AR024268A1 - Procedimiento para realizar cataliticamente reacciones multifase, en particular, hidroformilaciones - Google Patents
Procedimiento para realizar cataliticamente reacciones multifase, en particular, hidroformilacionesInfo
- Publication number
- AR024268A1 AR024268A1 ARP000102744A ARP000102744A AR024268A1 AR 024268 A1 AR024268 A1 AR 024268A1 AR P000102744 A ARP000102744 A AR P000102744A AR P000102744 A ARP000102744 A AR P000102744A AR 024268 A1 AR024268 A1 AR 024268A1
- Authority
- AR
- Argentina
- Prior art keywords
- procedure
- hydroformilations
- catalitically
- multiphase reactions
- performing multiphase
- Prior art date
Links
Classifications
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/49—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
- C07C45/50—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
-
- 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
- B01J19/2415—Tubular reactors
- B01J19/2435—Loop-type 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
- B01J19/26—Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles
-
- 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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
-
- 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
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
-
- 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
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00283—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
-
- 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
- B01J2219/00002—Chemical plants
- B01J2219/00027—Process aspects
- B01J2219/00033—Continuous 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
- 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
- B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger 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
- 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
- B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
- B01J2219/0011—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
-
- 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
- B01J2219/18—Details relating to the spatial orientation of the reactor
- B01J2219/185—Details relating to the spatial orientation of the reactor vertical
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)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Un procedimiento catalítico para llevar a acabo reacciones multifases en un reactor tubular, en donde el catalizador se encuentra en la fase continua y porlo menos un material de partida se encuentra en la fase dispersa, siendo el factor de carga Bd el reactor tubular igual o mayor que 0,8. El procedimiento esparticularmente adecuado para la hidroformilacion de olefinas. Los aldehidos así preparados pueden usarse en la preparacion de alcoholes, ácidos carboxílicos oen condensaciones deadoles.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19925384A DE19925384A1 (de) | 1999-06-02 | 1999-06-02 | Verfahren zur katalytischen Durchführung von Mehrphasenreaktionen, insbesondere Hydroformylierungen |
Publications (1)
Publication Number | Publication Date |
---|---|
AR024268A1 true AR024268A1 (es) | 2002-09-25 |
Family
ID=7910094
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP000102744A AR024268A1 (es) | 1999-06-02 | 2000-06-02 | Procedimiento para realizar cataliticamente reacciones multifase, en particular, hidroformilaciones |
Country Status (20)
Country | Link |
---|---|
US (1) | US6492564B1 (es) |
EP (1) | EP1057524B1 (es) |
JP (1) | JP2001026566A (es) |
KR (1) | KR100648847B1 (es) |
