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 carburante

Info

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
Application number
ES502752A
Other languages
English (en)
Other versions
ES502752A0 (es
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SnamProgetti SpA
Original Assignee
SnamProgetti SpA
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SnamProgetti SpA filed Critical SnamProgetti SpA
Publication of ES8204760A1 publication Critical patent/ES8204760A1/es
Publication of ES502752A0 publication Critical patent/ES502752A0/es
Granted legal-status Critical Current

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.
ES502752A 1980-05-16 1981-05-15 Procedimiento para la obtencion de una mezcla de metanol y alcoholes superiores grado carburante Granted ES502752A0 (es)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Also Published As

Publication number Publication date
BE888799A (fr) 1981-11-16
CU21284A3 (en) 1985-12-16
PH16550A (en) 1983-11-16
PL231186A1 (es) 1981-12-23
AU7059081A (en) 1981-11-19
GB2076423A (en) 1981-12-02
YU121281A (en) 1983-04-30
ATA179881A (de) 1985-06-15
ZA813274B (en) 1982-05-26
NO154171C (no) 1986-07-30
FI811517L (fi) 1981-11-17
KR840001860B1 (ko) 1984-10-23
FI75142B (fi) 1988-01-29
KR830006406A (ko) 1983-09-24
CS224613B2 (en) 1984-01-16
RO82284B (ro) 1983-07-30
PL129214B1 (en) 1984-04-30
FR2482584A1 (fr) 1981-11-20
AT379580B (de) 1986-01-27
NO154171B (no) 1986-04-21
FR2482584B1 (es) 1984-05-04
SE451142B (sv) 1987-09-07
IT1148864B (it) 1986-12-03
US4460378A (en) 1984-07-17
GB2076423B (en) 1984-07-04
DE3119306A1 (de) 1982-03-04
GR75228B (es) 1984-07-13
AU543346B2 (en) 1985-04-18
DE3119306C2 (de) 1984-04-19
FI75142C (fi) 1988-05-09
RO82284A (ro) 1983-08-03
NZ196806A (en) 1984-03-16
NL8102404A (nl) 1981-12-16
ES502752A0 (es) 1982-04-01
IT8022117A0 (it) 1980-05-16
NO811644L (no) 1981-11-17
DK203681A (da) 1981-11-17
SU1442066A3 (ru) 1988-11-30
IN155671B (es) 1985-02-23
CA1159256A (en) 1983-12-27
IE51105B1 (en) 1986-10-01
JPH0232312B2 (es) 1990-07-19
DD158913A5 (de) 1983-02-09
TR20809A (tr) 1982-09-16
SE8103073L (sv) 1981-11-17
BR8102808A (pt) 1982-02-02
JPS5710690A (en) 1982-01-20
EG15388A (en) 1986-09-30
IE810787L (en) 1981-11-16
CH648342A5 (it) 1985-03-15
LU83366A1 (fr) 1982-01-20

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