GB1364357A - Process for producing methanol in tubular heaters - Google Patents
Process for producing methanol in tubular heatersInfo
- Publication number
- GB1364357A GB1364357A GB2118672A GB2118672A GB1364357A GB 1364357 A GB1364357 A GB 1364357A GB 2118672 A GB2118672 A GB 2118672A GB 2118672 A GB2118672 A GB 2118672A GB 1364357 A GB1364357 A GB 1364357A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- diameter
- tube
- particles
- tubes
- 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
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title abstract 9
- 239000003054 catalyst Substances 0.000 abstract 7
- 239000002245 particle Substances 0.000 abstract 6
- 239000007789 gas Substances 0.000 abstract 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 238000009835 boiling Methods 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 239000012809 cooling fluid Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 abstract 1
- 238000003786 synthesis reaction Methods 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/1512—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by reaction conditions
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/153—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the catalyst used
- C07C29/154—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the catalyst used containing copper, silver, gold, or compounds thereof
-
- 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
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
-
- 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)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
1364357 Preparation of CH 3 OH in a tubular reactor METALLGESELLSCHAFT AG 5 May 1972 [14 May 1971] 21186/72 Heading C2C Methanol is obtained by passing hydrogen and oxides of carbon at 230-280 C. under a pressure of 10-200 Kg./cm.<SP>2</SP> above atmospheric pressure over a particulate Cu-containing catalyst contained in a metallic tube or tubes, which is or are contacted on the outside by a cooling fluid (e.g. boiling H 2 O under pressure), the mass velocity m of the synthesis gas (e.g. fresh gas plus recycle gas) entering the catalyst tube or tubes, in Kg./square metre/second, the height L of the catalyst bed in metres and the inside diameter D of the tube(s) in millimetres being defined by the equations wherein p is the density of the gas in Kg./m.<SP>3</SP>, d is the catalyst particle diameter in mm. and the empirical factors have the values: The catalyst particles are preferably spherical or cylindrical with a diameter > 3 mm. (e.g. 5-12 mm.) and include annular particles with an outer diameter of 10-20 mm. and a wall thickness of 3-6 mm. and the particles preferably have a bulk density > 1Kg./litre (e.g. 1À5-2 Kg./l.). Examples 3 and 4 describe the production of methanol using reactors containing (a) 184 tubes (L = 6m., D = 34mm.) packed with catalyst particles of diameter 5 mm. and (b) 1 tube (L = 16m., D = 100 mm.) packed with catalyst particles of diameter 12 mm. respectively.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE2123950A DE2123950C3 (en) | 1971-05-14 | 1971-05-14 | Method and device for the production of methanol in tube furnaces |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1364357A true GB1364357A (en) | 1974-08-21 |
Family
ID=5807864
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB2118672A Expired GB1364357A (en) | 1971-05-14 | 1972-05-05 | Process for producing methanol in tubular heaters |
Country Status (13)
| Country | Link |
|---|---|
| JP (1) | JPS5622854B1 (en) |
| AT (1) | AT315812B (en) |
| BE (1) | BE782411A (en) |
| CS (1) | CS155114B2 (en) |
| DE (1) | DE2123950C3 (en) |
| ES (2) | ES401998A1 (en) |
| FI (1) | FI57097C (en) |
| FR (1) | FR2137450B1 (en) |
| GB (1) | GB1364357A (en) |
| IT (1) | IT955366B (en) |
| NL (1) | NL7206004A (en) |
| SE (1) | SE397341B (en) |
| ZA (1) | ZA722720B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4369255A (en) * | 1980-07-29 | 1983-01-18 | Metallgesellschaft Aktiengesellschaft | Method of obtaining improved equilibrium conditions and of simultaneously producing steam under high pressure in the production of methanol |