CN (1) | CN1229318C (es) |
AR (1) | AR024268A1 (es) |
AT (1) | ATE387954T1 (es) |
BR (1) | BR0002178B1 (es) |
CA (1) | CA2310516C (es) |
DE (2) | DE19925384A1 (es) |
ES (1) | ES2301458T3 (es) |
ID (1) | ID26185A (es) |
MX (1) | MXPA00001215A (es) |
MY (1) | MY125133A (es) |
PL (1) | PL199506B1 (es) |
RO (1) | RO121180B1 (es) |
RU (1) | RU2266894C2 (es) |
SG (1) | SG86401A1 (es) |
TW (1) | TW537930B (es) |
ZA (1) | ZA200002740B (es) |
Families Citing this family (75)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19925385A1 (de) * | 1999-06-02 | 2000-12-07 | Oxeno Olefinchemie Gmbh | Verfahren zur katalytischen Durchführung von Mehrphasenreaktionen, insbesondere Vinylierungen von Carbonsäuren |
DE19957528A1 (de) * | 1999-11-30 | 2001-05-31 | Oxeno Olefinchemie Gmbh | Verfahren zur Hydroformylierung von Olefinen |
DE19957522A1 (de) * | 1999-11-30 | 2001-05-31 | Oxeno Olefinchemie Gmbh | Verfahren zur katalytischen Durchführung von Aldolkondensationen mittels Mehrphasenreaktion |
US6922411B1 (en) * | 2000-09-29 | 2005-07-26 | Voxeo Corporation | Networked computer telephony system driven by web-based applications |
DE10058383A1 (de) | 2000-11-24 | 2002-05-29 | Oxeno Olefinchemie Gmbh | Neue Phosphininverbindungen und deren Metallkomplexe |
CA2431524A1 (en) * | 2000-12-15 | 2002-06-20 | Hobolth Instruments Aps | Method and apparatus for continuous processing of organic material |
DE10106186A1 (de) | 2001-02-10 | 2002-08-14 | Oxeno Olefinchemie Gmbh | Verfahren zur Kondensation von Aldehyden mit Ketonen mittels Mehrphasenreaktion |
DE10106482A1 (de) * | 2001-02-13 | 2002-08-14 | Basf Ag | Hydroformylierung |
WO2003029180A1 (de) * | 2001-09-26 | 2003-04-10 | Oxeno Olefinchemie Gmbh | Phthalsäurealkylestergemische mit kontrollierter viskosität |
DE10149348A1 (de) | 2001-10-06 | 2003-04-10 | Oxeno Olefinchemie Gmbh | Verfahren zur Herstellung von 1-Olefin mit Palladiumcarbenverbindungen |
US8853266B2 (en) * | 2001-12-06 | 2014-10-07 | University Of Tennessee Research Foundation | Selective androgen receptor modulators for treating diabetes |
DE10210918B4 (de) | 2002-03-13 | 2004-06-03 | Oxeno Olefinchemie Gmbh | Verfahren zur Herstellung von Bisphosphiten |
FR2838431B1 (fr) | 2002-04-11 | 2005-05-06 | Inst Francais Du Petrole | Procede d'hydroformylation mettant en oeuvre un catalyseur a base de cobalt dans un liquide ionique non-aqueux avec un recyclage du catalyseur ameliore |
DE10220801A1 (de) * | 2002-05-10 | 2003-11-20 | Oxeno Olefinchemie Gmbh | Verfahren zur Rhodium-katalysierten Hydroformylierung von Olefinen unter Reduzierung der Rhodiumverluste |
DE10223593A1 (de) * | 2002-05-27 | 2003-12-11 | Degussa | Hydroxydiphosphine und deren Verwendung in der Katalyse |
DE10225565A1 (de) | 2002-06-10 | 2003-12-18 | Oxeno Olefinchemie Gmbh | Katalysator und Verfahren zur Hydrierung von aromatischen Verbindungen |
CA2506258A1 (en) | 2002-08-31 | 2004-03-25 | Oxeno Olefinchemie Gmbh | Process for preparing aldehydes by hydroformylation of olefinically unsaturated compounds, catalyzed by unmodified complexes of metals of groups 8 to 10 of the pte in the presenceof cyclic carbonic esters |
RU2337090C2 (ru) | 2002-08-31 | 2008-10-27 | Оксено Олефинхеми Гмбх | Способ гидроформилирования олефиновых соединений в присутствии циклических эфиров угольной кислоты |
DE10257499A1 (de) | 2002-12-10 | 2004-07-01 | Oxeno Olefinchemie Gmbh | Verfahren zur Herstellung von 1-Olefinen durch katalytische Spaltung von 1-Alkoxyalkanen |
WO2004099112A1 (ja) * | 2003-05-07 | 2004-11-18 | Mitsubishi Chemical Corporation | アルデヒドの製造方法 |
