US3348610A - Heat exchangers for cooling fresh cracked gases or the like - Google Patents

Heat exchangers for cooling fresh cracked gases or the like Download PDF

Info

Publication number
US3348610A
US3348610A US534157A US53415766A US3348610A US 3348610 A US3348610 A US 3348610A US 534157 A US534157 A US 534157A US 53415766 A US53415766 A US 53415766A US 3348610 A US3348610 A US 3348610A
Authority
US
United States
Prior art keywords
jacket
steam
interior
heating tubes
chamber
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.)
Expired - Lifetime
Application number
US534157A
Inventor
Vollhardt Fromut
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.)
Schmidtsche Heissdampf GmbH
Original Assignee
Schmidtsche Heissdampf GmbH
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 Schmidtsche Heissdampf GmbH filed Critical Schmidtsche Heissdampf GmbH
Application granted granted Critical
Publication of US3348610A publication Critical patent/US3348610A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

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
    • F28F9/04—Arrangements for sealing elements into header boxes or end plates
    • F28F9/16—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling
    • F28F9/18—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling by welding
    • 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
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00054—Controlling or regulating the heat exchange system
    • B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2219/00067—Liquid level measurement
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00085—Plates; Jackets; Cylinders
    • 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
    • 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
    • F28F2009/222—Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
    • F28F2009/226—Transversal partitions

