EP0053248A2 - Echangeur de chaleur - Google Patents

Echangeur de chaleur Download PDF

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Publication number
EP0053248A2
EP0053248A2 EP81108203A EP81108203A EP0053248A2 EP 0053248 A2 EP0053248 A2 EP 0053248A2 EP 81108203 A EP81108203 A EP 81108203A EP 81108203 A EP81108203 A EP 81108203A EP 0053248 A2 EP0053248 A2 EP 0053248A2
Authority
EP
European Patent Office
Prior art keywords
tube
plates
jacket
hoods
inner tubes
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.)
Withdrawn
Application number
EP81108203A
Other languages
German (de)
English (en)
Other versions
EP0053248A3 (fr
Inventor
Heribert Dr. Kuerten
Hubert Puestel
Rudi Schulz
Georg Weber
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.)
BASF SE
Original Assignee
BASF SE
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 BASF SE filed Critical BASF SE
Publication of EP0053248A2 publication Critical patent/EP0053248A2/fr
Publication of EP0053248A3 publication Critical patent/EP0053248A3/fr
Withdrawn legal-status Critical Current

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Classifications

    • 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
    • F28F9/0246—Arrangements for connecting header boxes with flow lines
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/06—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation
    • C10G1/065—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation in the presence of a solvent
    • 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
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16—Heat-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
    • F28D7/1607—Heat-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 particular pattern of flow of the heat exchange media, e.g. change of flow direction
    • 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
    • F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates

Definitions

  • the present invention relates to a heat exchanger for use in coal hydrogenation plants at pressures from 200 to 700 bar and temperatures from 100 to 500 o C with a tube bundle arranged in a closed pressure vessel with tube-side inlet and outlet nozzles for the coal slurry and / or cycle gas, with shell-side Inlet and outlet nozzle for the heat-emitting circulating gas, in which the inner tubes are arranged between hoods closed by tube plates, and the hoods are connected by hood nozzles to the tube-side inlet and outlet nozzles for the pulp and / or the circulating gas.
  • the inner tubes have an outer diameter of 23 mm and an inner diameter of 14 mm. Under these conditions, it is possible to accommodate between 200 to 300 inner tubes arranged parallel to a tube bundle in a pressure vessel.
  • the hoods in the known designs are conical, the difference in thermal expansion between the tube bundle and the pressure vessel is absorbed by a stuffing box.
  • the known design has several disadvantages. For example, the conical hoods take up even more dead space with larger diameters than with diameters that were customary in the past.
  • the coal slurry and the cycle gas, which are guided around the pipes in the known constructions, can be of diameters. Do not distribute larger than 600 mm evenly over the entire cross-section of the jacket space.
  • baffles when driving with pulp and circulating gas around the pipes: this is disadvantageous in two respects.
  • the heat transfer coefficient becomes smaller than that of one cross flow achieved by chicane, and on the other hand the stability of the inner tubes is jeopardized by vibrations, the risk of vibrations can only be partially contained by installing inner tubes with a wall thickness of 4.5 mm and an outer diameter of 23 mm. In addition, it cannot be avoided that leaks occur on the stuffing box.
  • the hood connections are connected to the pipe-side inlet and outlet connections for the coal slurry and / or the cycle gas via weld seams.
  • a hood is arranged as an impact body at a distance of 500 to 1,000 mm from the jacket-side inlet connection.
  • the advantages achieved by the invention are, above all, that larger diameters can be used to save material. Damaged or clogged bundles can be installed and removed faster than with the previously known construction.
  • the arrangement of baffles on the jacket side increases the heat transfer and avoids the risk of vibrations of the inner tubes.
  • the installation of an expansion adapter prevents the pulp and / or circulating gas flowing on the pipe side from mixing with the circulating gas which emits heat and the jacket side.
  • FIG. 1 shows a longitudinal section through a heat exchanger according to the invention
  • FIG. 2 shows an enlarged partial view of this heat exchanger.
  • a tube bundle is arranged in a pressure vessel, consisting of a cylindrical jacket 1 with a flanged jacket hood 2, and a welded-on jacket 3, a tube bundle is arranged.
  • This tube bundle in turn consists of inner tubes 4, which are welded into tube plates 5 and 6.
  • the hoods 7 and 8 seal the coal pulp flowing on the pipe side and / or the circulating gas.
  • a hood connector 9 connects the hood 7 to the pipe-side outlet connector 11.
  • a hood connector 10 connects the hood 8 to the pipe-side inlet connector 12.
  • the welded connection between the hood connector 9, 10 and the outlet and inlet connector is shown in FIG.
  • the tube bundle contains baffle plates on the jacket side, which consist either of alternately arranged ring plates 13 and discs 14.
  • baffle plates which is not shown, but is used for horizontal heat exchangers, consists of circular sections.
  • the baffle plates are fastened with tie rods 15 to one of the two plates 5, 6.
  • the jacket 1 and the tube bundle have different wall temperatures during operation, and they also consist of materials with different coefficients of thermal expansion; therefore an expansion compensation intermediate piece 16 is installed in the hood connector 9 or 10.
  • the jacket-side inlet connector 17 is arranged so that the flow pulse is deflected with the hood 7.
  • Jacket-side inlet and outlet nozzles 18 can be rotated according to the requirements of the pipe routing as desired on a width circle of the spherical jacket hood.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Paper (AREA)
EP81108203A 1980-11-28 1981-10-12 Echangeur de chaleur Withdrawn EP0053248A3 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3044902 1980-11-28
DE19803044902 DE3044902A1 (de) 1980-11-28 1980-11-28 Waermeaustauscher

