GB1169241A - A Method of Partially Removing Carbon Dioxide from a Methanol Synthesis Gas - Google Patents
A Method of Partially Removing Carbon Dioxide from a Methanol Synthesis GasInfo
- Publication number
- GB1169241A GB1169241A GB309967A GB309967A GB1169241A GB 1169241 A GB1169241 A GB 1169241A GB 309967 A GB309967 A GB 309967A GB 309967 A GB309967 A GB 309967A GB 1169241 A GB1169241 A GB 1169241A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- synthesis
- carbon dioxide
- synthesis gas
- methanol
- 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
- 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
- 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
- C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
- C01B3/52—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with liquids; Regeneration of used liquids
-
- 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
- C07C29/1516—Multisteps
- C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0415—Purification by absorption in liquids
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/047—Composition of the impurity the impurity being carbon monoxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/0475—Composition of the impurity the impurity being carbon dioxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/0495—Composition of the impurity the impurity being water
Abstract
1,169,241. Separating carbon dioxide from methanol synthesis gas. METALLGESELLSCHAFT A.G. 20 Jan., 1967 [22 Jan., 1966], No. 3099/67. Heading B1L. [Also in Division C2] In the synthesis of methanol wherein synthesis gas is obtained from light hydrocarbons such as light petroleum or natural gas, by cracking with oxygen or steam, carbon dioxide is partially removed from the synthesis gas stream. Thus, hot synthesis gas from cracker I is led to cooler 12 and then to separator 14 for removal of condensables, before being compressed to synthesis pressure in compressor 16 and thereafter divided into two branch streams by three way valve 18. One branch stream 19 is passed to washing tower 3 in which the gas is washed at ambient temperature with crude methanol taken from pressure separator 5, optionally by way of a decompression tank (113; see Fig. 2; not shown), by means of re-pressurising pump 21, and the washed gas is recombined at a suitable junction 23 with second branch stream before being passed, optionally in association with recycled gas, to synthesis reactor 4. The carbon dioxide-containing methanol which collects in the bottom of washing column 3 is passed through expansion valve 35 to decompression tank 6 before being transferred to distillation column 7 for recovery of the products.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEM68099A DE1262987B (en) | 1966-01-22 | 1966-01-22 | Process for adjusting the carbon dioxide content in methanol synthesis gas |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1169241A true GB1169241A (en) | 1969-10-29 |
Family
ID=7312465
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB309967A Expired GB1169241A (en) | 1966-01-22 | 1967-01-20 | A Method of Partially Removing Carbon Dioxide from a Methanol Synthesis Gas |
Country Status (4)
Country | Link |
---|---|
JP (1) | JPS4920281B1 (en) |
BE (1) | BE692777A (en) |
DE (1) | DE1262987B (en) |
GB (1) | GB1169241A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2288722A1 (en) * | 1974-10-21 | 1976-05-21 | Shell Int Research | METHOD FOR THE PREPARATION OF METHANOL |
US3962300A (en) * | 1970-05-19 | 1976-06-08 | Metallgesellschaft Aktiengesellschaft | Process for producing methanol |
US4087449A (en) * | 1975-08-27 | 1978-05-02 | Metallgesellschaft Aktiengesellschaft | Process for producing methanol |
US4093029A (en) * | 1976-06-21 | 1978-06-06 | Mobil Oil Corporation | Utilization of low BTU natural gas |
EP0067491A2 (en) * | 1981-06-12 | 1982-12-22 | Stamicarbon B.V. | Process for the preparation of methanol |
EP4043423A1 (en) * | 2021-02-16 | 2022-08-17 | Union Engineering A/S | Biomethanol production system and method |
-
1966
- 1966-01-22 DE DEM68099A patent/DE1262987B/en active Pending
-
1967
- 1967-01-17 BE BE692777D patent/BE692777A/xx unknown
- 1967-01-20 GB GB309967A patent/GB1169241A/en not_active Expired
- 1967-01-21 JP JP400467A patent/JPS4920281B1/ja active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3962300A (en) * | 1970-05-19 | 1976-06-08 | Metallgesellschaft Aktiengesellschaft | Process for producing methanol |
FR2288722A1 (en) * | 1974-10-21 | 1976-05-21 | Shell Int Research | METHOD FOR THE PREPARATION OF METHANOL |
US4087449A (en) * | 1975-08-27 | 1978-05-02 | Metallgesellschaft Aktiengesellschaft | Process for producing methanol |
US4093029A (en) * | 1976-06-21 | 1978-06-06 | Mobil Oil Corporation | Utilization of low BTU natural gas |
EP0067491A2 (en) * | 1981-06-12 | 1982-12-22 | Stamicarbon B.V. | Process for the preparation of methanol |
EP0067491A3 (en) * | 1981-06-12 | 1983-02-09 | Stamicarbon B.V. | Process for the preparation of methanol |
EP4043423A1 (en) * | 2021-02-16 | 2022-08-17 | Union Engineering A/S | Biomethanol production system and method |
Also Published As
Publication number | Publication date |
---|---|
DE1262987B (en) | 1968-03-14 |
JPS4920281B1 (en) | 1974-05-23 |
BE692777A (en) | 1967-07-03 |
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