DE10329042A1 (de) * | 2003-06-27 | 2005-01-13 | Oxeno Olefinchemie Gmbh | Verfahren zur Herstellung von 1-Octen aus Crack-C4 |
DE10359628A1 (de) * | 2003-12-18 | 2005-07-21 | Oxeno Olefinchemie Gmbh | Katalysator und Verfahren zur Herstellung von 1-Olefinen aus 2-Hydroxyalkanen |
DE10360772A1 (de) * | 2003-12-23 | 2005-07-28 | Oxeno Olefinchemie Gmbh | Verfahren zur Herstellung von Organoacylphosphiten |
DE10360771A1 (de) * | 2003-12-23 | 2005-07-28 | Oxeno Olefinchemie Gmbh | Verfahren zur Herstellung von dreiwertigen Organophosphor-Verbindungen |
DE102004033410A1 (de) * | 2004-02-14 | 2005-09-01 | Oxeno Olefinchemie Gmbh | Verfahren zur Herstellung von Olefinen mit 8 bis 12 Kohlenstoffatomen |
DE102004011081A1 (de) * | 2004-03-06 | 2005-09-22 | Oxeno Olefinchemie Gmbh | Verfahren zur Herstellung von tertiären Carbonsäuren |
DE102004013514A1 (de) * | 2004-03-19 | 2005-10-06 | Oxeno Olefinchemie Gmbh | Verfahren zur Hydroformylierung von Olefinen in Anwesenheit von neuen phosphororganischen Verbindungen |
DE102004021128A1 (de) * | 2004-04-29 | 2005-11-24 | Oxeno Olefinchemie Gmbh | Vorrichtung und Verfahren für die kontinuierliche Umsetzung einer Flüssigkeit mit einem Gas an einem festen Katalysator |
FR2874335B1 (fr) * | 2004-08-19 | 2006-11-24 | Petroval Sa | Procede de remplissage d'une enceinte avec un lit de particules a densite variable |
DE102005036039A1 (de) | 2004-08-28 | 2006-03-02 | Oxeno Olefinchemie Gmbh | Verfahren zur Herstellung von 2,7-Octadienylderivaten |
DE102004063673A1 (de) * | 2004-12-31 | 2006-07-13 | Oxeno Olefinchemie Gmbh | Verfahren zur kontinuierlichen katalytischen Hydrierung von hydrierbaren Verbindungen an festen, im Festbett angeordneten Katalysatoren mit einem wasserstoffhaltigen Gas |
US7422904B2 (en) * | 2005-02-04 | 2008-09-09 | Exxonmobil Chemical Patents Inc. | Method of operating a fixed bed reactor under predetermined hydraulic conditions |
DE102005014055A1 (de) * | 2005-03-23 | 2006-09-28 | Degussa Ag | Unsymmetrisch substituierte Phospholankatalysatoren |
US7649112B2 (en) | 2005-07-25 | 2010-01-19 | Saudi Basic Industries Corporation | Integrated plant for producing 2-ethyl-hexanol and methacrylic acid and a method based thereon |
DE102005035816A1 (de) * | 2005-07-30 | 2007-02-01 | Oxeno Olefinchemie Gmbh | Verfahren zur Hydrierung von Oxo-Aldehyden mit hohen Estergehalten |
DE102005042464A1 (de) * | 2005-09-07 | 2007-03-08 | Oxeno Olefinchemie Gmbh | Carbonylierungsverfahren unter Zusatz von sterisch gehinderten sekundären Aminen |
DE102005055866A1 (de) * | 2005-11-23 | 2007-05-24 | Hte Ag The High Throughput Experimentation Company | Verfahren zur Herstellung von Aryl-Aryl gekoppelter Verbindungen |
BRPI0718007B1 (pt) * | 2006-11-09 | 2017-10-24 | Mitsubishi Chemical Corporation | Method of co-production of normal butanol and isobutylic village |
DE102008002187A1 (de) | 2008-06-03 | 2009-12-10 | Evonik Oxeno Gmbh | Verfahren zur Herstellung von C5-Aldehydgemischen mit hohem n-Pentanalanteil |
MX2011005525A (es) | 2008-11-26 | 2011-06-06 | Elevance Renewable Sciences | Metodos para producir turbosina a partir de cargas de alimentacion de aceite natural a traves de reacciones de division por oxigeno. |
DK2352712T3 (en) | 2008-11-26 | 2018-09-10 | Elevance Renewable Sciences | PROCEDURES FOR PREPARING JET FUEL FROM NATURAL OIL MATERIALS THROUGH METATES REACTIONS |
CN101768059A (zh) * | 2008-12-19 | 2010-07-07 | 四川省达科特能源科技有限公司 | 采用静态混合反应器连续进行单烯烃氢甲酰化的方法 |
CN101768062B (zh) * | 2009-01-05 | 2013-11-06 | 四川省达科特能源科技有限公司 | 由催化干气提浓气同时制备丙醛和丁醛的工业方法 |
