EA200901294A1 - Система и способ получения хлорбензола (варианты) - Google Patents

Система и способ получения хлорбензола (варианты)

Info

Publication number
EA200901294A1
EA200901294A1 EA200901294A EA200901294A EA200901294A1 EA 200901294 A1 EA200901294 A1 EA 200901294A1 EA 200901294 A EA200901294 A EA 200901294A EA 200901294 A EA200901294 A EA 200901294A EA 200901294 A1 EA200901294 A1 EA 200901294A1
Authority
EA
Eurasian Patent Office
Prior art keywords
high shear
chlorobenzene
chlorbenzen
options
obtaining
Prior art date
Application number
EA200901294A
Other languages
English (en)
Other versions
EA017547B1 (ru
Inventor
Аббас Хассан
Ибрагим Багхерзадех
Райфорд Г. Энтони
Грегори Босинге
Азиз Хассан
Original Assignee
ЭйчАДи КОПЭРЕЙШН
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 ЭйчАДи КОПЭРЕЙШН filed Critical ЭйчАДи КОПЭРЕЙШН
Publication of EA200901294A1 publication Critical patent/EA200901294A1/ru
Publication of EA017547B1 publication Critical patent/EA017547B1/ru

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
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
    • B01F27/271—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
    • B01F27/2711—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator provided with intermeshing elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80—Mixing plants; Combinations of mixers
    • B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80—Mixing plants; Combinations of mixers
    • B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
    • B01F33/811—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles in two or more consecutive, i.e. successive, mixing receptacles or being consecutively arranged
    • 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
    • B01J19/0053—Details of the reactor
    • B01J19/0066—Stirrers
    • 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
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/1806—Stationary reactors having moving elements inside resulting in a turbulent flow of the reactants, such as in centrifugal-type reactors, or having a high Reynolds-number
    • 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
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising 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
    • 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
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • B01J8/222—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid in the presence of a rotating device only
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00—Preparation of halogenated hydrocarbons
    • C07C17/093—Preparation of halogenated hydrocarbons by replacement by halogens
    • C07C17/10—Preparation of halogenated hydrocarbons by replacement by halogens of hydrogen atoms
    • C07C17/12—Preparation of halogenated hydrocarbons by replacement by halogens of hydrogen atoms in the ring of aromatic compounds
    • 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
    • B01J2219/00004—Scale aspects
    • B01J2219/00006—Large-scale industrial plants
    • 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
    • B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00083—Coils
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761—Details of the reactor
    • B01J2219/00763—Baffles
    • B01J2219/00779—Baffles attached to the stirring means

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

Использование механического устройства высокой скорости сдвига при получении хлорбензола позволяет уменьшить влияние ограничений, связанных с массопереносом в ходе реакции, и тем самым улучшить способ получения хлорбензола. Система получения хлорбензола из бензола и хлора содержит реактор и внешнее устройство высокой скорости сдвига, выход которого связан текучей средой с входом реактора, устройство высокой скорости сдвига способно создать эмульсию пузырьков газообразного хлора в жидком бензоле.
EA200901294A 2007-06-27 2008-06-13 Система и способ получения хлорбензола (варианты) EA017547B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US94652407P 2007-06-27 2007-06-27
PCT/US2008/066904 WO2009002732A1 (en) 2007-06-27 2008-06-13 High shear process for the production of chlorobenzene

Publications (2)

Publication Number Publication Date
EA200901294A1 true EA200901294A1 (ru) 2010-02-26
EA017547B1 EA017547B1 (ru) 2013-01-30

Family

ID=40161416

Family Applications (1)

Application Number Title Priority Date Filing Date
EA200901294A EA017547B1 (ru) 2007-06-27 2008-06-13 Система и способ получения хлорбензола (варианты)

Country Status (4)

Country Link
US (2) US20090005619A1 (ru)
EP (1) EP2132159A4 (ru)
EA (1) EA017547B1 (ru)
WO (1) WO2009002732A1 (ru)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8304584B2 (en) 2007-06-27 2012-11-06 H R D Corporation Method of making alkylene glycols
US8394861B2 (en) * 2007-06-27 2013-03-12 Hrd Corporation Gasification of carbonaceous materials and gas to liquid processes
US8282266B2 (en) 2007-06-27 2012-10-09 H R D Corporation System and process for inhibitor injection
US7491856B2 (en) 2007-06-27 2009-02-17 H R D Corporation Method of making alkylene glycols
US20090005619A1 (en) 2007-06-27 2009-01-01 H R D Corporation High shear process for the production of chlorobenzene
EP2542336B1 (en) * 2010-03-05 2016-11-23 H R D Corporation High shear process for the production of halogenated and/or sulfonated paraffins
US9493709B2 (en) 2011-03-29 2016-11-15 Fuelina Technologies, Llc Hybrid fuel and method of making the same
AU2015358565B2 (en) 2014-12-03 2020-11-05 Drexel University Direct incorporation of natural gas into hydrocarbon liquid fuels
CN108484351B (zh) * 2018-04-19 2020-10-30 北京阳光欣禾科技有限公司 一种生产氯代环己烷的高效氯化反应工艺方法
WO2020212542A1 (en) * 2019-04-17 2020-10-22 Shell Internationale Research Maatschappij B.V. Stirred injection mixing process
CN110142010B (zh) * 2019-05-27 2021-09-17 河北鸿新源化工有限公司 以芳香族化合物氯化反应生产多氯芳香族化合物的生产方法及生产装置

