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WO1982000343A1 - Heat exchanger for flowing media - Google Patents

Heat exchanger for flowing media Download PDF

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Publication number
WO1982000343A1
WO1982000343A1 PCT/NO1981/000030 NO8100030W WO8200343A1 WO 1982000343 A1 WO1982000343 A1 WO 1982000343A1 NO 8100030 W NO8100030 W NO 8100030W WO 8200343 A1 WO8200343 A1 WO 8200343A1
Authority
WO
WIPO (PCT)
Prior art keywords
casing
intermediate space
inlet
outlet
heat exchanger
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.)
Ceased
Application number
PCT/NO1981/000030
Other languages
French (fr)
Inventor
R Holen
B Borg
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to AU73702/81A priority Critical patent/AU7370281A/en
Publication of WO1982000343A1 publication Critical patent/WO1982000343A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • 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
    • F28D7/10Heat-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 one within the other, e.g. concentrically
    • F28D7/12Heat-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 one within the other, e.g. concentrically the surrounding tube being closed at one end, e.g. return type
    • 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
    • F28D7/02Heat-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 helically coiled
    • F28D7/026Heat-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 helically coiled the conduits of only one medium being helically coiled and formed by bent members, e.g. plates, the coils having a cylindrical configuration

Definitions

  • the present invention relates to a heat exchanger for flowing media.
  • Heat exchangers of various types have already been known. As a rule, heat exchangers comprise one or several tube banks the ends of which are connected by rolling or welding to the end plates of the tubular exchanger. To manufacture such heat exchangers is relatively costly and, in addition, they are difficult to maintain and repair. Also hot plate exchangers of various types have been known. Most of them have the common feature that they require many seals and are prone to leakages.
  • the object of the invention consists in bringing about a heat exchanger consisting of few sturdy parts which can be easily assembled and easily dismantled, the individual parts being easily replaced if necessary.
  • Another object of the invention consists in bringing about a heat exchanger the width and length of which is small by comparison with the size of the heat exchanging surface and the efficiency attained. These characteristics are achieved by bringing about a heat exchanger with the characteristics stated in the claims.
  • the medium to be heated is passed to and fro along a double helix in the space between the heating surface tubes, subject to one 180° reversal while passing through the heat exchanger, as a result of which the pressure drops to a relatively slight degree and the energy required for pumping is correspondingly reduced.
  • Another advantage with the design according to the invention consists in the fact that the construction requires relatively little precision, which is conducive to more economical production.
  • the invention is explained in greater detail below with the aid of an example and with reference to the drawing which shows a longitudinal section through a heat exchanger in accordance with the invention.
  • the heat exchanger can be used for heating/cooling of different media, but in the example it is assumed that it serves for heating water with the aid of steam.
  • the drawing shows a horizontal design of the heat exchanger but a vertical design is equally feasible.
  • the heat exchanger comprises a cylindrical casing 1 with a wall 2 and a base 3.
  • One end, 4, of the casing is open and ends in an outer flange ring 5.
