DE2430769A1 - Verfahren zur durchfuehrung einer stark exothermen chemischen reaktion - Google Patents
Verfahren zur durchfuehrung einer stark exothermen chemischen reaktionInfo
- Publication number
- DE2430769A1 DE2430769A1 DE2430769A DE2430769A DE2430769A1 DE 2430769 A1 DE2430769 A1 DE 2430769A1 DE 2430769 A DE2430769 A DE 2430769A DE 2430769 A DE2430769 A DE 2430769A DE 2430769 A1 DE2430769 A1 DE 2430769A1
- Authority
- DE
- Germany
- Prior art keywords
- reaction
- stage
- reactor
- chemical
- liquid
- 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.)
- Withdrawn
Links
- 238000006243 chemical reaction Methods 0.000 title claims description 94
- 238000000034 method Methods 0.000 title claims description 15
- 239000007789 gas Substances 0.000 claims description 30
- 239000003054 catalyst Substances 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000000126 substance Substances 0.000 claims description 10
- 229910001868 water Inorganic materials 0.000 claims description 10
- 229910052739 hydrogen Inorganic materials 0.000 claims description 8
- 239000001257 hydrogen Substances 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 7
- 239000000376 reactant Substances 0.000 claims description 7
- 239000007795 chemical reaction product Substances 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 claims 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 19
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical class [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 11
- 229910002091 carbon monoxide Inorganic materials 0.000 description 9
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 8
- 238000001816 cooling Methods 0.000 description 8
- 229910002090 carbon oxide Inorganic materials 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 230000002401 inhibitory effect Effects 0.000 description 2
- 239000003245 coal Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- MWWATHDPGQKSAR-UHFFFAOYSA-N propyne Chemical group CC#C MWWATHDPGQKSAR-UHFFFAOYSA-N 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0496—Heating or cooling the reactor
-
- 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
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
-
- 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
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0457—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being placed in separate reactors
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
- B01J2208/00044—Temperature measurement
- B01J2208/00061—Temperature measurement of the reactants
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
- B01J2208/00088—Flow rate measurement
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00141—Coils
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00283—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S423/00—Chemistry of inorganic compounds
- Y10S423/06—Temperature control
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE2430769A DE2430769A1 (de) | 1974-06-26 | 1974-06-26 | Verfahren zur durchfuehrung einer stark exothermen chemischen reaktion |
| FR7509053A FR2276090A1 (fr) | 1974-06-26 | 1975-03-24 | Procede et dispositif pour la mise en oeuvre d'une reaction chimique fortement exothermique |
| GB2476675A GB1470643A (en) | 1974-06-26 | 1975-06-10 | Carrying out of highly exothermic chemical reactions |
| US05/588,515 US4212817A (en) | 1974-06-26 | 1975-06-19 | Control of highly exothermic chemical reactions |
| ZA00754061A ZA754061B (en) | 1974-06-26 | 1975-06-25 | Method of carrying out a pronouncedly exothermic chemical reaction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE2430769A DE2430769A1 (de) | 1974-06-26 | 1974-06-26 | Verfahren zur durchfuehrung einer stark exothermen chemischen reaktion |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE2430769A1 true DE2430769A1 (de) | 1976-01-15 |
Family
ID=5919046
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE2430769A Withdrawn DE2430769A1 (de) | 1974-06-26 | 1974-06-26 | Verfahren zur durchfuehrung einer stark exothermen chemischen reaktion |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US4212817A (enExample) |
| DE (1) | DE2430769A1 (enExample) |
| FR (1) | FR2276090A1 (enExample) |
| GB (1) | GB1470643A (enExample) |
| ZA (1) | ZA754061B (enExample) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102018201561A1 (de) * | 2018-02-01 | 2019-08-01 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Rohrreaktor und Verfahren zum Betreiben eines Rohrreaktors |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3247821A1 (de) * | 1982-12-23 | 1984-09-27 | Kernforschungsanlage Jülich GmbH, 5170 Jülich | Reaktionsrohr fuer eine exotherme, heterogen katalysierte gasreaktion, insbesondere zur fuehrung einer methanisierungsreaktion |
