AU2001258079A1 - An apparatus for the controlled optimized addition of reactants in continuous flow reaction systems and methods of using the same - Google Patents

An apparatus for the controlled optimized addition of reactants in continuous flow reaction systems and methods of using the same

Info

Publication number
AU2001258079A1
AU2001258079A1 AU2001258079A AU5807901A AU2001258079A1 AU 2001258079 A1 AU2001258079 A1 AU 2001258079A1 AU 2001258079 A AU2001258079 A AU 2001258079A AU 5807901 A AU5807901 A AU 5807901A AU 2001258079 A1 AU2001258079 A1 AU 2001258079A1
Authority
AU
Australia
Prior art keywords
continuous flow
reactants
methods
same
reaction
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.)
Abandoned
Application number
AU2001258079A
Other languages
English (en)
Inventor
Alaa Eldin Mostafa Adris
Abdullah A. Al-Nutaifi
Fahad A. Al-Sherehy
Shahid M. Azam
Tarique Hakeem
Shickh Kareemuddin
Munawwar Saudagar
Mustafa A. Soliman
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Saudi Basic Industries Corp
Original Assignee
Saudi Basic Industries Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Saudi Basic Industries Corp filed Critical Saudi Basic Industries Corp
Publication of AU2001258079A1 publication Critical patent/AU2001258079A1/en
Abandoned legal-status Critical Current

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
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • 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
    • B01J19/0006—Controlling or regulating processes
    • B01J19/0013—Controlling the temperature of the process
    • 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
    • B01J19/0006—Controlling or regulating processes
    • B01J19/002—Avoiding undesirable reactions or side-effects, e.g. avoiding explosions, or improving the yield by suppressing side-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
    • B01J19/2425—Tubular reactors in parallel
    • 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
    • B01J19/244—Concentric 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
    • 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
    • B01J8/065—Feeding reactive fluids
    • 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
    • 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1818—Feeding of the fluidising gas
    • B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
    • 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836—Heating and cooling 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
    • 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
    • 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
    • B01J2208/0023—Plates; Jackets; Cylinders with some catalyst tubes being empty, e.g. dummy tubes or flow-adjusting rods
    • 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
    • B01J2208/0053—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
    • 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
    • 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
    • B01J2219/00162—Controlling or regulating processes controlling the 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00245—Avoiding undesirable reactions or side-effects
    • B01J2219/00259—Preventing runaway of the chemical reaction
    • 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
    • B01J2219/00245—Avoiding undesirable reactions or side-effects
    • B01J2219/00259—Preventing runaway of the chemical reaction
    • B01J2219/00263—Preventing explosion of the chemical mixture

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Treating Waste Gases (AREA)
  • Control Of Non-Electrical Variables (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
AU2001258079A 2000-05-05 2001-05-04 An apparatus for the controlled optimized addition of reactants in continuous flow reaction systems and methods of using the same Abandoned AU2001258079A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US09/565,779 US6977064B1 (en) 2000-05-05 2000-05-05 Apparatus for the controlled optimized addition of reactants in continuous flow reaction systems
US09/565,779 2000-05-05
PCT/CA2001/000613 WO2001085333A2 (en) 2000-05-05 2001-05-04 An apparatus for the controlled optimized addition of reactants in continuous flow reaction systems and methods of using the same

Publications (1)

Publication Number Publication Date
AU2001258079A1 true AU2001258079A1 (en) 2001-11-20

Family

ID=24260051

Family Applications (1)

Application Number Title Priority Date Filing Date
AU2001258079A Abandoned AU2001258079A1 (en) 2000-05-05 2001-05-04 An apparatus for the controlled optimized addition of reactants in continuous flow reaction systems and methods of using the same

Country Status (9)

Country Link
US (2) US6977064B1 (de)
EP (2) EP1284815B1 (de)
KR (1) KR100742842B1 (de)
AT (1) ATE468914T1 (de)
AU (1) AU2001258079A1 (de)
DE (1) DE60142229D1 (de)
ES (1) ES2345535T3 (de)
GC (2) GC0000225A (de)
WO (1) WO2001085333A2 (de)

