ES2032023T3 - Procedimiento de hidrogenacion. - Google Patents
Procedimiento de hidrogenacion.Info
- Publication number
- ES2032023T3 ES2032023T3 ES198888311188T ES88311188T ES2032023T3 ES 2032023 T3 ES2032023 T3 ES 2032023T3 ES 198888311188 T ES198888311188 T ES 198888311188T ES 88311188 T ES88311188 T ES 88311188T ES 2032023 T3 ES2032023 T3 ES 2032023T3
- Authority
- ES
- Spain
- Prior art keywords
- hydrogenation
- bed
- hydrogen
- organic feedstock
- containing gas
- 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 - Lifetime
Links
- 238000005984 hydrogenation reaction Methods 0.000 title abstract 9
- 238000000034 method Methods 0.000 title abstract 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 5
- 229910052739 hydrogen Inorganic materials 0.000 abstract 5
- 239000001257 hydrogen Substances 0.000 abstract 5
- 239000003054 catalyst Substances 0.000 abstract 4
- 239000007789 gas Substances 0.000 abstract 3
- 239000002245 particle Substances 0.000 abstract 3
- 125000004432 carbon atom Chemical group C* 0.000 abstract 2
- 239000012527 feed solution Substances 0.000 abstract 2
- 239000007788 liquid Substances 0.000 abstract 2
- 239000007791 liquid phase Substances 0.000 abstract 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 abstract 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 abstract 1
- 239000003701 inert diluent Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/02—Monohydroxylic acyclic alcohols
- C07C31/125—Monohydroxylic acyclic alcohols containing five to twenty-two 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
- B01J8/02—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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B31/00—Reduction in general
-
- 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
- C07C29/132—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 an oxygen containing functional group
- C07C29/136—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 an oxygen containing functional group of >C=O containing groups, e.g. —COOH
- C07C29/14—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 an oxygen containing functional group of >C=O containing groups, e.g. —COOH of a —CHO group
- C07C29/141—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 an oxygen containing functional group of >C=O containing groups, e.g. —COOH of a —CHO group with hydrogen or hydrogen-containing gases
-
- 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
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
- B01J2208/00044—Temperature measurement
- B01J2208/00061—Temperature measurement of the reactants
-
- 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
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00141—Coils
-
- 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
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00212—Plates; Jackets; Cylinders
-
- 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
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00256—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles in a heat exchanger for the heat exchange medium separate from 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00477—Controlling the temperature by thermal insulation means
- B01J2208/00495—Controlling the temperature by thermal insulation means using insulating materials or refractories
-
- 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
- B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
-
- 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
- B01J2208/00539—Pressure
