US5063250A
Expired / Lapsed
US
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Process for the production of methanol
Assignee: Mitsubishi Gas Chemical Co Inc
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Filing: 1990-08-27
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Granted: 1991-11-05
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Expires: 2010-08-27
Abstract
Abstract This invention provides a process for the production of methanol which comprises steps of (a) reacting hydrocarbon with steam to generate synthesis gas composed of hydrogen, carbon monoxide and carbon dioxide as main components, (b) reacting the synthesis gas on a methanol synthesis catalyst to synthesize crude methanol, and (c) feeding the resultant crude methanol directly to a distillation column and distilling the crude methanol to separate prified methanol and an effluent water containing all or part of low boiling organic compounds, high boiling organic compounds and organic acids, the above step (c) being a step for the distillation and separation carried out without adding any alkali compound to neutralize the organic acids in the crude methanol obtained in the above step (b), the process including a step of bringing the effluent water resulting from the above step (c) into contact with gaseous hydrocarbon to humidify the hydrocarbon, the humidified hydrocarbon being used as a material for hydrocarbon and steam used in the above step (a).
Inventors
- 👤 Katsutoshi Murayama
- 👤 Hideaki Nagai
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 19:30
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/15; C07C29/151; C07C29/1516; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
317 words
A process for the production of methanol from hydrocarbon, which comprises the steps of: (a) reacting hydrocarbon with steam to generate a synthesis gas composed of hydrogen, carbon monoxide and carbon dioxide as main components, (b) reacting the synthesis gas on a methanol synthesis catalyst to synthesize crude methanol, (c) feeding the crude methanol to a distillation column, without adding any alkaline compound to neutralize organic acids in the crude methanol, to distill the crude methanol and separate it into a purified methanol and effluent water containing low-boiling organic compounds, high-boiling organic compounds and organic acids, said distillation column composed of stainless steel having a composition of 18 to 20% by weight of Cr, 8 to 10.5% by weight of Ni and not more than 0.08% by weight of C in its portions contacting the low-boiling organic compounds, high-boiling organic compounds or organic acids, (d) bringing the effluent water into contact with preheated gaseous hydrocarbon in an apparatus composed of stainless steel having a composition of 16 to 26% by weight of Cr, 6 to 14% by weight of Ni, 2 to 4% by weight of Mo and not more than 0.03% by weight of C in its portions contacting the low-boiling organic compounds, high-boiling organic compounds or organic acids to humidify the hydrocarbon, and (e) feeding the humidified hydrocarbon for use in step (a), wherein step (d) contains a step of humidifying the hydrocarbon with the effluent water from step (c) by means of a heat exchanger humidifier using, as a heat source, heat of the synthesis gas generated in step (a), or a step of humidifying the hydrocarbon, pre-heated to 250° to 430° C., with the effluent water from step (c) by means of a heat-insulated humidifier, and then humidifying the hydrocarbon with water by means of a heat exchanger humidifier using, as a heat source, heat of the synthesis gas generated in step (a).
Claim 2
Dependent Claim
317 words
A process for the production of methanol from hydrocarbon, which comprises the steps of: (a) reacting hydrocarbon with steam to generate a synthesis gas composed of hydrogen, carbon monoxide and carbon dioxide as main components, (b) reacting the synthesis gas on a methanol synthesis catalyst to synthesize crude methanol, (c) feeding the crude methanol to a distillation column, without adding any alkaline compound to neutralize organic acids in the crude methanol, to distill the crude methanol and separate it into a purified methanol and effluent water containing low-boiling organic compounds, high-boiling organic compounds and organic acids, said distillation column composed of stainless steel having a composition of 18 to 20% by weight of Cr, 8 to 10.5% by weight of Ni and not more than 0.08% by weight of C in its portions contacting the low-boiling organic compounds, high-boiling organic compounds or organic acids, (d) bringing the effluent water into contact with preheated gaseous hydrocarbon in an apparatus composed of stainless steel having a composition of 16 to 26% by weight of Cr, 6 to 14% by weight of Ni, 2 to 4% by weight of Mo and not more than 0.03% by weight of C in its portions contacting the low-boiling organic compounds, high-boiling organic compounds or organic acids to humidify the hydrocarbon, and (e) feeding the humidified hydrocarbon for use in step (a), wherein step (d) contains a step of humidifying the hydrocarbon with the effluent water from step (c) by means of a heat exchanger humidifier using, as a heat source, heat of the synthesis gas generated in step (a), or a step of humidifying the hydrocarbon, pre-heated to 250° to 430° C., with the effluent water from step (c) by means of a heat-insulated humidifier, and then humidifying the hydrocarbon with water by means of a heat exchanger humidifier using, as a heat source, heat of the synthesis gas generated in step (a).
Claim 3
Dependent Claim
20 words
A process for the production of methanol according to claim 1, wherein steam is further added to the humidified hydrocarbon.
Claim 4
Dependent Claim
47 words
A process for the production of methanol according to claim 1, wherein the humidified hydrocarbon is humidified by the effluent water resulting from step (c) containing high boiling organic compounds and/or low boiling organic compounds extracted from the middle part of the distillation column in step (c).
Claim 5
Dependent Claim
38 words
A process for the production of methanol according to claim 1, wherein 1/10 to 1/20 of the effluent water resulting from step (c) is removed before the effluent water is used to humidify the hydrocarbon in step (d).
References Cited (Backward Citations)
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| 7.5 Years (Year 8) | 1998-11-04 | 1999-05-06 | 1999-11-05 | $3760.00 | Window Closed / Lapsed |
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