WO1991012224A3 - Circulating bed cofeed conversion reactor and method for converting light hydrocarbons to olefins, gasoline and methanol - Google Patents

Circulating bed cofeed conversion reactor and method for converting light hydrocarbons to olefins, gasoline and methanol Download PDF

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Publication number
WO1991012224A3
WO1991012224A3 PCT/US1991/000937 US9100937W WO9112224A3 WO 1991012224 A3 WO1991012224 A3 WO 1991012224A3 US 9100937 W US9100937 W US 9100937W WO 9112224 A3 WO9112224 A3 WO 9112224A3
Authority
WO
WIPO (PCT)
Prior art keywords
light hydrocarbons
gasoline
methanol
olefins
cofeed
Prior art date
Application number
PCT/US1991/000937
Other languages
French (fr)
Other versions
WO1991012224A2 (en
Inventor
Charanjit Singh Bains
Martin Paul Grosboll
Behzad Jazayeri
Original Assignee
Lyondell Petrochem
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 Lyondell Petrochem filed Critical Lyondell Petrochem
Priority to EP91904659A priority Critical patent/EP0515500A1/en
Priority to CA002075891A priority patent/CA2075891A1/en
Priority to PCT/US1991/000937 priority patent/WO1991012224A2/en
Publication of WO1991012224A2 publication Critical patent/WO1991012224A2/en
Publication of WO1991012224A3 publication Critical patent/WO1991012224A3/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15Preparation 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
    • C07C29/151Preparation 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
    • C07C29/1516Multisteps
    • C07C29/1518Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1845Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised
    • B01J8/1863Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised followed by a downward movement outside the reactor and subsequently re-entering it
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/38Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/388Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/76Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/76Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
    • C07C2/82Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen oxidative coupling
    • C07C2/84Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen oxidative coupling catalytic
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15Preparation 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
    • C07C29/151Preparation 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
    • C07C29/152Preparation 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 reactor used
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/04Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C10L1/06Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/02Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the alkali- or alkaline earth metals or beryllium
    • C07C2523/04Alkali metals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • C07C2523/32Manganese, technetium or rhenium
    • C07C2523/34Manganese
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00Chemistry of hydrocarbon compounds
    • Y10S585/929Special chemical considerations
    • Y10S585/943Synthesis from methane or inorganic carbon source, e.g. coal

Abstract

The invention provides a method of converting light hydrocarbons to olefins, gasoline and methanol. In the first stage, a gas containing one or more light hydrocarbons is synthesized to higher hydrocarbons including raw gasoline. However, at commercially acceptable selectivities using currently available catalyst, a majority of the light hydrocarbons remain unsynthesized. In addition, the synthesis produces significant quantities of carbon dioxide and some carbon monoxide. In this method the unsynthesized light hydrocarbons and the oxides of carbon are used to produce methanol, which can be used for several purposes including gasoline or ethylene synthesis.
PCT/US1991/000937 1990-02-12 1991-02-12 Circulating bed cofeed conversion reactor and method for converting light hydrocarbons to olefins, gasoline and methanol WO1991012224A2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP91904659A EP0515500A1 (en) 1990-02-12 1991-02-12 Circulating bed cofeed conversion reactor and method for converting light hydrocarbons to olefins, gasoline and methanol
CA002075891A CA2075891A1 (en) 1990-02-12 1991-02-12 Circulating bed cofeed conversion reactor and method for converting light hydrocarbons to olefins, gasoline and methanol
PCT/US1991/000937 WO1991012224A2 (en) 1990-02-12 1991-02-12 Circulating bed cofeed conversion reactor and method for converting light hydrocarbons to olefins, gasoline and methanol

Applications Claiming Priority (6)

Application Number Priority Date Filing Date Title
US07/479,086 US5026934A (en) 1990-02-12 1990-02-12 Method for converting light hydrocarbons to olefins, gasoline and methanol
US479,086 1990-02-12
US53191090A 1990-06-01 1990-06-01
US531,910 1990-06-01
PCT/US1991/000937 WO1991012224A2 (en) 1990-02-12 1991-02-12 Circulating bed cofeed conversion reactor and method for converting light hydrocarbons to olefins, gasoline and methanol
CN91101783.6A CN1064474A (en) 1990-02-12 1991-02-25 The method of converting light hydrocarbons to olefins, gasoline and methyl alcohol

Publications (2)

Publication Number Publication Date
WO1991012224A2 WO1991012224A2 (en) 1991-08-22
WO1991012224A3 true WO1991012224A3 (en) 1992-04-02

Family

ID=36764652

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1991/000937 WO1991012224A2 (en) 1990-02-12 1991-02-12 Circulating bed cofeed conversion reactor and method for converting light hydrocarbons to olefins, gasoline and methanol

Country Status (6)

Country Link
US (1) US5026934A (en)
EP (1) EP0515500A1 (en)
CN (1) CN1064474A (en)
CA (1) CA2075891A1 (en)
NZ (1) NZ237096A (en)
WO (1) WO1991012224A2 (en)

