EP0377089A1 - Echangeur de chaleur, particulièrement pour refroidir du gaz de craquage - Google Patents

Echangeur de chaleur, particulièrement pour refroidir du gaz de craquage Download PDF

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Publication number
EP0377089A1
EP0377089A1 EP89119375A EP89119375A EP0377089A1 EP 0377089 A1 EP0377089 A1 EP 0377089A1 EP 89119375 A EP89119375 A EP 89119375A EP 89119375 A EP89119375 A EP 89119375A EP 0377089 A1 EP0377089 A1 EP 0377089A1
Authority
EP
European Patent Office
Prior art keywords
heat exchanger
rings
tube
gas
inlet
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.)
Granted
Application number
EP89119375A
Other languages
German (de)
English (en)
Other versions
EP0377089B1 (fr
Inventor
Peter Brücher
Wolfgang Kehrer
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.)
Deutsche Babcock Borsig AG
Original Assignee
Borsig GmbH
Deutsche Babcock Borsig AG
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 Borsig GmbH, Deutsche Babcock Borsig AG filed Critical Borsig GmbH
Publication of EP0377089A1 publication Critical patent/EP0377089A1/fr
Application granted granted Critical
Publication of EP0377089B1 publication Critical patent/EP0377089B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/0265—Header 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
    • 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
    • C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/002—Cooling of cracked gases
    • 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
    • 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
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0075—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for syngas or cracked gas cooling systems

Definitions

  • the invention relates to a heat exchanger, in particular for cooling cracked gas, with the features of the preamble of claim 1.
  • the gas flow supplied through the inlet nozzle spreads out in accordance with the expansion of the chamber cross-section.
  • the flow is uneven in such a way that the edge zones are flowed through less than the core zone.
  • the invention has for its object to provide a generic heat exchanger with such internals that both equalize the flow through the inlet end chamber and protect the tube plate from erosion.
  • the carbon particles carried by the gas flowing at high speed in the area of the core flow meet the rods of the insert, as a result of which their kinetic energy is destroyed.
  • the particles braked in this way are carried along by the gas and can no longer lead to erosion damage to the tube plate and the tubes.
  • the incident gas flow is partially directed radially outwards by the insert.
  • a partial flow can flow in the required amount between the ring distances to the pipes in the central area of the pipe plate.
  • Appropriate arrangement and dimensioning of the rods enables gas to be applied to all tubes of the tube bundle in a very uniform manner. The deflection of the gas flow to the outside is favored if the rods formed into rings form a cone.
  • the heat exchanger consists of a tube bundle of straight tubes 1, which are held in two tube plates 2 on both sides of the tube bundle.
  • the tube bundle is enclosed by an outer jacket 3 which, together with the tube plates 2, delimits an interior space through which boiling and high-pressure water flows.
  • the tube plate 2 is followed by an end chamber 4 on the gas inlet side and on the gas outlet side (not shown), which is provided with a nozzle 5 for supplying or discharging the gas.
  • the diameter of the nozzle 5 is significantly smaller than the diameter of the tube plate 2 , so that the end chamber 4 widens conically.
  • an insert 6 is arranged, which serves as a distribution element and as an impact protection.
  • the insert 6 is limited to that part of the tube plate 2 which is located in the area of the core flow of the gas supplied through the nozzle 5 and which is therefore most at risk from erosion.
  • the insert 6 consists of profile or round bars which are shaped into polygonal or round rings 7.
  • the insert 6 can be flat, the rings being concentric and arranged in one plane. It is advantageous to arrange the rings 7 - as shown - on a cone, the tip of which points to the socket 5.
  • the rings 7 are arranged at axial distances from one another.
  • the outside diameter of a ring 7 corresponds approximately to the inside diameter of the ring 7 following in the direction of the tube plate 2.
  • the diameter of the ring 7 adjacent to the tube plate 2 is somewhat larger than the diameter of the nozzle 5. This means that the projection area of the nozzle 5 on the tube plate 2 completely covered.
  • the rings 7 are connected to intersecting webs 8 which are fastened to the wall of the end chamber 4.
  • part of the inflowing gas is deflected into the edge zone, while another part of the gas passes between the rings 7 of the insert 6.
  • the diameter of the rods 7 formed to the rings and the mutual distance can be chosen so large that the distribution of the gas over the cross section of the tube plate 2 is uniform.
  • the arrows 10 in the left part of FIG. 1 show, the carbon particles carried along by the gas and flowing in a straight line meet the rings 7 and are braked.
  • the staggered arrangement of the rings 7 ensures that the carbon particles cannot hit the tube plate 2 at high speed.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Details Of Heat-Exchange And Heat-Transfer (AREA)
EP89119375A 1988-12-19 1989-10-19 Echangeur de chaleur, particulièrement pour refroidir du gaz de craquage Expired - Lifetime EP0377089B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3842727A DE3842727A1 (de) 1988-12-19 1988-12-19 Waermetauscher insbesondere zum kuehlen von spaltgas
DE3842727 1988-12-19

Publications (2)

Publication Number Publication Date
EP0377089A1 true EP0377089A1 (fr) 1990-07-11
EP0377089B1 EP0377089B1 (fr) 1992-01-29

Family

ID=6369540

Family Applications (1)

Application Number Title Priority Date Filing Date
EP89119375A Expired - Lifetime EP0377089B1 (fr) 1988-12-19 1989-10-19 Echangeur de chaleur, particulièrement pour refroidir du gaz de craquage

Country Status (4)

