ES2079996A1 - Reactor with porous ceramic wall and method for obtaining hydrocarbons from methane - Google Patents
Reactor with porous ceramic wall and method for obtaining hydrocarbons from methaneInfo
- Publication number
- ES2079996A1 ES2079996A1 ES09301314A ES9301314A ES2079996A1 ES 2079996 A1 ES2079996 A1 ES 2079996A1 ES 09301314 A ES09301314 A ES 09301314A ES 9301314 A ES9301314 A ES 9301314A ES 2079996 A1 ES2079996 A1 ES 2079996A1
- Authority
- ES
- Spain
- Prior art keywords
- methane
- reactor
- porous ceramic
- ceramic wall
- hydrocarbons
- 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
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title abstract 8
- 229930195733 hydrocarbon Natural products 0.000 title abstract 4
- 150000002430 hydrocarbons Chemical class 0.000 title abstract 4
- 239000000919 ceramic Substances 0.000 title abstract 2
- 238000000034 method Methods 0.000 title abstract 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 abstract 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 abstract 2
- 239000005977 Ethylene Substances 0.000 abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 1
- 239000004215 Carbon black (E152) Substances 0.000 abstract 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 239000003054 catalyst Substances 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 239000003153 chemical reaction reagent Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 239000001301 oxygen Substances 0.000 abstract 1
- 229910052760 oxygen Inorganic materials 0.000 abstract 1
- 239000012466 permeate Substances 0.000 abstract 1
Classifications
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2475—Membrane reactors
-
- 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
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
- B01J8/009—Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Reactor with porous ceramic wall and method for obtaining ethane, ethylene and other hydrocarbons from methane. A feed containing methane passes through a catalyst bed wholly or partly placed to one side of a porous medium through which a gas containing oxygen permeates. Ethane, ethylene and other hydrocarbons are obtained, together with oxides of carbon and hydrogen. The hydrocarbon selectivity which can be achieved for a given level of methane conversion is greater than in a fixed bed reactor in which the reagents are fed simultaneously to the reactor inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ES9301314A ES2079996B1 (en) | 1993-06-14 | 1993-06-14 | REACTOR WITH POROUS CERAMIC WALL AND METHOD FOR OBTAINING HYDROCARBONS FROM METHANE. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ES9301314A ES2079996B1 (en) | 1993-06-14 | 1993-06-14 | REACTOR WITH POROUS CERAMIC WALL AND METHOD FOR OBTAINING HYDROCARBONS FROM METHANE. |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| ES2079996A1 true ES2079996A1 (en) | 1996-01-16 |
| ES2079996B1 ES2079996B1 (en) | 1996-08-01 |
Family
ID=8282185
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES9301314A Expired - Fee Related ES2079996B1 (en) | 1993-06-14 | 1993-06-14 | REACTOR WITH POROUS CERAMIC WALL AND METHOD FOR OBTAINING HYDROCARBONS FROM METHANE. |
Country Status (1)
| Country | Link |
|---|---|
| ES (1) | ES2079996B1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES2164544A1 (en) * | 1999-07-22 | 2002-02-16 | Univ Zaragoza | ZEOLITIC MEMBRANE REACTOR FOR OBTAINING METHANOL AND OTHER ALCOHOLS FROM SYNTHESIS GAS |
| EP1080779B1 (en) * | 1999-09-02 | 2004-12-08 | Haldor Topsoe A/S | Reactor for catalytic selective oxidation of a hydrocarbon substrate |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES2193801B1 (en) * | 2000-05-29 | 2005-03-01 | Universidad De Zaragoza | REACTOR FOR OBTAINING COMPOUNDS FOR HIGH INDEX GASOLINE FROM OCTANO FROM LIGHT OLEFINS. |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4791079A (en) * | 1986-06-09 | 1988-12-13 | Arco Chemical Company | Ceramic membrane for hydrocarbon conversion |
| US5025108A (en) * | 1988-04-05 | 1991-06-18 | Institut Francais Du Petrole | Process for producing olefins from natural gas |
| US5106590A (en) * | 1990-05-11 | 1992-04-21 | Davy Mckee (London) Limited | Gas mixer and distributor with heat exchange between incoming gases |
-
1993
- 1993-06-14 ES ES9301314A patent/ES2079996B1/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4791079A (en) * | 1986-06-09 | 1988-12-13 | Arco Chemical Company | Ceramic membrane for hydrocarbon conversion |
| US5025108A (en) * | 1988-04-05 | 1991-06-18 | Institut Francais Du Petrole | Process for producing olefins from natural gas |
| US5106590A (en) * | 1990-05-11 | 1992-04-21 | Davy Mckee (London) Limited | Gas mixer and distributor with heat exchange between incoming gases |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES2164544A1 (en) * | 1999-07-22 | 2002-02-16 | Univ Zaragoza | ZEOLITIC MEMBRANE REACTOR FOR OBTAINING METHANOL AND OTHER ALCOHOLS FROM SYNTHESIS GAS |
| EP1080779B1 (en) * | 1999-09-02 | 2004-12-08 | Haldor Topsoe A/S | Reactor for catalytic selective oxidation of a hydrocarbon substrate |
| US7087801B2 (en) | 1999-09-02 | 2006-08-08 | Haldor Topsoe A/S | Process for catalytic selective oxidation of a hydrocarbon substrate |
Also Published As
| Publication number | Publication date |
|---|---|
| ES2079996B1 (en) | 1996-08-01 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EC2A | Search report published |
Date of ref document: 19930614 Kind code of ref document: B1 Effective date: 19930614 |
|
| FD2A | Announcement of lapse in spain |
Effective date: 20141120 |