US20170153061A1 - Falling film evaporator - Google Patents

Falling film evaporator Download PDF

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Publication number
US20170153061A1
US20170153061A1 US15/319,323 US201515319323A US2017153061A1 US 20170153061 A1 US20170153061 A1 US 20170153061A1 US 201515319323 A US201515319323 A US 201515319323A US 2017153061 A1 US2017153061 A1 US 2017153061A1
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US
United States
Prior art keywords
tank
isolation member
refrigerant
outlet pipe
vapor outlet
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.)
Abandoned
Application number
US15/319,323
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English (en)
Inventor
Shun Yoshioka
Keita Hattori
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.)
Daikin Industries Ltd
Original Assignee
Daikin Industries Ltd
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Filing date
Publication date
Application filed by Daikin Industries Ltd filed Critical Daikin Industries Ltd
Assigned to DAIKIN INDUSTRIES, LTD. reassignment DAIKIN INDUSTRIES, LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HATTORI, KEITA, YOSHIOKA, SHUN
Publication of US20170153061A1 publication Critical patent/US20170153061A1/en
Abandoned legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D5/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation
    • F28D5/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation in which the evaporating medium flows in a continuous film or trickles freely over the conduits
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00—Evaporators; Condensers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00—Evaporators; Condensers
    • F25B39/02—Evaporators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00—Evaporators; Condensers
    • F25B39/02—Evaporators
    • F25B39/028—Evaporators having distributing means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0017—Flooded core heat exchangers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D3/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
    • F28D3/04—Distributing arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16—Heat-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 in parallel spaced relation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2339/00—Details of evaporators; Details of condensers
    • F25B2339/02—Details of evaporators
    • F25B2339/024—Evaporators with refrigerant in a vessel in which is situated a heat exchanger
    • F25B2339/0242—Evaporators with refrigerant in a vessel in which is situated a heat exchanger having tubular elements

Definitions

  • the present invention relates to a falling film evaporator.
  • patent literature 1 JP-A No. H 8-189726 discloses a falling film evaporator.
  • the falling film evaporator is a heat exchanger in which a liquid refrigerant distribution apparatus is provided between a heat transfer tube group in a tank and a vapor outlet pipe extending out from the upper portion of the tank; the liquid refrigerant distribution apparatus allows liquid refrigerant to fall downwardly onto the heat transfer tube group, the heat transfer tube group allows the fallen liquid refrigerant to evaporate.
  • Gas refrigerant evaporated by the heat transfer tube group flows out of the tank through the vapor outlet pipe extending out from the upper portion of the tank and is sent to a compressor.
  • the refrigerant in a gas-liquid two-phase state flows into the liquid refrigerant distribution apparatus through a refrigerant inlet pipe provided on the tank.
  • the gas refrigerant in the refrigerant in a gas-liquid two-phase state which has flowed into the liquid refrigerant distribution apparatus and the gas refrigerant generated as a result of evaporating with the heat transfer tube group flow toward the vapor outlet pipe provided in the upper portion of the tank.
  • the liquid refrigerant downwardly falling from the liquid refrigerant distribution apparatus is less prone to flowing out through the vapor outlet pipe because the liquid refrigerant is distant from the vapor outlet pipe.
  • the vapor outlet pipe extends out from a location other than the upper middle portion of the tank, for example, in the case in which a different member needs to be disposed on the upper portion of the tank, in the case in which an end of the vapor outlet pipe is not connected to the upper portion of the tank, or the like, the following portions of the liquid refrigerant downwardly falling from the liquid refrigerant distribution apparatus are generated, some portion is prone to reaching the vapor outlet pipe, and other portion is less prone to reaching the vapor outlet pipe.
  • the gas refrigerant flowing through this portion may carry the liquid refrigerant to cause the carryover in which the liquid refrigerant flows out of the tank through the vapor outlet pipe.
  • the present invention has been created in view of the above. It is an object of the present invention to provide a falling film evaporator which is able to reduce an outflow of liquid refrigerant even in the case in which the vapor outlet pipe is provided in a location other than the upper middle portion of the tank.
  • a falling film evaporator is a falling film evaporator used for a refrigeration apparatus.
  • the falling film evaporator includes a heat transfer tube group, a tank, a liquid refrigerant distribution part, a vapor outlet pipe, and an isolation member.
  • the heat transfer tube group has a plurality of heat transfer tubes flowing heat medium therein and longitudinally extending.
  • the tank has the heat transfer tube group disposed therein and is provided with a refrigerant flow inlet.
  • the liquid refrigerant distribution part allows liquid refrigerant of refrigerant in a gas-liquid two-phase state supplied in the tank through the refrigerant flow inlet to downwardly fall onto the heat transfer tube group.
  • the vapor outlet pipe extends out from a lateral or upper position of the tank other than a top of the tank as viewed in the longitudinal direction of the tank.
  • the isolation member covers a place below a lowest portion of a connection portion of the tank and the vapor outlet pipe as viewed in the axial direction of the heat transfer tubes, extends between the vapor outlet pipe and the liquid refrigerant distribution part, and allows refrigerant to pass through an upper portion.
  • the isolation member is provided such that the longitudinal direction of the isolation member is same as the longitudinal direction of the heat transfer tubes.
  • the position in which the vapor outlet pipe extends out from the tank is a lateral or upper position of the tank other than a top of the tank as viewed in the longitudinal direction of the tank, for example, the vapor outlet pipe may be provided such that the vapor outlet pipe extends out from a position higher than the liquid refrigerant distribution part.
  • the lateral or upper position (excluding the top) in which the vapor outlet pipe extends out as viewed in the longitudinal direction of the tank can be in a range of ⁇ 10 through ⁇ 100 degrees from the vertically top relative to the center of gravity of the tank as viewed in the longitudinal direction of the tank.
  • the longitudinal direction of the isolation member does not need to be exactly same as the longitudinal direction of the heat transfer tubes; for example, the longitudinal direction of the heat transfer tubes may be different from the longitudinal direction of the isolation member in a range of ⁇ 10 degrees to be substantially same as the longitudinal direction of the isolation member.
  • liquid refrigerant may be present close to the vapor outlet pipe.
