EA008849B1 - Проточные реакторы для химических превращений с использованием гетерогенных катализаторов - Google Patents
Проточные реакторы для химических превращений с использованием гетерогенных катализаторов Download PDFInfo
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- EA008849B1 EA008849B1 EA200400768A EA200400768A EA008849B1 EA 008849 B1 EA008849 B1 EA 008849B1 EA 200400768 A EA200400768 A EA 200400768A EA 200400768 A EA200400768 A EA 200400768A EA 008849 B1 EA008849 B1 EA 008849B1
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- Eurasian Patent Office
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 95
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- 229910052757 nitrogen Inorganic materials 0.000 description 1
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- 239000004323 potassium nitrate Substances 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 239000002516 radical scavenger Substances 0.000 description 1
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
- F28F13/08—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by varying the cross-section of the flow channels
-
- 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
- B01J8/067—Heating or cooling the reactor
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/215—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of saturated hydrocarbyl groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
- C07C51/252—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/255—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/163—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing
- F28D7/1638—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing with particular pattern of flow or the heat exchange medium flowing inside the conduits assemblies, e.g. change of flow direction from one conduit assembly to another one
- F28D7/1646—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing with particular pattern of flow or the heat exchange medium flowing inside the conduits assemblies, e.g. change of flow direction from one conduit assembly to another one with particular pattern of flow of the heat exchange medium flowing outside the conduit assemblies, e.g. change of flow direction
-
- 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
- B01J2208/00212—Plates; Jackets; Cylinders
- B01J2208/00221—Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
-
- 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
- B01J2208/00654—Controlling the process by measures relating to the particulate material
- B01J2208/00707—Fouling
-
- 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
- Y02P20/582—Recycling of unreacted starting or intermediate materials
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Thermal Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Geometry (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Furan Compounds (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/920,981 US7316804B2 (en) | 2001-08-02 | 2001-08-02 | Flow reactors for chemical conversions with heterogeneous catalysts |
| PCT/US2002/022550 WO2003011449A1 (en) | 2001-08-02 | 2002-07-16 | Flow reactors for chemical conversions with hetergeneouos catalysts |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EA200400768A1 EA200400768A1 (ru) | 2004-12-30 |
