US2237239A - Refrigeration apparatus - Google Patents

Refrigeration apparatus Download PDF

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US2237239A
US2237239A US8324A US832435A US2237239A US 2237239 A US2237239 A US 2237239A US 8324 A US8324 A US 8324A US 832435 A US832435 A US 832435A US 2237239 A US2237239 A US 2237239A
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header
coil
refrigerant
coils
inlet
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US8324A
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Lawrence C Smith
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Fedders Manufacturing Co Inc
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Fedders Manufacturing Co Inc
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
    • 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
    • F28D7/08Heat-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 otherwise bent, e.g. in a serpentine or zig-zag
    • 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
    • F28D7/08Heat-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 otherwise bent, e.g. in a serpentine or zig-zag
    • F28D7/082Heat-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 otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
    • F28D7/085Heat-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 otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration in the form of parallel conduits coupled by bent portions
    • F28D7/087Heat-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 otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration in the form of parallel conduits coupled by bent portions assembled in arrays, each array being arranged in the same plane
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/0282Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by varying the geometry of conduit ends, e.g. by using inserts or attachments for modifying the pattern of flow at the conduit inlet or outlet

Definitions

  • This invention relates to improvements in refriger'ation systems.
  • the invention is particularly directed to systems in which a plurality of independent cooling coil units are supplied by a common header or reservoir.
  • the ends orterminals of each coil were simply connected to communicate with the header with little or no attention given to apportioning the liquid refrigerant.
  • deviations in level due to inaccuracies in assembly or installation, have caused certain coils to be deprived of their proportionate supply of refrigerant, with accompanying ineiiiciencies in the entire system.
  • a common header as a supply means for two or more cooling coil units, whereloops to provide a continuous refrigerant pasbrazing as indicated by the numeral '30.
  • Fig. 4 is a partial longitudinal section through the upper header of an installation similar to that of Fig. 1, provided with adiflerent type of metering port.
  • the principles of the invention are applied to ⁇ a cooling device I0 which is specifically adapted for use in air conditioning systems in which a moving body of air is forced to ow through a duct in which the coil islocated.
  • the coolg ⁇ device I0 is formed of horizontally disposed feed and suction headers I2 and I3. which are organized with individual vertically disposed cooling coils orY units I6, I1, I8, I3, 23, 2
  • the lower or suction header I3 is formed Vwith holes 28 for receiving elbows or discharge terminals 29, which are secured to the lower extremity of each coil.
  • Each pair of adjacent coils are provided with common cross ns 3
  • the coils may be remote from each other in other systems to be supplied with individual iin structures.
  • the cooling device is inserted in a refrigerant circuit, which includes a supply conduit 40 having a terminal-fitting 33 entering the head 3l of the feed header l2, and a. suction conduit 35 communicating with the suction header '
  • the supply conduit iseprovided with a suitable control such as a thermostatic expansion valve 31, which, aswell understood in theartycontains a valve 33 which opens or closes an orifice 39 in response to temperature variations in the suction conduit 35, under con-lV trol of the bulb B. ⁇ Liquid refrigerant is thus introduced into the header i2 in controlled quan- .titles dependent upon the orifice area of the valve.
  • the device I D is positioned transversely in an air duct 4
  • the air flows'across the fins. from left to right in Fig. 1, and .it has been practically demonstrated that a preferential heat exchange condition is set up in this type of installation, in which the heat transfer from thecoils'to the air stream progressively diminishes in succeeding coils as the result of loss -of air velocity and the progressive reduction of temperature differential.
  • the first coil Ii in one installation was found to bear over thirty per cent of the total heat transfer load and the remaining coils progressively less to a factor of seven per cent on the last coil 23.
  • I propose to effect a proportionate feed in a4 multiple coil system from a common header by providing ports in the portions of the coil feed terminals within the feed header I2. These ports may be formed as axial slits or saw cuts.
  • 617 to 23h, inclusive is advantageously made substantially equal to the orifice area of the thermostatie valve orifice 39 under full throttle.v
  • the relative size of the slits may be easily computed; for example,
  • the slit area of the first terminal ISa would be thirty per cent of the area of the valve orifice, as reected by its load factor, while the slot width of the last terminal would be seven per cent of the orifice area.
