[go: up one dir, main page]

US2591878A - Oxygen regenerator - Google Patents

Oxygen regenerator Download PDF

Info

Publication number
US2591878A
US2591878A US50496A US5049648A US2591878A US 2591878 A US2591878 A US 2591878A US 50496 A US50496 A US 50496A US 5049648 A US5049648 A US 5049648A US 2591878 A US2591878 A US 2591878A
Authority
US
United States
Prior art keywords
passages
passage
spaced apart
coils
extending
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
US50496A
Inventor
Philip S Rogers
Willard O Emmons
John W Godfrey
Kelso James Milton
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.)
Motors Liquidation Co
Original Assignee
General Motors Corp
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 General Motors Corp filed Critical General Motors Corp
Priority to US50496A priority Critical patent/US2591878A/en
Application granted granted Critical
Publication of US2591878A publication Critical patent/US2591878A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J5/00Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
    • F25J5/002Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2205/00Processes or apparatus using other separation and/or other processing means
    • F25J2205/24Processes or apparatus using other separation and/or other processing means using regenerators, cold accumulators or reversible heat exchangers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/32Details on header or distribution passages of heat exchangers, e.g. of reboiler-condenser or plate heat exchangers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/42Modularity, pre-fabrication of modules, assembling and erection, horizontal layout, i.e. plot plan, and vertical arrangement of parts of the cryogenic unit, e.g. of the cold box
    • 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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0093Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids

Definitions

  • atmospheric air can be cooled to a very low temperature and then separated by distillation and rectification into its main constituents, namely, oxygen and nitrogen. Efiiciency of the process is increased by pre-coolingthe incoming compressed air and this conveniently and economically can be done through the utilization of cold oxygen produced by the process and the cold waste nitrogen.
  • an oxygen regenerator can be. employed and so arranged as to serve also as a purifier of the air by removal of normally present moisture and carbon dioxide. Purification is accomplished by the temperature drop in that as the air becomes very cold the impurities condense on the heat exchange surfaces over which the air sweeps.
  • the assembly is illustrated as comprising a group of flat plates 6 in superposed spaced relation affording a stack of fluid flow passages which cormnunicate selectively at one end with connector pipes or tubes 1, 8, 9 and I0 and at the opposite end with similar connector pipes la, 8a, 9a and Ito.
  • the serpentine ribbons H set on edge for brazed attachment to the opposing faces of passage Walls with their successive straight lengths extending transversely of the passage.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