| EA008849B1 true EA008849B1 (ru) | 2007-08-31 |
Family
ID=25444736
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EA200400768A EA008849B1 (ru) | 2001-08-02 | 2002-07-16 | Проточные реакторы для химических превращений с использованием гетерогенных катализаторов |
Country Status (17)
| Country | Link |
|---|---|
| US (3) | US7316804B2 (https=) |
| EP (2) | EP1412077B8 (https=) |
| JP (1) | JP4323950B2 (https=) |
| KR (3) | KR20100019540A (https=) |
| CN (1) | CN1531458B (https=) |
| AP (1) | AP1819A (https=) |
| AT (1) | ATE529183T1 (https=) |
| AU (1) | AU2002322502B2 (https=) |
| BR (1) | BR0211454A (https=) |
| CA (1) | CA2451090A1 (https=) |
| EA (1) | EA008849B1 (https=) |
| ES (1) | ES2373310T3 (https=) |
| MX (1) | MXPA04000890A (https=) |
| MY (1) | MY142104A (https=) |
| NO (1) | NO20040456L (https=) |
| TW (1) | TW579421B (https=) |
| WO (1) | WO2003011449A1 (https=) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2726178C1 (ru) * | 2017-06-09 | 2020-07-09 | Шаньдун Новэй Фармасьютикал Флюид Систем Ко., Лтд | Трубная камера отклонения потока, непрерывный проточный реактор и система непрерывных проточных реакций с системой управления |
Families Citing this family (75)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7316804B2 (en) * | 2001-08-02 | 2008-01-08 | Ineos Usa Llc | Flow reactors for chemical conversions with heterogeneous catalysts |
| DE10250406B4 (de) * | 2001-10-30 | 2007-10-25 | Hitachi, Ltd. | Reaktionsvorrichtung und Mischsystem |
| BR0214991A (pt) * | 2001-12-28 | 2004-12-14 | Mitsubishi Chem Corp | Métodos para a oxtdação catalìtica em fase vapor e para compactar um catalisador |
| WO2003078052A1 (en) * | 2002-03-11 | 2003-09-25 | Battelle Memorial Institute | Microchannel reactors with temperature control |
| US8206666B2 (en) * | 2002-05-21 | 2012-06-26 | Battelle Memorial Institute | Reactors having varying cross-section, methods of making same, and methods of conducting reactions with varying local contact time |
| US6989134B2 (en) * | 2002-11-27 | 2006-01-24 | Velocys Inc. | Microchannel apparatus, methods of making microchannel apparatus, and processes of conducting unit operations |
| FR2849031A1 (fr) * | 2002-12-19 | 2004-06-25 | Bp Lavera Snc | Procede de fabrication d'oxyde d'ethylene |
| US7195059B2 (en) * | 2003-05-06 | 2007-03-27 | H2Gen Innovations, Inc. | Heat exchanger and method of performing chemical processes |
| US20050135978A1 (en) * | 2003-10-14 | 2005-06-23 | Mourad Hamedi | Method and apparatus for optimizing throughput in a trickle bed reactor |
| US7470408B2 (en) | 2003-12-18 | 2008-12-30 | Velocys | In situ mixing in microchannels |
| DE102004018267B4 (de) * | 2004-04-15 | 2007-05-03 | Man Dwe Gmbh | Reaktoranordnung zur Durchführung katalytischer Gasphasenreaktionen |
| CN100415356C (zh) * | 2004-06-24 | 2008-09-03 | 华东理工大学 | 一种适用于高热敏性物质的气固相反应装置 |
| US7468455B2 (en) * | 2004-11-03 | 2008-12-23 | Velocys, Inc. | Process and apparatus for improved methods for making vinyl acetate monomer (VAM) |
| US7371361B2 (en) * | 2004-11-03 | 2008-05-13 | Kellogg Brown & Root Llc | Maximum reaction rate converter system for exothermic reactions |