| US4552747A (en) * | 1984-06-20 | 1985-11-12 | Gaa Engineered Systems, Inc. | Temperature moderation of an oxygen enriched Claus sulfur plant |
| US4826670A (en) * | 1985-03-20 | 1989-05-02 | Air Products And Chemicals, Inc. | Oxygen enriched claus system with sulfuric acid injection |
| US4923306A (en) * | 1987-01-08 | 1990-05-08 | Westinghouse Electric Corp. | Stable isothermal calorimeter |
| US5840933A (en) * | 1996-10-29 | 1998-11-24 | Arco Chemical Technology, L.P. | Catalytic converter system and progress |
| US6641625B1 (en) | 1999-05-03 | 2003-11-04 | Nuvera Fuel Cells, Inc. | Integrated hydrocarbon reforming system and controls |
| EP1581784A4 (en) | 2002-06-13 | 2009-06-24 | Nuvera Fuel Cells Inc | TEMPERATURE REGULATION IN A PREFERENTIAL OXIDATION REACTOR |
| US20080132717A1 (en) * | 2006-12-04 | 2008-06-05 | Bernard Cooker | Propylene oxide system |
| WO2019118762A1 (en) * | 2017-12-14 | 2019-06-20 | Iti Technologies, Inc. | Chemical process and product |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE954907C (de) * | 1952-09-16 | 1956-12-27 | Ruhrchemie Ag | Verfahren zur kombinierten Reinigung und Methanisierung von Kohlenoxyde und Wasserstoff neben anderen Bestandteilen enthaltenden Gasgemischen |
Family Cites Families (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2662911A (en) * | 1948-10-01 | 1953-12-15 | Metallgesellschaft Ag | Temperature control in the catalytic hydrogenation of carbon monoxide |
| GB791946A (en) * | 1955-02-25 | 1958-03-12 | Kohlenscheidungs Gmbh | Process for the conversion and methanisation of carbon monoxide-containing gases |
| DE1110147B (de) * | 1955-11-26 | 1961-07-06 | Ruhrchemie Ag | Verfahren zur katalytischen Methanisierung von im wesentlichen nur Kohlendioxyd und Wasserstoff enthaltenden Gasgemischen |
| US3441393A (en) * | 1966-01-19 | 1969-04-29 | Pullman Inc | Process for the production of hydrogen-rich gas |
| GB1271721A (en) * | 1968-05-03 | 1972-04-26 | Gas Council | A process for the production of methane-containing gases |
| DE2212700C2 (de) * | 1972-03-16 | 1982-07-08 | Metallgesellschaft Ag, 6000 Frankfurt | Verfahren zur Erzeugung eines methanreichen, mit Erdgas austauschbaren Gases |
| US3890113A (en) * | 1973-06-25 | 1975-06-17 | Texaco Inc | Production of methane |
| DE2335659C2 (de) * | 1973-07-13 | 1982-10-28 | Krupp-Koppers Gmbh, 4300 Essen | Verfahren zur Erzeugung eines methanhaltigen Gases |
| US3904386A (en) * | 1973-10-26 | 1975-09-09 | Us Interior | Combined shift and methanation reaction process for the gasification of carbonaceous materials |
| US3927998A (en) * | 1973-12-28 | 1975-12-23 | Texaco Inc | Production of methane-rich gas stream |
| US3927999A (en) * | 1973-12-28 | 1975-12-23 | Texaco Inc | Methane-rich gas process |
-
1974
- 1974-06-26 DE DE2430769A patent/DE2430769A1/de not_active Withdrawn
-
1975
- 1975-03-24 FR FR7509053A patent/FR2276090A1/fr active Granted
- 1975-06-10 GB GB2476675A patent/GB1470643A/en not_active Expired
- 1975-06-19 US US05/588,515 patent/US4212817A/en not_active Expired - Lifetime
- 1975-06-25 ZA ZA00754061A patent/ZA754061B/xx unknown
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE954907C (de) * | 1952-09-16 | 1956-12-27 | Ruhrchemie Ag | Verfahren zur kombinierten Reinigung und Methanisierung von Kohlenoxyde und Wasserstoff neben anderen Bestandteilen enthaltenden Gasgemischen |
Non-Patent Citations (3)
| Title |
|---|
| ULLMANN: Encyclopädie der technischen Chemie, 4. Aufl., Bd. 2, 1972, S. 445, 660 * |
| ULLMANN: Encyclopädie der technischen Chemie, 4. Aufl., Bd. 3, 1973, S. 476, 477 * |
| ULLMANN: Encyclopädie der technischen Chemie, 4. Aufl., Bd. 3, 1973, S. 478, 479 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102018201561A1 (de) * | 2018-02-01 | 2019-08-01 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Rohrreaktor und Verfahren zum Betreiben eines Rohrreaktors |
Also Published As
| Publication number | Publication date |
|---|---|
| ZA754061B (en) | 1976-05-26 |
| GB1470643A (en) | 1977-04-14 |
| FR2276090B1 (enExample) | 1979-03-09 |
| FR2276090A1 (fr) | 1976-01-23 |
| US4212817A (en) | 1980-07-15 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| OD | Request for examination | ||
| 8139 | Disposal/non-payment of the annual fee |