NO961324D0 - Fremgangsmåte og apparat for injeksjon av forvarmet oksygen til en höytemperaturreaktor - Google Patents
Fremgangsmåte og apparat for injeksjon av forvarmet oksygen til en höytemperaturreaktorInfo
- Publication number
- NO961324D0 NO961324D0 NO961324A NO961324A NO961324D0 NO 961324 D0 NO961324 D0 NO 961324D0 NO 961324 A NO961324 A NO 961324A NO 961324 A NO961324 A NO 961324A NO 961324 D0 NO961324 D0 NO 961324D0
- Authority
- NO
- Norway
- Prior art keywords
- high temperature
- temperature reactor
- preheated oxygen
- injecting preheated
- injecting
- Prior art date
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
- 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
- C01B3/42—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 using moving solid particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1818—Feeding of the fluidising gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1818—Feeding of the fluidising gas
- B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
-
- 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
- C01B3/363—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 characterised by the burner used
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Inorganic Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/416,622 US5588974A (en) | 1995-04-04 | 1995-04-04 | Process, and apparatus, for the injection of preheated oxygen into a high temperature reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| NO961324D0 true NO961324D0 (no) | 1996-04-01 |
| NO961324L NO961324L (no) | 1996-10-07 |
Family
ID=23650674
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO961324A NO961324L (no) | 1995-04-04 | 1996-04-01 | Fremgangsmåte og apparat for injeksjon av forvarmet oksygen til en höytemperaturreaktor |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US5588974A (no) |
| EP (1) | EP0736485B1 (no) |
| AU (1) | AU695905B2 (no) |
| CA (1) | CA2172755C (no) |
| DE (1) | DE69603401T2 (no) |
| NO (1) | NO961324L (no) |
Families Citing this family (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7066973B1 (en) | 1996-08-26 | 2006-06-27 | Nuvera Fuel Cells | Integrated reformer and shift reactor |
| US5980782A (en) * | 1997-04-25 | 1999-11-09 | Exxon Research And Engineering Co. | Face-mixing fluid bed process and apparatus for producing synthesis gas |
| CA2282948A1 (en) | 1998-09-16 | 2000-03-16 | University Technologies International, Inc. | Low temperature autothermal steam reformation of methane in a fluidized bed |
| JP2000203802A (ja) | 1999-01-13 | 2000-07-25 | Toyota Motor Corp | 改質器 |
| US6986797B1 (en) | 1999-05-03 | 2006-01-17 | Nuvera Fuel Cells Inc. | Auxiliary reactor for a hydrocarbon reforming system |
| US6641625B1 (en) | 1999-05-03 | 2003-11-04 | Nuvera Fuel Cells, Inc. | Integrated hydrocarbon reforming system and controls |
| US6126438A (en) * | 1999-06-23 | 2000-10-03 | American Air Liquide | Preheated fuel and oxidant combustion burner |
| TWI241392B (en) * | 1999-09-20 | 2005-10-11 | Japan Science & Tech Agency | Apparatus and method for gasifying solid or liquid fuel |
| CA2489299A1 (en) | 2002-06-13 | 2003-12-24 | Darryl Pollica | Preferential oxidation reactor temperature regulation |
| US7034196B2 (en) * | 2002-06-19 | 2006-04-25 | Exxonmobil Chemical Patents Inc. | Method and apparatus for reducing decomposition byproducts in a methanol to olefin reactor system |
| US6737556B2 (en) * | 2002-10-21 | 2004-05-18 | Exxonmobil Chemical Patents Inc. | Method and system for reducing decomposition byproducts in a methanol to olefin reactor system |