| GB0509747D0 (en) * | 2005-05-13 | 2005-06-22 | Ashe Morris Ltd | Variable volume heat exchangers |
| JP5641693B2 (ja) * | 2005-12-19 | 2014-12-17 | ビーピー エクスプロレーション オペレーティング カンパニー リミテッドBp Exploration Operating Company Limited | 1種もしくはそれ以上の気相反応体からの凝縮相生成物の製造方法 |
| RU2326424C2 (ru) * | 2006-01-23 | 2008-06-10 | Новомосковский институт Российского химико-технологического университета им. Д.И. Менделеева | Система автоматического поддержания температурного профиля в реакторе |
| DE102006060507A1 (de) * | 2006-12-19 | 2008-06-26 | Basf Se | Reaktor zur Durchführung einer Reaktion zwischen zwei fluiden Edukten an einem Katalysatorbett mit Vorvermischen der fluiden Edukte in einer Einmischvorrichtung |
| DE102006060509A1 (de) * | 2006-12-19 | 2008-06-26 | Basf Se | Reaktor zur Durchführung einer kontinuierlichen Oxidehydrierung sowie Verfahren |
| US8206667B2 (en) * | 2007-12-31 | 2012-06-26 | Chevron U.S.A. Inc. | Membrane reactor with in-situ dehydration and method for using the same |
| US7745667B2 (en) * | 2008-04-07 | 2010-06-29 | Velocys | Microchannel apparatus comprising structured walls, chemical processes, methods of making formaldehyde |
| US20100150825A1 (en) * | 2008-12-17 | 2010-06-17 | Pfefferle William C | Method for effectively controlling the temperature of oxide-coated short-channel-length metallic structures |
| JP5691152B2 (ja) * | 2009-09-30 | 2015-04-01 | 三菱化学株式会社 | プレート式反応器を用いた反応生成物の製造方法 |
| KR101257411B1 (ko) | 2009-10-09 | 2013-04-23 | 주식회사 엘지화학 | (메트)아크릴산의 제조방법 |
| RU2440400C2 (ru) * | 2010-02-01 | 2012-01-20 | Инфра Текнолоджиз Лтд | Способ получения синтетических жидких углеводородов и реактор для проведения синтеза фишера-тропша |
| DE102010040757A1 (de) | 2010-09-14 | 2012-03-15 | Man Diesel & Turbo Se | Rohrbündelreaktor |
| CN102649697B (zh) * | 2011-02-25 | 2014-07-02 | 中国石油化工股份有限公司 | 通过草酸酯气相加氢制乙二醇的方法 |
| CN102649685B (zh) * | 2011-02-25 | 2015-11-25 | 中国石油化工股份有限公司 | 草酸酯高效率生产乙二醇的方法 |
| US9803153B2 (en) | 2011-04-14 | 2017-10-31 | Gas Technology Institute | Radiant non-catalytic recuperative reformer |
| KR101297597B1 (ko) * | 2011-04-19 | 2013-08-19 | 한국화학연구원 | 합성가스로부터 탄화수소를 제조하기 위한 반응장치 |
| JP5967588B2 (ja) * | 2011-10-19 | 2016-08-10 | パナソニックIpマネジメント株式会社 | 熱交換器 |
| ITMI20112040A1 (it) * | 2011-11-10 | 2013-05-11 | D E L Co S R L | Impianto per la dealogenazione e la rigenerazione in continuo di oli minerali contaminati da composti organici clorurati |
| US9133079B2 (en) | 2012-01-13 | 2015-09-15 | Siluria Technologies, Inc. | Process for separating hydrocarbon compounds |
| CA2874526C (en) | 2012-05-24 | 2022-01-18 | Siluria Technologies, Inc. | Oxidative coupling of methane systems and methods |
| US9670113B2 (en) | 2012-07-09 | 2017-06-06 | Siluria Technologies, Inc. | Natural gas processing and systems |
| WO2014089479A1 (en) | 2012-12-07 | 2014-06-12 | Siluria Technologies, Inc. | 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 |
| CA3123783A1 (en) | 2014-01-08 | 2015-07-16 | Lummus Technology Llc | Ethylene-to-liquids systems and methods |
| CA2935946C (en) | 2014-01-09 | 2022-05-03 | Siluria Technologies, Inc. | Oxidative coupling of methane implementations for olefin production |
| US10377682B2 (en) | 2014-01-09 | 2019-08-13 | Siluria Technologies, Inc. | Reactors and systems for oxidative coupling of methane |