Family Cites Families (50)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3654107A (en) * 1968-01-18 1972-04-04 Atlantic Richfield Co Process for chlorination of saturated hydrocarbons
US3984484A (en) * 1968-02-09 1976-10-05 Hooker Chemicals & Plastics Corporation Distillation in Raschig-phenol process
US3887167A (en) * 1971-02-09 1975-06-03 Du Pont Apparatus for manufacture of organic isocyanates
US3781320A (en) * 1971-02-09 1973-12-25 Du Pont Process for manufacture of organic isocyanates
US4329525A (en) * 1978-02-21 1982-05-11 The Lummus Company Production of chlorinated compounds by use of molten salts
US4886905A (en) * 1981-01-30 1989-12-12 Eastman Kodak Company Preparation of ethyl acetate
DE3132692A1 (de) * 1981-08-19 1983-03-17 Bayer Ag, 5090 Leverkusen Verfahren zur halogenierung von organischen verbindungen
JPS61172837A (ja) * 1985-01-28 1986-08-04 Ihara Chem Ind Co Ltd 核ハロゲン化置換ベンゼン類の製造方法
JPS61183235A (ja) * 1985-02-12 1986-08-15 Hodogaya Chem Co Ltd クロロベンゼンの製造方法
NL8702735A (nl) * 1987-11-17 1989-06-16 Dorr Oliver Inc Werkwijze voor het weken van granen met een nieuw enzympreparaat.
US4950831A (en) * 1989-09-28 1990-08-21 Ethyl Corporation Coupling process
US5009816A (en) * 1990-04-26 1991-04-23 Union Carbide Industrial Gases Technology Corporation Broad liquid level gas-liquid mixing operations
US5279463A (en) * 1992-08-26 1994-01-18 Holl Richard A Methods and apparatus for treating materials in liquids
US5264087A (en) * 1992-10-13 1993-11-23 Eastman Kodak Company Method for refining acetic anhydride by distillation
US5382358A (en) * 1993-03-24 1995-01-17 Yeh; George C. Apparatus for dissolved air floatation and similar gas-liquid contacting operations
US5451348A (en) * 1994-04-18 1995-09-19 Praxair Technology, Inc. Variable liquid level eductor/impeller gas-liquid mixing apparatus and process
DE4428018A1 (de) * 1994-08-08 1996-02-15 Bayer Ag Verfahren zur Herstellung von aromatischen Aminen
US6194625B1 (en) * 1994-09-30 2001-02-27 Stratco, Inc. Alkylation by controlling olefin ratios
KR19980702782A (ko) * 1995-03-09 1998-08-05 혼 마가렛 에이. 녹말 액화 방법
US5710355A (en) * 1996-06-10 1998-01-20 Occidental Chemical Corporation Method of making chlorobenzenes
CA2201224C (en) 1997-03-27 2004-12-07 Annette Lynn Burke Dual shear mixing element
US6383237B1 (en) * 1999-07-07 2002-05-07 Deborah A. Langer Process and apparatus for making aqueous hydrocarbon fuel compositions, and aqueous hydrocarbon fuel compositions
US6368367B1 (en) * 1999-07-07 2002-04-09 The Lubrizol Corporation Process and apparatus for making aqueous hydrocarbon fuel compositions, and aqueous hydrocarbon fuel composition
US6368366B1 (en) * 1999-07-07 2002-04-09 The Lubrizol Corporation Process and apparatus for making aqueous hydrocarbon fuel compositions, and aqueous hydrocarbon fuel composition
EP0990638A1 (en) * 1998-10-01 2000-04-05 Kvaerner Process Technology Limited Process
JP2000143706A (ja) 1998-11-10 2000-05-26 Mitsubishi Chemicals Corp α−オレフィン重合体の製造方法
US6251289B1 (en) * 1999-06-03 2001-06-26 Grt, Inc. Treatment of contaminated liquids with oxidizing gases and liquids
US6742774B2 (en) * 1999-07-02 2004-06-01 Holl Technologies Company Process for high shear gas-liquid reactions
US6471392B1 (en) * 2001-03-07 2002-10-29 Holl Technologies Company Methods and apparatus for materials processing
US7538237B2 (en) * 1999-07-02 2009-05-26 Kreido Laboratories Process for high shear gas-liquid reactions
US6827749B2 (en) * 1999-07-07 2004-12-07 The Lubrizol Corporation Continuous process for making an aqueous hydrocarbon fuel emulsions
US6530964B2 (en) 1999-07-07 2003-03-11 The Lubrizol Corporation Continuous process for making an aqueous hydrocarbon fuel
CZ292620B6 (cs) * 1999-10-14 2003-11-12 Sulzer Chemtech Ltd. Způsob výroby etylacetátu a zařízení k provádění tohoto způsobu
US6768021B2 (en) * 1999-12-22 2004-07-27 Celanese International Corporation Process improvement for continuous ethyl acetate production
JP2002003505A (ja) 2000-06-20 2002-01-09 Japan Polychem Corp α−オレフィン重合体の製造方法
JP4306943B2 (ja) 2000-10-13 2009-08-05 電気化学工業株式会社 エチレン−酢酸ビニル系共重合体エマルジョン組成物
GB0202065D0 (en) * 2002-01-30 2002-03-13 Watson Brown Hsm Ltd Mixing
US7098360B2 (en) * 2002-07-16 2006-08-29 Kreido Laboratories Processes employing multiple successive chemical reaction process steps and apparatus therefore
WO2004025260A2 (en) * 2002-09-11 2004-03-25 Kreido Laboratories Methods and apparatus for high-shear mixing and reacting of materials
US6787036B2 (en) * 2003-01-21 2004-09-07 Fbc Technologies, Inc. Method and apparatus for aerating wastewater
TW200504093A (en) 2003-05-12 2005-02-01 Dow Global Technologies Inc Polymer composition and process to manufacture high molecular weight-high density polyethylene and film therefrom
US6868366B1 (en) * 2003-09-16 2005-03-15 General Electric Company Method for measuring piping forces acting on a turbine casing
US20080260902A1 (en) 2004-04-21 2008-10-23 Michael Van Houten Process for Increasing Throughput of Corn for Oil Extraction
CA2507897A1 (en) 2004-06-07 2005-12-07 Dover Chemical Corporation High shear process for making metallic esters
US7276126B2 (en) * 2005-06-03 2007-10-02 Tate And Lyle Ingredients Americas, Inc. Production of enzyme-resistant starch by extrusion
WO2007023864A1 (ja) 2005-08-24 2007-03-01 Nsi Co., Ltd. 泡発生装置
US7935840B2 (en) * 2006-02-21 2011-05-03 Nextgen Fuel, Inc. Method for continuous production of biodiesel fuel
MX2008012883A (es) * 2006-04-11 2008-10-13 Basf Se Proceso continuo para realizar una reaccion quimica en la que una fase gaseosa se añade a una corriente de carga que comprende una o mas fases solidas que se han disuelto o dispersado en agua.
US20090005619A1 (en) * 2007-06-27 2009-01-01 H R D Corporation High shear process for the production of chlorobenzene
CN102026716B (zh) * 2008-07-03 2014-07-09 Hrd有限公司 高剪切旋转固定床反应器

