SG11201704589QA - Hydrocarbon conversion to ethylene - Google Patents
Hydrocarbon conversion to ethyleneInfo
- Publication number
- SG11201704589QA SG11201704589QA SG11201704589QA SG11201704589QA SG11201704589QA SG 11201704589Q A SG11201704589Q A SG 11201704589QA SG 11201704589Q A SG11201704589Q A SG 11201704589QA SG 11201704589Q A SG11201704589Q A SG 11201704589QA SG 11201704589Q A SG11201704589Q A SG 11201704589QA
- Authority
- SG
- Singapore
- Prior art keywords
- ethylene
- hydrocarbon conversion
- hydrocarbon
- conversion
- Prior art date
Links
Classifications
-
- 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
- C07C4/04—Thermal 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/248—Reactors comprising multiple separated flow channels
- B01J19/2485—Monolithic reactors
-
- 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
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
-
- 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
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0403—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal
- B01J8/0423—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more otherwise shaped beds
- B01J8/0438—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more otherwise shaped beds the beds being placed next to each other
-
- 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
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0496—Heating or cooling the reactor
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/04—Ethylene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
- C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds only
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/26—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with discontinuously preheated non-moving solid material, e.g. blast and run
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00513—Controlling the temperature using inert heat absorbing solids in the 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00548—Flow
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00164—Controlling or regulating processes controlling the flow
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201462093003P | 2014-12-17 | 2014-12-17 | |
EP15153727 | 2015-02-04 | ||
PCT/US2015/060906 WO2016099739A1 (en) | 2014-12-17 | 2015-11-16 | Hydrocarbon conversion to ethylene |
Publications (1)
Publication Number | Publication Date |
---|---|
SG11201704589QA true SG11201704589QA (en) | 2017-07-28 |
Family
ID=52440612
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SG11201704589QA SG11201704589QA (en) | 2014-12-17 | 2015-11-16 | Hydrocarbon conversion to ethylene |
Country Status (5)
Country | Link |
---|---|
US (2) | US9499457B2 (en) |
EP (1) | EP3233771A1 (en) |
CN (1) | CN107001185A (en) |
SG (1) | SG11201704589QA (en) |
WO (1) | WO2016099739A1 (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10385468B2 (en) | 2016-06-06 | 2019-08-20 | Ih Ip Holdings Limited | Plasma frequency trigger |
WO2018044555A1 (en) | 2016-08-31 | 2018-03-08 | Exxonmobil Chemical Patents Inc. | Hydrocarbon pyrolysis |
US11130916B2 (en) | 2016-08-31 | 2021-09-28 | Exxonmobil Chemical Patents Inc. | Pyrolysis reactor approach temperature |
WO2018044558A1 (en) | 2016-08-31 | 2018-03-08 | Exxonmobil Chemical Patents Inc. | Pyrolysis product compression |
US10577292B2 (en) | 2016-08-31 | 2020-03-03 | Exxonmobil Chemical Patents Inc. | Hydrocarbon conversion |
WO2018044552A1 (en) | 2016-08-31 | 2018-03-08 | Exxonmobil Chemical Patents Inc. | Hydrocarbon pyrolysis |
US10711203B2 (en) | 2016-08-31 | 2020-07-14 | Exxonmobil Chemical Patents Inc. | Hydrocarbon pyrolysis |
WO2018170263A1 (en) * | 2017-03-17 | 2018-09-20 | Sabic Global Technologies, B.V. | A process for the production of c2 hydrocarbons via partial oxidative pyrolysis of methane integrated with endothermic c2h6 + co2 quench reactions |