Definitions

  • An object of the invention is to provide a construction which consists of tube plates closing the two ends of an upright pressure jacket, one for the gas inlet head and the other for the gas outlet head, with at least that tube plate located at the gas inlet side consisting of stepwise arranged chambers interconnected with each other in gastight manner, the stepwise arrangement ascending from the interior outwardly with the interior of said chambers connected with the interior of the pressure jacket by openings in the chamber wall, and groups of essentially rectilinear heating tubes extending through the interior of the pressure jacket having their ends fixed in the tube plates.
  • a further object is to provide heat exchangers which are especially suitable for the cooling of fresh cracked gases wherein consideration is given not only to the high temperature and to the high pressure at which the cracked gases to be cooled are supplied in considerable amount, but also to their tendency to re-form, i.e., to coke precipitation and thus to undesired coke deposits in the heating tubes of the cooler.
  • This last-mentioned property of cracked gases has been limited to a minimum after the cause of this behavior of cracked gases was discovered, and a correlation between the dwell time of the cracked gases being cooled in the gas inlet head of the cooler and the threshold of re-formation of the cracked gases in the heating tubes of the cooler established. It was found that the threshold of undesired coke separation could be controlled by reducing the time of dwell of the cracked gases in the gas inlet head.
  • a still further object is to provide a construction wherein an effective decrease of the time of dwell of the cracked gases in the gas inlet head is realized by a special construction of the latter and of the appurtenant tube plate of the cooler, which makes it possible to limit the coke precipitation to a tenable minimum.
  • a further object is to provide a simplification which consists in subdividing the pressure jacket interior into a lower water chamber and a steam chamber located at the gas outlet side and in arranging the steam chamber above the highest water level and locating between the latter the steam discharge conduits of the cooler by means of guiding plates in such a manner as to form interconnected sections through which the heating tubes extend and in which the steam passing therethrough to the steam discharge outlets is forced to impinge on the heating tubes.
  • a further object is to provide a construction which makes it possible to eliminate a common steam drum
  • a further object of the invention consists in so constructing the pressure jacket of the cooler that it is widened at its upper end, adjacent the gas outlet, relative to the lower portion of the pressure jacket, thereby forming an enlarged steam chamber.
  • This object presents not only the possibility of an increased steam volume capacity in the steam chamber of the cooler, but it further also appreciably enlarges the water space and thereby the water content of the cooler, since the lower part of the steam chamber constructed according to the invention is filled with water as in a normal steam drum.
  • a further object is to construct the chambers forming the tube bottoms at the gas inlet side with openings which interconnect the interior of the pressure jacket with the interior of the chambers, these openings being situated at the upper side of the chambers and in the side walls below said upper side.
  • FIG. 1 shows a longitudinal sectional view with parts in elevation of a heat exchanger with uniformly extending pressure jacket
  • FIG. 2 shows a similar view of a modified heat exchanger with a widened upper end portion of the pressure jacket
  • FIG. 3 shows a similar view of the lower part of a heat exchanger at the gas inlet side.
  • the heat exchanger shown in FIGS. 1 and 3, consists of an outer pressure jacket 1, the ends of which are tightly closed by tube plates 2 and 3. At least one of these two tube plates, and particularly plate 2 located near the gas inlet end, comprises chambers 4.
  • the chambers 4 are annular and concentrically and stepwise arranged relative to each other.
  • the tube plate 3 closing the gas outlet end of the pressure jacket 1 can be constructed as a flat plate, or as an arched plate, or, as tube plate 2, can be composed of chambers 4. Chambers 4 of the tube plate 2 as well as tube plate 3 are traversed by heating tubes 5 welded thereto and these tubes 5 extend through the interior of the pressure jacket 1 from plate to plate.
  • the cracked gases to be cooled are supplied through the gas inlet head 6 which covers plate 2 and is distributed to the heating tubes 5. After passing through the heating tubes 5, the cooled cracked gases are withdrawn through the gas discharge head 7 which covers plate 3 and the with an inside diameter which is somewhat larger than the outer diameter of heating tubes 5.
  • openings 18 are arranged below the openings 10, i.e., at a lower level. This assures a separate natural circulation of the cooling medium through the interior of chambers 4. The course of the thus-produced flow is indicated by arrows on FIG. 3.
  • a cooling water level 11 is maintained so that a steam chamber 12 of sufiicient size remains thereabove.
  • the steam chamber 12 thus arranged in the pressure jacket interior 8, between the tube plate 3 and cooling water level -11, is subdivided into individual sections 14 by the guide plates 13 or similar builtin parts.
  • the guide plates 13 are provided at one side thereof with an opening 15 adjacent the inner wall of the pressure jacket 1, so that a connection is established between the individual successive sections 14.
  • the successive guide plates 13 are arranged so that they are opposed with respect to each other.
  • the steam developed from the cooling water and rising from the cooling water level 11 is forced to traverse, at times transversely of the longitudinal axis thereof, all of thesuccessively arranged sections 14 through which the heating tubes pass vertically, after which the steam leaves the steam chamber '12 through the steam discharge outlet 16 arranged in the topmost section 14.
  • the steam chamber 12' is widened relative to the lower part of the cooler.
  • the cracked gas cooler has increased steam receiving capacity and greater cooling water content.
  • a heat exchanger for cooling fresh cracked gases or the like comprising a vertical pressure jacket, means for supplying water to the interior of said jacket, tube plates located at the ends of said jacket, a gas inlet head located at the lower end of said jacket and a gas outlet head located at the top of said jacket, the tube plate at the lower-end of said jacket comprising step-wise arranged chambers interconnected with each other in gas tight relation, said chambers having openings in the chamber wall communicating with the interior of said pressure jacket, rectilinear heating tubes extending through the interior of said jacket and having their ends fixed to said tube plates, the interior of said pressure jacket being subdivided into a lower water chamber and an upper steam chamber, said jacket having a steam discharge outlet from said steam chamber, guide plates located in said steam chamber above the highest water level forming interconnected sections through which said heating tubes extend so that steam passing through said section to said steam discharge outlet are forced into contact with said heating tubes.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