  • the isolation member is provided to prevent liquid refrigerant close to the vapor outlet pipe from directly flowing toward the vapor outlet pipe. More specifically, even if the liquid refrigerant attempts to flow beyond the isolation member through the upper portion of the isolation member, the liquid refrigerant is less prone to flowing upwardly and less prone to reaching the vapor outlet pipe due to the own weight of the liquid refrigerant.
  • the liquid refrigerant is less prone to reaching the vapor outlet pipe because the isolation member is provided such that the longitudinal direction of the isolation member is same as the longitudinal direction of the heat transfer tubes, so that the isolation member is configured to lengthen a movement distance through which the liquid refrigerant needs to flow around a longitudinal end portion of the isolation member to reach the vapor outlet pipe.
  • a falling film evaporator according to a second aspect is the falling film evaporator according to the first aspect, in which the isolation member extends to an inner surface of the tank above the vapor outlet pipe as viewed in the axial direction of the heat transfer tubes and has an upper opening through an upper portion of the isolation member in the thickness direction thereof, or the isolation member extends, beyond an upper side of the vapor outlet pipe as viewed in the direction in which the vapor outlet pipe extends out from the tank, short of a portion of the inner surface of the tank above the vapor outlet pipe to form an upper gap.
  • the number of the upper gaps is not limited to one, and projections and depressions may be formed in the upper end portion of the isolation member to form a plurality of upper gaps between the isolation member and the inner surface of the tank.
  • a falling film evaporator according to the third aspect is the falling film evaporator according to the second aspect, in which the upper openings or the upper gaps are separately provided such that the upper openings or the upper gaps closer to the vapor outlet pipe have larger passage resistances to refrigerant passing through the upper openings or the upper gaps.
  • a falling film evaporator according to the fourth aspect is the falling film evaporator according to the second or third aspect, in which the upper opening or the upper gap is provided in a position vertically higher than the connection portion of the vapor outlet pipe and the tank.
  • a falling film evaporator according to the fifth aspect is the falling film evaporator according to any one of the second through fourth aspects, in which an oil return opening is formed in the lower end of the isolation member, or an oil return gap is formed between the lower end of the isolation member and the inner surface of the tank.
  • the oil return opening and the oil return gap are smaller than the upper opening and the upper gap.
  • a falling film evaporator according to the sixth aspect is the falling film evaporator according to any one of the first through fifth aspects, in which a longitudinal end portion of the isolation member is connected to an inner wall of the tank.
  • the liquid refrigerant can be more effectively prevented from reaching the vapor outlet pipe via the longitudinal end portion of the isolation member.
  • an outflow of the liquid refrigerant from the vapor outlet pipe is able to be prevented.
  • the flow velocity of the refrigerant in the vicinity of the vapor outlet pipe is able to be effectively reduced.
  • the liquid refrigerant is readily prevented from reaching the vapor outlet pipe against its own weight.
  • the liquid refrigerant can be more effectively prevented from reaching the vapor outlet pipe via the longitudinal end portion of the isolation member.
  • FIG. 1 is an external view of a falling film evaporator according to an embodiment of the present invention.
  • FIG. 2 is a schematic perspective view illustrating an internal structure of the falling film evaporator.
  • FIG. 3 is a cross sectional view of the falling film evaporator as viewed in the horizontal direction orthogonal to the longitudinal direction of a tank.
  • FIG. 4 is a cross sectional view of a portion of the falling film evaporator at a vapor outlet pipe as viewed in the longitudinal direction of the tank.
  • FIG. 5 is a cross sectional view of a portion of a falling film evaporator according to other embodiment A at a vapor outlet pipe as viewed in the longitudinal direction of a tank.
  • FIG. 6 is a schematic perspective view illustrating an internal structure of a falling film evaporator according to other embodiment B.
  • FIG. 7 is a cross sectional view illustrating a detailed side shape of a falling film evaporator according to other embodiment E taken along the line G-G of FIG. 4 .
  • FIG. 8 is a cross sectional view illustrating a detailed side shape of a falling film evaporator according to other embodiment H taken along the line G-G of FIG. 4 .
  • FIG. 9 is a cross sectional view illustrating a detailed side shape of a falling film evaporator according to other embodiment I taken along the line G-G of FIG. 4 .
  • FIG. 1 is an external view of a falling film evaporator 1 according to an embodiment of the present invention.
  • the falling film evaporator 1 is used as an evaporator of a relatively large capacity refrigeration apparatus such as a centrifugal chiller. More specifically, such a refrigeration apparatus is provided with the falling film evaporator 1 as well as a compressor, a radiator, an expansion mechanism and the like (not illustrated).
  • a vapor compression refrigerant circuit is configured with these devices. Then, in such a vapor compression refrigerant circuit, gas refrigerant discharged from the compressor radiates heat in the radiator. This refrigerant, which has radiated heat in the radiator, is decompressed in the expansion mechanism to be refrigerant in a gas-liquid two-phase state.
  • This refrigerant in a gas-liquid two-phase state flows into the falling film evaporator 1 , exchanges heat with heat medium such as water and brine to evaporate into gas refrigerant, and flows out of the falling film evaporator 1 .
  • This gas refrigerant which has flowed out of the falling film evaporator 1 , again is sucked into the compressor.
  • the liquid refrigerant which has not been evaporated as a result of the exchange of heat with the heat medium such as water and brine, merges with refrigerant in a gas-liquid two-phase state flowing into the falling film evaporator 1 through a liquid refrigerant return tube or the like (not illustrated), and again flows into the falling film evaporator 1 .
  • FIG. 1 is a perspective view illustrating an internal structure of the falling film evaporator 1 .
  • FIG. 3 is a cross sectional view of the falling film evaporator 1 as viewed in the horizontal direction orthogonal to the longitudinal direction of the tank 10 there, the isolation member 50 is not illustrated).
  • FIG. 4 is a cross sectional view of a portion of the falling film evaporator 1 in which the vapor outlet pipe 18 is located as viewed in the longitudinal direction of the tank 10 .
  • the terms used in the description below to express directions “upper”, “lower”, “left”, “right”, “horizontal”, and the like refer to directions in a state in which the falling film evaporator 1 is installed in use as illustrated in FIG. 1 .