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/0061—Controlling the level
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Iron Core Of Rotating Electric Machines (AREA)
- Glass Compositions (AREA)
- Catalysts (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Lock And Its Accessories (AREA)
- Valve-Gear Or Valve Arrangements (AREA)
- Valve Device For Special Equipments (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
SE DESCRIBE UN PROCEDIMIENTO DE HIDROGENACION CATALITICA EN FASE LIQUIDA EN EL QUE SE PONE EN CONTACTO UNA SUSTANCIA ORGANICA, TAL COMO ALDEHIDO QUE TIENE DE 2 A 20 C, CON H, EN PRESENCIA DE UN CATALIZADOR SOLIDO EN CONDICIONES DE HIDROGENACION PARA PRODUCIR UN PRODUCTO DE HIDROGENACION TAL COMO EL ALCOHOL CORRESPONDIENTE CON 2 A 20 C. LA ALIMENTACION DE LA SUSTANCIA ORGANICA SE MEZCLA CON UN DILUYENTE INERTE Y SE DIRIGE EN COCORRIENTE CON UN GAS QUE CONTIENE EL H A LA ZONA DE HIDROGENACION DONDE ESTA EL LECHO DE PARTICULAS DE CATALIZADOR EN CONDICIONES ADECUADAS DE TEMPERATURA Y PRESION. SE HACEN PRECISIONES SOBRE VELOCIDADES DE FLUJO Y CIRCUNSTANCIAS DEL MISMO. EL GAS DEBE TENER ENTRE 1.0 Y 1.5 VECES APROXIMADAMENTE LA CANTIDAD DE H ESTEQUIOMETRICA, TEORICAMENTE NECESARIA, PARA CONVERTIR LA SUSTANCIA ORGANICA DE PARTIDA EN EL PRODUCTO HIDROGENADO.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB878728156A GB8728156D0 (en) | 1987-12-02 | 1987-12-02 | Process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2032023T3 true ES2032023T3 (es) | 1993-01-01 |
Family
ID=10627851
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES198888311188T Expired - Lifetime ES2032023T3 (es) | 1987-12-02 | 1988-11-25 | Procedimiento de hidrogenacion. |
Country Status (15)
| Country | Link |
|---|---|
| US (1) | US5093535A (es) |
| EP (2) | EP0319208B1 (es) |
| JP (1) | JP2675171B2 (es) |
| KR (1) | KR960004878B1 (es) |
| CN (1) | CN1024535C (es) |
| AT (1) | ATE74898T1 (es) |
| AU (1) | AU2725688A (es) |
| CA (1) | CA1328117C (es) |
| DE (1) | DE3870171D1 (es) |
| ES (1) | ES2032023T3 (es) |
| GB (1) | GB8728156D0 (es) |
| IN (1) | IN172818B (es) |
| MX (1) | MX170124B (es) |
| WO (1) | WO1989005286A1 (es) |
| ZA (1) | ZA889062B (es) |
Families Citing this family (77)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB8917862D0 (en) * | 1989-08-04 | 1989-09-20 | Davy Mckee London | Process |
| US5360920A (en) * | 1992-08-07 | 1994-11-01 | The Procter & Gamble Company | Hydrogenation in a plate heat exchanger |
| WO1994006738A1 (en) * | 1992-09-14 | 1994-03-31 | Unichema Chemie B.V. | Process for the production of alcohols |
| JP2526404B2 (ja) * | 1993-10-15 | 1996-08-21 | 工業技術院長 | 触媒反応方法 |
| US5744655A (en) * | 1996-06-19 | 1998-04-28 | The Dow Chemical Company | Process to make 2,3-dihalopropanols |
| US5877358A (en) * | 1996-09-23 | 1999-03-02 | Exxon Chemical Patents Inc. | Alcohol hydrogenation with intermediate recycle |
| DE19641707A1 (de) | 1996-10-10 | 1998-04-16 | Basf Ag | Verfahren zur Herstellung von 1,4-Butandiol durch katalytische Hydrierung von 1,4-Butindiol |
| DE19844325A1 (de) * | 1998-09-28 | 2000-03-30 | Degussa | Verfahren zur Herstellung von Alkoholen durch katalytische Hydrierung von Aldehyden oder Ketonen |
| FR2789683B1 (fr) | 1999-02-17 | 2002-02-15 | Roquette Freres | Procede continu de preparation d'un ose hydrogene de haute purete par hydrogenation catalytique |
| DE19933348B4 (de) * | 1999-07-16 | 2005-11-17 | Oxeno Olefinchemie Gmbh | Verfahren zur Reduzierung oxidischer Hydrierkontakte |