Also Published As

Publication number Publication date
WO2009002732A1 (en) 2008-12-31
US20100183486A1 (en) 2010-07-22
EA017547B1 (ru) 2013-01-30
EP2132159A1 (en) 2009-12-16
US20090005619A1 (en) 2009-01-01
US8771605B2 (en) 2014-07-08
EP2132159A4 (en) 2012-10-24

Similar Documents

Publication Publication Date Title
EA200901294A1 (ru) Система и способ получения хлорбензола (варианты)
EA200901478A1 (ru) Система и способ получения циклогексана
EA201490136A1 (ru) Способ и устройство для ферментации синтез-газа коэффициентом массопереноса
CO7160038A2 (es) Un método y dispositivo de control de flujo
EA201591264A1 (ru) Реактор с мешалкой
EP2679284A3 (en) Chemical oxygen generator with bimetal reaction control
EA201391446A1 (ru) Газ высокого давления для жидкостного процесса
TWD153161S (zh) 脫氣供氣模組
BRPI0520513A2 (pt) sistema e método para realização de experimentos quìmicos paralelos
BR102012029292A8 (pt) Métodos de cimentar uma coluna tubular em um poço, em um poço submarino e em um poço que se estende de uma cabeça de poço
EA201390028A1 (ru) Находящаяся под давлением колонна для разделения газов и способ регенерирования газа конечной переработки высокого давления
EA200870587A1 (ru) Способ и реактор для получения углеродных нановолокон
MX2021006163A (es) Sistema de reactor y proceso para la modificacion de madera.
AR066574A1 (es) Un sistema reactor, un proceso de produccion de oxido de olefina 1,2-diol 1,2-diol eter , 1,2-carbonato o alcanolamina
GB2478460B (en) Molten salt treatment system and process
BR112012008012A2 (pt) método e sistema para cultivar algas.
JP2012510635A5 (ru)
CN106608811A (zh) 一种采用微通道反应器制备氯丙烷的方法
WO2016020692A3 (en) Apparatus and method for water treatment by an advanced oxidation process
EA200901479A1 (ru) Система и способ получения гидроперекиси кумола
EA200901293A1 (ru) Система и способ получения циклогексанола (варианты)
MY164751A (en) Subsea compression assembly
CO6680680A2 (es) Sistema de reactor químico y método que utiliza una bomba de turbina regenerativa para producir gas combustible
EA200901224A1 (ru) Система и способ получения уксусного ангидрида
WO2006049897A3 (en) Gravity pressure vessel and related apparatus and methods

Legal Events

Date Code Title Description
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM AZ BY KZ KG MD TJ TM RU