Families Citing this family (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004033060A2 (en) * 2002-06-21 2004-04-22 Exxonmobil Chemical Patents Inc. Controlling solids circulation in a gas-solids reaction system
GB2400330B (en) * 2003-04-10 2007-05-30 Dynamic Proc Solutions Plc Filtration apparatus
DE102004040472A1 (de) * 2004-08-20 2006-03-02 Man Dwe Gmbh Verfahren und Rohrbündelreaktor zur Durchführung endothermer oder exothermer Gasphasenreaktionen
US7416571B2 (en) * 2005-03-09 2008-08-26 Conocophillips Company Compact mixer for the mixing of gaseous hydrocarbon and gaseous oxidants
KR100838970B1 (ko) 2005-04-29 2008-06-16 주식회사 엘지화학 유량 배분 균일성이 향상된 환상도관
US7998418B1 (en) 2006-06-01 2011-08-16 Nanotek, Llc Evaporator and concentrator in reactor and loading system
US7641860B2 (en) * 2006-06-01 2010-01-05 Nanotek, Llc Modular and reconfigurable multi-stage microreactor cartridge apparatus
US7854902B2 (en) * 2006-08-23 2010-12-21 Nanotek, Llc Modular and reconfigurable multi-stage high temperature microreactor cartridge apparatus and system for using same
US7931921B2 (en) * 2007-02-16 2011-04-26 Maier Frederick P Method of substantially preventing or inhibiting summer bentgrass decline
ES2378332T3 (es) * 2007-03-15 2012-04-11 Dow Global Technologies Llc Mezclador para un reactor de flujo continuo
US8603407B2 (en) 2007-03-21 2013-12-10 Precision Combustion, Inc. Catalytic isobutane alkylation
WO2008118808A1 (en) 2007-03-23 2008-10-02 Advion Bioscience, Inc. Liquid chromatography-mass spectrometry
SI2240269T1 (sl) 2007-12-27 2019-08-30 Elcon Recycling Center (2003) Ltd. Varna predelava tekočine z nadzorovanjem in zmanjševanjem eksplozivnosti parno-plinskih vrst, tvorjenih iz nje ali vsebovanih v njej
GB201000156D0 (en) 2010-01-07 2010-02-24 Gas2 Ltd Isothermal reactor for partial oxidisation of methane
DE102010040757A1 (de) * 2010-09-14 2012-03-15 Man Diesel & Turbo Se Rohrbündelreaktor
WO2012049210A1 (en) * 2010-10-13 2012-04-19 Buss Chem Tech Ag Process and apparatus for continuous high temperature short-time alkoxylation (ethoxylation, propoxylation) of chemical substances with active hydrogen atoms
CN103209760B (zh) * 2011-10-12 2015-11-25 曼柴油机和涡轮机欧洲股份公司 实施催化气相反应的管束式反应器
KR101424610B1 (ko) 2013-06-14 2014-08-04 (주) 라미나 코어-쉘 입자 제조장치 및 이를 이용한 코어-쉘 입자 제조방법
CA2937478C (en) * 2014-02-10 2021-03-09 Archer Daniels Midland Company Improved multiphase low mixing processes
US10076739B1 (en) 2014-07-22 2018-09-18 Precision Combustion, Inc. Chemical reactor for use with overly reactive chemicals
US9958211B2 (en) 2015-03-12 2018-05-01 Bayotech, Inc. Nested-flow heat exchangers and chemical reactors
US10686204B2 (en) * 2015-08-10 2020-06-16 Nissan Motor Co., Ltd. Solid oxide fuel cell system
WO2017134504A1 (en) * 2016-02-01 2017-08-10 Sabic Global Technologies B.V. Methods for direct epoxidation of propylene with oxygen
WO2017144584A1 (en) * 2016-02-26 2017-08-31 Shell Internationale Research Maatschappij B.V. Alkane oxidative dehydrogenation (odh)
EP3490961B1 (de) * 2016-07-26 2021-03-10 Shell Internationale Research Maatschappij B.V. Oxidative dehydrierung (odh) von ethan
PL3490962T3 (pl) * 2016-07-26 2021-09-13 Shell Internationale Research Maatschappij B.V. Utleniające odwodornienie (odh) etanu
FR3063562B1 (fr) * 2017-03-02 2021-05-21 Ingenico Group Dispositif de support pour terminal de paiement
CN108786671B (zh) 2017-04-27 2021-04-23 中国科学院大连化学物理研究所 甲醇和/或二甲醚与苯制对二甲苯联产低碳烯烃的流化床装置及方法
CN108794291B (zh) * 2017-04-27 2020-11-27 中国科学院大连化学物理研究所 甲醇和/或二甲醚与甲苯制对二甲苯联产低碳烯烃的流化床装置及方法
WO2019050702A1 (en) * 2017-09-08 2019-03-14 Battelle Energy Alliance, Llc SYSTEMS AND METHODS FOR OXIDATION OF FLUIDS
US10994860B2 (en) 2017-12-20 2021-05-04 Hamilton Sunstrand Corporation Catalytic fuel tank inerting system
US10569896B2 (en) 2017-12-20 2020-02-25 Hamilton Sundstrand Corporation Catalytic fuel tank inerting system
US11040928B1 (en) 2018-04-23 2021-06-22 Precision Combustion, Inc. Process for converting alkanes to olefins
US11052347B2 (en) * 2018-12-21 2021-07-06 Entegris, Inc. Bulk process gas purification systems
US10434484B1 (en) * 2019-03-29 2019-10-08 Emerging Fuels Technology, Inc. Stacked zone vertical tubular reactor
GB201911815D0 (en) * 2019-08-16 2019-10-02 Univ Nottingham Reaction Apparatus
WO2022241561A1 (en) * 2021-05-20 2022-11-24 Nuionic Technologies (Canada) Inc. Systems, apparatuses, utilization of microwave energy within a microwave reactor
CN113617295B (zh) * 2021-08-18 2022-08-09 中国科学院广州地球化学研究所 一种反应炉和物料生产工艺