| EP3848114A1 (en) * | 2014-04-02 | 2021-07-14 | Haldor Topsøe A/S | Process and pseudo-isothermal reactor for production of methanol |
| JP2018501084A (ja) * | 2014-11-14 | 2018-01-18 | サビック グローバル テクノロジーズ ベスローテン フエンノートシャップ | 固定床反応器及びそれに関する方法 |
| US10793490B2 (en) | 2015-03-17 | 2020-10-06 | Lummus Technology Llc | Oxidative coupling of methane methods and systems |
| US9334204B1 (en) | 2015-03-17 | 2016-05-10 | Siluria Technologies, Inc. | Efficient oxidative coupling of methane processes and systems |
| US20160289143A1 (en) | 2015-04-01 | 2016-10-06 | Siluria Technologies, Inc. | Advanced oxidative coupling of methane |
| JP2018127398A (ja) * | 2015-05-12 | 2018-08-16 | 株式会社ダイセル | 酸化反応用リアクター、及び酸化物の製造方法 |
| US9328297B1 (en) | 2015-06-16 | 2016-05-03 | Siluria Technologies, Inc. | Ethylene-to-liquids systems and methods |
| US20170107162A1 (en) | 2015-10-16 | 2017-04-20 | Siluria Technologies, Inc. | Separation methods and systems for oxidative coupling of methane |
| JP2017113746A (ja) * | 2015-12-21 | 2017-06-29 | ガス テクノロジー インスティテュート | 放射状の非触媒性の回収改質装置 |
| CN108474629B (zh) * | 2015-12-28 | 2021-11-02 | 开利公司 | 用于热交换器应用的折叠导管 |
| US9944573B2 (en) | 2016-04-13 | 2018-04-17 | Siluria Technologies, Inc. | Oxidative coupling of methane for olefin production |
| US10889762B2 (en) * | 2016-12-09 | 2021-01-12 | Velocys Technologies Limited | Process for operating a highly productive tubular reactor |
| US20180169561A1 (en) | 2016-12-19 | 2018-06-21 | Siluria Technologies, Inc. | Methods and systems for performing chemical separations |
| ES2881297T3 (es) * | 2017-02-10 | 2021-11-29 | Technobell D O O Koper | Reactor tubular de doble zona mejorado y método para llevar a cabo la producción de anhídrido maleico mediante la oxidación de n-butano |
| HUE064375T2 (hu) | 2017-05-23 | 2024-03-28 | Lummus Technology Inc | Metán oxidatív csatolási folyamatainak integrálása |
| WO2018234975A1 (en) * | 2017-06-21 | 2018-12-27 | Sabic Global Technologies, B.V. | Improved reactor designs for heterogeneous catalytic reactions |
| AU2018298234B2 (en) | 2017-07-07 | 2022-11-17 | Lummus Technology Llc | Systems and methods for the oxidative coupling of methane |
| CN108607475A (zh) * | 2018-04-28 | 2018-10-02 | 上海奕玛化工科技有限公司 | 一种草酸二甲酯加氢制乙二醇用反应器 |
| CN109289713B (zh) * | 2018-10-18 | 2021-04-20 | 辽宁石油化工大学 | 一种蚊香盘管等温反应器及使用方法 |
| CN110701804A (zh) * | 2019-11-14 | 2020-01-17 | 佛山光腾新能源股份有限公司 | 一种基于甲醇催化加热的液体加热装置 |
| EP3892367A1 (en) * | 2020-04-09 | 2021-10-13 | Röhm GmbH | A tube bundle reactor and method for the production of methacrylic acid through the partial oxidation of methacrolein |
| JPWO2021224980A1 (https=) * | 2020-05-08 | 2021-11-11 | ||
| US12583810B2 (en) | 2020-06-01 | 2026-03-24 | Solugen, Inc. | Trickle bed reactor |
| GB2598579A (en) * | 2020-09-02 | 2022-03-09 | Unisa | Tubular reactors |
| CN112050202B (zh) * | 2020-09-03 | 2023-04-28 | 福大紫金氢能科技股份有限公司 | 一种管式氨分解反应器 |
| CN112050663A (zh) * | 2020-09-14 | 2020-12-08 | 刘延林 | 一种均匀化液冷式通风降温装置 |
| JP2024519340A (ja) * | 2021-05-11 | 2024-05-10 | アーケマ・インコーポレイテッド | 熱交換器のチューブシート監視方法 |
| CN117642257A (zh) * | 2021-05-11 | 2024-03-01 | 阿科玛股份有限公司 | 用于监测热交换器的管片的方法 |
| JP2023012391A (ja) * | 2021-07-13 | 2023-01-25 | 三菱重工業株式会社 | 等温化した反応装置 |
