FR2375171A1 - Procede de production de methanol - Google Patents
Procede de production de methanolInfo
- Publication number
- FR2375171A1 FR2375171A1 FR7738621A FR7738621A FR2375171A1 FR 2375171 A1 FR2375171 A1 FR 2375171A1 FR 7738621 A FR7738621 A FR 7738621A FR 7738621 A FR7738621 A FR 7738621A FR 2375171 A1 FR2375171 A1 FR 2375171A1
- Authority
- FR
- France
- Prior art keywords
- section
- methanol
- distillation
- steam
- low pressure
- 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
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
- C07C29/1516—Multisteps
- C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S203/00—Distillation: processes, separatory
- Y10S203/08—Waste heat
-
- 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
- Y10S203/00—Distillation: processes, separatory
- Y10S203/20—Power plant
-
- 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
- Y10S203/00—Distillation: processes, separatory
- Y10S203/24—Mobile, marine distiller
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Cette invention concerne un procédé de production de méthanol. Ce procédé comprend une section de production de gaz de synthèse, une section de synthèse du méthanol et une section de distillation du méthanol. Il comporte un système autonome dans lequel de la vapeur à basse pression est obtenue par échange thermique avec un courant fluide à 120-300 degrés C du processus, la vapeur à basse pression est utilisée comme vapeur vive pour chauffer au moins la colonne de distillation de la section de distillation, et l'eau prélevée à la base d'une colonne de distillation de cette section est utilisée comme charge pour le système autonome de production de vapeur. Ce procédé permet ainsi de réaliser des économies énergétiques importantes.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB53505/76A GB1592949A (en) | 1976-12-22 | 1976-12-22 | Methanol |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2375171A1 true FR2375171A1 (fr) | 1978-07-21 |
FR2375171B3 FR2375171B3 (fr) | 1980-08-08 |
Family
ID=10468052
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR7738621A Granted FR2375171A1 (fr) | 1976-12-22 | 1977-12-21 | Procede de production de methanol |
Country Status (8)
Country | Link |
---|---|
US (1) | US4149940A (fr) |
JP (1) | JPS5379807A (fr) |
CA (1) | CA1101446A (fr) |
DE (1) | DE2757478A1 (fr) |
FR (1) | FR2375171A1 (fr) |
GB (1) | GB1592949A (fr) |
IT (1) | IT1090355B (fr) |
NL (1) | NL7714099A (fr) |
Families Citing this family (61)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4555310A (en) * | 1978-08-30 | 1985-11-26 | Phillips Petroleum Company | Method of utilizing energy of high pressure condensate |
JPS597313B2 (ja) * | 1980-02-08 | 1984-02-17 | チツソエンジニアリング株式会社 | アルコ−ルの蒸溜装置 |
US4456779A (en) * | 1983-04-26 | 1984-06-26 | Mobil Oil Corporation | Catalytic conversion of olefins to higher hydrocarbons |
US4665249A (en) * | 1984-12-19 | 1987-05-12 | Mobil Oil Corporation | Method for feeding an MTG conversion reactor |
JPH0692332B2 (ja) * | 1985-07-31 | 1994-11-16 | 三菱重工業株式会社 | メタノ−ルプラントの加圧蒸留方法 |
JPH0692333B2 (ja) * | 1985-07-31 | 1994-11-16 | 三菱重工業株式会社 | メタノ−ルプラントの加圧蒸留法 |
JPS6242940A (ja) * | 1985-08-16 | 1987-02-24 | Mitsubishi Gas Chem Co Inc | メタノ−ルの精製方法 |
US5718810A (en) * | 1996-03-19 | 1998-02-17 | The Dow Chemical Company | Methanol recovery using extractive distillation |
US7297236B1 (en) | 2001-06-30 | 2007-11-20 | Icm, Inc. | Ethanol distillation process |
US8293186B2 (en) * | 2004-07-29 | 2012-10-23 | Gas Technologies Llc | Method and apparatus for producing methanol |
US8202916B2 (en) * | 2004-07-29 | 2012-06-19 | Gas Technologies Llc | Method of and apparatus for producing methanol |
US7456327B2 (en) | 2004-07-29 | 2008-11-25 | Gas Technologies, Llc | Method for direct-oxygenation of alkane gases |
US7578981B2 (en) * | 2004-07-29 | 2009-08-25 | Gas Technologies Llc | System for direct-oxygenation of alkane gases |
US7642293B2 (en) * | 2004-07-29 | 2010-01-05 | Gas Technologies Llc | Method and apparatus for producing methanol with hydrocarbon recycling |
US7910787B2 (en) | 2004-07-29 | 2011-03-22 | Gas Technologies Llc | Method and system for methanol production |
US9180426B2 (en) * | 2004-07-29 | 2015-11-10 | Gas Technologies, Llc | Scrubber for methanol production system |