  • the tank 10 primarily has a shell 11 and heads 12 a , 12 b
  • the shell 11 is a transversely placed cylindrical member having openings in both longitudinal end portions.
  • the heads 12 a , 12 b are bowl-shaped members closing the openings in both of the longitudinal end portions of the shell 11 .
  • a head of the heads 12 a , 12 b disposed on the left side of the shell 1 is referred to as a head 12 a
  • a head of the heads 12 a , 12 b disposed on the right side of the shell 11 is referred to as a head 12 b.
  • a tube plate 13 a is interposed between the head 12 a and the shell 11 .
  • a tube plate 13 b is interposed between the head 12 b and the shell 11 .
  • the tube plates 13 a , 13 b are substantially disc-shaped members.
  • tube holes are formed to fix a plurality of heat transfer tubes 21 constituting the heat transfer tube group 20 in a state in which both longitudinal end portions of the heat transfer tubes 21 have been inserted therethrough.
  • a space in the tank 10 is horizontally divided into a head space SH 1 surrounded by the head 12 a and the tube plate 13 a , a shell space SS surrounded by the shell 11 and the tube plates 13 a , 13 b , and a head space SH 2 surrounded by the head 12 b and the tube plate 13 b.
  • the head 12 a is provided with a heat medium inlet pipe 14 and a heat medium outlet pipe 15 .
  • the heat medium inlet pipe 14 is a pipe member for allowing the heat medium to flow into the head space SH 1 in the tank 10 .
  • the heat medium inlet pipe 14 is provided in the lower portion of the head 12 a
  • the heat medium outlet pipe 15 is a pipe member for allowing the heat medium to flow out of the head 12 a of the tank 10 .
  • the heat medium outlet pipe 15 is provided in the upper portion of the head 12 a .
  • the head space SH 1 is vertically divided by a head space separate plate 16 into a lower head space SHi communicating with the heat medium inlet pipe 14 and an upper head space SHo communicating with the heat medium outlet pipe 15 .
  • the heat medium which has flowed into the lower head space SHi in the head 12 a through the heat medium inlet pipe 14 , flows into a plurality of heat transfer tubes 21 (here, heat transfer tubes 21 constituting the lower portion of the heat transfer tube group 20 ) communicating with the lower head space SHi, and is sent to the head space SH 2 .
  • the heat medium sent to this head space SH 2 has flowed and turned upwardly in the head space SH 2
  • the heat medium flows into a plurality of heat transfer tubes (here, heat transfer tubes 21 constituting the upper portion of the heat transfer tube group 20 ) communicating with the upper head space SHo, and is sent to the upper head space SHo.
  • the heat medium sent to this upper head space SHo flows out of the upper head space SHo through the heat medium outlet pipe 15 (i.e., the heat medium flows out of the falling film evaporator 1 ).
  • the shell 11 is provided with a refrigerant inlet pipe 17 , a vapor outlet pipe 18 , and a liquid outlet pipe 19 .
  • the refrigerant inlet pipe 17 is a pipe member for allowing the refrigerant in a gas-liquid two-phase state to flow into the shell space SS in the tank 10 .
  • the refrigerant inlet pipe 17 is provided in the upper portion of the shell 11 to the left of the shell 11 in the longitudinal direction thereof.
  • the refrigerant inlet pipe 17 has a refrigerant flow inlet in the end thereof in the shell 11 allowing the refrigerant to flow into the tank 10 .
  • the vapor outlet pipe 18 is a pipe member for allowing the gas refrigerant generated as a result of evaporating on the heat transfer tube group 20 to flow out of the shell space SS in the tank 10 .
  • this vapor outlet pipe 18 is provided in an upper portion of the shell 11 which is inclined at approximately 30 degrees from the upper direction at the top of the shell 11 as viewed in the longitudinal direction of the shell 11 .
  • the vapor outlet pipe 18 is also provided to extend out from a substantially longitudinal middle portion of the shell 11 . It should be noted that an axial inclination angle of the vapor outlet pipe 18 at a connection portion of the vapor outlet pipe 18 and the shell 11 may be in a range of ⁇ 10 through ⁇ 100 degrees or ⁇ 30 through ⁇ 60 degrees.
  • connection position of the vapor outlet pipe 18 and the shell 11 is located above a second stage refrigerant tray 35 of the liquid refrigerant distribution apparatus 30 .
  • the liquid outlet pipe 19 is a pipe member for flowing the liquid refrigerant which has not evaporated on the heat transfer tube group 20 out of the shell space SS in the tank 10 .
  • the liquid outlet pipe 19 is provided in the lower portion of the shell 11 at the substantially longitudinal middle of the shell 11 .
  • the liquid refrigerant distributed on the heat transfer tube group 20 exchanges heat with the heat medium flowing inside of the heat transfer tubes 21 constituting the heat transfer tube group 20 to evaporate into gas refrigerant.
  • the gas refrigerant generated as a result of evaporating on the heat transfer tube group 20 flows diagonally upwardly toward the vapor outlet pipe 18 , and flows out of the shell space SS in the tank 10 through the vapor outlet pipe 18 .
  • the gas refrigerant which has flowed out of this shell space SS in the tank 10 is again sucked into the compressor.
  • the liquid refrigerant which has not evaporated on the heat transfer tube group 20 flows out of the shell space SS in the tank 10 through the liquid outlet pipe 19 provided below the shell space SS in the tank 10 .
  • This liquid refrigerant which has flowed out of the shell space SS in the tank 10 merges with the refrigerant in a gas-liquid two-phase state flowing into the shell space SS in the tank 10 through the liquid refrigerant return tube and the like. Then this liquid refrigerant again flows into the shell space SS in the tank 10 through the refrigerant inlet pipe 17 .
  • the heat transfer tube group 20 has the plurality of heat transfer tubes 21 extending in the longitudinal direction of the tank 10 .
  • the heat transfer tube group 20 is disposed in a portion substantially horizontally middle and vertically lower in the shell space SS in the tank 10 as viewed in the longitudinal direction of the tank 10 .
