KR840004571A - Tube Sheet of Gasification System Heat Exchanger - Google Patents

Tube Sheet of Gasification System Heat Exchanger Download PDF

Info

Publication number
KR840004571A
KR840004571A KR1019830002024A KR830002024A KR840004571A KR 840004571 A KR840004571 A KR 840004571A KR 1019830002024 A KR1019830002024 A KR 1019830002024A KR 830002024 A KR830002024 A KR 830002024A KR 840004571 A KR840004571 A KR 840004571A
Authority
KR
South Korea
Prior art keywords
chamber
heat exchanger
inlet
tube
tube sheet
Prior art date
Application number
KR1019830002024A
Other languages
Korean (ko)
Inventor
안토니 리라트 죤
Original Assignee
알. 피. 와그너
웨스팅하우스 일렉트릭 코오포레이숀
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 알. 피. 와그너, 웨스팅하우스 일렉트릭 코오포레이숀 filed Critical 알. 피. 와그너
Publication of KR840004571A publication Critical patent/KR840004571A/en

Links

Classifications

    • 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
    • F28D3/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/48—Apparatus; Plants
    • C10J3/485—Entrained flow gasifiers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/723—Controlling or regulating the gasification process
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/86—Other features combined with waste-heat boilers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02—Header boxes; End plates
    • F28F9/0229—Double end plates; Single end plates with hollow spaces
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
    • C10J2300/1861—Heat exchange between at least two process streams
    • C10J2300/1892—Heat exchange between at least two process streams with one stream being water/steam

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Industrial Gases (AREA)

Abstract

내용 없음No content

Description

기체화 시스템 열교환기의 튜브쉬트Tube Sheet of Gasification System Heat Exchanger

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

제1도는 기술적 수준에 따르는 냉각 튜브쉬트 열교환기의 수평단면도.1 is a horizontal sectional view of a cooling tube sheet heat exchanger according to the technical level.

제2도는 본 발명에 따르는 냉각되고 압력이 균등한 튜브쉬트 열교환기의 수평단면도.2 is a horizontal cross-sectional view of a cooled and pressure uniform tube sheet heat exchanger according to the present invention.

제3도는 본 발명에 따르는 제거할 수 있고 냉각되고 압력이 균등한 튜브쉬트 열교환기의 수평단면도.3 is a horizontal cross-sectional view of a removable, cooled, pressure-uniform tubesheet heat exchanger according to the present invention.

Claims (6)

제1, 제2튜브쉬트(56,60)가 양쪽으로 가로질러 뻗어 있으며 미세하게 분산된 입자들이 함유된 유체 입구실과 출구실이 있는 동체(52,109), 상기 동체(52,109)내의 튜브 쉬트(56,60)사이에 지지되어 있는 많은 튜브들, 상기 제1, 제2튜브 쉬트간의 공간을 상기 동체(52)의 입구끝에 인접한 제1실과 출구끝에 인접한 제2실로 나누기 위해 상기 제1튜브 쉬트(56)로부터의 공간을 제외한 인접부근의 상기 동체(52)를 가로질러 뻗어있는 제3튜브 쉬트(60), 상기 임구실에 결합되어 유체를 함유하는 상기 미세분산입자를 상기 입구실로 들어오게 하고(상기 입구실로 부터의 흐름은 상기 튜브(62)를 지나 출구실로 통한다)유체를 함유하는 상기 미세분산입자와 의열교환관계에 있어서 냉각유체가 상기 제2실을 통해 흐르게 하고 완충유체가 상기 제1실을 통해 전도되게 하는 입구수단, 상기 입구와 상기 제1실간에 설치되어 상기 제1튜브 쉬트(56)를 가로지르는 압력차를 감소시키는 압력 균등수단(84,86)으로 구성됨을 특징으로 하며 연마성 미세분산입자를 운반하는 기체에 대한 열교환기.First and second tube sheets 56 and 60 extend across both sides of the body 52 and 109 with fluid inlet and outlet chambers containing finely dispersed particles, and tube sheets 56 within the body 52 and 109. 60, the first tube sheet 56 for dividing the space between the plurality of tubes, the first and second tube sheets, into a first chamber adjacent to the inlet end of the fuselage 52 and a second chamber adjacent to the outlet end. A third tube sheet 60 extending across the fuselage 52 in the vicinity of the vicinity except for the space therefrom, the microdispersed particles containing fluid being introduced into the inlet chamber and entering the inlet chamber (the inlet; The flow from the chamber passes through the tube 62 to the outlet chamber. In a heat exchange relationship with the microdispersion particles containing the fluid, a cooling fluid flows through the second chamber and a buffer fluid flows through the first chamber. Inversion However, it is provided between the inlet and the first chamber is characterized in that it consists of pressure equalization means (84,86) for reducing the pressure difference across the first tube sheet (56) and to carry abrasive microdispersion particles Heat exchanger for gas. 제1항에 있어서, 상기 균등 수단(84,86)이 상기 제1실과 상기 입구실에 상호 연결되고 파동 탱크(84)를 포함하는 도관(86)으로 구성됨을 특징으로 하는 열교환기.2. Heat exchanger according to claim 1, characterized in that the equalizing means (84,86) consist of conduits (86) interconnected to the first chamber and the inlet chamber and comprising a wave tank (84). 제1항내지 제2항에 있어서, 제3튜브 쉬트(123)가 상기 제1실과 제2실사이에 제3실을 형성하기 위해 상기 제3튜브 쉬트(119)로 부터의 공간을 제외한 인접부근의 상기 동체(109)를 가로질러 뻗어 있음을 특징으로 하는 열교환기.The method according to any one of claims 1 to 2, wherein the third tube sheet 123 is adjacent to each other except the space from the third tube sheet 119 to form a third chamber between the first chamber and the second chamber. Heat exchanger extending across said body (109). 제3항에 있어서, 상기 입구실과 상기 제3실사이의 제2압력균등 수단을 특징으로 하는 열교환기.4. A heat exchanger as claimed in claim 3, characterized in that a second pressure equalization means between said inlet chamber and said third chamber. 제3항내지 제4항에 있어서, 일렬로 배열된 제1, 제2튜브세트(121,127)로 구성되며 상기 제3실에서 분리될 수 있는 상기 튜브들과 상기 제3실을 통해 뻗어있는 단에서 필수적으로 분리될 수 있는 상기 동체(109)를 특징으로 하는 열교환기.5. The stage according to claim 3, wherein the tube comprises first and second tube sets 121 and 127 arranged in a row and extends through the third chamber and the tubes that can be separated from the third chamber. A heat exchanger characterized by the body 109 which can be essentially separated. 제1항내지 제5항중 어느 한항에 있어서, 펌프(80,105)와 상기 완충유체를 냉각시키는 열교환기(78,153)를 구성하는 흐름회로인 상기 완충유체 전도수단을 특징으로 하는 열교환기.6. The heat exchanger according to any one of claims 1 to 5, wherein said buffer fluid conduction means is a flow circuit constituting a pump (80,105) and a heat exchanger (78,153) for cooling said buffer fluid. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019830002024A 1982-05-11 1983-05-11 Tube Sheet of Gasification System Heat Exchanger KR840004571A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US37723082A 1982-05-11 1982-05-11
US377,230 1989-07-06