US7879296B2 (en) * | 2005-12-27 | 2011-02-01 | Gas Technologies Llc | Tandem reactor system having an injectively-mixed backmixing reaction chamber, tubular-reactor, and axially movable interface |
US7687669B2 (en) * | 2005-12-27 | 2010-03-30 | Gas Technologies Llc | Method for direct-oxygenation of alkane gases |
CA2692994C (fr) * | 2009-02-19 | 2015-07-21 | Conocophillips Company | Recuperation de petrole et capture du dioxyde de carbone assistees a la vapeur |
EP2322494B1 (fr) * | 2009-11-17 | 2013-01-09 | Lurgi GmbH | Fabrication de diméthyléther à partir de méthanol brut |
US20110132577A1 (en) * | 2009-12-03 | 2011-06-09 | Jay Stephen Kaufman | System for the use of waste heat |
US8575403B2 (en) | 2010-05-07 | 2013-11-05 | Celanese International Corporation | Hydrolysis of ethyl acetate in ethanol separation process |
US9272970B2 (en) | 2010-07-09 | 2016-03-01 | Celanese International Corporation | Hydrogenolysis of ethyl acetate in alcohol separation processes |
US8846988B2 (en) | 2010-07-09 | 2014-09-30 | Celanese International Corporation | Liquid esterification for the production of alcohols |
US8710279B2 (en) | 2010-07-09 | 2014-04-29 | Celanese International Corporation | Hydrogenolysis of ethyl acetate in alcohol separation processes |
US8664454B2 (en) | 2010-07-09 | 2014-03-04 | Celanese International Corporation | Process for production of ethanol using a mixed feed using copper containing catalyst |
US8884081B2 (en) | 2011-04-26 | 2014-11-11 | Celanese International Corporation | Integrated process for producing acetic acid and alcohol |
US9073816B2 (en) | 2011-04-26 | 2015-07-07 | Celanese International Corporation | Reducing ethyl acetate concentration in recycle streams for ethanol production processes |
US9024082B2 (en) | 2011-04-26 | 2015-05-05 | Celanese International Corporation | Using a dilute acid stream as an extractive agent |
US8927788B2 (en) | 2011-04-26 | 2015-01-06 | Celanese International Corporation | Process to recover alcohol with reduced water from overhead of acid column |
US9024084B2 (en) | 2011-04-26 | 2015-05-05 | Celanese International Corporation | Reduced energy alcohol separation process having controlled pressure |
US8686200B2 (en) | 2011-04-26 | 2014-04-01 | Celanese International Corporation | Process to recover alcohol from an acidic residue stream |
US8592635B2 (en) | 2011-04-26 | 2013-11-26 | Celanese International Corporation | Integrated ethanol production by extracting halides from acetic acid |
US8933278B2 (en) | 2011-04-26 | 2015-01-13 | Celanese International Corporation | Process for producing ethanol and reducing acetic acid concentration |
US8927784B2 (en) | 2011-04-26 | 2015-01-06 | Celanese International Corporation | Process to recover alcohol from an ethyl acetate residue stream |
US9000232B2 (en) | 2011-04-26 | 2015-04-07 | Celanese International Corporation | Extractive distillation of crude alcohol product |
US9000233B2 (en) | 2011-04-26 | 2015-04-07 | Celanese International Corporation | Process to recover alcohol with secondary reactors for hydrolysis of acetal |
WO2012149137A1 (fr) | 2011-04-26 | 2012-11-01 | Celanese International Corporation | Procédé de production d'éthanol à partir d'une charge d'acide acétique et d'une charge d'acétate d'éthyle recyclé |
US8907141B2 (en) | 2011-04-26 | 2014-12-09 | Celanese International Corporation | Process to recover alcohol with secondary reactors for esterification of acid |
US9024085B2 (en) | 2011-04-26 | 2015-05-05 | Celanese International Corporation | Process to reduce ethanol recycled to hydrogenation reactor |
US8927787B2 (en) | 2011-04-26 | 2015-01-06 | Celanese International Corporation | Process for controlling a reboiler during alcohol recovery and reduced ester formation |
US8754268B2 (en) | 2011-04-26 | 2014-06-17 | Celanese International Corporation | Process for removing water from alcohol mixtures |
CN103080053B (zh) | 2011-04-26 | 2015-08-12 | 国际人造丝公司 | 使用叠置床反应器生产乙醇的方法 |
US8686199B2 (en) | 2011-04-26 | 2014-04-01 | Celanese International Corporation | Process for reducing the concentration of acetic acid in a crude alcohol product |
US8877987B2 (en) | 2011-08-03 | 2014-11-04 | Celanese International Corportation | Process for producing anhydrous ethanol using extractive distillation column |