| DE10329491A1 (de) * | 2003-07-01 | 2005-01-27 | Basf Ag | Reaktor für gas/flüssig oder gas/flüssig/fest Reaktionen |
| US7416571B2 (en) * | 2005-03-09 | 2008-08-26 | Conocophillips Company | Compact mixer for the mixing of gaseous hydrocarbon and gaseous oxidants |
| TW200732038A (en) * | 2006-01-13 | 2007-09-01 | Bp Chem Int Ltd | Process and apparatus for reducing the probability of ignition in fluid bed-catalysed oxidation reactions |
| FI120515B (fi) * | 2008-02-08 | 2009-11-13 | Foster Wheeler Energia Oy | Kiertoleijureaktori happipolttoon ja menetelmä sellaisen reaktorin käyttämiseksi |
| EP2639288B1 (en) * | 2010-11-08 | 2019-10-09 | ZE Energy Inc. | Gasification furnace and gasification system |
| EP2607301A1 (de) * | 2011-12-20 | 2013-06-26 | Karl-Heinz Tetzlaff | Vorrichtung und Verfahren zur Erdgasreformierung |
| US10113740B2 (en) * | 2016-08-12 | 2018-10-30 | Gas Technology Institute | Fluidized bed combustion of carbonaceous fuels |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3227527A (en) * | 1963-03-04 | 1966-01-04 | Universal Oil Prod Co | High temperature reactor |
| US3477824A (en) * | 1966-12-15 | 1969-11-11 | Zink Co John | Burner and apparatus for reforming hydrocarbons |
| US3933445A (en) * | 1973-10-15 | 1976-01-20 | Exxon Research And Engineering Company | Process and apparatus for preventing deposits on a gas inlet nozzle |
| JPS5350019A (en) * | 1976-10-19 | 1978-05-08 | Nippon Steel Corp | Method of forming corrosion resistant film on surface of stainless steel product |
| US4595145A (en) * | 1984-10-01 | 1986-06-17 | Texaco Inc. | Air distribution apparatus for a fluid catalytic cracking catalyst regenerator |
| CA1333008C (en) * | 1988-03-28 | 1994-11-15 | Duane Arlen Goetsch | Synthesis gas preparation and catalyst therefor |
| US5372791A (en) * | 1992-04-20 | 1994-12-13 | Foster Wheeler Energy Corporation | Fluidized bed system and a fluidization and cooling nozzle for use therein |
| CA2081170C (en) * | 1992-10-22 | 2002-12-24 | Alaa-Eldin Moustafa Adris | Fluidized bed reaction system for steam/hydrocarbon gas reforming to produce hydrogen |
| US5405219A (en) * | 1994-05-18 | 1995-04-11 | Union Carbide Chemicals & Plastics Technology Corporation | Solids feeder |
| US5421842A (en) * | 1994-09-06 | 1995-06-06 | Exxon Research And Engineering Company | High energy level in situ attrition and break up of catalyst to maintain bed fluidization during high temperature operations |
-
1995
- 1995-04-04 US US08/416,622 patent/US5588974A/en not_active Expired - Fee Related
-
1996
- 1996-03-27 CA CA002172755A patent/CA2172755C/en not_active Expired - Fee Related
- 1996-04-01 NO NO961324A patent/NO961324L/no not_active Application Discontinuation
- 1996-04-01 DE DE69603401T patent/DE69603401T2/de not_active Expired - Fee Related
- 1996-04-01 EP EP96302295A patent/EP0736485B1/en not_active Expired - Lifetime
- 1996-04-02 AU AU50478/96A patent/AU695905B2/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| US5588974A (en) | 1996-12-31 |
| EP0736485B1 (en) | 1999-07-28 |
| EP0736485A1 (en) | 1996-10-09 |
| CA2172755C (en) | 2000-10-03 |
| AU695905B2 (en) | 1998-08-27 |
| DE69603401D1 (de) | 1999-09-02 |
| NO961324L (no) | 1996-10-07 |
| CA2172755A1 (en) | 1996-10-05 |
| DE69603401T2 (de) | 1999-11-25 |
| AU5047896A (en) | 1996-10-17 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FC2A | Withdrawal, rejection or dismissal of laid open patent application |