  • the casing 1 is preferably installed in an insulating enclosure 6 containing insulating material 7.
  • the wall 2 of the casing is provided with an outlet socket 8, in the present case for steam condensate.
  • the casing is also provided with a support or brackets 9.
  • a tubular insert 10 comprising two tubes one inside the other, the outer tube of which is designated 11 and has at one end an outer flange ring 12 which is the same size as the casing flange ring 5. its other end being provided with an inner flange ring 13 with an opening 14.
  • the diameter of the outer tube 11 is considerably smaller than that of the casing 1.
  • the inner tube 15 Coaxially with the outer tubs 11 there is within it an almost equally ⁇ ong inner tube 15 the diameter of which is considerably smaller than that of the outer tube.
  • the inner tube 15 is provided with a blind flange 16 having the same outer diameter as flange ring 5 of casing 1.
  • a t its other end the inner tube 15 has an outer flange ring 17 the outer diameter of which is
  • tubes 11 and 15 are such that the flange rings 13.17 abut one another when the tube flanges 12,16 are in contact.
  • Two helical baffles or vanes 18 and 19, respectively, are attached to the inner tube 15, forming between themselves two continuous helical passages 20 and 21, respectively.
  • the baffles 18, 19 are finnly attached to the inner tube 15 and have an outer diameter matching the inner diameter of the outer tube 11.
  • baffles 18,19 are attached at two roughly diametrically opposite points to the end flange 16, whereas the other ends of the baffles terminate at some distance from the flange ring 17, so that the passages 20,21 connect in the end part 22 of the intermediate space.
  • the intermediate space itself is designated 23.
  • the end flange 16 of the inner tube 15 is provided with a central inlet socket 27 in the present case for the introduction of heating steam.
  • the end flange 16 is provided with two dia metrically opposite sockets, i.e. the inlet socket 28 for water that is to be heated and the outlet socket 29 for water that has been heated.
  • the inlet socket 28 is directly connected with the passage
  • the flanges 5, 12 and ⁇ G are provided with aligned holes for screwing together with the aid of bolts 30 and nuts 31.
  • the outer intermediate space is designated 32.
  • the medium to be heated in the present case water
  • the medium to be heated is fed through socket 28 and will flow along one of the helical passages, 20, towards the end part 22 or intermediate space 23, where it is subjected to a change of direction amounting to 180° and will continue to flow back through the passage 21 leaving the heat exchanger in a heated condition through the outletsocket 29.
  • Superheated steam is fed through the central socket 27 and passes through the inner tube 15 and then, at base 3, through the intermediate space between the outer tube and the casing and along wall 2, whereupon it leaves the casing as cooled steam or condensate through the outlet socket 8.
  • Heat from the steam is transmitted to the water both through the inner tube 15 and the outer tube 11.
  • a certain transmission of heat also takes place through the baffles 18, 19.
  • Various flowing media can be heated or cooled, respectively. Such media are oil, brine, paint, air and various gases etc.
  • the capacity of the heat exchanger can be adapted in accordance with the various applications by altering the total length of the heat exchanger, altering the pitch of the helical baffles and altering the radial height of the baffles. Welded steel construction is preferable but other materials and methods of fabrication are feasible.
  • Casing base 3 may, for instance, be replaced by a cover.
  • the "helix” may in this case be turned by 180° within the intermediate space 23 and the sockets 28,29 may pass through the cover.
  • the design described is simplest. With a vertical design the outlet 8 would be provided in base 3.