' 3,348,610 v 5 sheets-sheet 1 ATTORNEYS R m 0 O vw m w W m 7 w I M m E 6 as. 5 w m F Oct. 24,1967 I I F-.VOLLHARDT HEAT EXCHANGERS FOR COOLING FRESH CRACKED GASES OR THE LIKE Filed March 14, 1966 FIG -i Oct. 24, 1967 F. VOLLHARDT HEAT EXCHANGERS FOR COOLING FRESH CRACKED GASES OR THE LIKE v5 Sheets-Sheet 2 Filed March 14, 1966 l m mm 50 V V I U m m .F
ATTORNEYS- Oct. 24, 1967 ,F. VOLLHARDT I ,5
HEAT EXCHANGERS FOR COOLING FRESH CRACKED GASES OR THE LIKE I Filed March 14, 1966 v v 3 sheets sheet 5 INVENTORY F romur VolIhordt BY v wmd fi (it ATTORNEYS United States Patent ()fiice 3,348,610 Patented Oct. 24, 1967 3,348,610 HEAT EXCHANGERS FOR COOLING FRESH CRACKED GASES OR THE LIKE Fromut Vollhardt, Gottingen, Germany, assignor to Schmidt-sche Heissdampf-Gesellschaft m.b.H., Kassel-Bettenhausen, Germany Filed Mar. 14, 1966, Ser. No. 534,157 Claims priority, application Germany, June 24, 1965, Sch 37,281 4 Claims. (Cl. 165-158) This invention relates to a heat exchanger for the cooling of fresh cracked gases or the like.
An object of the invention is to provide a construction which consists of tube plates closing the two ends of an upright pressure jacket, one for the gas inlet head and the other for the gas outlet head, with at least that tube plate located at the gas inlet side consisting of stepwise arranged chambers interconnected with each other in gastight manner, the stepwise arrangement ascending from the interior outwardly with the interior of said chambers connected with the interior of the pressure jacket by openings in the chamber wall, and groups of essentially rectilinear heating tubes extending through the interior of the pressure jacket having their ends fixed in the tube plates.
A further object is to provide heat exchangers which are especially suitable for the cooling of fresh cracked gases wherein consideration is given not only to the high temperature and to the high pressure at which the cracked gases to be cooled are supplied in considerable amount, but also to their tendency to re-form, i.e., to coke precipitation and thus to undesired coke deposits in the heating tubes of the cooler. This last-mentioned property of cracked gases has been limited to a minimum after the cause of this behavior of cracked gases was discovered, and a correlation between the dwell time of the cracked gases being cooled in the gas inlet head of the cooler and the threshold of re-formation of the cracked gases in the heating tubes of the cooler established. It was found that the threshold of undesired coke separation could be controlled by reducing the time of dwell of the cracked gases in the gas inlet head.
A still further object is to provide a construction wherein an effective decrease of the time of dwell of the cracked gases in the gas inlet head is realized by a special construction of the latter and of the appurtenant tube plate of the cooler, which makes it possible to limit the coke precipitation to a tenable minimum.
Normally the vapor (steam) developed from the cooling water is led directly to a steam drum. Because of the high pressure, about 140 atmospheres excess pressure, at which such a cracked gases cooling plant, consisting of a plurality of coolers which give off the therein-developed steam to a common steam drum, must be operated, the steam drum walls have to be inconveniently large and thick.
A further object is to provide a simplification which consists in subdividing the pressure jacket interior into a lower water chamber and a steam chamber located at the gas outlet side and in arranging the steam chamber above the highest water level and locating between the latter the steam discharge conduits of the cooler by means of guiding plates in such a manner as to form interconnected sections through which the heating tubes extend and in which the steam passing therethrough to the steam discharge outlets is forced to impinge on the heating tubes.
A further object is to provide a construction which makes it possible to eliminate a common steam drum,
since the separate guiding plates in the steam chamber make it possible to realize dry and slightly superheated steam which can then be directly conducted to the corresponding point of steam consumption by way of a steam collecting conduit.
A further object of the invention consists in so constructing the pressure jacket of the cooler that it is widened at its upper end, adjacent the gas outlet, relative to the lower portion of the pressure jacket, thereby forming an enlarged steam chamber. This object presents not only the possibility of an increased steam volume capacity in the steam chamber of the cooler, but it further also appreciably enlarges the water space and thereby the water content of the cooler, since the lower part of the steam chamber constructed according to the invention is filled with water as in a normal steam drum.
As a result of the shortening of the time of dwell at the gas inlet end of the heating tubes in the vicinity of the chambers, the available heat from the highly heated cracked gases exceeds the heat transfer conditions prevailing in the said vicinity, so that insupportable and injurious overheating can take place. To counteract this, a further object is to construct the chambers forming the tube bottoms at the gas inlet side with openings which interconnect the interior of the pressure jacket with the interior of the chambers, these openings being situated at the upper side of the chambers and in the side walls below said upper side. By this expedient, a natural secondary circulation of the cooling water is established in the vicinity of the chamber interior and thus in the vicinity of the ends of the heating tubes, which assures improved direct heat flow-off (discharge) to the cooling medium from the here especially large amount of available heat of the cracked gases.