WO2019164523A1 (en) * | 2018-02-26 | 2019-08-29 | Ihl Holdings Limited | A continuously running exothermic reactor system |
WO2019173570A1 (en) * | 2018-03-07 | 2019-09-12 | Sabic Global Technologies B.V. | Method and reactor for pyrolysis conversion of hydrocarbon gases |
US10941357B2 (en) | 2018-04-16 | 2021-03-09 | Swift Fuels, Llc | Process for converting C2—C5 hydrocarbons to gasoline and diesel fuel blendstocks |
US11279884B2 (en) | 2018-04-20 | 2022-03-22 | Exxonmobil Chemical Patents Inc. | Reverse flow reactors having low maldistribution parameter while containing asymmetric feeds, methods of using same, and pyrolysis products made from same |
WO2019204082A1 (en) | 2018-04-20 | 2019-10-24 | Exxonmobil Chemical Patents Inc. | Reverse flow reactors having high purge efficiencies while containing asymmetric feeds, methods of using same, and pyrolysis products made from same |
US10836965B2 (en) | 2018-04-24 | 2020-11-17 | Exxonmobil Chemical Patents Inc. | Reactor apparatus for non-oxidative hydrocarbon conversion to aromatics, methods of using same, and products made using same |
CN108949210A (en) * | 2018-07-31 | 2018-12-07 | 乳源东阳光氟树脂有限公司 | A kind of operation method of monomer pyrolysis furnace |
US11180699B1 (en) * | 2019-07-01 | 2021-11-23 | Gen Tech PTD, LLC | System and method for converting plastic into diesel |
US20230027105A1 (en) | 2019-12-30 | 2023-01-26 | Exxonmobil Chemical Patents Inc. | Pyrolysis Product Compression using CO2 Loop |
US11773335B2 (en) | 2021-01-22 | 2023-10-03 | ExxonMobil Technology and Engineering Company | Heat source for pyrolysis process |
WO2023137068A1 (en) * | 2022-01-14 | 2023-07-20 | Lummus Technology Llc | Plastic pyrolysis heating/reaction recipe |
Family Cites Families (40)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2319679A (en) | 1942-04-27 | 1943-05-18 | Wulff Process Company | Manufacture of acetylene by regenerative type of pyrolysis |
US2629753A (en) * | 1948-08-26 | 1953-02-24 | Dow Chemical Co | Making ethylene by catalytic pyrolysis |
US2692818A (en) | 1950-07-18 | 1954-10-26 | Allied Chem & Dye Corp | Removing nitrogen trichloride from chlorine |
US2678339A (en) | 1951-05-05 | 1954-05-11 | Wulff Process Company | Process of producting gases by pyrolysis |
US2692819A (en) | 1952-03-10 | 1954-10-26 | Wulff Process Company | Furnace and apparatus for producing acetylene by the pyrolysis of a suitable hydrocarbon |
US2956864A (en) | 1955-01-10 | 1960-10-18 | Wulff Process Company | Furnace assemblies and combination of such furnaces |
US4076698A (en) | 1956-03-01 | 1978-02-28 | E. I. Du Pont De Nemours And Company | Hydrocarbon interpolymer compositions |
US2967205A (en) | 1956-09-24 | 1961-01-03 | Wulff Process Company | Process of and apparatus for producing acetylene and ethylene |
US3024094A (en) | 1956-09-24 | 1962-03-06 | Wulff Process Company | Regenerative furnace and process of operating |
GB830574A (en) | 1957-12-23 | 1960-03-16 | Wulff Process Company | Process of producing acetylene and ethylene |
IT609922A (en) | 1959-06-06 | |||
US3093697A (en) | 1960-05-27 | 1963-06-11 | Union Carbide Corp | Process for producing acetylene |
US3305538A (en) | 1961-11-22 | 1967-02-21 | Montedison Spa | Polymerization process |
US3364190A (en) | 1964-04-27 | 1968-01-16 | Standard Oil Co | Process for polymerizing propylene to syndiotactic polypropylene |
CA849081A (en) | 1967-03-02 | 1970-08-11 | Du Pont Of Canada Limited | PRODUCTION OF ETHYLENE/.alpha.-OLEFIN COPOLYMERS OF IMPROVED PHYSICAL PROPERTIES |
GB1240182A (en) * | 1968-10-11 | 1971-07-21 | Union Carbide Corp | Method and apparatus for the control of regenerative furnaces in the pyrolysis of hydrocarbons |
US4302565A (en) | 1978-03-31 | 1981-11-24 | Union Carbide Corporation | Impregnated polymerization catalyst, process for preparing, and use for ethylene copolymerization |