Family Cites Families (46)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2596299A (en) * 1952-05-13 Sheetsxsheet i
US2453740A (en) * 1945-02-16 1948-11-16 Standard Oil Co Oxidation of organic compounds and manufacture of phthalic anhydride
US2518583A (en) 1945-06-27 1950-08-15 Universal Oil Prod Co Catalytic reactor
US2539415A (en) * 1947-03-14 1951-01-30 Hydrocarbon Research Inc Process and apparatus for the synthesis of hydrocarbons
US2584391A (en) * 1947-03-29 1952-02-05 Universal Oil Prod Co Apparatus for effecting fluidized contact between solid particles and fluid mediums
US2786801A (en) * 1952-04-04 1957-03-26 Gulf Research Development Co Fluid contacting process involving fluidized particles
US2809981A (en) * 1953-02-27 1957-10-15 Exxon Research Engineering Co Method of carrying out homogeneous vapor phase reactions
GB754507A (en) * 1953-11-12 1956-08-08 Exxon Research Engineering Co Improvements in or relating to fluid coking process and feed apparatus therefor
US2954281A (en) * 1954-09-27 1960-09-27 Stone & Webster Eng Corp Method and apparatus for the fluidized catalytic treatment of fluid reactants
US3162683A (en) 1959-06-23 1964-12-22 Exxon Research Engineering Co Liquid phase oxidation of alkyl-substituted aromatics
US3161683A (en) * 1960-02-09 1964-12-15 Acidos Grasos Limitada Process for partial oxidation of acetylene
NL298678A (de) 1962-10-02
US3513145A (en) 1966-02-25 1970-05-19 Crawford & Russell Inc Continuous mass polymerization processes
US3679651A (en) 1968-08-29 1972-07-25 Mitsui Toatsu Chemicals Method of polymerizing styrene
US3844936A (en) 1970-08-04 1974-10-29 Haldor Topsoe As Desulfurization process
US3838139A (en) 1971-08-16 1974-09-24 Monsanto Co Continuous mass styrene-type monomer polymerization process
BE830308A (nl) 1974-06-25 1975-12-17 Werkwijze ter bereiding van een slagvast polymeer van een vinylaromatische verbinding
US4056602A (en) 1975-08-20 1977-11-01 Thagard Technology Company High temperature chemical reaction processes utilizing fluid-wall reactors
DE2559661B2 (de) 1975-10-01 1978-10-26 Deggendorfer Werft Und Eisenbau Gmbh, 8360 Deggendorf Reaktionsapparat
NL7610318A (nl) * 1976-06-01 1977-12-05 Sun Ventures Inc Werkwijze voor het ammoxyderen van organische verbindingen tot nitrilen.
US4196170A (en) 1978-05-26 1980-04-01 Caterpillar Tractor Co. Multistage catalytic reactor having a pressure responsive gas flow control valve therein
US4250346A (en) 1980-04-14 1981-02-10 Union Carbide Corporation Low temperature oxydehydrogenation of ethane to ethylene
US4370470A (en) 1981-04-16 1983-01-25 Phillips Petroleum Company Multistage, agitated contactor and its use in continuous production of arylene sulfide polymer
US4818495A (en) 1982-11-05 1989-04-04 Union Carbide Corporation Reactor for fluidized bed silane decomposition
US4899003A (en) 1985-07-11 1990-02-06 Union Carbide Chemicals And Plastics Company Inc. Process for oxydehydrogenation of ethane to ethylene
JPH0638911B2 (ja) 1986-03-08 1994-05-25 日本セメント株式会社 非酸化物粉末の製造方法
US4692306A (en) 1986-03-24 1987-09-08 Kinetics Technology International Corporation Catalytic reaction apparatus
DE3806408A1 (de) 1988-02-29 1989-09-07 Uhde Gmbh Verfahren und vorrichtung zur erzeugung eines h(pfeil abwaerts)2(pfeil abwaerts) und co-enthaltenden synthesegases
DE3820947A1 (de) * 1988-06-21 1989-12-28 Deggendorfer Werft Eisenbau Wirbelschichtreaktor
IT1226303B (it) 1988-07-26 1990-12-27 Montedipe Spa Processo ed apparato per la devolatilizzazione di soluzioni di polimeri.
EP0383224B1 (de) 1989-02-17 1992-09-16 Jgc Corporation Rohrbündelapparat mit einer Zwischenrohrplatte
US5202517A (en) 1989-10-27 1993-04-13 Medalert Incorporated Process for production of ethylene from ethane
US5229102A (en) 1989-11-13 1993-07-20 Medalert, Inc. Catalytic ceramic membrane steam-hydrocarbon reformer
US4981676A (en) 1989-11-13 1991-01-01 Minet Ronald G Catalytic ceramic membrane steam/hydrocarbon reformer
US5300682A (en) 1991-06-10 1994-04-05 The Standard Oil Co. Catalytic oxidation of ethane to acetic acid
JP2778878B2 (ja) 1991-09-12 1998-07-23 株式会社日本触媒 エチレンオキシドの製造方法
US5622677A (en) * 1991-10-28 1997-04-22 Shell Oil Company Venturi riser reactor and process for catalytic cracking
US5300684A (en) 1991-12-09 1994-04-05 The Standard Oil Company Process for the fluidized bed oxidation of ethane to acetic acid
DE4207905A1 (de) * 1992-03-12 1993-09-16 Bayer Ag Festbettreaktoren mit kurzem katalysatorbett in stroemungsrichtung
US5384051A (en) * 1993-02-05 1995-01-24 Mcginness; Thomas G. Supercritical oxidation reactor
EP0893183A3 (de) 1993-03-02 1999-02-24 SRI International Exothermisches Verfahren mit porösem Mittel zur Reglung der Reaktionsgeschwindigkeit und der exothermischen Wärme
US5723094A (en) 1996-10-29 1998-03-03 Arco Chemical Technology, L.P. Reactor for chemical reactions
DE19723322A1 (de) * 1997-06-04 1998-12-10 Bayer Ag Reaktor zur Durchführung rascher stark exothermer Reaktionen und dessen Verwendung
US6013597A (en) 1997-09-17 2000-01-11 Saudi Basic Industries Corporation Catalysts for the oxidation of ethane to acetic acid processes of making same and, processes of using same
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
US20050086383A1 (en) * 2003-10-17 2005-04-21 Nokia Corporation Optimizing the compression efficiency in a packet data communication