With the above and other objects in view which will become apparent from the detailed description below, several modifications are shown in the drawings, in which:
FIG. 1 shows a longitudinal sectional view with parts in elevation of a heat exchanger with uniformly extending pressure jacket,
FIG. 2 shows a similar view of a modified heat exchanger with a widened upper end portion of the pressure jacket, and
FIG. 3 shows a similar view of the lower part of a heat exchanger at the gas inlet side.
The heat exchanger, shown in FIGS. 1 and 3, consists of an outer pressure jacket 1, the ends of which are tightly closed by tube plates 2 and 3. At least one of these two tube plates, and particularly plate 2 located near the gas inlet end, comprises chambers 4. The chambers 4 are annular and concentrically and stepwise arranged relative to each other.
The tube plate 3 closing the gas outlet end of the pressure jacket 1 can be constructed as a flat plate, or as an arched plate, or, as tube plate 2, can be composed of chambers 4. Chambers 4 of the tube plate 2 as well as tube plate 3 are traversed by heating tubes 5 welded thereto and these tubes 5 extend through the interior of the pressure jacket 1 from plate to plate.
The cracked gases to be cooled are supplied through the gas inlet head 6 which covers plate 2 and is distributed to the heating tubes 5. After passing through the heating tubes 5, the cooled cracked gases are withdrawn through the gas discharge head 7 which covers plate 3 and the with an inside diameter which is somewhat larger than the outer diameter of heating tubes 5.
Further openings 18 are arranged below the openings 10, i.e., at a lower level. This assures a separate natural circulation of the cooling medium through the interior of chambers 4. The course of the thus-produced flow is indicated by arrows on FIG. 3.
In the pressure jacket interior 8, a cooling water level 11 is maintained so that a steam chamber 12 of sufiicient size remains thereabove. The steam chamber 12 thus arranged in the pressure jacket interior 8, between the tube plate 3 and cooling water level -11, is subdivided into individual sections 14 by the guide plates 13 or similar builtin parts. The guide plates 13 are provided at one side thereof with an opening 15 adjacent the inner wall of the pressure jacket 1, so that a connection is established between the individual successive sections 14. The successive guide plates 13 are arranged so that they are opposed with respect to each other. As a result, the steam developed from the cooling water and rising from the cooling water level 11 is forced to traverse, at times transversely of the longitudinal axis thereof, all of thesuccessively arranged sections 14 through which the heating tubes pass vertically, after which the steam leaves the steam chamber '12 through the steam discharge outlet 16 arranged in the topmost section 14.
In the modification of FIG. 2, the steam chamber 12' is widened relative to the lower part of the cooler.
As a result, the cracked gas cooler has increased steam receiving capacity and greater cooling water content.
With water of poor quality, which would otherwise be rejected because of undesirable influence on the heating surfaces, it is possible to provide tube sections 17 in the transition area from water chamber to steam chamber, which sections 17 are drawn over the heating tubes 5 to provide protection against corrosion. An example is shown in FIG. 2.
It is thought that the invention and its advantages will be understood from the foregoing description and it is apparent that various changes may be made in the form, construction and arrangement of the parts without departing from the spirit and scope of the invention or sacrificing its material advantages, the forms hereinbefore described and illustrated in the drawings being merely preferred embodiments thereof.
I claim: I
1. A heat exchanger for cooling fresh cracked gases or the like comprising a vertical pressure jacket, means for supplying water to the interior of said jacket, tube plates located at the ends of said jacket, a gas inlet head located at the lower end of said jacket and a gas outlet head located at the top of said jacket, the tube plate at the lower-end of said jacket comprising step-wise arranged chambers interconnected with each other in gas tight relation, said chambers having openings in the chamber wall communicating with the interior of said pressure jacket, rectilinear heating tubes extending through the interior of said jacket and having their ends fixed to said tube plates, the interior of said pressure jacket being subdivided into a lower water chamber and an upper steam chamber, said jacket having a steam discharge outlet from said steam chamber, guide plates located in said steam chamber above the highest water level forming interconnected sections through which said heating tubes extend so that steam passing through said section to said steam discharge outlet are forced into contact with said heating tubes.
2. A heat exchanger as set forth in claim 1 wherein said guide plates are located in spaced horizontal relationship with staggered intercommunicating openings.
3. A heat exchanger as set forth in claim 1 wherein said pressure jacket is widened at its upper end adjacent said gas outlet head relative to the lower part of said pressure jacket to provide an enlarged steam chamber.
4. A heat exchanger as set forth in claim 1 wherein said stepwise arranged chambers are provided with additional openings located below said first named openings also communicating with the interior of said jacket.
References Cited UNITED STATES PATENTS 3,144,080 8/1964 Vollhardt 159 3,127,743 9/1964 Romanos 12'232 ROBERT A. OLEARY, Primary Examiner.
A. W. DAVIS, Examiner.