  • the heat transfer tubes 21 are disposed in multiple stages and multiple columns as viewed in the longitudinal direction of the tank 10 , here, in a staggered pattern of 11 columns 9 stages. Both of the longitudinal end portions of heat transfer tubes 21 extend to the tube plates 13 a , 13 b , and are fixed in the state in which the end portions have been inserted through the tube holes (not illustrated) of the tube plates 13 a , 13 b .
  • both of the longitudinal end portions of heat transfer tubes 21 constituting a vertically upper portion of the heat transfer tube group 20 communicate with the lower portion of the head space SH 2 and the lower head space SHi.
  • Both of the longitudinal end portions of the heat transfer tubes 21 constituting a vertically lower portion of the heat transfer tube group 20 communicate with the upper portion of the head space SH 12 and the upper head space SHo.
  • the number and the arrangement of the heat transfer tubes 21 constituting the heat transfer tube group 20 are not limited to the number and the arrangement in the present embodiment, and the number and/or the arrangement of the heat transfer tubes 21 different from those in the present embodiment may be employed. Moreover, in the case in which a tank having a tube plate and a head in only one longitudinal end portion of the shell is employed, a U-shaped heat transfer tube may be employed.
  • the liquid refrigerant distribution apparatus 30 is disposed vertically between the heat transfer tube group 20 in the shell space SS in the tank 10 and the vapor outlet pipe 18 .
  • the liquid refrigerant distribution apparatus 30 primarily has a header pipe 31 , a refrigerant tray 33 , and an upper cover 36 .
  • the header pipe 31 is a pipe member for introducing the refrigerant in a gas-liquid two-phase state supplied into the shell space SS in the tank 10 through the refrigerant inlet pipe 17 into the refrigerant tray 33 (here, a first stage refrigerant tray 34 ).
  • the header pipe 31 is a pipe member extending in the longitudinal direction of the tank 10 .
  • One end portion of the header pipe 31 (here, the left end portion) is connected to the refrigerant inlet pipe 17 .
  • the header pipe 31 has a substantially cross-sectional shape as viewed in the longitudinal direction of the tank 10 .
  • header pipe refrigerant holes 31 c are formed in an upper wall 31 a and the upper portions of side walls 31 b of the header pipe 31 , excluding the one end portion (here, the left end portion) connected to the refrigerant inlet pipe 17 and both longitudinal end walls of the header pipe 31 .
  • the header pipe refrigerant holes 31 c allow the refrigerant in a gas-liquid two-phase state flowing through the header pipe 31 to flow out toward the first stage refrigerant tray 34 .
  • a gas-liquid separation member 32 is provided on the header pipe 31 , excluding the one end portion (here, the left end portion of the header pipe 31 ) connected to the refrigerant inlet pipe 17 .
  • the gas-liquid separation member 32 covers the upper wall 31 a and the outer peripheries of the upper portions of the side walls 31 b of the header pipe 31 in a state in which the gas-liquid separation member 32 is spaced from the outer periphery of the header pipe 31 .
  • the gas-liquid separation member 32 has a substantially downward U-shaped cross-sectional shape as viewed in the longitudinal direction of the tank 10 . Then, in the gas-liquid separation member 32 , many header pipe vent holes 32 a are formed.
  • the header pipe vent holes 32 a are holes for permitting the gas refrigerant of the refrigerant in a gas-liquid two-phase state flowing inside the header pipe 31 , which has been supplied in the shell space SS in the tank 10 through the refrigerant inlet pipe 17 , to pass and for preventing the liquid refrigerant of the refrigerant in a gas-liquid two-phase state flowing inside the header pipe 31 , which has been supplied in the shell space SS in the tank 10 through the refrigerant inlet pipe 17 , from passing.
  • the refrigerant tray 33 is a tray-shaped member for allowing the liquid refrigerant of the refrigerant in a gas-liquid two-phase state, which has been supplied in the shell space SS in the tank 10 through the refrigerant inlet pipe 17 provided on and in the shell 11 of the tank 10 , to downwardly fall onto the lower heat transfer tube group 20 after accumulating the liquid refrigerant.
  • the refrigerant tray 33 primarily has the first stage refrigerant tray 34 and the second stage refrigerant tray 35 .
  • the first stage refrigerant tray 34 is a tray-shaped member allowing the liquid refrigerant of the refrigerant in a gas-liquid two-phase state, which has been supplied in the shell space SS in the tank 10 through the refrigerant inlet pipe 17 provided on and in the shell 11 of the tank 10 , to downwardly fall after accumulating the liquid refrigerant.
  • the first stage refrigerant tray 34 extends in the longitudinal direction of the tank 10 .
  • the first stage refrigerant tray 34 has a substantially upward U-shaped cross-sectional shape as viewed in the longitudinal direction of the tank 10 .
  • the header pipe 31 is disposed on a bottom wall 34 a of the first stage refrigerant tray 34 .
  • the refrigerant in a gas-liquid two-phase state which has been supplied in the shell space SS in the tank 10 through the refrigerant inlet pipe 17 , is introduced into the first stage refrigerant tray 34 through the header pipe refrigerant holes 31 c of the header pipe 31 and the header pipe vent holes 32 a of the gas-liquid separation member 32 .
  • the refrigerant in a gas-liquid two-phase state introduced in the first stage refrigerant tray 34 from the header pipe 31 is separated into gas and liquid by the gas-liquid separation member 32 .
  • the liquid refrigerant of the refrigerant in a gas-liquid two-phase state does not pass through the header pipe vent holes 32 a of the gas-liquid separation member 32 , is introduced into the first stage refrigerant tray 34 , and is accumulated in the first stage refrigerant tray 34 .
  • the liquid refrigerant accumulated in the first stage refrigerant tray 34 downwardly falls onto the lower second stage refrigerant tray 35 through a plurality of liquid refrigerant downwardly falling holes 34 c formed in the bottom wall 34 a of the first stage refrigerant tray 34 .
  • the gas refrigerant of the refrigerant in a gas-liquid two-phase state passes through the header pipe vent holes 32 a of the gas-liquid separation member 32 , and is introduced into a directly above-first stage refrigerant tray space SSd 1 directly above the first stage refrigerant tray 34 (here, a space vertically between the upper cover 36 and the first stage refrigerant tray 34 ).