AU2010307021B2 (en) | 2009-10-12 | 2016-02-18 | Wilmar Trading Pte Ltd | Methods of refining and producing fuel from natural oil feedstocks |
US9051519B2 (en) | 2009-10-12 | 2015-06-09 | Elevance Renewable Sciences, Inc. | Diene-selective hydrogenation of metathesis derived olefins and unsaturated esters |
US9382502B2 (en) | 2009-10-12 | 2016-07-05 | Elevance Renewable Sciences, Inc. | Methods of refining and producing isomerized fatty acid esters and fatty acids from natural oil feedstocks |
US9175231B2 (en) | 2009-10-12 | 2015-11-03 | Elevance Renewable Sciences, Inc. | Methods of refining natural oils and methods of producing fuel compositions |
US9000246B2 (en) | 2009-10-12 | 2015-04-07 | Elevance Renewable Sciences, Inc. | Methods of refining and producing dibasic esters and acids from natural oil feedstocks |
US8735640B2 (en) | 2009-10-12 | 2014-05-27 | Elevance Renewable Sciences, Inc. | Methods of refining and producing fuel and specialty chemicals from natural oil feedstocks |
US9169447B2 (en) | 2009-10-12 | 2015-10-27 | Elevance Renewable Sciences, Inc. | Methods of refining natural oils, and methods of producing fuel compositions |
US9222056B2 (en) | 2009-10-12 | 2015-12-29 | Elevance Renewable Sciences, Inc. | Methods of refining natural oils, and methods of producing fuel compositions |
US9365487B2 (en) | 2009-10-12 | 2016-06-14 | Elevance Renewable Sciences, Inc. | Methods of refining and producing dibasic esters and acids from natural oil feedstocks |
CN102826970B (zh) * | 2011-06-17 | 2015-08-19 | 中国石油化工股份有限公司 | 一种低碳烯烃氢甲酰化二段反应方法和装置 |
US9169174B2 (en) | 2011-12-22 | 2015-10-27 | Elevance Renewable Sciences, Inc. | Methods for suppressing isomerization of olefin metathesis products |
US9139493B2 (en) | 2011-12-22 | 2015-09-22 | Elevance Renewable Sciences, Inc. | Methods for suppressing isomerization of olefin metathesis products |
US9133416B2 (en) | 2011-12-22 | 2015-09-15 | Elevance Renewable Sciences, Inc. | Methods for suppressing isomerization of olefin metathesis products |
US9388098B2 (en) | 2012-10-09 | 2016-07-12 | Elevance Renewable Sciences, Inc. | Methods of making high-weight esters, acids, and derivatives thereof |
SG11201807000XA (en) | 2016-03-14 | 2018-09-27 | Bosch Gmbh Robert | Portable keypanel for intercom system |
CN106422994B (zh) * | 2016-10-21 | 2022-10-18 | 北京沃特尔水技术股份有限公司 | 一种制备碳铵类汲取液的方法及设备 |
CN106748943B (zh) * | 2016-12-30 | 2018-03-02 | 厦门金达威维生素有限公司 | 一种维生素a中间体双格氏缩合物的连续水解中和的方法及装置 |
CN109882148B (zh) * | 2017-12-01 | 2021-11-02 | 中国石油天然气股份有限公司 | 一种在线分流酸化施工实时监测方法 |
CN110526807B (zh) * | 2018-05-25 | 2021-04-23 | 上海载正化工科技发展有限公司 | 一种氢甲酰化反应制备醛的连续反应装置和方法 |
EP3976736A4 (en) | 2019-05-24 | 2023-04-12 | Eastman Chemical Company | THERMAL PYROLYTIC OIL TO A GAS-FED CRACKER FURNACE |
EP3976732A4 (en) | 2019-05-24 | 2023-05-17 | Eastman Chemical Company | MIXING SMALL QUANTITIES OF PYROLYTIC OIL INTO A LIQUID STREAM WHICH IS PROCESSED INTO A GAS CRACKER |
US11365357B2 (en) | 2019-05-24 | 2022-06-21 | Eastman Chemical Company | Cracking C8+ fraction of pyoil |
US12031091B2 (en) | 2019-05-24 | 2024-07-09 | Eastman Chemical Company | Recycle content cracked effluent |
US11319262B2 (en) | 2019-10-31 | 2022-05-03 | Eastman Chemical Company | Processes and systems for making recycle content hydrocarbons |
WO2021087032A1 (en) | 2019-10-31 | 2021-05-06 | Eastman Chemical Company | Processes and systems for formation of recycle-content hydrocarbon compositions |
KR20220091569A (ko) | 2019-10-31 | 2022-06-30 | 이스트만 케미칼 컴파니 | 재활용물 탄화수소 조성물의 생성을 위한 방법 및 시스템 |
US11945998B2 (en) | 2019-10-31 | 2024-04-02 | Eastman Chemical Company | Processes and systems for making recycle content hydrocarbons |