Publications (2)

Publication Number Publication Date
EP0053248A2 true EP0053248A2 (fr) 1982-06-09
EP0053248A3 EP0053248A3 (fr) 1982-11-24

Family

ID=6117847

Family Applications (1)

Application Number Title Priority Date Filing Date
EP81108203A Withdrawn EP0053248A3 (fr) 1980-11-28 1981-10-12 Echangeur de chaleur

Country Status (5)

Country Link
EP (1) EP0053248A3 (fr)
JP (1) JPS57117787A (fr)
AU (1) AU7794981A (fr)
DE (1) DE3044902A1 (fr)
ZA (1) ZA818241B (fr)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1712867A1 (fr) * 2005-04-08 2006-10-18 Balcke-Dürr GmbH Procédé permettant de joindre un tube avec une plaque tubulaire
KR100773680B1 (ko) * 2000-05-16 2007-11-05 킴벌리-클라크 월드와이드, 인크. 의류 측면 패널의 제공 및 접합
FR2939058A1 (fr) * 2008-12-03 2010-06-04 Air Liquide Procede de soudage de piquages tubulaires sur un reservoir ou analogue
US10684077B2 (en) 2015-04-24 2020-06-16 Hexsol Italy Srl Tube-nest heat exchanger with improved structure
CN112013037A (zh) * 2020-08-31 2020-12-01 东风商用车有限公司 一种离合器壳体的散热结构
CN112105515A (zh) * 2018-03-23 2020-12-18 摩丁制造公司 容许高压的液体-制冷剂热交换器

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10312788A1 (de) 2003-03-21 2004-09-30 Behr Gmbh & Co. Kg Abgaswärmetauscher und Dichteinrichtung für Abgaswärmetauscher
CN117646838B (zh) * 2024-01-29 2024-04-05 无锡佳龙换热器股份有限公司 一种套管换热器用的内外管柔性接头

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE449817A (fr) *
DE962171C (de) * 1953-12-12 1957-04-18 Basf Ag Waermetauscher
FR87777E (fr) * 1964-04-16 1966-02-11 Schmidt Sche Heissdampf échangeur de température, notamment pour le refroidissement de gaz sortant de craquage ou autres
DE1263969B (de) * 1965-03-19 1968-03-21 Hoesch Ag Prallverteiler fuer eine Kugelregenanlage
DE2341808A1 (de) * 1973-05-29 1975-01-02 Fbm Cost Mecc Spa Verfahren zur herstellung von waermetauschern
DE2330015A1 (de) * 1973-06-13 1975-01-09 Uhde Gmbh Friedrich Heissgaswaermetauscher mit verbundrohren
FR2345665A1 (fr) * 1976-03-22 1977-10-21 Kraftwerk Union Ag Generateur de vapeur pour reacteurs nucleaires a eau pressurisee

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE449817A (fr) *
DE962171C (de) * 1953-12-12 1957-04-18 Basf Ag Waermetauscher
FR87777E (fr) * 1964-04-16 1966-02-11 Schmidt Sche Heissdampf échangeur de température, notamment pour le refroidissement de gaz sortant de craquage ou autres
DE1263969B (de) * 1965-03-19 1968-03-21 Hoesch Ag Prallverteiler fuer eine Kugelregenanlage
DE2341808A1 (de) * 1973-05-29 1975-01-02 Fbm Cost Mecc Spa Verfahren zur herstellung von waermetauschern
DE2330015A1 (de) * 1973-06-13 1975-01-09 Uhde Gmbh Friedrich Heissgaswaermetauscher mit verbundrohren
FR2345665A1 (fr) * 1976-03-22 1977-10-21 Kraftwerk Union Ag Generateur de vapeur pour reacteurs nucleaires a eau pressurisee

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100773680B1 (ko) * 2000-05-16 2007-11-05 킴벌리-클라크 월드와이드, 인크. 의류 측면 패널의 제공 및 접합
EP1712867A1 (fr) * 2005-04-08 2006-10-18 Balcke-Dürr GmbH Procédé permettant de joindre un tube avec une plaque tubulaire
FR2939058A1 (fr) * 2008-12-03 2010-06-04 Air Liquide Procede de soudage de piquages tubulaires sur un reservoir ou analogue
US10684077B2 (en) 2015-04-24 2020-06-16 Hexsol Italy Srl Tube-nest heat exchanger with improved structure
CN112105515A (zh) * 2018-03-23 2020-12-18 摩丁制造公司 容许高压的液体-制冷剂热交换器
CN112105515B (zh) * 2018-03-23 2023-10-24 摩丁制造公司 容许高压的液体-制冷剂热交换器
CN112013037A (zh) * 2020-08-31 2020-12-01 东风商用车有限公司 一种离合器壳体的散热结构

Also Published As

Publication number Publication date
EP0053248A3 (fr) 1982-11-24
AU7794981A (en) 1982-06-03
ZA818241B (en) 1983-07-27
JPS57117787A (en) 1982-07-22
DE3044902A1 (de) 1982-07-08

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PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

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Owner name: RIT.TO ALL'OEB ALLO STATO DI DOMANDA;ING. C. GREGO

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Effective date: 19840924

RIN1 Information on inventor provided before grant (corrected)

Inventor name: WEBER, GEORG

Inventor name: SCHULZ, RUDI

Inventor name: PUESTEL, HUBERT

Inventor name: KUERTEN, HERIBERT, DR.