  • the gas refrigerant introduced in the directly above-first stage refrigerant tray space SSd 1 flows toward the vapor outlet pipe 18 , flows out of the shell space SS in the tank 10 through the vapor outlet pipe 18 together with the gas refrigerant generated as a result of evaporating on the heat transfer tube group 20 .
  • the second stage refrigerant tray 35 is a tray-shaped member allowing the liquid refrigerant downwardly falling from the first stage refrigerant tray 34 to downwardly fall onto the lower heat transfer tube group 20 after accumulating the liquid refrigerant.
  • the second stage refrigerant tray 35 extends in the longitudinal direction of the tank 10 .
  • the second stage refrigerant tray 35 is provided such that the longitudinal direction of the second stage refrigerant tray 35 is the same as the longitudinal direction of the heat transfer tubes 21 .
  • the second stage refrigerant tray 35 has a substantially upward U-shaped cross-sectional shape as viewed in the longitudinal direction of the tank 10 .
  • the second stage refrigerant tray 35 extends off the first stage refrigerant tray 34 as the second stage refrigerant tray 35 is viewed from below (likely, as the second stage refrigerant tray 35 is viewed in the longitudinal direction of the tank 10 ). That is, as the second stage refrigerant tray 35 is viewed in the longitudinal direction of the tank 10 , side walls 35 b of the second stage refrigerant tray 35 are disposed outside side walls 34 b of the first stage refrigerant tray 34 . Thereby, the liquid refrigerant downwardly falling from the first stage refrigerant tray 34 is introduced into the second stage refrigerant tray 35 , and is accumulated in the second stage refrigerant tray 35 .
  • the liquid refrigerant accumulated in the second stage refrigerant tray 35 downwardly falls onto the lower heat transfer tube group 20 through a plurality of liquid refrigerant downwardly falling holes 35 c formed in a bottom wall 35 a of the second stage refrigerant tray 35 .
  • a space vertically between the first stage refrigerant tray 34 and the second stage refrigerant tray 35 is referred to as a directly above-second stage refrigerant tray space SSd 2 .
  • the upper cover 36 is a roof-shaped member spaced above the refrigerant tray 33 (here, the first stage refrigerant tray 34 ) and covering the refrigerant tray 33 (here, the first stage refrigerant tray 34 ) thereabove and diagonally thereabove.
  • the upper cover 36 extends in the longitudinal direction of the tank 10 excluding the end portion (here, the left end portion of the header pipe 31 ) in which the refrigerant inlet pipe 17 is connected to the header pipe 31 .
  • the upper cover 36 has a substantially downward U-shaped cross-sectional shape as viewed in the longitudinal direction of the tank 10 .
  • the upper cover 36 has an upper wall 36 a having a horizontal plate-shaped cross-sectional shape as viewed in the longitudinal direction of the tank 10 , side walls 36 b extending diagonally downwardly from the end portion of the upper wall 36 a , and wall end portions 36 c extending downwardly from the lower ends of the side walls 36 b .
  • the side walls 36 b and the wall end portions 36 c of the upper cover 36 a extend diagonally downwardly toward locations lower than the lower edge of the connection portion of the vapor outlet pipe 18 and the shell 11 (a portion indicated by the point X in FIG. 5 ).
  • the upper wall 36 a of the upper cover 36 is located further above the header pipe 31 located above the second stage refrigerant tray 35 .
  • the upper cover 36 is viewed in the longitudinal direction of the tank 10 , the upper cover 36 is provided with projection walls 36 d downwardly projecting in positions outside the header pipe 31 and the gas-liquid separation member 32 as well as inner side of the side walls 34 b of the first stage refrigerant tray 34 .
  • the projection walls 36 d extend in the longitudinal direction of the tank 10 .
  • the upper cover 36 covers and extends off the first stage refrigerant tray 34 as the upper cover 36 is viewed from above (likewise, in the case in which as the upper cover 36 is viewed in the longitudinal direction of the tank 10 ).
  • the distribution apparatus space SSd is a space vertically between the upper cover 36 and the refrigerant tray 33 (here, the second stage refrigerant tray 35 ).
  • the distribution apparatus space SSd has the directly above-first stage refrigerant tray space SSd 1 as described above, the directly above-second stage refrigerant tray space SSd 2 as described above, and first stage refrigerant tray lateral spaces SSd 3 .
  • the first stage refrigerant tray lateral spaces SSd 3 are a space above the second stage refrigerant tray 35 and outside the side walls 34 b of the first stage refrigerant tray 34 as the liquid refrigerant distribution apparatus 30 is viewed in the longitudinal direction of the tank 10 .
  • spaces in the shell space SS in the tank 10 excluding the distribution apparatus space SSd constitute a vapor main flow path space SSv through which the gas refrigerant generated as a result of evaporating on the heat transfer tube group 20 flows toward the vapor outlet pipe 18 .
  • the vapor main flow path space SSv communicates with the first stage refrigerant tray lateral spaces SSd 3 of the distribution apparatus space SSd through gaps vertically between the end portions of the side walls 36 b of the upper cover 36 and upper ends of the side walls 35 b of the second stage refrigerant tray 35 as the liquid refrigerant distribution apparatus 30 is viewed in the longitudinal direction of the tank 10 .
  • the configuration having the first stage refrigerant tray 34 and the second stage refrigerant tray 35 is employed as a basic configuration of the liquid refrigerant distribution apparatus 30 . Then, such a liquid refrigerant distribution apparatus 30 and the heat transfer tube group 20 having the heat transfer tubes 21 constitute the falling film evaporator 1 allowing the liquid refrigerant to evaporate as a result of exchanging heat between the heat medium flowing inside the heat transfer tubes 21 and the liquid refrigerant downwardly falling from the second stage refrigerant tray 35 .
  • the isolation member 50 is provided in the tank 10 and in the vicinity of the portion connected to the vapor outlet pipe 18 .
