IN2014DN10387A - - Google Patents

Download PDF

Info

Publication number
IN2014DN10387A
IN2014DN10387A IN10387DEN2014A IN2014DN10387A IN 2014DN10387 A IN2014DN10387 A IN 2014DN10387A IN 10387DEN2014 A IN10387DEN2014 A IN 10387DEN2014A IN 2014DN10387 A IN2014DN10387 A IN 2014DN10387A
Authority
IN
India
Prior art keywords
pipes
reactor
plates
technical result
gas liquid
Prior art date
Application number
Inventor
Vladimir Vladimirovich Bushkov
Vladislav Sergeevich Stankevich
Original Assignee
Sibur Holding Public Joint Stock Co
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 Sibur Holding Public Joint Stock Co filed Critical Sibur Holding Public Joint Stock Co
Publication of IN2014DN10387A publication Critical patent/IN2014DN10387A/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J10/00Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • B01J19/006Baffles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/2415Tubular reactors
    • B01J19/2425Tubular reactors in parallel
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00074Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00081Tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00074Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00094Jackets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00164Controlling or regulating processes controlling the flow
    • B01J2219/00166Controlling or regulating processes controlling the flow controlling the residence time inside the reactor vessel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761Details of the reactor
    • B01J2219/00763Baffles
    • B01J2219/00765Baffles attached to the reactor wall
    • B01J2219/00777Baffles attached to the reactor wall horizontal
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24Stationary reactors without moving elements inside
    • B01J2219/2401Reactors comprising multiple separate flow channels

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The gas liquid reactor relates to the field of process equipment for the implementation of gas liquid processes and can be used in the chemical petrochemical and other industries. The technical result of the present invention is maximum target product output and a plug flow regime. A further technical result is increased convenience in using and maintaining the reactor. Another technical result is that the invention makes it possible to judge during the design stage and with high accuracy the geometrical parameters of the reactor and the effects thereof on the speed of the chemical process and the output of target product. The gas liquid reactor comprises a housing with pipes for the introduction of reagents and the removal of reaction products. The reactor housing contains a pipe bundle situated in such a way that the space between the pipes does not communicate with the internal volume of said pipes. The reactor housing is also provided with input and output pipes which communicate with the inter pipe space used for the supply of a coolant or heat carrier. A removable rod is installed in at least one of the pipes. Plates are attached to the rod each of which plates has at least one opening. The plates are arranged in such a way that the openings of neighboring plates are not coaxial in relation to one another.
IN10387DEN2014 2012-06-06 2013-06-05 IN2014DN10387A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU2012123526/05A RU2497567C1 (en) 2012-06-06 2012-06-06 Gas-fluid reactor
PCT/RU2013/000458 WO2013184034A2 (en) 2012-06-06 2013-06-05 Gas-liquid reactor

Publications (1)

Publication Number Publication Date
IN2014DN10387A true IN2014DN10387A (en) 2015-08-14

Family

ID=49682974

Family Applications (1)

Application Number Title Priority Date Filing Date
IN10387DEN2014 IN2014DN10387A (en) 2012-06-06 2013-06-05

Country Status (5)

Country Link
US (1) US9346033B2 (en)
CN (2) CN107224943A (en)
IN (1) IN2014DN10387A (en)
RU (1) RU2497567C1 (en)
WO (1) WO2013184034A2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2555557A (en) * 2016-05-10 2018-05-09 Continental automotive systems inc Oil separator for reducing residue deposits
CN107875995A (en) * 2016-09-29 2018-04-06 韩小凤 The relatively long gas-liquid partitioned reactor of liquid stream stroke
FR3096587B1 (en) * 2019-05-28 2021-06-11 Ifp Energies Now COMPARTMENTAL OLIGOMERIZATION REACTOR
CN112090388B (en) * 2020-09-07 2022-04-12 浙江大学 Continuous flow reactor and application thereof in chemical reaction and synthesis
CN113769678A (en) * 2021-10-22 2021-12-10 中国科学院上海硅酸盐研究所 Reaction device for synthesizing nano calcium carbonate by using carbon dioxide

