MX2018002766A - Diluyente de disipacion de calor en reactores de lecho fijo. - Google Patents
Diluyente de disipacion de calor en reactores de lecho fijo.Info
- Publication number
- MX2018002766A MX2018002766A MX2018002766A MX2018002766A MX2018002766A MX 2018002766 A MX2018002766 A MX 2018002766A MX 2018002766 A MX2018002766 A MX 2018002766A MX 2018002766 A MX2018002766 A MX 2018002766A MX 2018002766 A MX2018002766 A MX 2018002766A
- Authority
- MX
- Mexico
- Prior art keywords
- fixed bed
- diluent
- heat dissipating
- bed reactors
- thermal conductivity
- 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
- 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
- B01J8/0242—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 flow within the bed being predominantly vertical
- B01J8/025—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 flow within the bed being predominantly vertical in a cylindrical shaped 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
- 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
- B01J8/0242—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 flow within the bed being predominantly vertical
- B01J8/0257—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 flow within the bed being predominantly vertical in a cylindrical annular shaped 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
- B01J27/057—Selenium or tellurium; Compounds thereof
- B01J27/0576—Tellurium; Compounds thereof
-
- 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
- B01J8/0446—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 flow within the beds being predominantly vertical
- B01J8/0449—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 flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0453—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 flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/76—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
- C07C2/82—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen oxidative coupling
- C07C2/84—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen oxidative coupling catalytic
-
- 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
- C07C5/42—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor
- C07C5/48—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor with oxygen as an acceptor
-
- 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
- B01J2208/00513—Controlling the temperature using inert heat absorbing solids in the bed
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/02—Sulfur, selenium or tellurium; Compounds thereof
- C07C2527/057—Selenium or tellurium; Compounds thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Catalysts (AREA)
Abstract
La presente invención se relaciona con la incorporación en un reactor de lecho fijo de una reacción exotérmica que tiene un catalizador soportado en un soporte que tiene una conductividad térmica típicamente menor de 30 W/mK, dentro de los límites de control de temperatura de reacción de las partículas de disipación de calor que tienen una conductividad térmica de por lo menos 50 W/mK menor de 30 W/mK dentro de los límites de control de la temperatura reacción, ayuda a controlar la temperatura del lecho del reactor.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2904477A CA2904477A1 (en) | 2015-09-14 | 2015-09-14 | Heat dissipating diluent in fixed bed reactors |
PCT/IB2016/055365 WO2017046680A1 (en) | 2015-09-14 | 2016-09-08 | Heat dissipating diluent in fixed bed reactors |
Publications (1)
Publication Number | Publication Date |
---|---|
MX2018002766A true MX2018002766A (es) | 2018-04-13 |
Family
ID=57045236
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX2018002766A MX2018002766A (es) | 2015-09-14 | 2016-09-08 | Diluyente de disipacion de calor en reactores de lecho fijo. |
Country Status (10)
Country | Link |
---|---|
US (2) | US10668441B2 (es) |
EP (1) | EP3349890A1 (es) |
JP (1) | JP6828022B2 (es) |
KR (1) | KR102666333B1 (es) |
CN (1) | CN107949433A (es) |
BR (1) | BR112018004651B1 (es) |
CA (1) | CA2904477A1 (es) |
MX (1) | MX2018002766A (es) |