April 8} 1952' -P. 5. ROGERS ETAL 2,591,878
OXYGEN REGENERATOR 2 SHEETS-SHEET 1 Filed Sept. 22, 1948 April 8, 1952 P. s. ROGERS ETAL 2,591,878
OXYGEN REGENERATOR Filed Sept. 22, 1948 2 SHEETS-SHEET 2 Patented Apr. 8, 1952 Philip S. Rogers, Willard 0. Emmons, John W. Godfrey and James Milton 'Kelso, Lockport, N. Y., assignors to General Motors Corporation, Detroit, Mich., a corporation of Delaware Application September 22, 1948, SerialNo. 50,496
. 1 For the production of tonnage oxygen atmospheric air can be cooled to a very low temperature and then separated by distillation and rectification into its main constituents, namely, oxygen and nitrogen. Efiiciency of the process is increased by pre-coolingthe incoming compressed air and this conveniently and economically can be done through the utilization of cold oxygen produced by the process and the cold waste nitrogen. For working the low temperature products for the absorption of heat from the compressed air an oxygen regenerator can be. employed and so arranged as to serve also as a purifier of the air by removal of normally present moisture and carbon dioxide. Purification is accomplished by the temperature drop in that as the air becomes very cold the impurities condense on the heat exchange surfaces over which the air sweeps.
By periodically switching the paths of air and nitrogen through the device the nitrogen as it 6 Claims. (Cl. 257-245) row of pins successively joined by return bends at their opposite ends.
An important feature of the present invention is the elimination of flexibility in the coiled wire during handling and the provision automatically for proper location in the assembly by fitting or nesting the return bends at least along one end within a channel section strip which gives stifiness and provides spacer flanges or separators for the neighboring lengths of coiled wire when they are placed side by side for brazing or like T Figure l is a perspective View of an oxygen rewarms up in absorbing heat from the air acts to 1 vaporize moisture and carbon dioxide previously deposited from the air and carries out the impurities to complete the cycle.
For working the fluids to best advantage it is important that an abundance of surface be exposed in the flow paths without too much restriction to flow and that relatively thin walls separate adjoining passages. Italso is of consequence to incorporate ruggedness in the assembly of thin walls. These things are substantially achieved together with ease and simplicity of manufacture by the employment in general of a succession of spaced flat sheets closed at their edges to afford passages therebetween'and held apart throughout their width and breadth by a multiplicity of spaced struts in the nature of small diameter pins arranged in rows andjoined at opposite ends to the opposing faces of adjacent 7 thin walls.
The thinness and multitude of pins provides large surface area exposed within the small passages and their arrangement in longitudinal rows narrowly spaced apart minimizes resistance to fluid flow while insuring the sweeping of the surface by a maximum number of fluid particles.
To avoid the need during manufacture and assembly for handling the pins individually it is here proposed that all pins of each successive pair of rows be formed of one continuous piece of wire which can be handled as a unit and this contemplates the use of a serpentine or helical coil having straight or flattened sides or a narrow elongated loop formation. Thus the long straight sides of each helix constitute a double generator; Figure 2 is an end view thereof; Figure 3 is a broken away fragment in perspective; Figure 4 is an enlarged detail perspective of a few rows of coils with end loop locatorchannels fitted alternately to opposite ends of neighboring helical lengths of wire and Figure 5 is a section on line 5--5 of Figure 2.
In the drawings the assembly is illustrated as comprising a group of flat plates 6 in superposed spaced relation affording a stack of fluid flow passages which cormnunicate selectively at one end with connector pipes or tubes 1, 8, 9 and I0 and at the opposite end with similar connector pipes la, 8a, 9a and Ito.
As shown there are six passages and as pest seen in Figure 2 it will be noted that the first and the fifth passages are joined with the con nector tubes 8 and m; that the second and sixth passages are joined with connector tubes 9 and So; that the third passage is joined with the connector tubes 1 and la and that the fourth passage is joined with the connector tubes H and Illa. The construction is such that the unit may be placed in the oxygen producing system for fluid flow in either direction. The several con-- nector tubes are to be coupled by suitable valving which controls the flow of fluids through thepassages. Thus in one setting of the selector valves the connector tubes Ill and lta will carry oxygen after having been separated in the processing treatment; the connector tubes 7 and la will carry unbalanced air; the connector tubes 9 and 9a will carry compressed air to be treated and'whose temperature is to be lowered beforehand with an accompanying deposit of impurities and the connector tubes 8 and 8a will carry cold nitrogen. As an example of a resetting of the valves the compressed air to be chilled will be directed through the passages joined with the tubes 8 and 8a and the waste nitrogen will be directed through the passages joined by the connector tubes 9 and 9a and in taking on heat will vaporize and carry away those impurities previously deposited in the passages.