Country Link
US (1) US5029637A (fr)
EP (1) EP0377089B1 (fr)
JP (1) JP3012987B2 (fr)
DE (2) DE3842727A1 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995032263A1 (fr) * 1994-05-24 1995-11-30 Abb Lummus Global Inc. Refroidisseur rapide
DE19534823C2 (de) * 1995-09-20 2002-08-22 Ruhr Oel Gmbh Rohrbündel-Wärmeübertrager
WO2007068343A1 (fr) * 2005-12-13 2007-06-21 Tuchenhagen Dairy Systems Gmbh Dispositif d'action sur l'ecoulement dans la zone d'une plaque porte-tubes d'un echangeur de chaleur a faisceau de tubes

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3908277C2 (de) * 1989-03-14 1995-11-30 Oemv Deutschland Gmbh Erosionsschutz für Wärmetauscher
US5186249A (en) * 1992-06-08 1993-02-16 General Motors Corporation Heater core
US5816322A (en) * 1997-04-18 1998-10-06 Abb Lummus Global Inc. Quench cooler
US6845813B1 (en) * 2003-10-13 2005-01-25 Knighthawk Engineering Intra-body flow distributor for heat exchanger
CN101852556B (zh) * 2010-06-08 2012-06-27 南京工业大学 高温高含尘炉气急冷器
CN102538561B (zh) * 2012-03-01 2013-04-17 张家港格林沙洲锅炉有限公司 带烟气导流装置的变径连接管
CN102661671A (zh) * 2012-04-28 2012-09-12 泰州市远望换热设备有限公司 换热器进气口缓冲结构
CN105020690B (zh) * 2015-07-24 2017-03-22 桂阳三益科技有限公司 一种节能锅炉
SI3376150T1 (sl) 2017-03-14 2019-11-29 Alfa Laval Olmi S P A Zaščitna naprava za opremo z lupinami in cevmi
KR102343408B1 (ko) * 2017-11-17 2021-12-27 주식회사 엘지화학 열 교환기
CN111504119B (zh) * 2020-03-30 2022-05-31 浙江龙泉凯利达汽车空调有限公司 一种d型集流管换热器
KR102603025B1 (ko) * 2021-11-25 2023-11-16 한국기계연구원 극저온 수소 액화용 다채널 열교환기

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3048372A (en) * 1958-03-25 1962-08-07 Jr Robert P Newton Waste water heat reclaimer
US3552487A (en) * 1967-11-29 1971-01-05 Idemitsu Petrochemical Co Quenching apparatus for use with thermal cracking system
US4142578A (en) * 1977-09-12 1979-03-06 Exxon Research & Engineering Co. Heat exchanger impingement protection
GB2056653A (en) * 1979-08-01 1981-03-18 British Petroleum Co Heat exchanger

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR347843A (fr) * 1904-11-02 1905-03-24 Gottlob Friedrich Grotz Refroidisseur pour automobiles et autres véhicules
DE748857C (de) * 1940-09-28 1944-11-10 Zylindrischer gasgekuehlter Gas- oder Zwischenkuehler, z.B. fuer Ladeluft von Brennkraftmaschinen
DE1000194B (de) * 1952-07-18 1957-01-03 Schilde Maschb Ag Diffusor mit Waermetauscher
DE2008311C3 (de) * 1970-02-23 1974-03-07 Arbeitsgemeinschaft Lentjes-Rekuperator, 4000 Duesseldorf-Oberkassel Wärmetauscher
DE2160372C3 (de) * 1971-12-02 1975-07-17 1000 Berlin Vorrichtung zur gleichmäßigen Durchströmung eines Rohrbündelwärmetauschers
SU1080002A1 (ru) * 1982-11-19 1984-03-15 Новочеркасский электродный завод Графитовый теплообменник
SU1146535A1 (ru) * 1983-11-05 1985-03-23 Предприятие П/Я А-3884 Раздающий коллектор теплообменника
JPS60132569U (ja) * 1984-02-15 1985-09-04 帝人株式会社 多管式凝縮器
US4764254A (en) * 1987-05-21 1988-08-16 Rosenblad Corporation Falling film liquor heater having a screen to prevent clogging of a liquid distributing tray

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3048372A (en) * 1958-03-25 1962-08-07 Jr Robert P Newton Waste water heat reclaimer
US3552487A (en) * 1967-11-29 1971-01-05 Idemitsu Petrochemical Co Quenching apparatus for use with thermal cracking system
US4142578A (en) * 1977-09-12 1979-03-06 Exxon Research & Engineering Co. Heat exchanger impingement protection
GB2056653A (en) * 1979-08-01 1981-03-18 British Petroleum Co Heat exchanger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995032263A1 (fr) * 1994-05-24 1995-11-30 Abb Lummus Global Inc. Refroidisseur rapide
DE19534823C2 (de) * 1995-09-20 2002-08-22 Ruhr Oel Gmbh Rohrbündel-Wärmeübertrager
WO2007068343A1 (fr) * 2005-12-13 2007-06-21 Tuchenhagen Dairy Systems Gmbh Dispositif d'action sur l'ecoulement dans la zone d'une plaque porte-tubes d'un echangeur de chaleur a faisceau de tubes
US9127893B2 (en) 2005-12-13 2015-09-08 Gea Tds Gmbh Device for influencing the flow in the region of a tube support plate of a tube bundle heat exchanger

Also Published As

Publication number Publication date
JP3012987B2 (ja) 2000-02-28
JPH02195196A (ja) 1990-08-01
DE3842727C2 (fr) 1991-08-01
DE3842727A1 (de) 1990-06-21
US5029637A (en) 1991-07-09
EP0377089B1 (fr) 1992-01-29
DE58900802D1 (de) 1992-03-12

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