TW (1) | TW201716542A (es) |
WO (1) | WO2017046680A1 (es) |
Families Citing this family (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2013207783B2 (en) | 2012-01-13 | 2017-07-13 | Lummus Technology Llc | Process for providing C2 hydrocarbons via oxidative coupling of methane and for separating hydrocarbon compounds |
US9670113B2 (en) | 2012-07-09 | 2017-06-06 | Siluria Technologies, Inc. | Natural gas processing and systems |
AU2013355038B2 (en) | 2012-12-07 | 2017-11-02 | Lummus Technology Llc | Integrated processes and systems for conversion of methane to multiple higher hydrocarbon products |
EP3074119B1 (en) | 2013-11-27 | 2019-01-09 | Siluria Technologies, Inc. | Reactors and systems for oxidative coupling of methane |
WO2015105911A1 (en) | 2014-01-08 | 2015-07-16 | Siluria Technologies, Inc. | Ethylene-to-liquids systems and methods |
US10377682B2 (en) | 2014-01-09 | 2019-08-13 | Siluria Technologies, Inc. | Reactors and systems for oxidative coupling of methane |
EP3097068A4 (en) | 2014-01-09 | 2017-08-16 | Siluria Technologies, Inc. | Oxidative coupling of methane implementations for olefin production |
US9334204B1 (en) | 2015-03-17 | 2016-05-10 | Siluria Technologies, Inc. | Efficient oxidative coupling of methane processes and systems |
US10793490B2 (en) | 2015-03-17 | 2020-10-06 | Lummus Technology Llc | Oxidative coupling of methane methods and systems |
US20160289143A1 (en) | 2015-04-01 | 2016-10-06 | Siluria Technologies, Inc. | Advanced oxidative coupling of methane |
US9328297B1 (en) | 2015-06-16 | 2016-05-03 | Siluria Technologies, Inc. | Ethylene-to-liquids systems and methods |
WO2017065947A1 (en) | 2015-10-16 | 2017-04-20 | Siluria Technologies, Inc. | Separation methods and systems for oxidative coupling of methane |
CA3019396A1 (en) | 2016-04-13 | 2017-10-19 | Siluria Technologies, Inc. | Oxidative coupling of methane for olefin production |
EP3554672A4 (en) | 2016-12-19 | 2020-08-12 | Siluria Technologies, Inc. | PROCEDURES AND SYSTEMS FOR CHEMICAL DEPOSITION |
CA2953954A1 (en) * | 2017-01-06 | 2018-07-06 | Nova Chemicals Corporation | Double peroxide treatment of oxidative dehydrogenation catalyst |
KR102224278B1 (ko) | 2017-04-12 | 2021-03-08 | 주식회사 엘지화학 | 산화적 탈수소화 반응용 촉매 시스템, 이를 포함하는 산화적 탈수소화용 반응기 및 산화적 탈수소화 방법 |
HUE064375T2 (hu) | 2017-05-23 | 2024-03-28 | Lummus Technology Inc | Metán oxidatív csatolási folyamatainak integrálása |
US10836689B2 (en) | 2017-07-07 | 2020-11-17 | Lummus Technology Llc | Systems and methods for the oxidative coupling of methane |
KR102262896B1 (ko) * | 2017-11-30 | 2021-06-09 | 주식회사 엘지화학 | 산화적 탈수소화 반응용 촉매 시스템, 이를 포함하는 부타디엔 제조용 반응기 및 1,3-부타디엔의 제조방법 |
CN114340790A (zh) * | 2019-06-04 | 2022-04-12 | 丰田自动车欧洲公司 | 高度分散的金属负载的氧化物作为nh3-scr催化剂和合成过程 |
CN111632557B (zh) * | 2020-06-23 | 2024-06-14 | 浙江大学 | 一种用于热化学硫碘循环制氢的新型硫酸分解装置和方法 |
CN115155466B (zh) * | 2022-08-05 | 2023-10-13 | 中国石油大学(北京) | 一种甲烷氧化偶联制乙烯的耦合反应系统和方法 |
Family Cites Families (33)
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US2267767A (en) | 1940-10-24 | 1941-12-30 | Universal Oil Prod Co | Manufacture of catalysts |
US2478194A (en) | 1944-11-02 | 1949-08-09 | Houdry Process Corp | Catalyst pellet |
US3428703A (en) | 1967-01-27 | 1969-02-18 | Petro Tex Chem Corp | Dehydrogenation process using cobalt or nickel ferrite |
DE2949530A1 (de) * | 1979-12-08 | 1981-06-11 | Hoechst Ag, 6000 Frankfurt | Verfahren zur herstellung von 1,2-dichlorethan |
US5024984A (en) * | 1988-08-17 | 1991-06-18 | Amoco Corporation | Catalysts for the oxidative conversion of methane to higher hydrocarbons |
NL8902250A (nl) * | 1989-09-08 | 1991-04-02 | Veg Gasinstituut Nv | Werkwijze voor het uitvoeren van een chemische reactie en daarbij te gebruiken reactor. |
JP3836219B2 (ja) | 1996-09-12 | 2006-10-25 | 三井化学株式会社 | オレフィン気相重合の停止方法、オレフィン気相重合の開始方法およびオレフィンの気相重合装置 |
JPH10330343A (ja) * | 1997-04-04 | 1998-12-15 | Mitsubishi Chem Corp | ニトリルの製造方法 |
JP3948798B2 (ja) * | 1997-10-27 | 2007-07-25 | 株式会社日本触媒 | アクリル酸の製造方法 |
US6030920A (en) * | 1997-12-24 | 2000-02-29 | Saudi Basic Industries Corporation | Catalysts for producing acetic acid from ethane oxidation, processes of making same and method of using same |
