SG11201903490UA - Method and device for manufacturing propene and c4 hydrocarbon - Google Patents

Method and device for manufacturing propene and c4 hydrocarbon

Info

Publication number
SG11201903490UA
SG11201903490UA SG11201903490UA SG11201903490UA SG11201903490UA SG 11201903490U A SG11201903490U A SG 11201903490UA SG 11201903490U A SG11201903490U A SG 11201903490UA SG 11201903490U A SG11201903490U A SG 11201903490UA SG 11201903490U A SG11201903490U A SG 11201903490UA
Authority
SG
Singapore
Prior art keywords
hydrocarbons
hydrocarbon
product
propylene
propene
Prior art date
Application number
SG11201903490UA
Inventor
Mao Ye
Tao Zhang
Changqing He
Jinling Zhang
Xiangao Wang
Hailong Tang
Jinming Jia
Yinfeng Zhao
Zhongmin Liu
Original Assignee
Dalian Inst Chemical Physics Cas
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 Dalian Inst Chemical Physics Cas filed Critical Dalian Inst Chemical Physics Cas
Publication of SG11201903490UA publication Critical patent/SG11201903490UA/en

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • C07C1/22—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms by reduction
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/82—Phosphates
    • B01J29/84—Aluminophosphates containing other elements, e.g. metals, boron
    • B01J29/85—Silicoaluminophosphates (SAPO compounds)
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/12—Treating with free oxygen-containing gas
    • B01J38/30—Treating with free oxygen-containing gas in gaseous suspension, e.g. fluidised bed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical 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
    • B01J8/26—Chemical 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 two or more fluidised beds, e.g. reactor and regeneration installations
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00—Aliphatic unsaturated hydrocarbons
    • C07C11/02—Alkenes
    • C07C11/06—Propene
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00—Aliphatic unsaturated hydrocarbons
    • C07C11/02—Alkenes
    • C07C11/08—Alkenes with four carbon atoms
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00—Aliphatic unsaturated hydrocarbons
    • C07C11/12—Alkadienes
    • C07C11/16—Alkadienes with four carbon atoms
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/06—Catalytic processes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C9/00—Aliphatic saturated hydrocarbons
    • C07C9/02—Aliphatic saturated hydrocarbons with one to four carbon atoms
    • C07C9/10—Aliphatic saturated hydrocarbons with one to four carbon atoms with four carbon atoms
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1872—Details of the fluidised bed reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical 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
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/82—Phosphates
    • C07C2529/84—Aluminophosphates containing other elements, e.g. metals, boron
    • C07C2529/85—Silicoaluminophosphates (SAPO compounds)
    • 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
    • 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
    • Y02P20/584—Recycling of 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
    • 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
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/40—Ethylene production

Abstract

The present invention refers to a method and device for preparing propylene and C4 hydrocarbons from oxygen-containing compounds. By means of circulating 80 wt.% or more of the hydrocarbons with 5 or more carbons in the product into a catalytic cracking lift pipe to perform a cracking reaction to generate a product containing propylene and C4 hydrocarbons, the method improves the reaction rate of ethylene 5 alkylation, and the unit volume production capacity of reactor is high.
SG11201903490UA 2016-10-19 2016-10-19 Method and device for manufacturing propene and c4 hydrocarbon SG11201903490UA (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2016/102561 WO2018072140A1 (en) 2016-10-19 2016-10-19 Method and device for manufacturing propene and c4 hydrocarbon

Publications (1)

Publication Number Publication Date
SG11201903490UA true SG11201903490UA (en) 2019-05-30

Family

ID=62018634

Family Applications (1)

Application Number Title Priority Date Filing Date
SG11201903490UA SG11201903490UA (en) 2016-10-19 2016-10-19 Method and device for manufacturing propene and c4 hydrocarbon

Country Status (11)