US8895786B2 (en) | 2011-08-03 | 2014-11-25 | Celanese International Corporation | Processes for increasing alcohol production |
US8829253B2 (en) | 2011-08-19 | 2014-09-09 | Celanese International Corporation | Integrated process for producing ethanol from methanol |
US8853466B2 (en) | 2011-08-19 | 2014-10-07 | Celanese International Corporation | Integrated process for producing ethanol from methanol |
US8853467B2 (en) | 2011-08-19 | 2014-10-07 | Celanese International Corporation | Integrated process for producing ethanol |
US8704013B2 (en) | 2011-11-09 | 2014-04-22 | Celanese International Corporation | Integrated process for producing ethanol |
US8686201B2 (en) | 2011-11-09 | 2014-04-01 | Celanese International Corporation | Integrated acid and alcohol production process having flashing to recover acid production catalyst |
US8614359B2 (en) | 2011-11-09 | 2013-12-24 | Celanese International Corporation | Integrated acid and alcohol production process |
US8809599B2 (en) | 2011-11-09 | 2014-08-19 | Celanese International Corporation | Integrated process for producing ethanol and water balance control |
US8809598B2 (en) | 2011-11-09 | 2014-08-19 | Celanese International Corporation | Producing ethanol using two different streams from acetic acid carbonylation process |
US8802902B2 (en) | 2011-12-30 | 2014-08-12 | Celanese International Corporation | Pressure driven distillation for ethanol production and recovery from hydrogenation process |
US9353034B2 (en) | 2012-02-07 | 2016-05-31 | Celanese International Corporation | Hydrogenation process with reduced residence time for vapor phase reactants |
US8729318B1 (en) | 2012-11-20 | 2014-05-20 | Celanese International Corporation | Process for producing ethanol from methyl acetate |
CN104047650A (zh) * | 2014-06-26 | 2014-09-17 | 天津大学 | 蒸馏塔顶余能转化为电能的方法及装置 |
CN104492112B (zh) * | 2014-12-17 | 2016-06-22 | 亚太森博(山东)浆纸有限公司 | 一种汽提不凝气的处理装置及方法 |
US10745276B2 (en) | 2018-06-29 | 2020-08-18 | Praxair Technology, Inc. | Tail gas heating within PSA surge tank |
US12098657B2 (en) * | 2022-02-01 | 2024-09-24 | CRI, hf | Heat integration |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2437649A (en) * | 1944-11-20 | 1948-03-09 | Yorkshire Tar Distillers Ltd | Separation of phenols from hydrocarbon distillates by steam distillation |
US3230156A (en) * | 1961-09-08 | 1966-01-18 | Chemical Construction Corp | Purification of synthetic methanol by plural stage distillation |
US3186145A (en) * | 1963-01-28 | 1965-06-01 | Chemical Construction Corp | Absorption of impurities from hydrogencarbon monoxide synthesis gas |
US3406100A (en) * | 1966-12-16 | 1968-10-15 | Chemical Construction Corp | Purification of synthetic methanol by extractive distillation and subsequent distillation with plural side stream purges |
US3442770A (en) * | 1967-12-21 | 1969-05-06 | Vulcan Cincinnati Inc | Process for the purification of methanol by extractive distillation and plural stage distillation recovery |
US3597465A (en) * | 1968-03-04 | 1971-08-03 | Chemical Construction Corp | Production of synthetic methanol |
US3471371A (en) * | 1968-04-25 | 1969-10-07 | Foster Wheeler Corp | Steam stripping process with recycle water as a source of steam |
GB1272798A (en) * | 1969-10-27 | 1972-05-03 | Haldor Frederik Axel Topsoe | Low temperature methanol synthesis |
-
1976
- 1976-12-22 GB GB53505/76A patent/GB1592949A/en not_active Expired
-
1977
- 1977-12-15 US US05/860,949 patent/US4149940A/en not_active Expired - Lifetime
- 1977-12-20 NL NL7714099A patent/NL7714099A/xx not_active Application Discontinuation
- 1977-12-21 FR FR7738621A patent/FR2375171A1/fr active Granted
- 1977-12-21 IT IT31054/77A patent/IT1090355B/it active
- 1977-12-21 CA CA293,580A patent/CA1101446A/fr not_active Expired
- 1977-12-22 DE DE19772757478 patent/DE2757478A1/de not_active Withdrawn
- 1977-12-22 JP JP15504277A patent/JPS5379807A/ja active Pending
Also Published As
Publication number | Publication date |
---|---|
NL7714099A (nl) | 1978-06-26 |
IT1090355B (it) | 1985-06-26 |
GB1592949A (en) | 1981-07-15 |
FR2375171B3 (fr) | 1980-08-08 |
DE2757478A1 (de) | 1978-07-13 |
JPS5379807A (en) | 1978-07-14 |
CA1101446A (fr) | 1981-05-19 |
US4149940A (en) | 1979-04-17 |
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