A stack of thin wall plates, while promoting rapid heat transfer and having the advantage of lightweight, have a more important significance with reference to making up a smaller and more efficient package with great ruggedness by supplementing the wall surface area through the use of internal stiffening struts secured to the Walls and extending across the passages. Thus in the regions near opposite ends of each passage it is proposed to insert the serpentine ribbons H set on edge for brazed attachment to the opposing faces of passage Walls with their successive straight lengths extending transversely of the passage. These strips I i are apertured or formed throughout their length with a series of spaced and relatively large openings and since they are located immediately adjacent the fluid inlet and outlet connections which occupy a relatively small part of the width of the passage they serve not only as stiifeners and as increased radiation surfaces but also as spreader 'bafiies for the incoming fluid flow in that the fluid traveling from end to end will be more uniformly distributed throughout the passage. Through the intermediate length of each passage and extending in longitudinal rows transversely spaced apart are the pin struts it, each joined at opposite ends to the opposing surfaces of the passage and ex tending; on a straight line across the passage space.
By making the pins E2 of small diameter in relation to their length and spacing them closely together a very large number can be accommodated and they insure an abundance of surface area for carrying heat to and from the walls and for exposure to fluid flow. Their arrangement in rows minimizes fluid resistance. They are here constituted by successive straight runs of flattened helical coils of wire. The elongated convolutions are wrapped on a flat mandrel or otherwise formed so that successive wire pins have their opposite ends joined by return bends or end loops. fhus each continuous piece of helical wire consists of two spaced apart rows of spaced apart pins together with opposite end connecting loops. It is proposed that all the loops at least at one end of the elongated convolutions shall be nested or fitted within a channel section stiffener strip It. By fitting the channel to the coils as a subassembly the pins will be securely located and held against deflection and injury and rendered more convenient to handle. The several wire subassemblies may be placed side by side with the end channels alternately arranged for fixed abutment with the opposing faces of the passage walls. In this fashion the side flanges of the channels serve to space apart the neighboring wire helices at both the top and bottom, as viewed in Figure 4, with the flanges of the alternately disposed channels cooperating in succession and being aligned in pairs in common planes.
For ease of manufacture each intermediate wall plate 6 is transversely slitted for a short distance inwardly at each side and the material between the slits is alternately pressed upwardly as at M and downwardly as at 5 and preferably also formedwith terminal outwardly extending hottoming flanges, not shown. Similar formations extending downwardly, as at It, on the uppermost' wall'plate' and upwardly, as at IT, on the lowermost wall plate are also provided and the purpose of these several tabs is merely to space and locate the plates during the assembly operation and the subsequent brazing operation. Thereafter all of the tabs or if desired only the outwardly extending terminal portions may be sheared 01f completely.
For leakproof closure of the sides and ends of the passages between the stack of plates and for increased structural strength at the sides there are employed spacer bars [8 of relatively thick material inserted between the successive plates 6-6 at their edges at all four sides of the assembly. The use of such bars for closing purposes enables the temporary spacer tabs to be sheared off, as previously referred, to. The closure bars IS in the opposite ends of the assembly are arranged so as to leave openings for communication with the respective connector tubes. Thus by reference to Figure 5 it will be seen that the connector tube 8 is a short length of pipe having screw threads formed on one end for coupling purposes and having its opposite end closed by a cap l9 and being formed with a pair of s10ts on one side in alignment with two of the passages in the plate stack; Each slot I9 is enclosed by top and bottom plates 2li29 having circular openings defined by marginal flanges or collars 2i into which the tube is fitted. Between the outer edges of the cooperating plates 2Ei26 is-a U-shaped closure bar 22 to complete the fluid carrying conduit between the connector tube 8 and the heat exchanging passage. For adding stiffness a corrugated plate 23 is inserted between each set of plates 2ii20 with its corrugations extending in the direction of flow and constituting struts which tie the plates together. In like manner communication is provided between the remaining passages and their respective connector tubes.
After the several parts have been preformed they are broughttogether into the final stack assembly relation and by means of suitable locating fixtures they are so held and then placed in a brazing oven and intimately bonded at all-points of abutment. According to conventional practices the brazing material may be precoated on such contacting parts.
We claim:
1. In an oxygen regenerator or the like, a succession of superposed flat wall plates spaced apart, side and end closures for the spaces between the plates to thereby form a stack of sealed fluid flow passages, a series of inlet connectors arranged side by side at one end in selective communication with the fluid flow passages for delivery of several different fluids in staggered relation to successive fluid flow passages, a series of outlet connectors similarly arranged at the opposite end and each connector communicating with its fluid flow passage through an endclosure for a distance constituting a small fraction'of the passage width, apertured serpentine distributors located in the opposite ends of the passages and set on edge with opposite edges joined to the adjacent faces of said plates and thereby stiffening the'plate assembly, a series of flattened coils ofhelically wound wire extending longitudinally of each passage in transversely spaced side by side relation and with spacers between adjoining side lengths of the adjoining flattened coils, said spacers comprising longitudinally extending cha-nnels fitted in nested relation to the coil end loops, one for each coil and arranged-alternately on opposite end loops and secured by brazing or the like to both the wire coils and the plate surfaces.
2. In combination, spaced apart conduit walls, a series of flattened coils of wire arranged side by side within the space between said walls and with their straight portions extending across the space and their return loop portions adjacent opposite walls, and elongated elements of channel shape in transverse section, one for each coil, fitted in nested relation to said loop portions, said elements being fitted to ends opposite one another on succeeding coils and being alternately secured to opposing wall faces with the flanges thereof cooperating with one another to bear on and space apart the neighboring coils, said return loop portions extending generally transversely of said channels.
3. In a device of the character described, flat walls spaced apart to provide fluid flow space therebetween extending between an inlet and an outlet, channeled locator strips secured in parallel spaced relation on the opposing faces of said walls with the channels carried by opposing faces in offset staggered relation and arranged so that successive channel side flanges, extending inwardly from each face, are uniformly spaced apart and in planes common to successive flanges on the opposing face and a group of pin struts extending between opposing wall faces, comprising a succession of flat helical coils of wire having spaced apart straight side strut portions successively joined at opposite ends by return bends which nest between and are secured to succeeding flanges, said return bends extending transversely of said channels.
4. In an oxygen regenerator or the like, a stack of superposed passages for the flow of several different fluids, the walls of adjacent passages being common to said adjacent passages, each passage including spaced apart flat wall plates andhaving an inlet and an outlet spaced apart and near opposite ends of the passage; a row of spaced apart perforated distributor strips positioned between said wall plates adjacent each of the opposite ends of the passage near the inlet and outlet respectively, with each strip corresponding in width to the space between said wall plates and being set on edge and extending in a plane substantially at right angles to said wall plates, said strips being joined along opposite edges to adjoining faces of both plates; and a group of spaced pins throughout the passage between said rows of distributor strips, said pins comprising the straight sides of a series of flattened helical coils of wire whose opposite end loops are joined to said plates.
5. In an oxygen regenerator or the like, a group of spaced apart flat wall plates affording fluid passages therebetween, each passage having an inlet and an outlet for the entry and exit of fluid;
spacer pins within the passages comprising flattened helical coils of wire, each coil including two spaced apart rows of spaced apart pin portions, the successive pin portions in each row having their opposite ends joined by returnbends to adjacent pins in the opposite row, said coils being arranged'in side by side spaced apart relation; and elongated spacer flanges fitted between the pin portions of adjacent coils and being arranged alternately on opposite return bends of the coils and secured to said walls, said flanges extending in their longitudinal dimension generally transversely of said return bends.
6. Apparatus of the character described, including, means providing parallel spaced apart flat walls providing a fluid flow passage therebetween with an inlet and an outlet thereto; a plurality of flattened helical wire coils between the walls, each coil including two spaced apart rows of spaced apart pin portions extending at right angles to the surfaces of said walls, the successive pin portions in each row having their opposite ends joined by return bends to adjacent pins in the opposite row; and elongated coil spacing elements of channel shape in transverse section, said elements being fitted in nested relation over said return bends and having side flanges in bearing contact with adjacent coils to space said adjacent coils apart, said return bends extending generally transversely of said channel elements.
PHILIP S. ROGERS.
.. WILLARD O. EMMONS.
JOHN W. GODFREY. JAMES MILTON KELSO.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,409,967 Prat Mar. 21, 1922 2,093,256 Still Sept. 14, 1937 2,308,319 Stanton Jan. 12, 1943 2,439,208 Gloyer Apr. 6, 1948 FOREIGN PATENTS Number Country Date 559,107 Great Britain Feb. 3, 1944 574,949 Great Britain Jan. 28, 1946
US50496A 1948-09-22 1948-09-22 Oxygen regenerator Expired - Lifetime US2591878A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US50496A US2591878A (en) 1948-09-22 1948-09-22 Oxygen regenerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US50496A US2591878A (en) 1948-09-22 1948-09-22 Oxygen regenerator