US4243691A (en) | 1979-05-18 | 1981-01-06 | The Procter & Gamble Company | Sodium-free salt substitute |
US4659685A (en) | 1986-03-17 | 1987-04-21 | The Dow Chemical Company | Heterogeneous organometallic catalysts containing a supported titanium compound and at least one other supported organometallic compound |
US5019143A (en) | 1987-09-23 | 1991-05-28 | Mehrta Yuv R | Low pressure noncryogenic processing for ethylene recovery |
US5082481A (en) | 1990-04-10 | 1992-01-21 | Lummus Crest, Inc. | Membrane separation process for cracked gases |
AU675436B2 (en) | 1992-05-27 | 1997-02-06 | Exxon Chemical Patents Inc. | Production of high purity olefins |
US5452581A (en) | 1994-04-01 | 1995-09-26 | Dinh; Cong X. | Olefin recovery method |
US5672197A (en) | 1995-10-11 | 1997-09-30 | Rothchild; Ronald D. | Gas separation by continuous pressure-swing chromatography |
US5904880A (en) | 1996-12-31 | 1999-05-18 | Exxon Chemical Patents Inc. | One step conversion of methanol to hydrogen and carbon dioxide |
US6069288A (en) | 1996-12-31 | 2000-05-30 | Exxon Chemical Patents Inc. | Process for selectively separating hydrogen, or both hydrogen and carbon monoxide from olefinic hydrocarbons |
US5960643A (en) | 1996-12-31 | 1999-10-05 | Exxon Chemical Patents Inc. | Production of ethylene using high temperature demethanization |
US5927063A (en) | 1997-08-19 | 1999-07-27 | Exxon Chemical Patents Inc. | High efficiency reformed methanol gas turbine power plants |
US5892079A (en) | 1997-10-17 | 1999-04-06 | Sri International | Metallocene catalysts and associated methods of preparation and use |
US6293998B1 (en) | 1998-12-11 | 2001-09-25 | Uop Llc | Apparatus for use in pressure and temperature swing adsorption processes |
US6271428B1 (en) | 1999-07-22 | 2001-08-07 | Uop Llc | Process for the purification of a diolefin hydrocarbon stream |
US6293999B1 (en) | 1999-11-30 | 2001-09-25 | Uop Llc | Process for separating propylene from propane |
US6593506B1 (en) | 2000-10-12 | 2003-07-15 | Exxonmobil Chemical Patents Inc. | Olefin recovery in a polyolefin production process |
US7491250B2 (en) | 2002-06-25 | 2009-02-17 | Exxonmobil Research And Engineering Company | Pressure swing reforming |
US7846401B2 (en) | 2005-12-23 | 2010-12-07 | Exxonmobil Research And Engineering Company | Controlled combustion for regenerative reactors |
US7815873B2 (en) | 2006-12-15 | 2010-10-19 | Exxonmobil Research And Engineering Company | Controlled combustion for regenerative reactors with mixer/flow distributor |
US7914667B2 (en) | 2007-06-04 | 2011-03-29 | Exxonmobil Chemical Patents Inc. | Pyrolysis reactor conversion of hydrocarbon feedstocks into higher value hydrocarbons |
WO2011149635A1 (en) | 2010-05-28 | 2011-12-01 | Exxonmobil Chemical Patents Inc. | Reactor with reactor head and integrated valve |
EP2665801A1 (en) * | 2011-01-19 | 2013-11-27 | Exxonmobil Chemical Patents Inc. | Method and apparatus for converting hydrocarbons into olefins |
EP2758361A2 (en) * | 2011-09-23 | 2014-07-30 | Exxon-Mobil Chemical Patents Inc. | Hydrocarbon conversion process |
-
2015
- 2015-11-16 US US14/942,287 patent/US9499457B2/en active Active
- 2015-11-16 CN CN201580068295.9A patent/CN107001185A/en active Pending
- 2015-11-16 EP EP15802285.5A patent/EP3233771A1/en not_active Withdrawn
- 2015-11-16 WO PCT/US2015/060906 patent/WO2016099739A1/en active Application Filing
- 2015-11-16 SG SG11201704589QA patent/SG11201704589QA/en unknown
-
2016
- 2016-10-17 US US15/294,898 patent/US9809506B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP3233771A1 (en) | 2017-10-25 |
US9809506B2 (en) | 2017-11-07 |
US9499457B2 (en) | 2016-11-22 |
WO2016099739A1 (en) | 2016-06-23 |
CN107001185A (en) | 2017-08-01 |
US20170036971A1 (en) | 2017-02-09 |
US20160176781A1 (en) | 2016-06-23 |
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