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JP2925963B2 (en) * 1994-12-05 1999-07-28 石油公団 Method and apparatus for oxidative coupling of methane
US5733941A (en) * 1996-02-13 1998-03-31 Marathon Oil Company Hydrocarbon gas conversion system and process for producing a synthetic hydrocarbon liquid
US6130259A (en) * 1996-02-13 2000-10-10 Marathon Oil Company Hydrocarbon gas conversion system and process for producing a synthetic hydrocarbon liquid
US5861441A (en) * 1996-02-13 1999-01-19 Marathon Oil Company Combusting a hydrocarbon gas to produce a reformed gas
US6201029B1 (en) 1996-02-13 2001-03-13 Marathon Oil Company Staged combustion of a low heating value fuel gas for driving a gas turbine
US6313361B1 (en) 1996-02-13 2001-11-06 Marathon Oil Company Formation of a stable wax slurry from a Fischer-Tropsch reactor effluent
CA2257848A1 (en) * 1996-06-21 1997-12-24 Syntroleum Corporation Synthesis gas production system and method
MY118075A (en) 1996-07-09 2004-08-30 Syntroleum Corp Process for converting gas to liquids
US5950732A (en) * 1997-04-02 1999-09-14 Syntroleum Corporation System and method for hydrate recovery
US6011073A (en) 1997-10-10 2000-01-04 Syntroleum Corporation System and method for converting light hydrocarbons to heavier hydrocarbons with separation of water into oxygen and hydrogen
US6096934A (en) * 1998-12-09 2000-08-01 Uop Llc Oxidative coupling of methane with carbon conservation
US7838708B2 (en) 2001-06-20 2010-11-23 Grt, Inc. Hydrocarbon conversion process improvements
US6794417B2 (en) 2002-06-19 2004-09-21 Syntroleum Corporation System and method for treatment of water and disposal of contaminants produced by converting lighter hydrocarbons into heavier hydrocarbon
US7151198B2 (en) * 2002-12-30 2006-12-19 Exxonmobil Chemical Patents Inc. Integration of a methanol synthesis system with a methanol to olefin reaction system
US7161051B2 (en) * 2002-12-30 2007-01-09 Exxonmobil Chemical Patents Inc. Integration of a methanol synthesis system with a methanol to olefin reaction system
WO2005021468A1 (en) 2003-07-15 2005-03-10 Grt, Inc. Hydrocarbon synthesis
US20050171393A1 (en) 2003-07-15 2005-08-04 Lorkovic Ivan M. Hydrocarbon synthesis
US8642822B2 (en) 2004-04-16 2014-02-04 Marathon Gtf Technology, Ltd. Processes for converting gaseous alkanes to liquid hydrocarbons using microchannel reactor
US20060100469A1 (en) 2004-04-16 2006-05-11 Waycuilis John J Process for converting gaseous alkanes to olefins and liquid hydrocarbons
US7244867B2 (en) 2004-04-16 2007-07-17 Marathon Oil Company Process for converting gaseous alkanes to liquid hydrocarbons
US8173851B2 (en) 2004-04-16 2012-05-08 Marathon Gtf Technology, Ltd. Processes for converting gaseous alkanes to liquid hydrocarbons
US7674941B2 (en) 2004-04-16 2010-03-09 Marathon Gtf Technology, Ltd. Processes for converting gaseous alkanes to liquid hydrocarbons
US20080275284A1 (en) 2004-04-16 2008-11-06 Marathon Oil Company Process for converting gaseous alkanes to liquid hydrocarbons
EP2457887A1 (en) 2006-02-03 2012-05-30 GRT, Inc. Continuous process for converting natural gas to liquid hydrocarbons
EP1993951B1 (en) 2006-02-03 2014-07-30 GRT, Inc. Separation of light gases from bromine
CN101765574A (en) 2007-05-24 2010-06-30 Grt公司 Zone reactor incorporating reversible hydrogen halide capture and release
US7989507B2 (en) * 2008-05-20 2011-08-02 Siemens Aktiengesellschaft Production of fuel materials utilizing waste carbon dioxide and hydrogen from renewable resources
US8282810B2 (en) 2008-06-13 2012-10-09 Marathon Gtf Technology, Ltd. Bromine-based method and system for converting gaseous alkanes to liquid hydrocarbons using electrolysis for bromine recovery
AU2009270801B2 (en) 2008-07-18 2014-04-24 Reaction 35, Llc Continuous process for converting natural gas to liquid hydrocarbons
WO2011057982A2 (en) * 2009-11-10 2011-05-19 Shell Internationale Research Maatschappij B.V. Process for producing olefins
US8367884B2 (en) 2010-03-02 2013-02-05 Marathon Gtf Technology, Ltd. Processes and systems for the staged synthesis of alkyl bromides
US8198495B2 (en) 2010-03-02 2012-06-12 Marathon Gtf Technology, Ltd. Processes and systems for the staged synthesis of alkyl bromides
US8815050B2 (en) 2011-03-22 2014-08-26 Marathon Gtf Technology, Ltd. Processes and systems for drying liquid bromine
US8436220B2 (en) 2011-06-10 2013-05-07 Marathon Gtf Technology, Ltd. Processes and systems for demethanization of brominated hydrocarbons
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US8802908B2 (en) 2011-10-21 2014-08-12 Marathon Gtf Technology, Ltd. Processes and systems for separate, parallel methane and higher alkanes' bromination
US9193641B2 (en) 2011-12-16 2015-11-24 Gtc Technology Us, Llc Processes and systems for conversion of alkyl bromides to higher molecular weight hydrocarbons in circulating catalyst reactor-regenerator systems
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US3041273A (en) * 1953-09-09 1962-06-26 Sinclair Research Inc Process for the conversion of hydrocarbons with the use of an expanding transfer line reactor
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US4795849A (en) * 1987-08-04 1989-01-03 Atlantic Richfield Company Methane conversion process

Also Published As

Publication number Publication date
EP0515500A1 (en) 1992-12-02
CA2075891A1 (en) 1991-08-13
US5026934A (en) 1991-06-25
CN1064474A (en) 1992-09-16
NZ237096A (en) 1992-09-25
WO1991012224A2 (en) 1991-08-22

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