  • the header l2 would fill rapidly until the liquid level would approximately reach the top of the terminals, whereupon the level would remain constant as the result of equalization of orifice and slit areas until the valve setting changed.
  • the refrigerant would ll the header to approximately a half way mark, as
  • said refrigerant coil comprising an upper header disposed in a substantially horizontal plane, a plurality of rows of pipes depending from said header and having the upper ends thereof disposed within said header in vertical position, said rows being spaced and being adapted to be disposed along said duct in successive cross-sectional planes thereof, said header being formed with means for admitting refrigerant thereto, said pipe ends within said header being formed with apertures, the area of the aperture in one end row of pipe being greater than the area of the aperture in succeeding rows of pipes, the areas of the apertures gradually diminishing from one end of said header to the other.
  • a refrigerant coil connected to said valve, said coil comprising a horizontal header disposed at a high point of said coil and a plurality of rows of tubes depending from said coil, the upper end of each row of tubes extending into said header in a vertical direction to a point level always feed the correct amount of refrigl erant to their respective coils.
  • the terminals may each be formed with a r ow of holes ISc, I'Ic, lc,
  • a refrigerant coil adapted to be disposed in an air duct to effect the cooling of air moving adjacent the top of said header, each of said ends being formed with an aperture, the total areas of said apertures 'substantially equalling the area of said orifice, the areas of each aperture being different and being a maximum [at one end of the coil and a minimum at the opposite end, the intermediate apertures being pro' gressively proportioned between said maximum and minimum, whereby refrigerant admitted to said header may discharge in progressively varying quantities into all of said tubes in proportion to the area of the aperture therein and said rows may thereby be proportioned to differential load demands.
  • each of said separate coil members constituting a length of pipe disposed in a cross-sectional plane of said duct, said planes being spaced along said duct whereby air travelling therethrough successively contactsv said separate c'oil members, said separate coil members being bent back and forth to occupy a substantial portion of their respective cross-sectional planes from the top of said duct to the bottom thereof, the ends of said coil members' extending into said header to adjacent the top thereof.
  • said ends beingformed with apertures to admit refrigerant in said header to said coils, the areas of the apertures in the successive coil ends being progressively less from the coil adjacent the inlet end of the duetto the coil adjacent the outlet end of the duct, whereby the several coils will receive amounts of refrigerant proportioned to the change in the temperature differential between the air and refrigerant as the air moves past said coils.
  • An evaporator for cooling a stream of gas passing therethrough; said evaporator comprising an elongated inlet header and a series of heat exchange devices arranged one behind another with respect to the direction of flow of said gas; each of said devices having an inlet member extending vertically into said header and having an aperture with a predetermined area below the normal liquid level in said header, said areas progressively decreasing in size in a direction determined'by the direction of said flow and being graduated to distribute to ,the respective devices amounts of refrigerant determined by the relative positions of such devices with respect to each other and to the direction of flow of the gas.
  • An evaporator for cooling a stream ofA gas passing therethrough; said evaporator comprising an elongated inlet header ⁇ and a series of coils arranged one behind another with respect to the direction of flow of said gas; each of said coils having an inlet member extending vertically into said header and having an aperture with a predetermined area below the normal liquid level in said header, said areas progressively. decreasing in size in a direction'determined by the direction of said flow and being graduated to distribute to the respective coils amounts of refrigerant determined by the relative positions of such coils with respect to each other and to the direction of iiow of the gas.
  • An evaporator for cooling a stream of gas passing therethrough comprising an inlet header and a series of coils adapted to be contacted by said stream of gas, each of said coils having an inlet member extending into said header, each of said inlet members having formed therein below the normal liquid level in said header aperture means with a predetermined area, said areas of the different inlet members varying in size in accordance with the heat loads on the respective coils served thereby.
