ES8204760A1 - Procedimiento para la obtencion de una mezcla de metanol y alcoholes superiores grado carburante - Google Patents
Procedimiento para la obtencion de una mezcla de metanol y alcoholes superiores grado carburanteInfo
- Publication number
- ES8204760A1 ES8204760A1 ES502752A ES502752A ES8204760A1 ES 8204760 A1 ES8204760 A1 ES 8204760A1 ES 502752 A ES502752 A ES 502752A ES 502752 A ES502752 A ES 502752A ES 8204760 A1 ES8204760 A1 ES 8204760A1
- Authority
- ES
- Spain
- Prior art keywords
- mixture
- gases
- reactor
- methanol
- secondary reactor
- 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
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/023—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for spark ignition
-
- 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
- C07C29/1516—Multisteps
- C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
-
- 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
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Catalysts (AREA)
Abstract
PROCEDIMIENTO DE OBTENCION DE UNAMEZCLA E METANOL Y ALCOHOLES SUPERIORES GRADO CARBURANTE. CONSTA DE LAS SOGUIENTES FASES: 1) ALIMENTAR A UNREACTOR DE SINTESIS CON UNA MEZCLA DE CO Y H2. 2) EFRIGERAR LA MEZCLA DE REACCION CONSTITUIDA POR METANOL, ALCOHOLES SUPERIORES, AGUA Y GASES. 3) ENVIAR ESTA ULTIMA A UN REACTOR DE CONVERSION. 4) REFRIGERAR EL PRODUCTO DE REACCION. 5) SEPARAR LA FASE LIQUIDA CONSTITUIDA POR LA MEZCLA ALCOHOLICA Y LA FASE GASEOSA CONSTITUIDA POR CO, H2 Y CO2. 6) ENVIAR LA FASE GASEOSA A UNA SECCION DE ABSRCION PARA ELIMINAR EL CO2, SIENDO EL GAS PURIFICADO RECICLADO EN PARTE Y EN OTRA PARTE PURGADO. 7) EN VIAR LA FASE LIQUIDA A UNA SECCION DE EXTRACCION PAR ELIMINAR LOS GASES DISUELTOS EN LA MISMA EMPLEANDOSE COMO AGENTE EXTRACTOR LOS GASES DISUELTOS EN LA MISMA EMPLEANDOSE COMO AGENTE EXTRACTOR LOS GASES DE PURGA. 8) ENVIAR LA FASE LIQUIDA PURIFICADA A LA SECCION DE ABSORCION, DONDE ES IUTILIZADA COMO ABSORBENTE. LA TEMPERATURA DEL REACTOR OSCILA ENTRE 300 Y 500 GRADOSCENTIGRADOS, MIENTRAS QUE LAS PRESION DE SINTESIS ES SUPERIOR A 150 ATMOSFERAS.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT22117/80A IT1148864B (it) | 1980-05-16 | 1980-05-16 | Processo pe la produzione di una miscela di metanolo ed alcoli superiori grado carburante |
Publications (2)
Publication Number | Publication Date |
---|---|
ES8204760A1 true ES8204760A1 (es) | 1982-04-01 |
ES502752A0 ES502752A0 (es) | 1982-04-01 |
Family
ID=11191737
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES502752A Granted ES502752A0 (es) | 1980-05-16 | 1981-05-15 | Procedimiento para la obtencion de una mezcla de metanol y alcoholes superiores grado carburante |
Country Status (35)
Country | Link |
---|---|
US (1) | US4460378A (es) |
JP (1) | JPS5710690A (es) |
KR (1) | KR840001860B1 (es) |
AT (1) | AT379580B (es) |
AU (1) | AU543346B2 (es) |
BE (1) | BE888799A (es) |
BR (1) | BR8102808A (es) |
CA (1) | CA1159256A (es) |
CH (1) | CH648342A5 (es) |
CS (1) | CS224613B2 (es) |
CU (1) | CU21284A3 (es) |
DD (1) | DD158913A5 (es) |
DE (1) | DE3119306C2 (es) |
DK (1) | DK203681A (es) |
EG (1) | EG15388A (es) |
ES (1) | ES502752A0 (es) |
FI (1) | FI75142C (es) |
FR (1) | FR2482584A1 (es) |
GB (1) | GB2076423B (es) |