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)
  • Materials For Medical Uses (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

Un echangeur de chaleur pour des milieux en ecoulement avec des passages pour deux milieux a chauffer/refroidir disposes dans un corps (1) et separes par des surfaces de transmission de chaleur. Dans un corps ferme oblong, de preference de section circulaire, se trouve, en disposition coaxiale, un tube interne (15) dont le diametre est beaucoup plus petit que celui du corps. Le tube possede une entree (27) partant de l'exterieur et situee a une (la premiere) extremite du corps et une sortie a l'autre extremite opposee du corps, directement reliee avec l'interieur du corps. Un tube externe (11) dont le diametre est beaucoup plus grand que celui du tube interne et beaucoup plus petit que celui du corps est egalement monte dans le corps. L'espace intermediaire (23) entre les deux tubes (11, 15) est pourvu, a l'une des deux extremites, d'une entree (28) et d'une sortie (29), disposees separement, et il est ferme a l'autre extremite. L'espace intermediaire (32) entre le tube externe et le corps est ferme a une extremite et deux chicanes helicoidales sont montees en serie dans l'espace intermediaire entre les tubes de maniere a constituer deux passages helicoidaux (20, 21) connectes respectivement a l'entree et a la sortie. Les chicanes s'etendent a partir de la paroi extreme de l'espace intermediaire (23) comprenant l'entree et la sortie, respectivement, tandis que les extremites opposees des chicanes se terminent a une distance de l'extremite opposee de l'espace intermediaire de telle sorte que les passages helicoidaux passent l'un dans l'autre a cette derniere extremite (22), Le corps est pourvu d'une sortie d'evacuation (8).A heat exchanger for flowing media with passages for two heating / cooling media arranged in a body (1) and separated by heat transmitting surfaces. In an oblong firm body, preferably of circular section, there is, in coaxial arrangement, an internal tube (15) whose diameter is much smaller than that of the body. The tube has an inlet (27) extending from the exterior and located at one (the first) end of the body and an outlet at the other opposite end of the body, directly connected with the interior of the body. An outer tube (11) whose diameter is much larger than that of the inner tube and much smaller than that of the body is also mounted in the body. The intermediate space (23) between the two tubes (11, 15) is provided, at one of the two ends, with an inlet (28) and an outlet (29), arranged separately, and it is closed at the other end. The intermediate space (32) between the outer tube and the body is closed at one end and two helical baffles are mounted in series in the intermediate space between the tubes so as to constitute two helical passages (20, 21) connected respectively to entry and exit. The baffles extend from the extreme wall of the intermediate space (23) comprising the inlet and the outlet, respectively, while the opposite ends of the baffles terminate at a distance from the opposite end of the space intermediate so that the helical passages pass one into the other at this last end (22), the body is provided with an evacuation outlet (8).