  • said evaporator comprising an inlet header and a series of heat exchange devices adapted to be contacted by said stream of gas, each of said devices having an inlet member extending into said header, each of said inlet members having ,formed therein an aperture below the normal liquid level in said header, the areas of said apertures of the diierent inlet members varying in size and being graduated to distribute to the respective devices amounts of refrigerant determined by the heat' loads on said respective devices, each of saidinlet members having means for providing communication between the interior thereof and the interior of said header above the normal liquid level in said header.
  • An evaporator for cooling a stream of gas comprising an inlet header and a series of heat exchange devices adapted to be contacted by said streamof gas, each of said heat exchange devices having an inlet member extending into said header, each of said inlet members having formed therein below the normal liquidflevel in said header aperture means with a. predetermined area, said areas of the dif-v ferent inlet members being determined in accordance with the heat loads on the respective heat exchange devices served thereby, each of said /inlet members having means for providing communication between the interior thereof and the interior of said header above the normal liquid level in said header.

Description

April 1, 1941 L. c. SMITH 2,237,239 REFRIGERATION APAnA'rps K Filed Feb. 26, 1955 H1 ..1 IIIIIIIllIIIllllllIllIllllIllllI||llh'lllllllllllllllllll c.
Illllllllllllllllllll Illlllllllllllllllllllllllllllllllll /3 Cttorneg REFRIGERATION APPARATUS Lawrence C. Smith, Buffalo, N. Y., assignor to Fedders Manufacturing Company, Inc., Buffalo,
Application February 2s, 1935, serial No. 8,324
(o1. ca -127) Claims.
This invention relates to improvements in refriger'ation systems.
The invention is particularly directed to systems in which a plurality of independent cooling coil units are supplied by a common header or reservoir. In prior art structures of this nature the ends orterminals of each coil were simply connected to communicate with the header with little or no attention given to apportioning the liquid refrigerant. As a result, deviations in level, due to inaccuracies in assembly or installation, have caused certain coils to be deprived of their proportionate supply of refrigerant, with accompanying ineiiiciencies in the entire system.
This condition has been particularly aggravated in systems where, due to operating conditions, the coils have required different feed rates, and where an attempt has been made to cope with the problem by abandoning the common header in favor of the more expensive and somewhat impractical individual coil feed by separate thermostatic control valves.
According to the present invention, it is proposed to provide a common header as a supply means for two or more cooling coil units, whereloops to provide a continuous refrigerant pasbrazing as indicated by the numeral '30.
an air duct showing the cooling unit of Fig. i positioned therein; and,
Fig. 4 is a partial longitudinal section through the upper header of an installation similar to that of Fig. 1, provided with adiflerent type of metering port.
The principles of the invention are applied to` a cooling device I0 which is specifically adapted for use in air conditioning systems in which a moving body of air is forced to ow through a duct in which the coil islocated.
In Figs. 1 and 3, the coolg` device I0 is formed of horizontally disposed feed and suction headers I2 and I3. which are organized with individual vertically disposed cooling coils orY units I6, I1, I8, I3, 23, 2|, 22, and 23..'lhch unit may be a continuous pipe or fabricated of horizontally disposed tubes '2l connected by As shown in Fig. 2, the feed terminals preferably extend diametrically through the interior of the-header and engage the upper portion of the wall. Inasmuch as the positioning of the terminals relative to the axis ofthe header may be a significant consideration, as hereinafter set forth, it will be obvious Ithat abuttingthem against the wall ofthe header serves as a simple and efficient gaging or locating means.
The lower or suction header I3 is formed Vwith holes 28 for receiving elbows or discharge terminals 29, which are secured to the lower extremity of each coil.
Each pair of adjacent coils are provided with common cross ns 3| having aligned holes 32, through which the tubes 24 extend. 'Ihis lends a unitary structural characteristic to the assembly which is desirable in a cooling device for an air conditioning system. However, it'will be understood that the coils may be remote from each other in other systems to be supplied with individual iin structures.
The cooling device is inserted in a refrigerant circuit, which includes a supply conduit 40 having a terminal-fitting 33 entering the head 3l of the feed header l2, and a. suction conduit 35 communicating with the suction header '|35 through a head 36. The supply conduit iseprovided with a suitable control such as a thermostatic expansion valve 31, which, aswell understood in theartycontains a valve 33 which opens or closes an orifice 39 in response to temperature variations in the suction conduit 35, under con-lV trol of the bulb B.` Liquid refrigerant is thus introduced into the header i2 in controlled quan- .titles dependent upon the orifice area of the valve.