Claims (1)

1. A HEAT EXCHANGER FOR COOLING FRESH CRACKED GASES OR THE LIKE COMPRISING A VERTICAL PRESSURE JACKET, MEANS FOR SUPPLYING WATER TO THE INTERIOR OF SAID JACKET, TUBE PLATES LOCATED AT THE ENDS OF SAID JACKET, A GAS INLET HEAD LOCATED AT THE LOWER END OF SAID JACKET AND A GAS OUTLET HEAD LOCATED AT THE TOP OF SAID JACKET, THE TUBE PLATE AT THE LOWER END OF SAID JACKET COMPRISING STEP-WISE ARRANGED CHAMBERS INTERCONNECTED WITH EACH OTHER IN GAS TIGHT RELATION, SAID CHAMBERS HAVING OPENINGS IN THE CHAMBER WALL COMMUNICATING WITH THE INTERIOR OF SAID PRESSURE JACKET, RECTILINEAR HEATING TUBES EXTENDING THROUGH THE INTERIOR OF SAID JACKET AND HAVING THEIR ENDS FIXED TO SAID TUBE PLATES, THE INTERIOR OF SAID PRESSURE JACKET BEING SUBDIVIDED INTO A LOWER WATER CHAMBER AND AN UPPER STEAM CHAMBER, SAID JACKET HAVING A STEAM DISCHARGE OUTLET FROM SAID STEAM CHAMBER, GUIDE PLATES LOCATED IN SAID STEAM CHAMBER ABOVE THE HIGHEST WATER LEVEL FORMING INTERCONNECTED SECTIONS THROUGH WHICH SAID HEATING TUBES EXTEND SO THAT STEAM PASSING THROUGH SAID SECTION TO SAID STEAM DISCHARGE OUTLET ARE FORCED INTO CONTACT WITH SAID HEATING TUBES.
US534157A 1965-06-24 1966-03-14 Heat exchangers for cooling fresh cracked gases or the like Expired - Lifetime US3348610A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DESC037281 1965-06-24

Publications (1)

Publication Number Publication Date
US3348610A true US3348610A (en) 1967-10-24

Family

ID=7434204

Family Applications (1)

Application Number Title Priority Date Filing Date
US534157A Expired - Lifetime US3348610A (en) 1965-06-24 1966-03-14 Heat exchangers for cooling fresh cracked gases or the like