Description

Heat exchanger for flowing media
The present invention relates to a heat exchanger for flowing media.
Heat exchangers of various types have already been known. As a rule, heat exchangers comprise one or several tube banks the ends of which are connected by rolling or welding to the end plates of the tubular exchanger. To manufacture such heat exchangers is relatively costly and, in addition, they are difficult to maintain and repair. Also hot plate exchangers of various types have been known. Most of them have the common feature that they require many seals and are prone to leakages.
The object of the invention consists in bringing about a heat exchanger consisting of few sturdy parts which can be easily assembled and easily dismantled, the individual parts being easily replaced if necessary. Another object of the invention consists in bringing about a heat exchanger the width and length of which is small by comparison with the size of the heat exchanging surface and the efficiency attained. These characteristics are achieved by bringing about a heat exchanger with the characteristics stated in the claims. In a heat exchanger in accordance with the invention the medium to be heated is passed to and fro along a double helix in the space between the heating surface tubes, subject to one 180° reversal while passing through the heat exchanger, as a result of which the pressure drops to a relatively slight degree and the energy required for pumping is correspondingly reduced. Another advantage with the design according to the invention consists in the fact that the construction requires relatively little precision, which is conducive to more economical production.
The invention is explained in greater detail below with the aid of an example and with reference to the drawing which shows a longitudinal section through a heat exchanger in accordance with the invention. The heat exchanger can be used for heating/cooling of different media, but in the example it is assumed that it serves for heating water with the aid of steam. The drawing shows a horizontal design of the heat exchanger but a vertical design is equally feasible.
The heat exchanger comprises a cylindrical casing 1 with a wall 2 and a base 3. One end, 4, of the casing is open and ends in an outer flange ring 5. The casing 1 is preferably installed in an insulating enclosure 6 containing insulating material 7. The wall 2 of the casing is provided with an outlet socket 8, in the present case for steam condensate. The casing is also provided with a support or brackets 9. Coaxially within the casing 1 there is a tubular insert 10 comprising two tubes one inside the other, the outer tube of which is designated 11 and has at one end an outer flange ring 12 which is the same size as the casing flange ring 5. its other end being provided with an inner flange ring 13 with an opening 14. The diameter of the outer tube 11 is considerably smaller than that of the casing 1. There is also a considerable distance between flange 15 of the tube and base 3 of the casing.
Coaxially with the outer tubs 11 there is within it an almost equally ϊong inner tube 15 the diameter of which is considerably smaller than that of the outer tube. At one of its ends the inner tube 15 is provided with a blind flange 16 having the same outer diameter as flange ring 5 of casing 1. A t its other end the inner tube 15 has an outer flange ring 17 the outer diameter of which is
end of the tube is open and aligned with the flange opening 14 in the outer tube. The lengths of tubes 11 and 15 are such that the flange rings 13.17 abut one another when the tube flanges 12,16 are in contact. Two helical baffles or vanes 18 and 19, respectively, are attached to the inner tube 15, forming between themselves two continuous helical passages 20 and 21, respectively. The baffles 18, 19 are finnly attached to the inner tube 15 and have an outer diameter matching the inner diameter of the outer tube 11. At one end of the inner tube the ends of baffles 18,19 are attached at two roughly diametrically opposite points to the end flange 16, whereas the other ends of the baffles terminate at some distance from the flange ring 17, so that the passages 20,21 connect in the end part 22 of the intermediate space. The intermediate space itself is designated 23. When the heat exchanger is in its assembled state the flange rings of the tubes, 13 and 17. are screwed together with the aid of bolts 24 and nuts 25, thus tightly closing the end part 22 of intermediate space 23.
The end flange 16 of the inner tube 15 is provided with a central inlet socket 27 in the present case for the introduction of heating steam. In addition, the end flange 16 is provided with two dia metrically opposite sockets, i.e. the inlet socket 28 for water that is to be heated and the outlet socket 29 for water that has been heated. The inlet socket 28 is directly connected with the passage
20, and the outlet socket 29 is directly connected with the passage
21. At the end of the heat exchanger presently under discussion the flanges 5, 12 and \ G are provided with aligned holes for screwing together with the aid of bolts 30 and nuts 31. The outer intermediate space is designated 32.
When the heat exchanger is in operation, the medium to be heated, in the present case water, is fed through socket 28 and will flow along one of the helical passages, 20, towards the end part 22 or intermediate space 23, where it is subjected to a change of direction amounting to 180° and will continue to flow back through the passage 21 leaving the heat exchanger in a heated condition through the outletsocket 29. Superheated steam is fed through the central socket 27 and passes through the inner tube 15 and then, at base 3, through the intermediate space between the outer tube and the casing and along wall 2, whereupon it leaves the casing as cooled steam or condensate through the outlet socket 8. Heat from the steam is transmitted to the water both through the inner tube 15 and the outer tube 11. A certain transmission of heat also takes place through the baffles 18, 19. Various flowing media can be heated or cooled, respectively. Such media are oil, brine, paint, air and various gases etc.
To dismantle the heat exchanger one first releases the bolt 30 and withdraws the tubular insert 10. Then the bolt assembly 24,25 is dismantled and the inner tube drawn out of the outer tube. The capacity of the heat exchanger can be adapted in accordance with the various applications by altering the total length of the heat exchanger, altering the pitch of the helical baffles and altering the radial height of the baffles. Welded steel construction is preferable but other materials and methods of fabrication are feasible.
Modifications are possible. Casing base 3 may, for instance, be replaced by a cover. The "helix" may in this case be turned by 180° within the intermediate space 23 and the sockets 28,29 may pass through the cover. However, the design described is simplest. With a vertical design the outlet 8 would be provided in base 3.