Also Published As

Publication number Publication date
EP1541226A2 (de) 2005-06-15
KR100742842B1 (ko) 2007-07-25
US20060003402A1 (en) 2006-01-05
US7445758B2 (en) 2008-11-04
ATE468914T1 (de) 2010-06-15
WO2001085333A3 (en) 2002-09-06
WO2001085333A2 (en) 2001-11-15
GC0000225A (en) 2006-03-29
EP1284815B1 (de) 2010-05-26
GC0000413A (en) 2007-03-31
US6977064B1 (en) 2005-12-20
DE60142229D1 (de) 2010-07-08
KR20030022116A (ko) 2003-03-15
EP1284815A2 (de) 2003-02-26
EP1541226A3 (de) 2006-05-17
ES2345535T3 (es) 2010-09-27

Similar Documents

Publication Publication Date Title
EP1541226A3 (de) Vorrichtung zur kontrollierten und optimierten Zugabe von Reaktanten in kontinuierlichen Systemen und Verfahren zu dessen Verwendung
US5382741A (en) Process for the production of mono-olefins
CA2407831C (en) Process for the catalytic oxidation of hydrocarbons
CA2781762C (en) Catalytic oxidative dehydrogenation, and microchannel reactors for catalytic oxidative dehydrogenation
EP0656044B1 (de) Verfahren zur herstellung von monoolefinen
EP1899285B1 (de) Verfahren zur herstellung von ethylen
AU2001295190A1 (en) Process for the catalytic oxidation of hydrocarbons
Herguido et al. On the use of fluidized bed catalytic reactors where reduction and oxidation zones are present simultaneously
Schmidt et al. Partial oxidation of CH4 and C2H6 over noble metalcoated monoliths
Aartun et al. Temperature profiles and residence time effects during catalytic partial oxidation and oxidative steam reforming of propane in metallic microchannel reactors
AU2002213917A1 (en) Method for the dehydrogenation of hydrocarbons
US9433913B2 (en) Catalytic isobutane alkylation
CA2397719A1 (en) Method and reactor for autothermal dehydrogenation of hydrocarbons
CN113574009A (zh) 由通过催化部分氧化结合裂化制得的合成气生产甲醇的方法
Kerr et al. Vinyl esters as ethylene equivalents in the Khand annulation reaction
US20220332666A1 (en) Gas phase ozone-mediated selective oxidative dehydrogenation of alkanes
Lunsford et al. Steady-State production of olefins and aromatics in high yields from methane using an integrated recycle reaction system
Iskendirov et al. Methane oxidative coupling in the presence of hydrogen peroxide
AU1633397A (en) Process for preparing a heat treatment atmosphere and method for regulating said process