Country Status (1)

Country Link
US (1) US3348610A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3570458A (en) * 1968-05-25 1971-03-16 Mitsubishi Heavy Ind Ltd Heat exchanger construction
US3700030A (en) * 1969-11-13 1972-10-24 Air Liquide Heat exchanger support structure
FR2234519A1 (en) * 1973-06-22 1975-01-17 Uhde Gmbh Friedrich
US4724754A (en) * 1985-08-08 1988-02-16 Bertrand Crozat Apparatus for making molded confections
US5775412A (en) * 1996-01-11 1998-07-07 Gidding Engineering, Inc. High pressure dense heat transfer area heat exchanger
US20040253364A1 (en) * 2003-06-13 2004-12-16 Lucian Demmel Apparatus and method of thermally treating a confectionery mass
US8672021B2 (en) 2010-02-12 2014-03-18 Alfred N. Montestruc, III Simplified flow shell and tube type heat exchanger for transfer line exchangers and like applications

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3127743A (en) * 1961-12-28 1964-04-07 Gen Motors Corp Fluid tank pressurizing system
US3144080A (en) * 1961-03-02 1964-08-11 Schmidt Sche Heissdampf Heat exchanger for the cooling of freshly cracked gases or the like

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3144080A (en) * 1961-03-02 1964-08-11 Schmidt Sche Heissdampf Heat exchanger for the cooling of freshly cracked gases or the like
US3127743A (en) * 1961-12-28 1964-04-07 Gen Motors Corp Fluid tank pressurizing system

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3570458A (en) * 1968-05-25 1971-03-16 Mitsubishi Heavy Ind Ltd Heat exchanger construction
US3700030A (en) * 1969-11-13 1972-10-24 Air Liquide Heat exchanger support structure
FR2234519A1 (en) * 1973-06-22 1975-01-17 Uhde Gmbh Friedrich
US4724754A (en) * 1985-08-08 1988-02-16 Bertrand Crozat Apparatus for making molded confections
US5775412A (en) * 1996-01-11 1998-07-07 Gidding Engineering, Inc. High pressure dense heat transfer area heat exchanger
US20040253364A1 (en) * 2003-06-13 2004-12-16 Lucian Demmel Apparatus and method of thermally treating a confectionery mass
US7698995B2 (en) * 2003-06-13 2010-04-20 Chocotech Gmbh Apparatus and method of thermally treating a confectionery mass
US8672021B2 (en) 2010-02-12 2014-03-18 Alfred N. Montestruc, III Simplified flow shell and tube type heat exchanger for transfer line exchangers and like applications

Similar Documents

Publication Publication Date Title
US3187807A (en) Heat exchanger
SU1225496A3 (en) Steam generator
US4493291A (en) Gas cooler arrangement
US3433298A (en) Heat exchanger especially for the cooling of hot gases
US2729433A (en) Heat exchanger with removable tube banks
US3590912A (en) Vertical staggered surface feedwater heater
US3182719A (en) Multitubular heat exchanger
US3348610A (en) Heat exchangers for cooling fresh cracked gases or the like
US2946570A (en) Vertical feedwater heater
US3682241A (en) Heat exchanger, particularly for cooling fresh cracked and/or synthesis gases
US3507323A (en) Tube heat exchanger
US2812164A (en) Heat exchanger
US3903963A (en) Heat exchanger
US3363678A (en) Multi-pressure surface condenser
US4474141A (en) Heat exchanger for cooling a hot gas
HU191759B (en) Feed-water heater
US2059967A (en) Heat exchange apparatus
US4243097A (en) Waste heat boiler
US3797566A (en) Heat exchanger
US2122256A (en) Heat exchange apparatus
US1979751A (en) Heat exchange apparatus
US2536425A (en) Heater
US2184308A (en) Heat exchange apparatus
US3155158A (en) Header type tubular heat exchanger
US2555043A (en) Waste heat or surplus heat boiler