  • This isolation member 50 is provided so as to cover a place below the lowest portion (the point X in FIG. 4 ) of the connection portion of the tank 10 and the vapor outlet pipe 18 as viewed in the axial direction of the heat transfer tubes 21 , to extend between the vapor outlet pipe 18 and the liquid refrigerant distribution apparatus 30 , and to allow the refrigerant to pass through the upper portion thereof. As illustrated in FIG. 2 , this isolation member 50 extends in the longitudinal direction of the heat transfer tubes 21 , so that the longitudinal direction of the isolation member 50 ) is substantially same as the longitudinal direction of the heat transfer tubes 21 .
  • both of longitudinal ends of the isolation member 50 extend short of the tube plates 13 a , 13 b , so that the both ends are not welded or the like to the tube plates 13 a , 13 b or an inner wall of the tank 10 , and are open toward the longitudinal direction of the heat transfer tubes 21 .
  • the isolation member 50 extends, from a position below the lowest portion (the point X) of the connection portion of the tank 10 and the vapor outlet pipe 18 , beyond the upper side of the vapor outlet pipe 18 as viewed in the direction in which the vapor outlet pipe 18 extends out from the tank 10 , but the isolation member 50 does not extend to reach an inner surface of the tank 10 . It should be noted that, the isolation member 50 extends above the highest portion (the point Y in FIG. 4 ) of the connection portion of the tank 10 and the vapor outlet pipe 18 in the case in which the falling film evaporator 1 is horizontally viewed.
  • An upper gap 51 is formed between the upper end of the isolation member 50 and the inner surface of the tank 10 nearest the upper end of the isolation member 50 . It should be noted that, in the present embodiment, the upper end of the isolation member 50 is rectilinearly formed along the longitudinal direction of the heat transfer tubes 21 .
  • This upper gap 51 is provided above the highest portion (the point Y in FIG. 4 ) of the connection portion of the tank 10 and the vapor outlet pipe 18 to be disposed in a position higher than the connection portion of the tank 10 and the vapor outlet pipe 18 in the case in which the falling film evaporator 1 is horizontally viewed.
  • the isolation member 50 is welded to a portion of the inner wall of the tank 10 lower than the lowest portion (the point X) of the connection portion of the tank 10 and the vapor outlet pipe 18 to be fixed thereto.
  • the isolation member 50 extends from this fixation portion, that is, the portion lower than the lowest portion (the point X) of the connection portion of the tank 10 and the vapor outlet pipe 18 , slightly far toward the vicinity of the middle of the tank 10 , and horizontally toward the inside of the tank 10 as well as vertically toward the upper portion of the tank 10 . Then, a portion extending vertically upwardly is provided in the vicinity of the upper end of the isolation member 50 .
  • an oil return opening 52 which is a fine opening vertically therethrough is provided.
  • This oil return opening 52 has a maximum passage area configured to be smaller than the maximum passage area of the above described upper gap 51 .
  • the isolation member 50 is disposed to adjust the size of the passage area in the narrow gap between the upper cover 36 and the isolation member 50 such that the flow velocity of the refrigerant flowing through the portion distant from the vapor outlet pipe 18 is approximately same as the flow velocity of the refrigerant flowing through the portion close to the vapor outlet pipe 18 .
  • the gas refrigerant having a fast flow velocity may carry the liquid refrigerant to readily cause the carryover in which the liquid refrigerant flows out of the tank.
  • the connection position of the vapor outlet pipe 18 and the tank 10 is provided in a portion close to a position through which the liquid refrigerant passes, the carryover more readily occurs.
  • the vapor outlet pipe 18 is connected not to the top of the tank 10 but to an inclined position, so that the vapor outlet pipe 18 is connected to a portion close to a position through which the liquid refrigerant from the header pipe 31 and/or the liquid refrigerant distribution apparatus 30 passes. Even in such a connection state, the isolation member 50 is provided between the vapor outlet pipe 18 and the liquid refrigerant distribution apparatus 30 .
  • the refrigerant which have flowed out of the header pipe 31 flows around the upper cover 36 and further toward the vapor outlet pipe 18 side, and through the portion close to the vapor outlet pipe 18 , the refrigerant flows around the upper cover 36 , then further passes the narrow gap between the upper cover 36 and the isolation member 50 , and flows toward the vapor outlet pipe 18 side (here, because the open portions in both of the longitudinal end portions of the isolation member 50 are located away from the vapor outlet pipe 18 , the refrigerant hardly flows through the open portions).
  • the liquid refrigerant is less prone to passing through the upper gap 51 because channels to the vapor outlet pipe 18 are sufficiently long, and the upper gap 51 through which the refrigerant passes is provided upward in the tank 10 , so that the liquid refrigerant having a specific gravity greater than the gas refrigerant needs to upwardly rises and flows against its own weight.
  • the isolation member 50 can reduce an outflow of the liquid refrigerant.
  • the isolation member 50 is disposed to adjust the size of the passage area in the narrow gap between the upper cover 36 and the isolation member 50 such that the flow velocity of the refrigerant flowing through the portion distant from the vapor outlet pipe 18 is approximately same as the flow velocity of the refrigerant flowing through the portion close to the vapor outlet pipe 18 , the difference between the flow velocities of the refrigerant in the portion distant from the vapor outlet pipe 18 and the portion close to the vapor outlet pipe 18 can be reduced.
  • the isolation member 50 is provided, thereby enabling the refrigerant of the refrigerant passing through the header pipe 31 and the liquid refrigerant distribution apparatus 30 on the side close to the vapor outlet pipe 18 to flow long away around the isolation member 50 . Accordingly, it becomes possible to balance the distribution of the refrigerant flowing through the portion close to the vapor outlet pipe 18 and the refrigerant flowing through the portion distant from the vapor outlet pipe 18 . (6-2)
  • the upper gap 51 which is formed between the upper end of the isolation member 50 and the inner wall of the tank 10 , is provided above the highest portion (the point Y in FIG. 4 ) of the connection portion of the tank 10 and the vapor outlet pipe 18 in the case in which the falling film evaporator 1 is horizontally viewed. Therefore, the liquid refrigerant having a specific gravity greater than the gas refrigerant is able to be less prone to reaching the upper gap 51 .
  • the oil return opening 52 is formed in the vicinity of the lower end of the isolation member 50 , the accumulation of refrigerating machine oil between the isolation member 50 and the inner wall of the tank 10 is able to be prevented.
