ES8503717A1 - Auto-thermal reforming by partial oxidn. and steam reforming - Google Patents
Auto-thermal reforming by partial oxidn. and steam reformingInfo
- Publication number
- ES8503717A1 ES8503717A1 ES526076A ES526076A ES8503717A1 ES 8503717 A1 ES8503717 A1 ES 8503717A1 ES 526076 A ES526076 A ES 526076A ES 526076 A ES526076 A ES 526076A ES 8503717 A1 ES8503717 A1 ES 8503717A1
- Authority
- ES
- Spain
- Prior art keywords
- hydrocarbons
- steam reforming
- catalyst
- feed
- mixt
- 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
- 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
-
- 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
- C01B3/36—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 oxygen or mixtures containing oxygen as gasifying agents
-
- 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
- Y02P20/10—Process efficiency
Abstract
Prodn. of synthesis gas is effected in two stages: (i) catalytic partial oxidn. of a feed mixt. comprising hydrocarbon feed stream, H2O and O2-contg. gas; the preheated feed mixt. being contacted with a monolithic (honeycomb-type) catalyst (I) comprising Pd and Pt (andopt. Rh) on a refractory metal oxide, and (ii) catalytic steam reforming of the first-stage effluent over a Pt-Rh steam reforming catalyst. Specifically, the feed mixt. to stage (i) is controlled to give an H2O:C ratio of 0.5-5 and an O2:C ratio of 0.2-0.8, and the step is carried out at 1-142 atm. and at such temps. that at least part of (I) is at at least 121 deg.C above the ignition temp. of the inlet stream, providing cracking of any unoxidised 5C + hydrocarbons to light (4C or below) hydrocarbons. The specifically claimed embodiments relate to integrated processes utilising the H2-rich product gas for the prodn. of (A) ammonia, (B) methanol, (C) SNG and (D) liq. hydrocarbons. Very low catalytic metal loadings may be used. Operation is at relatively low H2O:C and O2:C ratios, without catalyst fouling by C deposition.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US43020082A | 1982-09-30 | 1982-09-30 | |
US43032082A | 1982-09-30 | 1982-09-30 | |
US43014782A | 1982-09-30 | 1982-09-30 | |
US06/430,451 US4844837A (en) | 1982-09-30 | 1982-09-30 | Catalytic partial oxidation process |
Publications (2)
Publication Number | Publication Date |
---|---|
ES526076A0 ES526076A0 (en) | 1985-03-01 |
ES8503717A1 true ES8503717A1 (en) | 1985-03-01 |
Family
ID=27503782
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES526076A Expired ES8503717A1 (en) | 1982-09-30 | 1983-09-29 | Auto-thermal reforming by partial oxidn. and steam reforming |
Country Status (2)
Country | Link |
---|---|
KR (1) | KR910009208B1 (en) |
ES (1) | ES8503717A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100361363B1 (en) * | 1994-06-22 | 2003-02-14 | 엘지전자 주식회사 | Drive device of full automatic washing machine |
-
1983
- 1983-09-29 KR KR1019830004626A patent/KR910009208B1/en not_active IP Right Cessation
- 1983-09-29 ES ES526076A patent/ES8503717A1/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
KR840006170A (en) | 1984-11-22 |
ES526076A0 (en) | 1985-03-01 |
KR910009208B1 (en) | 1991-11-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0262947B1 (en) | Catalytic generation of hydrogen from hydrocarbons | |
CA2222146A1 (en) | A method for flame stabilization in a process for preparing synthesis gas | |
KR100245781B1 (en) | Process for manufacturing synthesis gas and their device | |
CA2153304A1 (en) | Process for the preparation of hydrogen and carbon monoxide containing mixtures | |
WO1998008771A3 (en) | Method and apparatus for converting hydrocarbon fuel into hydrogen gas and carbon dioxide | |
CA2247528A1 (en) | Method for hot gas conditioning | |
EP0154492A3 (en) | Multiple-stage reactor system for a moving catalyst bed | |
WO1990006281A1 (en) | Production of ammonia from hydrocarbonaceous feedstock | |
ES8305291A1 (en) | Process for the preparation of organic compounds | |
US4176087A (en) | Method for activating a hydrodesulfurization catalyst | |
GB2165551B (en) | Process for the production of synthesis gas | |
EP0546152A1 (en) | Catalysts for the production of carbon monoxide | |
GB1503506A (en) | Combustible gases | |
Fujimoto et al. | Spillover effect on the stabilization of Cu-Zn catalyst for CO2 hydrogenation to methanol | |
ES8503717A1 (en) | Auto-thermal reforming by partial oxidn. and steam reforming | |
EP1202928B1 (en) | Process for producing syngas in a short contact time reactor using catalytic partial oxidation of hydrogen sulfide | |
GB1572071A (en) | Production of purified synthesis gas and carbon monoxide | |
ES281826A1 (en) | A procedure for forming a gaseous hydrogen-nitrogen current by refurbishing nafta with water vapor (Machine-translation by Google Translate, not legally binding) | |
JPS5543003A (en) | Preparation of methanol | |
GB944059A (en) | Process for the production of ammonia synthesis feed gas | |
JPS5763387A (en) | Preparation of fuel gas | |
INUI et al. | Synthesis-Gas Formation from Methanol over Ni Based Composite Catalysts | |
FR2355773A1 (en) | Hydrogen-contg. gas mixt. prodn. by hydrocarbon steam reforming - with some steam generated using process heat | |
EP0145288A3 (en) | Improved low severity hydrocarbon steam reforming process | |
乾智行 et al. | Synthesis-gas formation from methanol over Ni based compostie catalysts. |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FD1A | Patent lapsed |
Effective date: 19960603 |