WO2021092306A1 (en) | 2019-11-07 | 2021-05-14 | Eastman Chemical Company | Recycle content alpha olefins and fatty alcohols |
EP4055001A4 (en) | 2019-11-07 | 2024-02-14 | Eastman Chemical Company | MIXED ESTERS AND SOLVENTS WITH RECYCLED CONTENTS |
US12195674B2 (en) | 2021-09-21 | 2025-01-14 | Eastman Chemical Company | Using spent caustic solution from pygas treatment to neutralize halogens from liquified waste plastic |
CN113856565A (zh) * | 2021-10-14 | 2021-12-31 | 沈阳化工研究院有限公司 | 一种连续催化加氢制备对三氟甲氧基苯胺的装置及方法 |
CN115155461A (zh) * | 2022-07-12 | 2022-10-11 | 铜陵贝斯美科技有限公司 | 一种二烯烃等温加氢制备单烯烃的装置及工艺 |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB938831A (en) * | 1958-10-04 | 1963-10-09 | Hoechst Ag | Process for the manufacture of aldehydes, ketones and/or acids from unsaturated compounds |
GB938836A (en) * | 1959-01-07 | 1963-10-09 | Hoechst Ag | Process for the manufacture of carbonyl compounds |
DE2538037C3 (de) * | 1975-08-27 | 1988-11-10 | Hüls AG, 4370 Marl | Verfahren zur Hydroformylierung von Olefinen |
CA1090823A (en) * | 1976-04-08 | 1980-12-02 | Everard A.V. Brewester | Cyclic hydroformylation process |
DE3234701A1 (de) * | 1982-09-18 | 1984-04-05 | Ruhrchemie Ag, 4200 Oberhausen | Verfahren zur herstellung von aldehyden |
DE3341035A1 (de) * | 1983-11-12 | 1985-05-23 | Ruhrchemie Ag, 4200 Oberhausen | Verfahren zur herstellung von aldehyden |
DE19842371A1 (de) * | 1998-09-16 | 2000-03-23 | Oxeno Oelfinchemie Gmbh | Verfahren zur Herstellung von höheren Oxo-Alkoholen aus Olefingemischen |
-
1999
- 1999-06-02 DE DE19925384A patent/DE19925384A1/de not_active Withdrawn
-
2000
- 2000-02-03 MX MXPA00001215A patent/MXPA00001215A/es active IP Right Grant
- 2000-04-13 AT AT00108156T patent/ATE387954T1/de not_active IP Right Cessation
- 2000-04-13 EP EP00108156A patent/EP1057524B1/de not_active Expired - Lifetime
- 2000-04-13 ES ES00108156T patent/ES2301458T3/es not_active Expired - Lifetime
- 2000-04-13 DE DE50015005T patent/DE50015005D1/de not_active Expired - Lifetime
- 2000-04-24 TW TW089107681A patent/TW537930B/zh not_active IP Right Cessation
- 2000-05-29 PL PL340362A patent/PL199506B1/pl unknown
- 2000-05-30 JP JP2000160516A patent/JP2001026566A/ja active Pending
- 2000-05-31 CA CA2310516A patent/CA2310516C/en not_active Expired - Fee Related
- 2000-05-31 BR BRPI0002178-4A patent/BR0002178B1/pt not_active IP Right Cessation
- 2000-05-31 SG SG200002945A patent/SG86401A1/en unknown
- 2000-06-01 CN CNB001087991A patent/CN1229318C/zh not_active Expired - Fee Related
- 2000-06-01 RO ROA200000568A patent/RO121180B1/ro unknown
- 2000-06-01 MY MYPI20002461A patent/MY125133A/en unknown
- 2000-06-01 RU RU2000113882/04A patent/RU2266894C2/ru not_active IP Right Cessation
- 2000-06-01 ZA ZA200002740A patent/ZA200002740B/xx unknown
- 2000-06-01 KR KR1020000029965A patent/KR100648847B1/ko not_active IP Right Cessation
- 2000-06-02 AR ARP000102744A patent/AR024268A1/es not_active Application Discontinuation
- 2000-06-02 US US09/585,425 patent/US6492564B1/en not_active Expired - Lifetime
- 2000-06-02 ID IDP20000468D patent/ID26185A/id unknown
Also Published As
Publication number | Publication date |
---|---|
PL199506B1 (pl) | 2008-09-30 |
MY125133A (en) | 2006-07-31 |
CA2310516A1 (en) | 2000-12-02 |
CN1276364A (zh) | 2000-12-13 |
BR0002178A (pt) | 2001-01-02 |
JP2001026566A (ja) | 2001-01-30 |
MXPA00001215A (es) | 2002-04-24 |
EP1057524B1 (de) | 2008-03-05 |
RO121180B1 (ro) | 2007-01-30 |
PL340362A1 (en) | 2000-12-04 |
TW537930B (en) | 2003-06-21 |
CN1229318C (zh) | 2005-11-30 |