Publications (1)

Publication Number Publication Date
US2591878A true US2591878A (en) 1952-04-08

Family

ID=21965565

Family Applications (1)

Application Number Title Priority Date Filing Date
US50496A Expired - Lifetime US2591878A (en) 1948-09-22 1948-09-22 Oxygen regenerator

Country Status (1)

Country Link
US (1) US2591878A (en)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2784947A (en) * 1954-09-13 1957-03-12 Air Preheater Heat exchange assembly
US2813701A (en) * 1954-09-02 1957-11-19 United Aircraft Corp Cross-flow heat exchanger
US2814470A (en) * 1952-02-12 1957-11-26 Air Preheater Heat exchanger
US2870998A (en) * 1954-05-14 1959-01-27 Air Preheater Heat exchanger walls with coupled sinuous fin elements
US2961222A (en) * 1957-12-06 1960-11-22 Trane Co Heat exchanger
US3177932A (en) * 1963-06-24 1965-04-13 Hupp Corp Drum type heat transfer apparatus
US3216495A (en) * 1963-08-07 1965-11-09 Gen Motors Corp Stacked plate regenerators
US3313343A (en) * 1964-03-26 1967-04-11 Trane Co Heat exchange apparatus
US3495656A (en) * 1967-03-31 1970-02-17 Marston Excelsior Ltd Plate-type heat exchanger
US4002201A (en) * 1974-05-24 1977-01-11 Borg-Warner Corporation Multiple fluid stacked plate heat exchanger
US5462113A (en) * 1994-06-20 1995-10-31 Flatplate, Inc. Three-circuit stacked plate heat exchanger
US5964280A (en) * 1996-07-16 1999-10-12 Modine Manufacturing Company Multiple fluid path plate heat exchanger
US6615590B1 (en) * 1999-12-16 2003-09-09 Smc Corporation Heat exchanger for temperature control
US6705392B2 (en) * 2001-03-05 2004-03-16 Nissan Motor Co., Ltd. Heat exchanger
US20080236802A1 (en) * 2006-10-12 2008-10-02 Andreas Koepke Plate heat exchanger
US20090120607A1 (en) * 2007-11-08 2009-05-14 Cheon Peter Cooler for spatially confined cooling
DE102010015371A1 (en) * 2010-04-19 2011-10-20 Alexander Alles Fluid media distributing device for use in honeycomb channels in e.g. heat exchanger, has adjacent plates including wave type profiles, and intermediate layer arranged in slot channels and including ribbed plates and contact points
US20190024982A1 (en) * 2017-07-24 2019-01-24 Hamilton Sundstrand Corporation Heat exchanger assembly with parting sheet support
EP3671093A1 (en) * 2018-12-18 2020-06-24 Valeo Autosystemy SP. Z.O.O. A multi-circuit heat exchanger system

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1409967A (en) * 1920-10-29 1922-03-21 Prat Emile Heat exchanger
US2093256A (en) * 1935-01-10 1937-09-14 Still William Joseph Heat exchange element
US2308319A (en) * 1939-11-25 1943-01-12 Gen Electric Heat exchange surface
GB559107A (en) * 1942-10-29 1944-02-03 Edwin James Bowman Improvements in radiators for cooling liquids and for heating rooms
GB574949A (en) * 1943-11-18 1946-01-28 James Frank Belaieff Improvements in or relating to plate heat exchange apparatus
US2439208A (en) * 1945-09-25 1948-04-06 American Locomotive Co Heat exchanger

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1409967A (en) * 1920-10-29 1922-03-21 Prat Emile Heat exchanger
US2093256A (en) * 1935-01-10 1937-09-14 Still William Joseph Heat exchange element
US2308319A (en) * 1939-11-25 1943-01-12 Gen Electric Heat exchange surface
GB559107A (en) * 1942-10-29 1944-02-03 Edwin James Bowman Improvements in radiators for cooling liquids and for heating rooms
GB574949A (en) * 1943-11-18 1946-01-28 James Frank Belaieff Improvements in or relating to plate heat exchange apparatus
US2439208A (en) * 1945-09-25 1948-04-06 American Locomotive Co Heat exchanger