Claims

C l a i m s
1. A heat exchanger for flowing media comprising an outer casing (1) with passages for the two media to be heated/cooled within the casing and separated by heat transmission surfaces, c h ara c t e r i s e d in that, within a closed, oblong casing (1), preferably of circular cross-section, there are, in coaxial arrangement, an inner tube (15), the diameter of which is considerably smaller than that of the casing, with an inlet (27) from outside one (the first) end of the casing and with an outlet at the other, opposite end of the casing directly connected with the inside of the casing, an outer tube (11 ), the diameter of which is considerably larger than that of the inner tube and considerably smaller than that of the casing, whereby the intermediate space (23) between the two tubes (11,15) has at one end, separately arranged, an inlet (28) and an cutlet (23) and is closed at its other end, and the intermediate space (32) between the outer tube and the casing is closed at one end, in that two helical baffles are arranged in sequence within the intermediate space between the tubes and constitute helical passages (20,21) which are, respectively, connected with the said inlet (28) and the outlet (29), the said baffles extending from the end wall of intermediate space (23) comprising the said inlet (28) and outlet
(29), respectively, whereas the opposite ends of the baffles terminateat a distance from the opposite end of the intermediate space so that the two helical passages pass into one another at the latter end (22), and in that the casing (1) is provided with at least one drainage outlet (8).
2. A heat exchanger in accordance with claim 1, c h a r a c t e r i s e d in that the first, open end of casing (1) is closed by an outer flange ring (5) and the other end ist closed by a base (3) and in that the first end of the inner tube is closed by a flange (lo) with an inlet (27) leading to the inner tube (15) and with an inlet (28) and an outlet (29) leading to/from the intermediate space (23), the said flange having a diameter which roughly corresponds to that of the casing flange ring (5) and in that the other end of the inner tube is provided with a flange ring which closes or is equipped to close the intermediate space (23).
3. A heat exchanger in accordance with claim 1 or 2, c har a o t e r i s e d in that the outer tube (11) has at its first end a flange ring (12) with roughly the same diameter as that of the casing and at its other end an inner flange ring (13) which closes or is equipped to close the intermediate space (23).
4. A heat exchanger in accordance with one of claims 1 to 3, c h ar a c t e r i s e d in that the baffles (18,19) are firmly connected with the inner tube and at the ends with flange (16) of the inner tube (15), which is designed as a blind flange.
PCT/NO1981/000030 1980-07-11 1981-07-08 Heat exchanger for flowing media Ceased WO1982000343A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU73702/81A AU7370281A (en) 1980-07-11 1981-07-08 Heat exchanger for flowing media

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NO802084A NO146579C (en) 1980-07-11 1980-07-11 HEAT EXCHANGES FOR STREAMING MEDIA.
NO802084800711 1980-07-11

Publications (1)

Publication Number Publication Date
WO1982000343A1 true WO1982000343A1 (en) 1982-02-04

Family

ID=19885583

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/NO1981/000030 Ceased WO1982000343A1 (en) 1980-07-11 1981-07-08 Heat exchanger for flowing media

Country Status (3)

Country Link
EP (1) EP0055737A1 (en)
NO (1) NO146579C (en)
WO (1) WO1982000343A1 (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0235374A3 (en) * 1986-02-26 1988-07-27 Uhde Gmbh Cooling device for inclusion into a polymerization reactor
EP0449124A1 (en) * 1990-03-29 1991-10-02 Hubert Vogt Annular space heat exchanger
EP0560678A1 (en) * 1992-03-10 1993-09-15 Dumoutier Et Massetat Apparatus for purifying gaseous effluents
GB2273980A (en) * 1993-01-04 1994-07-06 Falmer Investment Ltd Concentric tube heat exchanger
FR2787563A1 (en) * 1998-12-22 2000-06-23 Db Ind Tubular heat exchanger assembly, comprises concentrically mounted tubes mutually terminated at a recessed flange assembly
CN105698570A (en) * 2014-12-11 2016-06-22 杭州富尔顿热能设备有限公司 Heat exchanger and manufacture method thereof
WO2016102219A1 (en) * 2014-12-24 2016-06-30 Nestec S.A. Heat transfer device and system integrating such a device
ITUA20163257A1 (en) * 2016-05-09 2016-08-09 Mario Chierico MODULAR ELEMENT FOR A CHOCOLATE TEMPERING MACHINE AND CHOCOLATE TEMPERING MACHINE.
US10240813B2 (en) 2014-12-11 2019-03-26 Fulton Group N.A., Inc. Fully-wetted, refractory-free tubeless fluid heating system with negligible thermal expansion stress
WO2019153648A1 (en) * 2018-02-08 2019-08-15 江苏文凤化纤集团有限公司 Heat exchange device for heat recovery of industrial air compressor
CN110567298A (en) * 2019-09-23 2019-12-13 重庆邮电大学 Nested formula spiral baffling board and heat exchanger
US10845126B2 (en) * 2014-04-16 2020-11-24 Enterex America LLC Counterflow helical heat exchanger
JP2023540695A (en) * 2020-09-07 2023-09-26 レール・リキード-ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード Heat exchanger and its use