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3230055A (en) * 1960-12-06 1966-01-18 Hans J Zimmer Apparatus for contacting liquid and gaseous reactants
GB1173302A (en) * 1966-07-20 1969-12-10 Rolls Royce Mixing Device and Mixing Method for Fluids
CN2145639Y (en) * 1993-02-17 1993-11-10 中国石油化工总公司 Tube-arranged reactor with externally combined meltal wire net tubes
CA2141886E (en) * 1994-05-11 1999-10-12 Federico Zardi Reactor for two-phase reactions, in particular for urea synthesis at high pressure and temperature
RU2102105C1 (en) * 1996-08-08 1998-01-20 Иван Петрович Слободяник Mass-transfer column
DE19801705A1 (en) * 1998-01-17 1999-07-22 Forschungszentrum Mittweida E Tubular reactor for potable water disinfection, process water sterilization and waste water decontamination
US6131891A (en) * 1998-03-30 2000-10-17 Uop Llc Fractionation column containing stacked fractionation trays
US6451268B1 (en) 1999-04-16 2002-09-17 Minerals Technologies Inc. Method and apparatus for continuous gas liquid reactions
RU2230593C2 (en) * 2000-07-25 2004-06-20 Юоп Ллк Rectifying column containing a panel of fractionating trays, a complete set of fractionating trays for installation in a column of fractional distillation and a method of installation of the fractionating trays in the column of fractional distillation
BY6340C1 (en) 2000-11-14 2004-06-30 Oao Grodno Azot Reactor of synthesis of carbamide
FR2830775B1 (en) * 2001-10-12 2004-08-27 Rhodia Polyamide Intermediates REACTOR FOR OXIDATION REACTION OF A LIQUID WITH A GAS
US7128885B2 (en) * 2002-12-23 2006-10-31 The Boc Group, Inc. NF3 production reactor
EA010067B1 (en) * 2004-12-20 2008-06-30 Асахи Касеи Кемикалз Корпорейшн Industrial evaporation apparatus
CN2937121Y (en) * 2006-08-11 2007-08-22 内蒙古海吉氯碱化工股份有限公司 Chloroethene reactor

Also Published As

Publication number Publication date
CN104507562A (en) 2015-04-08
CN107224943A (en) 2017-10-03
WO2013184034A3 (en) 2014-03-13
WO2013184034A2 (en) 2013-12-12
US20150231596A1 (en) 2015-08-20
RU2497567C1 (en) 2013-11-10
US9346033B2 (en) 2016-05-24

Similar Documents

Publication Publication Date Title
IN2014DN10387A (en)
EA201792299A1 (en) METHOD
WO2014128267A3 (en) Chemical vapour deposition device
WO2014183001A3 (en) Exhaust gas heat exchanger and method
RU2015142107A (en) METHOD AND DEVICE FOR PROTECTING INTERNAL SURFACES OF A PUMP BY AN ATOMIC-LAYER COATING
MX356160B (en) PROCESS and APPARATUS FOR ENDOTHERMIC REACTIONS.
WO2016100003A3 (en) Methods and apparatuses for co-processing pyrolysis oil
WO2015069762A3 (en) Chemical reactor with manifold for management of a flow of gaseous reaction medium thereto
MX2021006163A (en) Reactor system and process for wood modification.
TR201903355T4 (en) Method and apparatus for detecting a leak in at least one cooling device zone of an oven and an oven.
Tajik et al. Two dimensional CFD simulations of a flue-wall in the anode baking furnace for aluminum production
IN2014DN10774A (en)
NZ600415A (en) Charcoal manufacturing process and apparatus
CN203750475U (en) Ammonia gas and oxygen mixing device
CN204007234U (en) A kind of chemical industry hot gas cooler
WO2016089235A3 (en) Mechanism for production of hydrocarbon by pyrolysis of waste plastics and production method thereof
TR201908179T4 (en) Arrangement and process for recycling carbon and hydrocarbon from organic material by pyrolysis.
CN106017148A (en) Large-diameter quartz tube heat exchange equipment
MY185113A (en) Production method of ?-olefin oligomer
EA201500795A1 (en) REACTOR FOR PARTIAL OXIDATION OF HYDROCARBON GASES
MX2016002939A (en) Non-adiabatic catalytic reactor.
CA2951385C (en) Ozone generation device
IN2014KN01731A (en)
TN2014000019A1 (en) Gas/gas heat exchanger
CN205384237U (en) Device for measuring heavy oil coking trend