WO2010144297A3 - Multi-stage multi-tube shell-and-tube reactor - Google Patents

Multi-stage multi-tube shell-and-tube reactor Download PDF

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Publication number
WO2010144297A3
WO2010144297A3 PCT/US2010/037170 US2010037170W WO2010144297A3 WO 2010144297 A3 WO2010144297 A3 WO 2010144297A3 US 2010037170 W US2010037170 W US 2010037170W WO 2010144297 A3 WO2010144297 A3 WO 2010144297A3
Authority
WO
WIPO (PCT)
Prior art keywords
zones
reactor
tube
temperature control
stage
Prior art date
Application number
PCT/US2010/037170
Other languages
French (fr)
Other versions
WO2010144297A2 (en
Inventor
Yuon Chiu
Stephen A. Cottrell
Richard Durick Horwath
Haluk Kopkalli
Original Assignee
Honeywell International Inc.
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 Honeywell International Inc. filed Critical Honeywell International Inc.
Priority to EP10786590.9A priority Critical patent/EP2440318A4/en
Priority to KR1020117031137A priority patent/KR101826589B1/en
Priority to MX2011013226A priority patent/MX2011013226A/en
Priority to CN201080035128.1A priority patent/CN102458638B/en
Priority to JP2012514997A priority patent/JP5667624B2/en
Publication of WO2010144297A2 publication Critical patent/WO2010144297A2/en
Publication of WO2010144297A3 publication Critical patent/WO2010144297A3/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
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/06Chemical 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
    • B01J8/067Heating or cooling the reactor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16Heat-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
    • F28D7/163Heat-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
    • F28D7/1638Heat-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/0202Header boxes having their inner space divided by partitions
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/0265Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using guiding means or impingement means inside the header box
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212Plates; Jackets; Cylinders
    • B01J2208/00221Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212Plates; Jackets; Cylinders
    • B01J2208/0023Plates; Jackets; Cylinders with some catalyst tubes being empty, e.g. dummy tubes or flow-adjusting rods
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • F28F2009/222Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
    • F28F2009/226Transversal partitions
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2210/00Heat exchange conduits
    • F28F2210/08Assemblies of conduits having different features

Abstract

A multi-stage, multi-tube, shell-and-tube reactor which contains reaction zones and interstage temperature control (cooling/heating) zones in series. The reactor has at least two types of zones which both contribute to removing or supplying heat to the system depending on the system's need. The reactor will have a group of reaction zones which contain tubes packed with catalyst to progress the reaction and remove or supply heat simultaneously. There are also a number of interstage temperature control (cooling/heating) zones which are designed to supply or remove heat to or from the system. The positioning, number, and design of the zones will depend on the amount of temperature control desired and exothermic or endothermic nature of the processes to be conducted in the reactor.
PCT/US2010/037170 2009-06-09 2010-06-03 Multi-stage multi-tube shell-and-tube reactor WO2010144297A2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
EP10786590.9A EP2440318A4 (en) 2009-06-09 2010-06-03 Multi-stage multi-tube shell-and-tube reactor
KR1020117031137A KR101826589B1 (en) 2009-06-09 2010-06-03 Multi-Stage Multi-Tube Shell-and-Tube Reactor
MX2011013226A MX2011013226A (en) 2009-06-09 2010-06-03 Multi-stage multi-tube shell-and-tube reactor.
CN201080035128.1A CN102458638B (en) 2009-06-09 2010-06-03 Multi-stage multi-tube shell-and-tube reactor
JP2012514997A JP5667624B2 (en) 2009-06-09 2010-06-03 Multi-stage, multi-tube shell-and-tube reactor

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US12/481,107 US8034308B2 (en) 2009-06-09 2009-06-09 Multi-stage multi-tube shell-and-tube reactor
US12/481,107 2009-06-09

Publications (2)

Publication Number Publication Date
WO2010144297A2 WO2010144297A2 (en) 2010-12-16
WO2010144297A3 true WO2010144297A3 (en) 2011-03-03

Family

ID=43299914

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2010/037170 WO2010144297A2 (en) 2009-06-09 2010-06-03 Multi-stage multi-tube shell-and-tube reactor

Country Status (7)