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2814470A (en) * 1952-02-12 1957-11-26 Air Preheater Heat exchanger
US2870998A (en) * 1954-05-14 1959-01-27 Air Preheater Heat exchanger walls with coupled sinuous fin elements
US2813701A (en) * 1954-09-02 1957-11-19 United Aircraft Corp Cross-flow heat exchanger
US2784947A (en) * 1954-09-13 1957-03-12 Air Preheater Heat exchange assembly
US2961222A (en) * 1957-12-06 1960-11-22 Trane Co Heat exchanger
US3177932A (en) * 1963-06-24 1965-04-13 Hupp Corp Drum type heat transfer apparatus
US3216495A (en) * 1963-08-07 1965-11-09 Gen Motors Corp Stacked plate regenerators
US3313343A (en) * 1964-03-26 1967-04-11 Trane Co Heat exchange apparatus
US3495656A (en) * 1967-03-31 1970-02-17 Marston Excelsior Ltd Plate-type heat exchanger
US4081025A (en) * 1974-05-24 1978-03-28 Borg-Warner Corporation Multiple fluid stacked plate heat exchanger
US4002201A (en) * 1974-05-24 1977-01-11 Borg-Warner Corporation Multiple fluid stacked plate heat exchanger
US5462113A (en) * 1994-06-20 1995-10-31 Flatplate, Inc. Three-circuit stacked plate heat exchanger
US5964280A (en) * 1996-07-16 1999-10-12 Modine Manufacturing Company Multiple fluid path plate heat exchanger
US6615590B1 (en) * 1999-12-16 2003-09-09 Smc Corporation Heat exchanger for temperature control
US6705392B2 (en) * 2001-03-05 2004-03-16 Nissan Motor Co., Ltd. Heat exchanger
US20080236802A1 (en) * 2006-10-12 2008-10-02 Andreas Koepke Plate heat exchanger
US7740058B2 (en) 2006-10-12 2010-06-22 Modine Manufacturing Company Plate heat exchanger
US20090120607A1 (en) * 2007-11-08 2009-05-14 Cheon Peter Cooler for spatially confined cooling
DE102010015371A1 (en) * 2010-04-19 2011-10-20 Alexander Alles Fluid media distributing device for use in honeycomb channels in e.g. heat exchanger, has adjacent plates including wave type profiles, and intermediate layer arranged in slot channels and including ribbed plates and contact points
US20190024982A1 (en) * 2017-07-24 2019-01-24 Hamilton Sundstrand Corporation Heat exchanger assembly with parting sheet support
EP3671093A1 (en) * 2018-12-18 2020-06-24 Valeo Autosystemy SP. Z.O.O. A multi-circuit heat exchanger system
WO2020127440A1 (en) * 2018-12-18 2020-06-25 Valeo Autosystemy Sp. Z O.O. A multi-circuit heat exchanger system

Similar Documents

Publication Publication Date Title
US2591878A (en) Oxygen regenerator
US3528783A (en) Multilayer catalytic reactor
US6523606B1 (en) Heat exchanger tube block with multichamber flat tubes
US2812165A (en) Header units for plate type heat exchanger
DE69519445T2 (en) Heat exchanger
DE2416309C2 (en) Heat exchangers for refrigerating machines and processes for their manufacture
DE2232386B2 (en) Device for cold drying of gas, in particular air
US4174987A (en) Method of making heat exchange structure
DE19623245C2 (en) Heat exchanger
DE3248096C2 (en) Standing device for cooling gases under high pressure with a high proportion of dust
CH660519A5 (en) COOLING RIB HEAT EXCHANGER.
US2703700A (en) Heat interchanger
DE2742839C2 (en)
US3330336A (en) Heat exchanger tubes with longitudinal ribs
DE2045370A1 (en) Radial flow heat exchanger
DE1501603B1 (en) Finned tube cooler
DE19529227A1 (en) Storage block for regenerative heat exchangers
EP3730890A1 (en) Plate heat exchanger
CH367842A (en) Multi-flow countercurrent tubular heat exchanger
DE10359697A1 (en) Heat exchanger heat pump for hot water supply system has first and second fluid pipes and a partitioned corrugated panel
DE3009532C2 (en) Heat exchanger
DE1989033U (en) SECONDARY HEAT TRANSFER DEVICE FOR RADIATOR AND AIR HEATER.
DE2422168A1 (en) Heat exchanger with finned pipe clusters - has stabilising corrugated pipe spacers and pipe cluster straps
SU872936A1 (en) Shell-and-tube heat exchanger
DE623268C (en) Hollow bodies of any shape formed by solid, heat transferring partitions