Publications (1)

Publication Number Publication Date
KR840004571A true KR840004571A (en) 1984-10-22

Family

ID=23488269

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019830002024A KR840004571A (en) 1982-05-11 1983-05-11 Tube Sheet of Gasification System Heat Exchanger

Country Status (7)

Country Link
EP (1) EP0094097A3 (en)
JP (1) JPS58205085A (en)
KR (1) KR840004571A (en)
AU (1) AU1397883A (en)
CA (1) CA1196909A (en)
ES (1) ES8404502A1 (en)
ZA (1) ZA833020B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2659849B2 (en) * 1990-05-30 1997-09-30 三菱重工業株式会社 Pressurized gasifier
MY147234A (en) * 2006-04-12 2012-11-14 Shell Int Research Apparatus and process for cooling hot gas
JP2017156025A (en) * 2016-03-02 2017-09-07 東京電力ホールディングス株式会社 Heat exchange system

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR485126A (en) * 1916-04-26 1917-12-13 Oerlikon Maschf Tubular heat exchanger
US2862694A (en) * 1956-01-06 1958-12-02 Phillips Petroleum Co Heat exchanger
FR1405960A (en) * 1964-06-03 1965-07-16 D Applic Mecaniques Soc Ind Sealing device, applicable to tubular surface exchangers
US3312063A (en) * 1965-07-22 1967-04-04 James H Anderson Heat transfer at equalized pressure
GB1098550A (en) * 1965-10-04 1968-01-10 Commissariat Energie Atomique Method and device for providing protection against scale formation
GB1212526A (en) * 1967-06-15 1970-11-18 Foster Wheeler Brown Boilers Improvements in shell and tube heat exchangers
FR2247691A1 (en) * 1973-10-11 1975-05-09 Fives Cail Babcock Series flow through reheater hairpins improves efficiency - HP steam of reactor passes through longer hairpin bank thence inner rank

Also Published As

Publication number Publication date
ES522237A0 (en) 1984-04-16
ZA833020B (en) 1984-05-30
CA1196909A (en) 1985-11-19
JPS58205085A (en) 1983-11-29
EP0094097A2 (en) 1983-11-16
AU1397883A (en) 1983-11-17
ES8404502A1 (en) 1984-04-16
EP0094097A3 (en) 1984-05-09

Similar Documents

Publication Publication Date Title
US3537513A (en) Three-fluid heat exchanger
US2411097A (en) Heat exchanger
US2384714A (en) Tubular heat exchanger
JPS61114093A (en) Heat exchanger
US3483920A (en) Heat exchangers
KR840004538A (en) Seawater desalination unit
JPS5623700A (en) Heat exchanger
JPS6319794B2 (en)
US3670522A (en) Exchanger for cooling fluids
JPS56136973U (en)
US2864588A (en) Heat transfer method
GB1016725A (en) Heat exchangers for cooling liquids by means of gas coolants
US2537276A (en) Heat exchanger
JPS5841440B2 (en) Tube group heat exchanger
KR840004571A (en) Tube Sheet of Gasification System Heat Exchanger
US1916768A (en) Heat exchanger
EP0066425A3 (en) A heat exchanger
JPS5773392A (en) Corrugated fin type heat exchanger
US3307614A (en) Falling film type evaporators and method
US2578059A (en) Heat interchanger
US2608387A (en) Fractional distillation apparatus
US3811663A (en) Intimate gas-liquid contact method and apparatus
GB1336820A (en) Cooler for dust-laden air or gases
US3318375A (en) Block-type heat exchanger
GB721870A (en) Improvements in or relating to heat exchange apparatus

Legal Events

Date Code Title Description
WITB Written withdrawal of application