| WO2012146904A1 (en) | 2011-04-27 | 2012-11-01 | Davy Process Technology Limited | Process for the synthesis of methanol |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102007024934B4 (en) | 2007-05-29 | 2010-04-29 | Man Dwe Gmbh | Tube bundle reactors with pressure fluid cooling |
| RU2570573C2 (en) * | 2011-02-25 | 2015-12-10 | Чайна Петролеум Энд Кемикал Корпорейшн | Method of producing ethylene glycol |
-
1971
- 1971-05-14 DE DE2123950A patent/DE2123950C3/en not_active Expired
- 1971-12-31 FR FR717147752A patent/FR2137450B1/fr not_active Expired
-
1972
- 1972-03-28 AT AT266272A patent/AT315812B/en not_active IP Right Cessation
- 1972-04-20 BE BE782411A patent/BE782411A/en not_active IP Right Cessation
- 1972-04-20 CS CS268572A patent/CS155114B2/cs unknown
- 1972-04-21 ZA ZA722720A patent/ZA722720B/en unknown
- 1972-04-22 ES ES401998A patent/ES401998A1/en not_active Expired
- 1972-04-25 FI FI1179/72A patent/FI57097C/en active
- 1972-05-04 NL NL7206004A patent/NL7206004A/xx not_active Application Discontinuation
- 1972-05-05 GB GB2118672A patent/GB1364357A/en not_active Expired
- 1972-05-10 IT IT24149/72A patent/IT955366B/en active
- 1972-05-12 SE SE7206299A patent/SE397341B/en unknown
- 1972-05-15 JP JP4851772A patent/JPS5622854B1/ja active Pending
- 1972-12-22 ES ES409957A patent/ES409957A1/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4369255A (en) * | 1980-07-29 | 1983-01-18 | Metallgesellschaft Aktiengesellschaft | Method of obtaining improved equilibrium conditions and of simultaneously producing steam under high pressure in the production of methanol |
| WO2012146904A1 (en) | 2011-04-27 | 2012-11-01 | Davy Process Technology Limited | Process for the synthesis of methanol |
Also Published As
| Publication number | Publication date |
|---|---|
| FR2137450A1 (en) | 1972-12-29 |
| JPS5622854B1 (en) | 1981-05-27 |
| DE2123950B2 (en) | 1974-09-26 |
| ZA722720B (en) | 1973-05-30 |
| FR2137450B1 (en) | 1973-06-29 |
| BE782411A (en) | 1972-08-16 |
| CS155114B2 (en) | 1974-05-30 |
| NL7206004A (en) | 1972-11-16 |
| DE2123950C3 (en) | 1975-06-12 |
| ES409957A1 (en) | 1975-12-01 |
| AT315812B (en) | 1974-06-10 |
| DE2123950A1 (en) | 1972-11-30 |
| SE397341B (en) | 1977-10-31 |
| IT955366B (en) | 1973-09-29 |
| FI57097C (en) | 1980-06-10 |
| FI57097B (en) | 1980-02-29 |
| ES401998A1 (en) | 1975-03-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| GB1329025A (en) | Process and apparatus for contacting a liquid with solid particles | |
| MY119458A (en) | Preparation of 1,4-butanediol by catalytic hydrogenation of 1,4-butynediol | |
| US2637625A (en) | Gaseous diffusion process | |
| GB1316002A (en) | Fluid bed reactors | |
| GB1364357A (en) | Process for producing methanol in tubular heaters | |
| ES407581A1 (en) | Reactor for producing methanol and process | |
| GB1376921A (en) | Method of and apparatus for coating particles especially nuclear fuel particles for nuclear reactors | |
| GB1283656A (en) | System for effecting contact between fluid reactants and finely divided solid catalyst particles | |
| GB726841A (en) | Process and apparatus for contacting vaporized hydrocarbons with fluidised finely divided solid catalyst | |
| FR2450799B1 (en) | ||
| GB1319519A (en) | Control system for fluid catalytic cracking process | |
| US2481226A (en) | Two-stage reduction process for producing metal catalyst | |
| GB1226875A (en) | ||
| ES409355A1 (en) | Method for obtaining titanium dioxide having a controlled particle size | |
| GB1359377A (en) | Method and apparatus for controlling solids flow in a fluidised bed | |
| GB1485394A (en) | Catalytic hydrogenation process and apparatus | |
| GB1430616A (en) | Process for producing a reducing gas | |
| GB1340104A (en) | Reaction vessels | |
| GB1354073A (en) | Process and apparatus for the oxygenative cracking of hydrocarbons | |
| US3216801A (en) | Process for producing hydrogen | |
| JPS57192489A (en) | Hydrocarbon reforming furnace | |
| ES407252A1 (en) | Fluid-solid contacting apparatus | |
| US2734781A (en) | fowler | |
| GB1086221A (en) | Production of catalysts | |
| GB1356151A (en) | Reactor for the catalytic synthesis of ammonia at high temperatures and pressures |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PS | Patent sealed [section 19, patents act 1949] | ||
| PCNP | Patent ceased through non-payment of renewal fee |