GR (1) | GR75228B (es) |
IE (1) | IE51105B1 (es) |
IN (1) | IN155671B (es) |
IT (1) | IT1148864B (es) |
LU (1) | LU83366A1 (es) |
NL (1) | NL8102404A (es) |
NO (1) | NO154171C (es) |
NZ (1) | NZ196806A (es) |
PH (1) | PH16550A (es) |
PL (1) | PL129214B1 (es) |
RO (1) | RO82284A (es) |
SE (1) | SE451142B (es) |
SU (1) | SU1442066A3 (es) |
TR (1) | TR20809A (es) |
YU (1) | YU121281A (es) |
ZA (1) | ZA813274B (es) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4787915A (en) * | 1981-03-24 | 1988-11-29 | Carbon Fuels Corporation | Method of varying rheology characteristics of novel coal derived fuel system |
IT1169281B (it) * | 1981-12-02 | 1987-05-27 | Assoreni & Snamprogetti Spa | Sistema catalitico e procedimento per la produzione di miscele di metanolo ed alcoli superiori |
FR2529544B1 (fr) * | 1982-07-05 | 1987-11-13 | Inst Francais Du Petrole | Produit d'alcools a partir de gaz de synthese |
US4705532A (en) * | 1985-07-15 | 1987-11-10 | The Standard Oil Company | Alcohol compositions for blending with gasoline |
US4762858A (en) * | 1985-09-16 | 1988-08-09 | The Dow Chemical Company | Syngas conversion to oxygenates by reduced yttrium/lanthanide/actinide-modified catalyst |
JP2560311B2 (ja) * | 1987-02-27 | 1996-12-04 | 三菱瓦斯化学株式会社 | メタノ−ルないし混合アルコ−ルの製造法 |
DE3810421A1 (de) * | 1988-03-26 | 1989-10-05 | Union Rheinische Braunkohlen | Verbessertes verfahren zur katalytischen herstellung eines alkoholgemischs mit erhoehtem isobutanolgehalt |
IT1276931B1 (it) * | 1995-10-13 | 1997-11-03 | Snam Progetti | Procedimento per produrre miscele di metanolo ed alcoli superiori |
AU1280299A (en) * | 1997-10-28 | 1999-05-17 | University Of Kansas, The | Blended compression-ignition fuel containing light synthetic crude and blending stock |
US20080260631A1 (en) | 2007-04-18 | 2008-10-23 | H2Gen Innovations, Inc. | Hydrogen production process |
GB201808019D0 (en) * | 2018-05-17 | 2018-07-04 | Johnson Matthey Davy Technologies Ltd | Process for synthesising methanol |
Family Cites Families (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE342014A (es) * | ||||
US1791568A (en) * | 1923-02-22 | 1931-02-10 | Ig Farbenindustrie Ag | Manufacture of oxygenated organic compounds |
US1569775A (en) * | 1924-09-04 | 1926-01-12 | Basf Ag | Synthetic manufacture of methanol |
US2010005A (en) * | 1932-04-06 | 1935-08-06 | Du Pont | Motor fuel |
US2281228A (en) * | 1939-03-03 | 1942-04-28 | Solvay Process Co | Process for synthesizing methanol |
DE824038C (de) * | 1949-11-10 | 1951-12-10 | Basf Ag | Verfahren zur Herstellung von Isobutylalkohol |
DE936715C (de) * | 1950-12-10 | 1955-12-22 | Linde Eismasch Ag | Verfahren zum Reinigen von Gasen durch Tiefkuehlung |
DE944186C (de) * | 1950-12-22 | 1956-06-07 | Basf Ag | Verfahren zur Gewinnung wasserstoffhaltiger Synthesegase |
US2964551A (en) * | 1957-03-27 | 1960-12-13 | Ici Ltd | Production of unsaturated hydrocarbons and methanol |
DE1442981A1 (de) * | 1963-07-30 | 1969-01-02 | Basf Ag | Verfahren zur Herstellung von Wasserstoff |
GB1159035A (en) * | 1965-08-18 | 1969-07-23 | Ici Ltd | Methanol Synthesis. |
FR1521405A (fr) * | 1966-01-22 | 1968-04-19 | Metallgesellschaft Ag | Procédé pour l'élimination partielle de l'anhydride carbonique dans les gaz employés pour la synthèse du méthanol |