EP1057524A2 (de) | 2000-12-06 |
ES2301458T3 (es) | 2008-07-01 |
ATE387954T1 (de) | 2008-03-15 |
CA2310516C (en) | 2010-02-09 |
DE50015005D1 (de) | 2008-04-17 |
EP1057524A3 (de) | 2002-04-17 |
US6492564B1 (en) | 2002-12-10 |
ID26185A (id) | 2000-12-07 |
DE19925384A1 (de) | 2000-12-07 |
RU2266894C2 (ru) | 2005-12-27 |
ZA200002740B (en) | 2000-12-11 |
KR100648847B1 (ko) | 2006-11-24 |
SG86401A1 (en) | 2002-02-19 |
KR20010049467A (ko) | 2001-06-15 |
BR0002178B1 (pt) | 2010-10-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AR024268A1 (es) | Procedimiento para realizar cataliticamente reacciones multifase, en particular, hidroformilaciones | |
RU2000113882A (ru) | Способ каталитического осуществления многофазных реакций, в особенности реакций гидроформилирования | |
EP1106596A3 (de) | Verfahren zur katalytischen Durchführung von Aldolkonensationen mittels Mehrphasenreaktion | |
DE69813444D1 (de) | Katalysatorkomponenten und katalysatoren für die polymerisation von olefinen | |
EP1106594A3 (de) | Verfahren zur Hydroformylierung von Olefinen | |
DE69731496D1 (de) | Katalysator für die Herstellung von Dimethylether, Verfahren zur Katalysatorherstellung und Verfahren zur Herstellung von Dimethylether | |
DE69521990D1 (de) | Aus supersäuren hergestellte lewissäure enthaltende trägerkatalysatoren, die für umwandlungsreaktionen von kohlenwasserstoffen verwendbar sind. | |
ATE237622T1 (de) | Katalysatoren für die herstellung von olefinpolymeren | |
DE60036852D1 (de) | Katalysatorkomponenten für die polymerisation von olefinen und daraus erhaltene katalysatoren | |
BR9901568A (pt) | Processos para a preparação de um catalisador e de aldeído não saturado ou ácido carboxílico, e, catalisador. | |
DE59800868D1 (de) | Verfahren zur herstellung von porös geträgerten metall-nanopartikelhaltigen katalysatoren, insbesondere für die gasphasenoxidation von ethylen und essigsäure zu vinylacetat | |
ES2165452T3 (es) | Procedimiento y catalizador para mejorar un hidrocarburo pesado. | |
NL1008843A1 (nl) | Stoomconversieproces en katalysator. | |
DE69823988D1 (de) | Gruppe 8-10 übergangsmetallkatalysator für die polymerisation von olefinen | |
BRPI0408629B1 (pt) | processo para a oxidaÇço parcial de propeno a Ácido acrÍlico em fase gasosa | |
EP1057525A3 (de) | Verfahren zur katalytischen Durchführung von Mehrphasenreaktionen, insbesondere Vinylierungen von Carbonsäuren | |
MX9302991A (es) | Soportes catalizadores, catalizadores soportados, metodos para prepararlos y usarlos. | |
ID22586A (id) | Katalis dehidrogenasi oksidasi alkana rendah dan proses untuk memproduksi olefin | |
DE60130096D1 (de) | Übergangsmetallverbindungen, polymerisationskatalysatoren für olefine, olefinpolymere und verfahren zu deren herstellung | |
ID18044A (id) | Proses untuk pemisahan produk reaksi oksidasi dan katalis oksidasi | |
DE19981705T1 (de) | y-Oxo-Bis-Metallocen-Komplexvrbindungen und Katalysatoren, die dieselben für die Polymerisation von Olefinen verwenden, sowie Polymerisationsverfahren | |
EP1253974B1 (en) | Chemical process | |
DE68907382D1 (de) | Eta-phase-materialien, verfahren zu ihrer herstellung und verwendung als katalysatoren fuer die alkoholsynthese, die kohlenwasserstoffsynthese, die kohlenwasserstoffhydrierung und kohlenwasserstoffkonversionsreaktionen. | |
ES2132978T3 (es) | Procedimiento de alquilacion de varias etapas. | |
Amandi et al. | Heterogeneous reactions in supercritical carbon dioxide |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FA | Abandonment or withdrawal | ||
FB | Suspension of granting procedure |