  • the oil return opening 52 prevents the accumulation of the refrigerating machine oil
  • the oil return opening 52 having a size configured to be sufficiently smaller than the upper gap 51 prevents the liquid refrigerant from passing through the oil return opening 52 and reaching the vapor outlet pipe 18 .
  • the isolation member 50 is formed so as to extend such that the longitudinal direction of the isolation member 50 is same as the longitudinal direction of the heat transfer tubes 21 .
  • the upper gap 51 formed between the upper end of the isolation member 50 and the inner surface of the tank 10 is described as an example.
  • an isolation member 250 may extend to reach the inner wall of the tank 10 and have an upper opening 251 through in the thickness direction of isolation member 250 formed at an upper portion slightly below the upper end of the isolation member 250 .
  • both of the longitudinal ends of the isolation member 50 which are not welded or the like and are open, are described as an example.
  • both longitudinal ends 350 P. 350 Q of an isolation member 350 may extend to reach the tube plates 13 a , 13 b and be welded and the like to be connected to the tube plates 13 a , 13 b .
  • both of the longitudinal ends 350 P. 350 Q may be bent and the like toward the inner wall of the tank 10 side, and be welded and the like to be connected to the inner wall of the tank 10 .
  • the longitudinal end portions of the isolation member may be configured to be closed.
  • the liquid refrigerant can more effectively be prevented from more flowing toward the vapor outlet pipe 18 via the longitudinal end portions of the isolation member (passing outside the longitudinal end portions of the isolation member) and reaching the vapor outlet pipe 18 .
  • the heat transfer tube group 20 which is housed in the tank 10 , disposed such that the longitudinal direction of the heat transfer tube group 20 is same as the longitudinal direction of the tank 10 is described as an example.
  • the heat transfer tube group 20 housed in the tank 10 may be disposed such that the longitudinal direction of the heat transfer tube group 20 is different from the longitudinal direction of the tank 10 to some extent, for example, the heat transfer tube group 20 may be disposed in the tank 10 such that the angle between the longitudinal direction of the heat transfer tube group 20 and the longitudinal direction of the tank 10 falls within ⁇ 20 degrees.
  • the oil return opening 52 vertically through the isolation member 50 provided in the vicinity of the lower end of the isolation member 50 is described as an example.
  • an oil return gap may be formed between the lower end portion of the isolation member 50 and the inner wall of the tank 10 .
  • the oil return gap has a maximum passage area preferably configured to be smaller than the maximum passage area of the upper gap 51 .
  • the upper end of the isolation member 50 rectilinearly extending in the longitudinal direction of the heat transfer tubes 21 , and one gap formed between the upper end of the isolation member 50 and the inner wall of the tank 10 are described as examples.
  • upper gaps 451 may be separately constituted between the upper end of an isolation member 450 ) and the inner wall of the shell 11 of the tank 10 .
  • the upper end of an isolation member 450 may be configured to have portions extending to and contact the inner wall of the shell 11 and portions extending but not contacting the inner wall of the shell 11 .
  • connection position of the vapor outlet pipe 18 and the shell 11 located above the second stage refrigerant tray 35 of the liquid refrigerant distribution apparatus 30 is described as an example.
  • connection position of the vapor outlet pipe 18 and the shell 11 may be located at a height position equivalent to that of the second stage refrigerant tray 35 of the liquid refrigerant distribution apparatus 30 .
  • the isolation member 50 which is provided such that the longitudinal direction thereof is same as the longitudinal direction of the heat transfer tubes 21 and so as to extend short of the tube plates 13 a , 13 b , is described as an example.
  • the isolation member 50 in the longitudinal direction of the heat transfer tubes 21 has a length S, preferably, equal to or longer than twice as long as, and more preferably equal to or longer than three times as long as a distance T between end portions of the isolation member 50 in planes orthogonal to the longitudinal direction of the heat transfer tubes 21 .
  • the length S of the isolation member 50 in the longitudinal direction of the heat transfer tubes 21 is configured and arranged such that more refrigerant primarily passes through the upper gap 51 than the open portions of the both ends.
  • the upper end of the isolation member 50 rectilinearly extending in the longitudinal direction of the heat transfer tubes 21 , and one gap formed between the upper end of the isolation member 50 and the inner wall of the tank 10 are described as examples.
  • an isolation member 550 may have an upper end extending to reach the inner wall of the shell 11 of the tank 10 , and a plurality of upper openings 551 through the isolation member 550 in the thickness direction thereof may be formed in the upper portion of the isolation member 550 such that they are arranged along the longitudinal direction of the heat transfer tubes 21 , (which is also the longitudinal direction of the isolation member 550 ). Then, as illustrated in FIG. 8 , these upper openings 551 may be constituted such that the upper openings 551 closer to the vapor outlet pipe 18 have larger passage resistances to the refrigerant passing through the upper openings 551 .
  • portions 551 a separating the upper openings 551 may be provided such that intervals between portions 551 a closer to the vapor outlet pipe 18 are closer than intervals between the portions 551 a more distant from the vapor outlet pipe 18 .
  • the upper openings 551 may be provided such that the upper openings 551 closer to the vapor outlet pipe 18 have passage areas smaller than passage areas of the upper openings 551 more distant from the vapor outlet pipe 18 .
  • portions 551 a separating the upper openings 551 may be provided such that the sizes (distances between adjacent upper openings 551 ) of portions 551 a closer to the vapor outlet pipe 18 are larger (longer) than the sizes of portions 551 a more distant from the vapor outlet pipe 18 .
  • the configuration of other embodiment H, in which upper openings 551 closer to the vapor outlet pipe 18 have larger passage resistances to the refrigerant passing through the upper openings 551 is not limited to the isolation member 550 having the upper end extending to reach the inner wall of the shell 11 and the upper openings 551 formed in the isolation member 550 .
  • a plurality of upper gaps 651 is formed between the upper end of the isolation member 650 and the shell 11 ; the upper gaps 651 may be constituted such that upper gaps 651 closer to the vapor outlet pipe 18 have larger passage resistances to the refrigerant passing through the upper gaps 651 . More specifically, portions 651 a separating the upper gaps 651 (each portion 651 a has a given size) may be provided such that intervals between portions 651 a closer to the vapor outlet pipe 18 are narrower than intervals between portions 651 a more distant from the vapor outlet pipe 18 .