| TW202313528A (zh) | 2021-08-31 | 2023-04-01 | 美商祿幕斯科技有限責任公司 | 用於執行甲烷的氧化耦合的方法及系統 |
| CN113921992A (zh) * | 2021-09-16 | 2022-01-11 | 河北金力新能源科技股份有限公司 | 高耐热锂电隔膜及其制备方法和应用 |
| CN115228388A (zh) * | 2022-07-20 | 2022-10-25 | 武汉工程大学 | 具氢分离机制的热管-列管式固定床丙烷脱氢反应器 |
| CN115364806B (zh) * | 2022-08-11 | 2024-09-17 | 中山致安化工科技有限公司 | 一种连续流反应器 |
| CN115738921B (zh) * | 2022-11-29 | 2024-08-27 | 东方电气集团东方锅炉股份有限公司 | 一种反应器进出口多腔室均匀冷却的列管式顺酐反应器系统 |
| GB2641900A (en) * | 2024-06-17 | 2025-12-24 | Siemens Industry Software Ltd | Catalytic reactions |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2040432A (en) * | 1979-01-10 | 1980-08-28 | Hisaka Works Ltd | Heat conducting element for plate heat exchanger |
| JPS6154229A (ja) * | 1984-08-24 | 1986-03-18 | Mitsubishi Heavy Ind Ltd | 反応器 |
| EP1033167A2 (de) * | 1999-03-03 | 2000-09-06 | Basf Aktiengesellschaft | Rohrbündelreaktor mit gestuftem Innendurchmesser |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH493811A (de) * | 1967-09-06 | 1970-07-15 | Basf Ag | Wärmetauschvorrichtung |
| BE793928A (fr) | 1972-01-13 | 1973-05-02 | Deggendorfer Werft Eisenbau | Appareil pour la mise en oeuvre de processus chimiques exothermiques et endothermiques |
| DE2221288C3 (de) | 1972-04-29 | 1975-04-17 | Deggendorfer Werft Und Eisenbau Gmbh, 8360 Deggendorf | Reaktionsapparat zur Durchführung katalytischer Reaktionen in mehreren Stufen |
| DE2230127C3 (de) | 1972-06-21 | 1975-03-13 | Deggendorfer Werft Und Eisenbau Gmbh, 8360 Deggendorf | Reaktionsapparat zur Durchführung endothermer chemischer Prozesse |
| DE2929300A1 (de) | 1979-07-19 | 1981-01-29 | Linde Ag | Reaktor zur durchfuehrung katalytischer endothermer oder exothermer reaktionen |
| US4472527A (en) * | 1982-03-31 | 1984-09-18 | Mitsubishi Chemical Industries Ltd. | Process for preparing an oxidation catalyst composition |
| CA1223895A (en) * | 1984-03-05 | 1987-07-07 | Hugo I. De Lasa | Pseudodiabatic reactor for exothermal catalytic conversions |
| DE3409159A1 (de) | 1984-03-13 | 1985-09-26 | Deggendorfer Werft Und Eisenbau Gmbh, 8360 Deggendorf | Rohrbuendel-reaktionsapparat |
| DE3874759D1 (de) | 1988-12-13 | 1992-10-22 | Deggendorfer Werft Eisenbau | Rohrbuendelreaktor. |
| ATE171649T1 (de) | 1993-07-05 | 1998-10-15 | Packinox Sa | Verfahren und vorrichtung zur regulierung der temperaturen von reaktionen |
| US5510308A (en) * | 1994-10-19 | 1996-04-23 | E. I. Du Pont De Nemours And Company | Cation and vanadium substituted heteropolyacid catalysts for vapor phase oxidation |
| US7316804B2 (en) * | 2001-08-02 | 2008-01-08 | Ineos Usa Llc | Flow reactors for chemical conversions with heterogeneous catalysts |
-
2001
- 2001-08-02 US US09/920,981 patent/US7316804B2/en not_active Expired - Fee Related
-
2002
- 2002-07-16 KR KR1020097027101A patent/KR20100019540A/ko not_active Ceased
- 2002-07-16 ES ES02756496T patent/ES2373310T3/es not_active Expired - Lifetime
- 2002-07-16 EP EP02756496A patent/EP1412077B8/en not_active Expired - Lifetime
- 2002-07-16 WO PCT/US2002/022550 patent/WO2003011449A1/en not_active Ceased
- 2002-07-16 EP EP10010957A patent/EP2314372A1/en not_active Withdrawn
- 2002-07-16 KR KR10-2004-7001565A patent/KR20040019101A/ko not_active Ceased