In assembly, the device I D is positioned transversely in an air duct 4| `(Fig. 3) so that the fins 29 are parallel vto the direction of air iiow therein. The air flows'across the fins. from left to right in Fig. 1, and .it has been practically demonstrated that a preferential heat exchange condition is set up in this type of installation, in which the heat transfer from thecoils'to the air stream progressively diminishes in succeeding coils as the result of loss -of air velocity and the progressive reduction of temperature differential. For example, the first coil Ii in one installation was found to bear over thirty per cent of the total heat transfer load and the remaining coils progressively less to a factor of seven per cent on the last coil 23.
I propose to effect a proportionate feed in a4 multiple coil system from a common header by providing ports in the portions of the coil feed terminals within the feed header I2. These ports may be formed as axial slits or saw cuts. VFor example, as shown in Fig. 1, the terminals l6a to 23a inclusive are supplied with slits 16h, IIb, |8b, lsb, 20h, 2lb, 22h, and 23h, all of which vary in width in decreasing ratio from the widest slit |617, and in direct ratio to the previously discussed load factor.
Where a large reserve supply of refrigerant is desiredin the header l2, the total area of the slits |617 to 23h, inclusive, is advantageously made substantially equal to the orifice area of the thermostatie valve orifice 39 under full throttle.v
With this value as a basis, the relative size of the slits may be easily computed; for example,
the slit area of the first terminal ISa would be thirty per cent of the area of the valve orifice, as reected by its load factor, while the slot width of the last terminal would be seven per cent of the orifice area.
It will be obvious, therefore, that under a full throttle valve condition, the header l2 would fill rapidly until the liquid level would approximately reach the top of the terminals, whereupon the level would remain constant as the result of equalization of orifice and slit areas until the valve setting changed. Similarly, under normal supply conditions, where the valve orifice is partially closed, the refrigerant would ll the header to approximately a half way mark, as
shown in Fig. 1. In any event, the level varies with the orifice opening, and the slits at any CFI through said duct, said refrigerant coil comprising an upper header disposed in a substantially horizontal plane, a plurality of rows of pipes depending from said header and having the upper ends thereof disposed within said header in vertical position, said rows being spaced and being adapted to be disposed along said duct in successive cross-sectional planes thereof, said header being formed with means for admitting refrigerant thereto, said pipe ends within said header being formed with apertures, the area of the aperture in one end row of pipe being greater than the area of the aperture in succeeding rows of pipes, the areas of the apertures gradually diminishing from one end of said header to the other.
2. In combination with a refrigerant control valve having a predetermined orifice area under full throttle, a refrigerant coil connected to said valve, said coil comprising a horizontal header disposed at a high point of said coil and a plurality of rows of tubes depending from said coil, the upper end of each row of tubes extending into said header in a vertical direction to a point level always feed the correct amount of refrigl erant to their respective coils.
Other formations may be substituted for. the
slits to obtain approximately the same results. For example, the terminals may each be formed with a r ow of holes ISc, I'Ic, lc, |90, etc., with the total area of each row of holes corresponding to the load factors of their respective coils. It is recommended that holes in the adjacent terminals be positioned in the same plane to prevent irregular relative feed conditions.l
.As a practical consideration, it is extremely difficult to obtain an absolutely co-planar relation between the bottom of the slits, since slight discrepancies in assembly of units up to ten feet in depth are apt to occur. In installing the unit, slight errors in levelling the feed header may alsol be made. These errors have caused con- -siderable trouble` in prior art structures, as previously discussed, and, while in the present invention similar errors may also occur, it will be observed that the great height of the slits in proportion to their width renders slight errors inconsequential, particularly when the header has a relatively high -liquid level.
From the foregoing description, it will be understood that I propose to apply the invention to any multi-coil unit refrigerant system, and therefore the invention is not to be limited to the precise means described, but rather is to be construed in the light of the following claims.