  • the upper gaps 651 may be provided such that the upper gaps 651 closer to the vapor outlet pipe 18 have passage areas smaller than passage areas of the upper gaps 651 more distant from the vapor outlet pipe 18 .
  • the portions 651 a separating the upper gaps 651 may be provided such that the sizes (distances between adjacent upper gaps 651 ) of portions 651 a closer to the vapor outlet pipe 18 are larger (longer) than the sizes of portions 651 a more distant from the vapor outlet pipe 18 .
  • the present invention is widely applicable to a falling film evaporator in which a liquid refrigerant distribution apparatus is provided vertically between a heat transfer tube group in a tank and a vapor outlet pipe on the upper portion of the tank; the liquid refrigerant distribution apparatus allows liquid refrigerant of refrigerant in a gas-liquid two-phase state supplied in the tank through a refrigerant inlet pipe to fall downwardly onto the heat transfer tube group, the heat transfer tube group allows the liquid refrigerant to evaporate.

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  • 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)
  • Details Of Heat-Exchange And Heat-Transfer (AREA)
US15/319,323 2014-07-01 2015-06-29 Falling film evaporator Abandoned US20170153061A1 (en)

Applications Claiming Priority (3)

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JP2014136332A JP2016014495A (ja) 2014-07-01 2014-07-01 流下液膜式蒸発器
JP2014-136332 2014-07-01
PCT/JP2015/068703 WO2016002723A1 (ja) 2014-07-01 2015-06-29 流下液膜式蒸発器

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EP (1) EP3165851A4 (zh)
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US20170254573A1 (en) * 2016-03-07 2017-09-07 Daikin Applied Americas Inc. Heat exchanger
US20180306519A1 (en) * 2015-10-21 2018-10-25 Technip France Device for the exchange of heat between a first fluid intended to be vaporized and a second fluid intended to be cooled and/or condensed, and associated installation and method
US10132537B1 (en) * 2017-05-22 2018-11-20 Daikin Applied Americas Inc. Heat exchanger
EP3832247A1 (en) * 2019-12-03 2021-06-09 Carrier Corporation Flooded evaporator
US11266039B2 (en) * 2018-06-07 2022-03-01 Fujitsu Limited Liquid immersion tank
US11486615B2 (en) * 2017-03-31 2022-11-01 Carrier Corporation Flow balancer and evaporator having the same
US11536497B2 (en) * 2020-02-13 2022-12-27 Lg Electronics Inc. Evaporator
EP4071433A4 (en) * 2020-01-14 2023-01-18 Daikin Industries, Ltd. PLATE HEAT EXCHANGER
US11619428B2 (en) * 2018-04-06 2023-04-04 Carrier Corporation Integrated separator and distributor
US11624533B2 (en) 2020-02-13 2023-04-11 Lg Electronics Inc. Evaporator
US20230392837A1 (en) * 2022-06-03 2023-12-07 Trane International Inc. Evaporator charge management and method for controlling the same
US11898780B2 (en) 2020-02-13 2024-02-13 Lg Electronics Inc. Evaporator
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CN108709339A (zh) * 2018-07-02 2018-10-26 珠海格力电器股份有限公司 布液器、降膜蒸发器以及空调
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US20180306519A1 (en) * 2015-10-21 2018-10-25 Technip France Device for the exchange of heat between a first fluid intended to be vaporized and a second fluid intended to be cooled and/or condensed, and associated installation and method
US11686531B2 (en) * 2015-10-21 2023-06-27 Technip Energies France Device for the exchange of heat between a first fluid intended to be vaporized and a second fluid intended to be cooled and/or condensed, and associated installation and method
US10746441B2 (en) * 2016-03-07 2020-08-18 Daikin Applied Americas Inc. Heat exchanger
US20170254573A1 (en) * 2016-03-07 2017-09-07 Daikin Applied Americas Inc. Heat exchanger
US11486615B2 (en) * 2017-03-31 2022-11-01 Carrier Corporation Flow balancer and evaporator having the same
US10132537B1 (en) * 2017-05-22 2018-11-20 Daikin Applied Americas Inc. Heat exchanger
US11619428B2 (en) * 2018-04-06 2023-04-04 Carrier Corporation Integrated separator and distributor
EP4350254A1 (en) * 2018-04-06 2024-04-10 Carrier Corporation Integrated separator and distributor
EP3775722B1 (en) * 2018-04-06 2024-01-03 Carrier Corporation Integrated separator and distributor
US11266039B2 (en) * 2018-06-07 2022-03-01 Fujitsu Limited Liquid immersion tank
US11739988B2 (en) 2019-12-03 2023-08-29 Carrier Corporation Flooded evaporator
EP3832247A1 (en) * 2019-12-03 2021-06-09 Carrier Corporation Flooded evaporator
EP4071433A4 (en) * 2020-01-14 2023-01-18 Daikin Industries, Ltd. PLATE HEAT EXCHANGER
US11698228B2 (en) 2020-01-14 2023-07-11 Daikin Industries, Ltd. Shell-and-plate heat exchanger
US11624533B2 (en) 2020-02-13 2023-04-11 Lg Electronics Inc. Evaporator
US11536497B2 (en) * 2020-02-13 2022-12-27 Lg Electronics Inc. Evaporator
US11898780B2 (en) 2020-02-13 2024-02-13 Lg Electronics Inc. Evaporator
US12055329B2 (en) * 2021-04-28 2024-08-06 Daikin Industries, Ltd. Pipe coupling structure and refrigeration cycle apparatus
US20230392837A1 (en) * 2022-06-03 2023-12-07 Trane International Inc. Evaporator charge management and method for controlling the same
US12066224B2 (en) * 2022-06-03 2024-08-20 Trane International Inc. Evaporator charge management and method for controlling the same

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EP3165851A1 (en) 2017-05-10
JP2016014495A (ja) 2016-01-28
EP3165851A4 (en) 2018-03-21
CN106662381A (zh) 2017-05-10

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Effective date: 20150915

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Free format text: EXPRESSLY ABANDONED -- DURING EXAMINATION