- 2002-07-16 CA CA002451090A patent/CA2451090A1/en not_active Abandoned
- 2002-07-16 BR BR0211454-2A patent/BR0211454A/pt not_active Application Discontinuation
- 2002-07-16 AT AT02756496T patent/ATE529183T1/de active
- 2002-07-16 AP APAP/P/2004/002965A patent/AP1819A/en active
- 2002-07-16 CN CN028143531A patent/CN1531458B/zh not_active Expired - Fee Related
- 2002-07-16 MX MXPA04000890A patent/MXPA04000890A/es not_active Application Discontinuation
- 2002-07-16 AU AU2002322502A patent/AU2002322502B2/en not_active Ceased
- 2002-07-16 JP JP2003516674A patent/JP4323950B2/ja not_active Expired - Fee Related
- 2002-07-16 EA EA200400768A patent/EA008849B1/ru not_active IP Right Cessation
- 2002-07-16 KR KR1020117002066A patent/KR20110017463A/ko not_active Ceased
- 2002-07-23 TW TW091116381A patent/TW579421B/zh not_active IP Right Cessation
- 2002-07-24 MY MYPI20022799A patent/MY142104A/en unknown
-
2004
- 2004-02-02 NO NO20040456A patent/NO20040456L/no not_active Application Discontinuation
-
2007
- 2007-12-04 US US11/999,296 patent/US8080215B2/en not_active Expired - Fee Related
-
2011
- 2011-02-04 US US12/929,624 patent/US8232415B2/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2040432A (en) * | 1979-01-10 | 1980-08-28 | Hisaka Works Ltd | Heat conducting element for plate heat exchanger |
| JPS6154229A (ja) * | 1984-08-24 | 1986-03-18 | Mitsubishi Heavy Ind Ltd | 反応器 |
| EP1033167A2 (de) * | 1999-03-03 | 2000-09-06 | Basf Aktiengesellschaft | Rohrbündelreaktor mit gestuftem Innendurchmesser |
Non-Patent Citations (1)
| Title |
|---|
| PATENT ABSTRACTS OF JAPAN, vol. 010, no. 214 (C-362), 25 July, 1986 (1986-07-25) & JP 61054229 A (MITSUBISHI HEAVY IND LTD.), 18 March, 1986 (1986-03-18), cited in the application, abstract; figures 1-4 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2726178C1 (ru) * | 2017-06-09 | 2020-07-09 | Шаньдун Новэй Фармасьютикал Флюид Систем Ко., Лтд | Трубная камера отклонения потока, непрерывный проточный реактор и система непрерывных проточных реакций с системой управления |
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| Publication number | Publication date |
|---|---|
| EA200400768A1 (ru) | 2004-12-30 |
| ES2373310T3 (es) | 2012-02-02 |
| ATE529183T1 (de) | 2011-11-15 |
| AU2002322502B2 (en) | 2008-05-22 |
| CN1531458B (zh) | 2010-06-09 |
| CN1531458A (zh) | 2004-09-22 |
| AP1819A (en) | 2008-01-10 |
| NO20040456L (no) | 2004-05-03 |
| TW579421B (en) | 2004-03-11 |
| MY142104A (en) | 2010-09-15 |
| WO2003011449A1 (en) | 2003-02-13 |
| CA2451090A1 (en) | 2003-02-13 |
| JP4323950B2 (ja) | 2009-09-02 |
| US20090043114A1 (en) | 2009-02-12 |
| KR20110017463A (ko) | 2011-02-21 |
| US7316804B2 (en) | 2008-01-08 |
| US8232415B2 (en) | 2012-07-31 |
| US20030068261A1 (en) | 2003-04-10 |
| KR20100019540A (ko) | 2010-02-18 |
| EP2314372A1 (en) | 2011-04-27 |
| MXPA04000890A (es) | 2004-05-21 |
| US8080215B2 (en) | 2011-12-20 |
| JP2005518265A (ja) | 2005-06-23 |
| EP1412077B8 (en) | 2012-03-21 |
| KR20040019101A (ko) | 2004-03-04 |
| EP1412077A1 (en) | 2004-04-28 |
| BR0211454A (pt) | 2004-08-17 |
| AP2004002965A0 (en) | 2004-03-31 |
| US20110144356A1 (en) | 2011-06-16 |
| EP1412077B1 (en) | 2011-10-19 |
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