I claim:
1. A refrigerant coil adapted to be disposed in an air duct to effect the cooling of air moving adjacent the top of said header, each of said ends being formed with an aperture, the total areas of said apertures 'substantially equalling the area of said orifice, the areas of each aperture being different and being a maximum [at one end of the coil and a minimum at the opposite end, the intermediate apertures being pro' gressively proportioned between said maximum and minimum, whereby refrigerant admitted to said header may discharge in progressively varying quantities into all of said tubes in proportion to the area of the aperture therein and said rows may thereby be proportioned to differential load demands.
3. T'he combination with an air duct having closed sides and open ends and means for moving air through said duct from one of said ends to the other, of a refrigerant coil disposed in said duct, said coil comprising a substantially horizontal header disposed at a high point in said duct, means for admitting refrigerant to said header, and a plurality of separate coil members connected to said header., each of said separate coil members constituting a length of pipe disposed in a cross-sectional plane of said duct, said planes being spaced along said duct whereby air travelling therethrough successively contactsv said separate c'oil members, said separate coil members being bent back and forth to occupy a substantial portion of their respective cross-sectional planes from the top of said duct to the bottom thereof, the ends of said coil members' extending into said header to adjacent the top thereof. said ends beingformed with apertures to admit refrigerant in said header to said coils, the areas of the apertures in the successive coil ends being progressively less from the coil adjacent the inlet end of the duetto the coil adjacent the outlet end of the duct, whereby the several coils will receive amounts of refrigerant proportioned to the change in the temperature differential between the air and refrigerant as the air moves past said coils.
4. An evaporator for cooling a stream of gas passing therethrough; said evaporator comprising an elongated inlet header and a series of heat exchange devices arranged one behind another with respect to the direction of flow of said gas; each of said devices having an inlet member extending vertically into said header and having an aperture with a predetermined area below the normal liquid level in said header, said areas progressively decreasing in size in a direction determined'by the direction of said flow and being graduated to distribute to ,the respective devices amounts of refrigerant determined by the relative positions of such devices with respect to each other and to the direction of flow of the gas.
5. An evaporator for cooling a stream ofA gas passing therethrough; said evaporator comprising an elongated inlet header` and a series of coils arranged one behind another with respect to the direction of flow of said gas; each of said coils having an inlet member extending vertically into said header and having an aperture with a predetermined area below the normal liquid level in said header, said areas progressively. decreasing in size in a direction'determined by the direction of said flow and being graduated to distribute to the respective coils amounts of refrigerant determined by the relative positions of such coils with respect to each other and to the direction of iiow of the gas. i
6. An evaporator for cooling a stream of gas devices arranged one behind another with respect to the direction of flow of said gas; each of said devices having an inlet member extendpassing therethrough; said evaporator compris- Y ing an inlet header and a series of heat exchange ing into said header to a point above thenormal liquid level therein and having aperture means with a predetermined area below the normal liquid level in said header, said areas varying in size and being graduated to distribute to the respective devices amounts of refrigerant determined by the relative positions of such devices with respect to each other and to the direction i of flow of the gas.
distribute to the respective devices amounts of refrigerant determined by the heat loads on said respective devices.
8. An evaporator for cooling a stream of gas passing therethrough, said evaporator comprising an inlet header and a series of coils adapted to be contacted by said stream of gas, each of said coils having an inlet member extending into said header, each of said inlet members having formed therein below the normal liquid level in said header aperture means with a predetermined area, said areas of the different inlet members varying in size in accordance with the heat loads on the respective coils served thereby.
9. Anevaporator for cooling a stream of gas,
said evaporator comprising an inlet header and a series of heat exchange devices adapted to be contacted by said stream of gas, each of said devices having an inlet member extending into said header, each of said inlet members having ,formed therein an aperture below the normal liquid level in said header, the areas of said apertures of the diierent inlet members varying in size and being graduated to distribute to the respective devices amounts of refrigerant determined by the heat' loads on said respective devices, each of saidinlet members having means for providing communication between the interior thereof and the interior of said header above the normal liquid level in said header.