| US6716339B2 (en) | 2001-03-30 | 2004-04-06 | Corning Incorporated | Hydrotreating process with monolithic catalyst |
| US6632414B2 (en) * | 2001-03-30 | 2003-10-14 | Corning Incorporated | Mini-structured catalyst beds for three-phase chemical processing |
| CN1558927A (zh) * | 2001-09-25 | 2004-12-29 | ����ɭ���ڻ�ѧר����˾ | 增塑聚氯乙烯 |
| US7279018B2 (en) * | 2002-09-06 | 2007-10-09 | Fortum Oyj | Fuel composition for a diesel engine |
| EP1566372B1 (en) * | 2002-11-27 | 2018-01-10 | New Japan Chemical Co., Ltd. | Method of hydrogenation reaction |
| EP1670883A1 (en) * | 2003-09-13 | 2006-06-21 | ExxonMobil Chemical Patents Inc. | Lubricating compositions for automotive gears |
| US7473811B2 (en) * | 2003-11-13 | 2009-01-06 | Neste Oil Oyj | Process for the hydrogenation of olefins |
| US7422904B2 (en) * | 2005-02-04 | 2008-09-09 | Exxonmobil Chemical Patents Inc. | Method of operating a fixed bed reactor under predetermined hydraulic conditions |
| US8022258B2 (en) | 2005-07-05 | 2011-09-20 | Neste Oil Oyj | Process for the manufacture of diesel range hydrocarbons |
| US12203035B2 (en) | 2005-07-05 | 2025-01-21 | Neste Oyj | Process for the manufacture of diesel range hydrocarbons |
| DE102005042185A1 (de) | 2005-09-06 | 2007-03-08 | Basf Ag | Verfahren zur Abtrennung von polymeren Nebenprodukten aus 1,4-Butindiol |
| DE102005042184A1 (de) | 2005-09-06 | 2007-03-08 | Basf Ag | Verfahren zur Abtrennung von polymeren Nebenprodukten aus 1,4-Butindiol |
| US7649099B2 (en) * | 2006-01-26 | 2010-01-19 | Battelle Memorial Institute | Method of forming a dianhydrosugar alcohol |
| US7772412B2 (en) * | 2006-01-26 | 2010-08-10 | Battelle Memorial Institute | Methods for dehydration of sugars and sugar alcohols |
| US7728156B2 (en) * | 2006-01-26 | 2010-06-01 | Battelle Memorial Institute | Method of performing sugar dehydration and catalyst treatment |
| US7615652B2 (en) * | 2006-01-26 | 2009-11-10 | Battelle Memorial Institute | Two-stage dehydration of sugars |
| ES2336852T3 (es) * | 2006-07-25 | 2010-04-16 | Basf Se | Procedimiento para el reprocesamiento de descargas de hidrogenacion que contienen disolventes. |
| US7759531B2 (en) | 2007-02-15 | 2010-07-20 | Basf Aktiengesellschaft | Process for preparing 1,4-butanediol |
| DE102007011483A1 (de) * | 2007-03-07 | 2008-09-18 | Evonik Degussa Gmbh | Verfahren zur Herstellung von 3-Aminomethyl-3,5,5-trimethylcyclohexylamin |
| WO2009009322A1 (en) * | 2007-07-06 | 2009-01-15 | Best Energies, Inc. | Integrated facility for producing alcohol using homoacidogenic fermentation |
| US7811447B2 (en) * | 2007-08-01 | 2010-10-12 | Uop Llc | Method of transferring particles from one pressure zone to another pressure zone |
| US8003834B2 (en) * | 2007-09-20 | 2011-08-23 | Uop Llc | Integrated process for oil extraction and production of diesel fuel from biorenewable feedstocks |
| US8575409B2 (en) | 2007-12-20 | 2013-11-05 | Syntroleum Corporation | Method for the removal of phosphorus |
| US20090300971A1 (en) | 2008-06-04 | 2009-12-10 | Ramin Abhari | Biorenewable naphtha |
| US8581013B2 (en) | 2008-06-04 | 2013-11-12 | Syntroleum Corporation | Biorenewable naphtha composition and methods of making same |
| US7982079B2 (en) * | 2008-09-11 | 2011-07-19 | Uop Llc | Integrated process for production of diesel fuel from renewable feedstocks and ethanol denaturizing |
| US8231804B2 (en) | 2008-12-10 | 2012-07-31 | Syntroleum Corporation | Even carbon number paraffin composition and method of manufacturing same |
| CN101787305B (zh) * | 2009-01-23 | 2013-03-20 | 中国石油化工股份有限公司 | 一种液相循环加氢处理方法和反应系统 |