DE1290123B (de) * | 1966-11-11 | 1969-03-06 | Union Rheinische Braunkohlen | Verfahren zur kontinuierlichen Reinigung von Methanolsynthesegas |
US3950369A (en) * | 1968-04-08 | 1976-04-13 | Imperial Chemical Industries Limited | Methanol production |
US3940428A (en) * | 1968-12-30 | 1976-02-24 | Imperial Chemical Industries Limited | Methanol production |
US3763205A (en) * | 1971-05-10 | 1973-10-02 | Du Pont | Methanol process with recycle |
JPS5243579A (en) * | 1975-09-30 | 1977-04-05 | Taishiyou Koruku Kougiyou Kk | Method of producing crown stopper |
CA1136114A (en) * | 1978-05-15 | 1982-11-23 | Harley F. Hardman | Preparation of alcohols from synthesis gas |
EP0011404B1 (en) * | 1978-11-10 | 1982-12-29 | Imperial Chemical Industries Plc | Integrated process for synthesis of methanol and of ammonia |
DE2904008A1 (de) * | 1979-02-02 | 1980-08-07 | Linde Ag | Verfahren zur herstellung von rohwasserstoff und methanol |
-
1980
- 1980-05-16 IT IT22117/80A patent/IT1148864B/it active
-
1981
- 1981-04-07 IE IE787/81A patent/IE51105B1/en unknown
- 1981-04-13 GR GR64666A patent/GR75228B/el unknown
- 1981-04-13 NZ NZ196806A patent/NZ196806A/en unknown
- 1981-04-20 PH PH25516A patent/PH16550A/en unknown
- 1981-04-21 AT AT0179881A patent/AT379580B/de not_active IP Right Cessation
- 1981-04-25 EG EG231/81A patent/EG15388A/xx active
- 1981-04-30 BR BR8102808A patent/BR8102808A/pt unknown
- 1981-05-04 RO RO81104183A patent/RO82284A/ro unknown
- 1981-05-07 DK DK203681A patent/DK203681A/da not_active Application Discontinuation
- 1981-05-11 CU CU8135453A patent/CU21284A3/es unknown
- 1981-05-12 TR TR20809A patent/TR20809A/xx unknown
- 1981-05-13 YU YU01212/81A patent/YU121281A/xx unknown
- 1981-05-13 FR FR8109484A patent/FR2482584A1/fr active Granted
- 1981-05-14 DE DE3119306A patent/DE3119306C2/de not_active Expired
- 1981-05-14 NO NO811644A patent/NO154171C/no unknown
- 1981-05-14 JP JP7153981A patent/JPS5710690A/ja active Granted
- 1981-05-14 GB GB8114776A patent/GB2076423B/en not_active Expired
- 1981-05-14 AU AU70590/81A patent/AU543346B2/en not_active Ceased
- 1981-05-14 KR KR1019810001658A patent/KR840001860B1/ko active IP Right Grant
- 1981-05-14 BE BE0/204783A patent/BE888799A/fr not_active IP Right Cessation
- 1981-05-15 LU LU83366A patent/LU83366A1/fr unknown
- 1981-05-15 PL PL1981231186A patent/PL129214B1/pl unknown
- 1981-05-15 FI FI811517A patent/FI75142C/fi not_active IP Right Cessation
- 1981-05-15 SE SE8103073A patent/SE451142B/sv not_active IP Right Cessation
- 1981-05-15 DD DD81230003A patent/DD158913A5/de unknown
- 1981-05-15 CA CA000377750A patent/CA1159256A/en not_active Expired
- 1981-05-15 ZA ZA00813274A patent/ZA813274B/xx unknown
- 1981-05-15 ES ES502752A patent/ES502752A0/es active Granted
- 1981-05-15 NL NL8102404A patent/NL8102404A/nl not_active Application Discontinuation
- 1981-05-15 CH CH3207/81A patent/CH648342A5/it not_active IP Right Cessation
- 1981-05-15 CS CS813623A patent/CS224613B2/cs unknown
- 1981-05-15 SU SU813285557A patent/SU1442066A3/ru active
- 1981-05-15 IN IN519/CAL/81A patent/IN155671B/en unknown
-
1983
- 1983-07-18 US US06/514,546 patent/US4460378A/en not_active Expired - Fee Related
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