10. An evaporator for cooling a stream of gas, said evaporator comprising an inlet header and a series of heat exchange devices adapted to be contacted by said streamof gas, each of said heat exchange devices having an inlet member extending into said header, each of said inlet members having formed therein below the normal liquidflevel in said header aperture means with a. predetermined area, said areas of the dif-v ferent inlet members being determined in accordance with the heat loads on the respective heat exchange devices served thereby, each of said /inlet members having means for providing communication between the interior thereof and the interior of said header above the normal liquid level in said header.
LAWRENCE C. SMITH.
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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2874555A (en) * 1955-12-01 1959-02-24 Gen Motors Corp Evaporator arrangement
DE1139515B (en) * 1960-03-23 1962-11-15 Esslingen Maschf Method and device for supplying the refrigerant from a collecting tank under compressor pressure to the evaporator pipes of cooling devices, in particular artificial ice rinks
US3212278A (en) * 1963-06-07 1965-10-19 Phillips Petroleum Co Fluid distribution system
US3286482A (en) * 1964-07-10 1966-11-22 Carrier Corp Apparatus for controlling refrigerant flow in a refrigeration machine
DE1501552A1 (en) * 1966-02-09 1969-11-06 Kritzer Richard Walker Heat exchange element
US3499296A (en) * 1968-05-17 1970-03-10 Carrier Corp Refrigerant flow control mechanism
US3976128A (en) * 1975-06-12 1976-08-24 Ford Motor Company Plate and fin heat exchanger
US4738309A (en) * 1984-09-13 1988-04-19 Heinz Schilling Kg Gas/liquid or gas/gas exchanger
US6272881B1 (en) * 1998-04-03 2001-08-14 Denso Corporation Refrigerant evaporator and manufacturing method for the same
US6363965B1 (en) 1998-08-25 2002-04-02 Eaton Aeroquip Inc. Manifold assembly
EP2392881A1 (en) * 2010-06-04 2011-12-07 Thermofin GmbH Heat exchanger for phase converting coolant with horizontal distribution and collection pipe
US8783057B2 (en) 2011-02-22 2014-07-22 Colmac Coil Manufacturing, Inc. Refrigerant distributor

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2874555A (en) * 1955-12-01 1959-02-24 Gen Motors Corp Evaporator arrangement
DE1139515B (en) * 1960-03-23 1962-11-15 Esslingen Maschf Method and device for supplying the refrigerant from a collecting tank under compressor pressure to the evaporator pipes of cooling devices, in particular artificial ice rinks
US3212278A (en) * 1963-06-07 1965-10-19 Phillips Petroleum Co Fluid distribution system
US3286482A (en) * 1964-07-10 1966-11-22 Carrier Corp Apparatus for controlling refrigerant flow in a refrigeration machine
DE1501552A1 (en) * 1966-02-09 1969-11-06 Kritzer Richard Walker Heat exchange element
US3499296A (en) * 1968-05-17 1970-03-10 Carrier Corp Refrigerant flow control mechanism
US3976128A (en) * 1975-06-12 1976-08-24 Ford Motor Company Plate and fin heat exchanger
US4738309A (en) * 1984-09-13 1988-04-19 Heinz Schilling Kg Gas/liquid or gas/gas exchanger
US6272881B1 (en) * 1998-04-03 2001-08-14 Denso Corporation Refrigerant evaporator and manufacturing method for the same
US6363965B1 (en) 1998-08-25 2002-04-02 Eaton Aeroquip Inc. Manifold assembly
EP2392881A1 (en) * 2010-06-04 2011-12-07 Thermofin GmbH Heat exchanger for phase converting coolant with horizontal distribution and collection pipe
WO2011151218A1 (en) * 2010-06-04 2011-12-08 Thermofin Gmbh Heat exchanger for phase-changing refrigerant, with horizontal distributing and collecting tube
US9945593B2 (en) 2010-06-04 2018-04-17 Thermofin Gmbh Heat exchanger for phase-changing refrigerant, with horizontal distributing and collecting tube
US8783057B2 (en) 2011-02-22 2014-07-22 Colmac Coil Manufacturing, Inc. Refrigerant distributor

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