| CN102803189B (zh) | 2010-03-15 | 2016-01-20 | 埃克森美孚化学专利公司 | 用于生产醇的方法 |
| US8394900B2 (en) | 2010-03-18 | 2013-03-12 | Syntroleum Corporation | Profitable method for carbon capture and storage |
| EP2489720A1 (en) | 2011-02-15 | 2012-08-22 | Neste Oil Oyj | Renewable oil with low iron content and its use in hydrotreatment process |
| NL2008611C2 (nl) * | 2012-04-05 | 2013-10-09 | Mooij Agro B V | Inrichting voor het aan een gasstroom onderwerpen van producten, bijvoorbeeld ten behoeve van een droog- of vries-procédé. |
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| EP2757088B1 (de) * | 2013-01-22 | 2016-08-03 | Covestro Deutschland AG | Verfahren zur Herstellung von aromatischen Aminen |
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| US9328303B2 (en) | 2013-03-13 | 2016-05-03 | Reg Synthetic Fuels, Llc | Reducing pressure drop buildup in bio-oil hydroprocessing reactors |
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| CN103566837B (zh) * | 2013-11-13 | 2015-09-30 | 山西大学 | 一种适用于加氢放热反应的外循环反应装置 |
| US9758452B2 (en) * | 2014-02-07 | 2017-09-12 | The Chemours Company Fc, Llc | Integrated process for the production of Z-1,1,1,4,4,4-hexafluoro-2-butene |
| US20160368842A1 (en) * | 2014-02-25 | 2016-12-22 | Biochemtex S.P.A. | Continuous process for producing an ethylene glycol stream |
| KR101612099B1 (ko) * | 2014-06-25 | 2016-04-14 | (주)테크윈 | 전기분해장치 |
| KR101600037B1 (ko) * | 2014-06-26 | 2016-03-07 | (주)테크윈 | 선박평형수 처리시스템 |
| DE102014223427A1 (de) | 2014-11-17 | 2016-05-19 | Hydrogenious Technologies Gmbh | Verfahren und Anlage zum Erzeugen und Speichern von Wasserstoff |
| CN104492445A (zh) * | 2014-12-18 | 2015-04-08 | 复旦大学 | 一种用于草酸二甲酯气相催化加氢合成乙二醇及乙醇酸甲酯的催化剂及其制备方法 |
| MX369759B (es) | 2015-01-19 | 2019-11-20 | Evonik Operations Gmbh | Preparación combinada de buteno y octeno a partir de eteno. |
| MY194991A (en) | 2015-06-30 | 2022-12-29 | Takeda Pharmaceuticals Co | Method for producing pyrrole compound |
| PL3374340T3 (pl) | 2015-11-10 | 2022-04-11 | Dow Technology Investments Llc | Sposób wytwarzania aldehydów |
| ES2901236T3 (es) | 2016-02-11 | 2022-03-21 | Dow Technology Investments Llc | Procesos para convertir olefinas en alcoholes, éteres o combinaciones de los mismos |
| US11111228B2 (en) * | 2016-06-23 | 2021-09-07 | Natco Pharma Limited | Process for the preparation of pomalidomide and its purification |
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| US11207652B2 (en) * | 2017-07-28 | 2021-12-28 | Basf Se | Device and method for catalytically converting chemical substances at dwell times in the range of 0.1-10 seconds |
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| CN109225073B (zh) * | 2018-09-17 | 2021-01-15 | 清华大学 | 一种微填充床内加氢反应装置及其进行加氢反应的方法 |
| CN111099965B (zh) * | 2018-10-25 | 2024-03-12 | 中国石油化工股份有限公司 | 一种1,5-戊二醇的液相加氢精制方法 |
| CN109908843B (zh) * | 2019-04-23 | 2019-12-31 | 宁波巨化新材料有限公司 | 丙醛加氢反应器 |
| CN112920015B (zh) * | 2019-12-06 | 2025-02-21 | 陶氏技术投资有限责任公司 | 用于精炼由醛的氢化衍生的醇的方法 |
| KR102322998B1 (ko) * | 2019-12-19 | 2021-11-10 | 한국과학기술연구원 | 액상유기수소운반체를 이용한 고순도 수소 정제/저장 장치 및 수소 정제/저장 방법 |
| US11976017B2 (en) | 2019-12-19 | 2024-05-07 | Dow Technology Investments Llc | Processes for preparing isoprene and mono-olefins comprising at least six carbon atoms |
| ES3054301T3 (en) * | 2020-09-24 | 2026-02-02 | T En Process Tech Inc | Continuous processes for the selective conversion of aldohexose-yielding carbohydrate to ethylene glycol using low concentrations of retro-aldol catalyst |
