05 CA CA165,188A patent/CA983718A/en not_active Expired
- 1973-03-15 GB GB1246873A patent/GB1429331A/en not_active Expired
- 1973-04-07 DE DE2317674A patent/DE2317674A1/en active Pending
- 1973-04-09 NL NL7304918A patent/NL7304918A/xx not_active Application Discontinuation
- 1973-04-10 BE BE129848A patent/BE798011A/en unknown
- 1973-04-10 FR FR7312812A patent/FR2205567B1/fr not_active Expired
- 1973-04-12 ES ES413603A patent/ES413603A1/en not_active Expired
- 1973-04-12 IT IT68066/73A patent/IT980838B/en active
- 1973-05-11 IN IN1117/CAL/73A patent/IN142078B/en unknown
- 1973-06-18 AR AR248632A patent/AR217610A1/en active
- 1973-09-28 BR BR7588/73A patent/BR7307588D0/en unknown
- 1973-10-31 ZA ZA738380*A patent/ZA738380B/en unknown
Also Published As
Publication number | Publication date |
---|---|
AU5202173A (en) | 1974-08-15 |
DE2317674A1 (en) | 1974-05-16 |
IN142078B (en) | 1977-05-28 |
IT980838B (en) | 1974-10-10 |
BE798011A (en) | 1973-07-31 |
FR2205567A1 (en) | 1974-05-31 |
BR7307588D0 (en) | 1974-10-29 |
CA983718A (en) | 1976-02-17 |
AR217610A1 (en) | 1980-04-15 |
AU468086B2 (en) | 1975-12-18 |
US3862899A (en) | 1975-01-28 |
FR2205567B1 (en) | 1976-05-21 |
NL7304918A (en) | 1974-05-09 |
ZA738380B (en) | 1974-09-25 |
ES413603A1 (en) | 1976-01-01 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PCNP | Patent ceased through non-payment of renewal fee |