Country Link
US (1) US8034308B2 (en)
EP (1) EP2440318A4 (en)
JP (1) JP5667624B2 (en)
KR (1) KR101826589B1 (en)
CN (1) CN102458638B (en)
MX (1) MX2011013226A (en)
WO (1) WO2010144297A2 (en)

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RU2539984C1 (en) * 2013-12-24 2015-01-27 Открытое акционерное общество Научно-исследовательский институт "Ярсинтез" (ОАО НИИ "Ярсинтез") Reactor with stationary layer of catalyst

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JP5777370B2 (en) * 2011-03-30 2015-09-09 三菱重工業株式会社 Reboiler
US8969634B2 (en) 2011-09-26 2015-03-03 Honeywell International Inc. Combination reactor system
JP5995447B2 (en) * 2012-01-17 2016-09-21 三菱重工業株式会社 Gasoline production equipment
EP2817389A4 (en) * 2012-02-21 2016-01-20 Ceramatec Inc Compact ft combined with micro-fibrous supported nano-catalyst
WO2013126341A1 (en) 2012-02-21 2013-08-29 Ceramatec, Inc. Compact fischer tropsch system with integrated primary and secondary bed temperature control
WO2014074458A1 (en) * 2012-11-06 2014-05-15 H R D Corporation Reactor and catalyst for converting natural gas to organic compounds
US9777965B2 (en) * 2013-03-15 2017-10-03 Thar Energy Llc Countercurrent heat exchanger/reactor
CN104061808B (en) * 2014-07-04 2016-08-17 大连海新工程技术有限公司 The horizontal shell-and-tube heat exchanger that medium is detained can be prevented
EP3218448A1 (en) 2014-11-14 2017-09-20 SABIC Global Technologies B.V. Multi stage fischer-tropsch reactor and methods of producing hydrocarbons
CN104567515B (en) * 2015-01-07 2016-03-16 无锡锡州机械有限公司 Stainless steel heat exchanger tube sheet unit
WO2017027491A1 (en) * 2015-08-10 2017-02-16 Primus Green Energy Inc. Multi-stage reactor and system for making methanol in a once-through process and methods therefor
KR101818442B1 (en) 2016-03-24 2018-01-16 한국과학기술연구원 shell-and-multi-triple concentric-tube reactor and heat exchanger
WO2018231764A1 (en) * 2017-06-12 2018-12-20 Honeywell International Inc. Method to produce hfo-1234yf from tcp by suppressing the bubble/dew point
US20200040259A1 (en) * 2018-08-03 2020-02-06 EnerSysNet U.S. Holdings, Inc. Biomass processing devices, systems, and methods
KR102575566B1 (en) * 2018-09-06 2023-09-07 퍼블릭 조인트 스톡 컴퍼니 “시부르 홀딩” Bubble shell-and-tube device
US11465951B2 (en) 2018-12-12 2022-10-11 Sabic Global Technologies B.V. Dimerization of cyclopentadiene using shell and tube heat exchanger
KR20220113351A (en) 2019-12-20 2022-08-12 엠. 테크닉 가부시키가이샤 flow reactor
JP6813234B1 (en) 2019-12-26 2021-01-13 エム・テクニック株式会社 Flow reactor
JP6813233B1 (en) 2019-12-26 2021-01-13 エム・テクニック株式会社 Heat exchanger
US11408688B2 (en) * 2020-06-17 2022-08-09 Mahle International Gmbh Heat exchanger
TW202237260A (en) * 2021-01-19 2022-10-01 美商科學設計有限公司 Tube to tube sheet welding for fabrication of vertical boiling reactor with reduced tube pitch

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Also Published As

Publication number Publication date
JP2012529626A (en) 2012-11-22
CN102458638A (en) 2012-05-16
CN102458638B (en) 2015-07-29
EP2440318A2 (en) 2012-04-18
US20100307726A1 (en) 2010-12-09
MX2011013226A (en) 2012-02-28
EP2440318A4 (en) 2016-10-05
US8034308B2 (en) 2011-10-11
WO2010144297A2 (en) 2010-12-16
KR20120036891A (en) 2012-04-18
KR101826589B1 (en) 2018-02-07
JP5667624B2 (en) 2015-02-12

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