| US11319269B2 (en) | 2020-09-24 | 2022-05-03 | Iowa Corn Promotion Board | Continuous processes for the selective conversion of aldohexose-yielding carbohydrate to ethylene glycol using low concentrations of retro-aldol catalyst |
| US11884614B2 (en) | 2022-05-26 | 2024-01-30 | Chevron Phillips Chemical Company Lp | Normal alpha olefin synthesis using decarbonylative olefination |
| WO2024026285A1 (en) | 2022-07-27 | 2024-02-01 | Chevron Phillips Chemical Company Lp | SYNTHESIS OF n-HEPTANE FROM OLEFINS AND RELATED PRODUCTION SYSTEMS |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1002372A (en) * | 1961-04-25 | 1965-08-25 | Chisso Corp | Process for continuously hydrogenating higher aldehydes in liquid phase |
| BE754868A (fr) * | 1969-08-16 | 1971-02-15 | Basf Ag | Procede pour la mise en oeuvre de reactions exothermiques entreun gaz et un liquide |
| DE2040501C3 (de) * | 1970-08-14 | 1984-01-05 | Basf Ag, 6700 Ludwigshafen | Verfahren zur Durchführung von exothermen Reaktionen zwischen einem Gas und einer Flüssigkeit |
| DE2257673B1 (de) * | 1972-11-24 | 1974-03-28 | Verfahren zur herstellung von aliphatischen alkoholen | |
| JPS5812053A (ja) * | 1981-07-15 | 1983-01-24 | Nec Corp | 情報処理装置 |
| US4451677A (en) * | 1981-08-20 | 1984-05-29 | Davy Mckee (London) Limited | Multistage aldehyde hydrogenation |
| US4510092A (en) * | 1982-03-19 | 1985-04-09 | Uop Inc. | Continuous reduction of edible oils |
| US4626604A (en) * | 1985-09-11 | 1986-12-02 | Davy Mckee (London) Limited | Hydrogenation process |
| GB8613354D0 (en) * | 1986-06-03 | 1986-07-09 | Davy Mckee Ltd | Process |
| GB8702654D0 (en) * | 1987-02-06 | 1987-03-11 | Davy Mckee Ltd | Process |
-
1987
- 1987-12-02 GB GB878728156A patent/GB8728156D0/en active Pending
-
1988
- 1988-11-25 JP JP1505574A patent/JP2675171B2/ja not_active Expired - Fee Related
- 1988-11-25 US US07/476,453 patent/US5093535A/en not_active Expired - Lifetime
- 1988-11-25 DE DE8888311188T patent/DE3870171D1/de not_active Expired - Lifetime
- 1988-11-25 KR KR1019890701448A patent/KR960004878B1/ko not_active Expired - Lifetime
- 1988-11-25 EP EP88311188A patent/EP0319208B1/en not_active Expired - Lifetime
- 1988-11-25 ES ES198888311188T patent/ES2032023T3/es not_active Expired - Lifetime
- 1988-11-25 WO PCT/GB1988/001027 patent/WO1989005286A1/en not_active Ceased
- 1988-11-25 AU AU27256/88A patent/AU2725688A/en not_active Abandoned
- 1988-11-25 AT AT88311188T patent/ATE74898T1/de not_active IP Right Cessation
- 1988-11-25 EP EP88910086A patent/EP0393093A1/en active Pending
- 1988-11-30 MX MX013998A patent/MX170124B/es unknown
- 1988-11-30 IN IN853MA1988 patent/IN172818B/en unknown
- 1988-12-01 CA CA000584688A patent/CA1328117C/en not_active Expired - Fee Related
- 1988-12-02 CN CN88108327A patent/CN1024535C/zh not_active Expired - Lifetime
- 1988-12-02 ZA ZA889062A patent/ZA889062B/xx unknown
Also Published As
| Publication number | Publication date |
|---|---|
| EP0319208A1 (en) | 1989-06-07 |
| DE3870171D1 (de) | 1992-05-21 |
| CN1033377A (zh) | 1989-06-14 |
| ZA889062B (en) | 1989-08-30 |
| IN172818B (es) | 1993-12-04 |
| EP0393093A1 (en) | 1990-10-24 |
| CN1024535C (zh) | 1994-05-18 |
| MX170124B (es) | 1993-08-09 |
| WO1989005286A1 (en) | 1989-06-15 |
| GB8728156D0 (en) | 1988-01-06 |
| JP2675171B2 (ja) | 1997-11-12 |
| EP0319208B1 (en) | 1992-04-15 |
| US5093535A (en) | 1992-03-03 |
| ATE74898T1 (de) | 1992-05-15 |
| JPH03501483A (ja) | 1991-04-04 |
| KR900700422A (ko) | 1990-08-13 |
| KR960004878B1 (ko) | 1996-04-16 |
| CA1328117C (en) | 1994-03-29 |
| AU2725688A (en) | 1989-07-05 |
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