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1419583A (en) * 1964-01-17 1965-12-03 Nestable and removable baffle heat exchangers
NO122756B (en) * 1968-09-17 1971-08-09 P Langsholt
FR2404825A1 (en) * 1977-10-01 1979-04-27 Funke Waerme Apparate Kg TUBULAR HEAT EXCHANGER

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1419583A (en) * 1964-01-17 1965-12-03 Nestable and removable baffle heat exchangers
NO122756B (en) * 1968-09-17 1971-08-09 P Langsholt
FR2404825A1 (en) * 1977-10-01 1979-04-27 Funke Waerme Apparate Kg TUBULAR HEAT EXCHANGER

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0235374A3 (en) * 1986-02-26 1988-07-27 Uhde Gmbh Cooling device for inclusion into a polymerization reactor
EP0449124A1 (en) * 1990-03-29 1991-10-02 Hubert Vogt Annular space heat exchanger
EP0560678A1 (en) * 1992-03-10 1993-09-15 Dumoutier Et Massetat Apparatus for purifying gaseous effluents
FR2688577A1 (en) * 1992-03-10 1993-09-17 Dumoutier Massetat Sa DEVICE FOR PURIFYING GASEOUS EFFLUENTS.
GB2273980A (en) * 1993-01-04 1994-07-06 Falmer Investment Ltd Concentric tube heat exchanger
FR2787563A1 (en) * 1998-12-22 2000-06-23 Db Ind Tubular heat exchanger assembly, comprises concentrically mounted tubes mutually terminated at a recessed flange assembly
WO2000037872A1 (en) * 1998-12-22 2000-06-29 Db Industrie Heat exchanger with annular space
US10845126B2 (en) * 2014-04-16 2020-11-24 Enterex America LLC Counterflow helical heat exchanger
US10228190B2 (en) 2014-12-11 2019-03-12 Fulton Group N.A., Inc. Ribbed tubeless heat exchanger for fluid heating systems including a rib component and methods of manufacture thereof
US10240813B2 (en) 2014-12-11 2019-03-26 Fulton Group N.A., Inc. Fully-wetted, refractory-free tubeless fluid heating system with negligible thermal expansion stress
CN105698570A (en) * 2014-12-11 2016-06-22 杭州富尔顿热能设备有限公司 Heat exchanger and manufacture method thereof
US11045039B2 (en) 2014-12-24 2021-06-29 Societe Des Produits Nestle S.A. Heat transfer device and system integrating such a device
WO2016102219A1 (en) * 2014-12-24 2016-06-30 Nestec S.A. Heat transfer device and system integrating such a device
JP2018506325A (en) * 2014-12-24 2018-03-08 ネステク ソシエテ アノニム Heat transfer device and system incorporating such a device
RU2717794C2 (en) * 2014-12-24 2020-03-25 Сосьете Де Продюи Нестле С.А. Heat exchange device and system, including such device
AU2015371517B2 (en) * 2014-12-24 2020-08-13 Société des Produits Nestlé S.A. Heat transfer device and system integrating such a device
EP3243390A1 (en) * 2016-05-09 2017-11-15 Mario Chierico Modular element for a tempering machine for chocolate and tempering machine for chocolate
ITUA20163257A1 (en) * 2016-05-09 2016-08-09 Mario Chierico MODULAR ELEMENT FOR A CHOCOLATE TEMPERING MACHINE AND CHOCOLATE TEMPERING MACHINE.
WO2019153648A1 (en) * 2018-02-08 2019-08-15 江苏文凤化纤集团有限公司 Heat exchange device for heat recovery of industrial air compressor
CN110567298A (en) * 2019-09-23 2019-12-13 重庆邮电大学 Nested formula spiral baffling board and heat exchanger
CN110567298B (en) * 2019-09-23 2021-03-16 重庆邮电大学 Nested formula spiral baffling board and heat exchanger
JP2023540695A (en) * 2020-09-07 2023-09-26 レール・リキード-ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード Heat exchanger and its use

Also Published As

Publication number Publication date
NO146579B (en) 1982-07-19
NO146579C (en) 1982-10-27
EP0055737A1 (en) 1982-07-14
NO802084L (en) 1982-01-12

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