DE10122027A1 (de) * | 2001-05-07 | 2002-05-23 | Basf Ag | Verfahren zur Herstellung von Acrylsäure durch heterogen katalysierte Partialoxidation von Propan |
US6589907B2 (en) * | 2000-09-28 | 2003-07-08 | Rohm And Haas Company | Zn and/or Ga promoted multi-metal oxide catalyst |
US6642173B2 (en) * | 2001-04-25 | 2003-11-04 | Rohm And Haas Company | Catalyst |
US6645905B2 (en) * | 2001-04-25 | 2003-11-11 | Rohm And Haas Company | Annealed and promoted catalyst |
US6841699B2 (en) * | 2001-04-25 | 2005-01-11 | Rohm And Haas Company | Recalcined catalyst |
JP4092090B2 (ja) * | 2001-06-26 | 2008-05-28 | 株式会社日本触媒 | 固体粒子充填反応器およびその反応器を用いた接触気相酸化方法 |
RU2004115326A (ru) * | 2001-10-16 | 2005-10-27 | БП Кемикэлз Лимитед (GB) | Катализатор окисления этана и способ, в котором исрользуют этот катализатор |
WO2005061414A1 (en) * | 2003-12-24 | 2005-07-07 | Lg Chem, Ltd. | Method of producing unsaturated acid in fixed-bed catalytic partial oxidation reactor with enhanced heat control system |
KR100850857B1 (ko) * | 2005-02-01 | 2008-08-06 | 주식회사 엘지화학 | 불포화 지방산의 제조방법 |
EP1890802A2 (en) * | 2005-05-25 | 2008-02-27 | Velocys, Inc. | Support for use in microchannel processing |
JP4549290B2 (ja) | 2005-12-16 | 2010-09-22 | 住友化学株式会社 | 多管式反応装置 |
US7824574B2 (en) | 2006-09-21 | 2010-11-02 | Eltron Research & Development | Cyclic catalytic upgrading of chemical species using metal oxide materials |
CN101015802B (zh) * | 2007-02-09 | 2010-09-15 | 东南大学 | 用于丙烷脱氢制丙烯的催化剂及其制备方法 |
EP2313385A2 (en) * | 2008-07-14 | 2011-04-27 | Velocys Inc. | Process for making ethylene oxide using microchannel process technology |
JP5232584B2 (ja) * | 2008-09-26 | 2013-07-10 | 東亞合成株式会社 | アクリル酸の製造方法 |
TWI398264B (zh) * | 2009-02-03 | 2013-06-11 | Shiseido Co Ltd | 毛髮調理劑組成物及其低能量製造方法 |
CA2655841C (en) * | 2009-02-26 | 2016-06-21 | Nova Chemicals Corporation | Supported oxidative dehydrogenation catalyst |
US8519210B2 (en) * | 2009-04-02 | 2013-08-27 | Lummus Technology Inc. | Process for producing ethylene via oxidative dehydrogenation (ODH) of ethane |
IT1394068B1 (it) * | 2009-05-13 | 2012-05-25 | Milano Politecnico | Reattore per reazioni catalitiche esotermiche o endotermiche |
JP6068617B2 (ja) | 2012-03-28 | 2017-01-25 | ローム アンド ハース カンパニーRohm And Haas Company | エチレン及び酢酸の製造工程 |
WO2014075075A1 (en) * | 2012-11-12 | 2014-05-15 | Ceramatec, Inc. | A fixed bed reactor heat transfer structure |
EP3024782B1 (en) * | 2013-07-26 | 2019-06-12 | SABIC Global Technologies B.V. | Method and apparatus for producing high purity phosgene |
CA2833822C (en) * | 2013-11-21 | 2020-08-04 | Nova Chemicals Corporation | Inherently safe odh operation |
-
2015
- 2015-09-14 CA CA2904477A patent/CA2904477A1/en not_active Abandoned
-
2016
- 2016-09-06 TW TW105128755A patent/TW201716542A/zh unknown
- 2016-09-08 MX MX2018002766A patent/MX2018002766A/es unknown
- 2016-09-08 JP JP2018513484A patent/JP6828022B2/ja active Active
- 2016-09-08 WO PCT/IB2016/055365 patent/WO2017046680A1/en active Application Filing
- 2016-09-08 BR BR112018004651-5A patent/BR112018004651B1/pt active IP Right Grant
- 2016-09-08 KR KR1020187007374A patent/KR102666333B1/ko active IP Right Grant
- 2016-09-08 CN CN201680053019.XA patent/CN107949433A/zh active Pending
- 2016-09-08 EP EP16774989.4A patent/EP3349890A1/en not_active Withdrawn
- 2016-09-08 US US15/762,729 patent/US10668441B2/en active Active
-
2020
- 2020-04-27 US US16/859,246 patent/US11110423B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
EP3349890A1 (en) | 2018-07-25 |
US11110423B2 (en) | 2021-09-07 |
JP2018529515A (ja) | 2018-10-11 |
BR112018004651B1 (pt) | 2021-02-23 |
US20200254414A1 (en) | 2020-08-13 |
TW201716542A (zh) | 2017-05-16 |
US20180272303A1 (en) | 2018-09-27 |
KR20180052637A (ko) | 2018-05-18 |
KR102666333B1 (ko) | 2024-05-14 |
WO2017046680A1 (en) | 2017-03-23 |
CN107949433A (zh) | 2018-04-20 |
BR112018004651A2 (pt) | 2018-09-25 |
JP6828022B2 (ja) | 2021-02-10 |
CA2904477A1 (en) | 2017-03-14 |
US10668441B2 (en) | 2020-06-02 |
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