Country Link
US (1) US10626062B2 (en)
EP (1) EP3530642B1 (en)
JP (1) JP6864957B2 (en)
KR (1) KR102243320B1 (en)
AU (1) AU2016427078B2 (en)
BR (1) BR112019008029B1 (en)
MY (1) MY190048A (en)
RU (1) RU2726483C1 (en)
SG (1) SG11201903490UA (en)
WO (1) WO2018072140A1 (en)
ZA (1) ZA201903068B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108786670B (en) * 2017-04-27 2021-01-26 中国科学院大连化学物理研究所 Method for preparing p-xylene and co-producing low-carbon olefin by methanol and/or dimethyl ether and toluene
CN108794291B (en) * 2017-04-27 2020-11-27 中国科学院大连化学物理研究所 Fluidized bed device and method for preparing p-xylene and co-producing low-carbon olefin by methanol and/or dimethyl ether and toluene
CN108786672B (en) * 2017-04-27 2021-01-26 中国科学院大连化学物理研究所 Method for preparing p-xylene and co-producing low-carbon olefin by using methanol and/or dimethyl ether and benzene
CN111054281B (en) * 2018-10-17 2022-03-11 中国石油化工股份有限公司 Catalyst fluidized bed reactor, reaction system and method using system
CN109701454B (en) * 2019-01-28 2024-02-13 安庆市泰发能源科技有限公司 Butane dehydrogenation start-up circulation heating device

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US5028310A (en) * 1989-11-08 1991-07-02 Texaco Inc. Reduction of SOx in regenerator off gas of a fluid cracking unit
US5914433A (en) * 1997-07-22 1999-06-22 Uop Lll Process for producing polymer grade olefins
US6455749B1 (en) 1997-10-03 2002-09-24 Exxonmobil Chemical Patents, Inc. Method for increasing light olefin yield by conversion of a heavy hydrocarbon fraction of a product to light olefins
US7232936B1 (en) * 2000-02-22 2007-06-19 Exxonmobil Chemical Patents Inc. Conversion of oxygenate to olefins with staged injection of oxygenate
US6303839B1 (en) * 2000-06-14 2001-10-16 Uop Llc Process for producing polymer grade olefins
DE10233975A1 (en) 2002-07-25 2004-02-12 Lurgi Ag Device for the production of propylene from methanol comprises preferably two or three vertically arranged reaction stages having a form-selective pentasil-type zeolite catalyst with heat exchangers arranged between the stages
CN101177374B (en) 2006-11-07 2011-06-01 中国科学院大连化学物理研究所 Method for producing propylene by carbinol or dimethyl ether
CN101348404B (en) * 2007-07-18 2011-11-30 中国石油化工股份有限公司 Method for improving ethylene and propene yield in methyl alcohol or dimethyl ether conversion process
US8269056B2 (en) * 2007-11-19 2012-09-18 Shell Oil Company Process for the preparation of an olefinic product
CN101260013B (en) 2008-04-24 2011-07-20 中国石油化工股份有限公司 Method for preparing low-carbon olefins from oxygen-containing compound
CN102463086B (en) * 2010-11-17 2014-01-22 中国石油化工股份有限公司 Reaction device for co-producing low-carbon olefin and p-xylene
CN103193574B (en) * 2012-01-10 2015-01-07 中国石油化工股份有限公司 On-stream method of methanol to light olefin reaction-regeneration device
RU2487160C1 (en) * 2012-03-26 2013-07-10 Борис Захарович Соляр Procedure for catalytic cracking of hydrocarbon material with yield of light olefins and device for its implementation
US20140148631A1 (en) * 2012-07-03 2014-05-29 Shell Oil Company Process for preparing ethylene and/or propylene
CA2877799A1 (en) * 2012-07-03 2014-01-09 Shell Internationale Research Maatschappij B.V. Process for preparing ethylene and/or propylene
CN103804110B (en) * 2012-11-13 2015-11-11 神华集团有限责任公司 Organic oxygen-containing compound producing light olefins and C 5+hydrocarbon catalytic pyrolysis coupling technique
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Also Published As

Publication number Publication date
US20190241480A1 (en) 2019-08-08
MY190048A (en) 2022-03-23
RU2726483C1 (en) 2020-07-14
EP3530642A4 (en) 2020-03-25
EP3530642A1 (en) 2019-08-28
WO2018072140A1 (en) 2018-04-26
ZA201903068B (en) 2020-09-30
BR112019008029A2 (en) 2019-07-09
KR102243320B1 (en) 2021-04-21
JP2020500840A (en) 2020-01-16
BR112019008029B1 (en) 2022-03-22
JP6864957B2 (en) 2021-04-28
US10626062B2 (en) 2020-04-21
EP3530642B1 (en) 2024-01-24
AU2016427078A1 (en) 2019-06-06
AU2016427078B2 (en) 2020-04-02
KR20190062546A (en) 2019-06-05

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