US20100154467A1 - Gas-Liquid Separator and Refrigeration System With Gas-Liquid Seperator - Google Patents

Gas-Liquid Separator and Refrigeration System With Gas-Liquid Seperator Download PDF

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Publication number
US20100154467A1
US20100154467A1 US12/087,873 US8787307A US2010154467A1 US 20100154467 A1 US20100154467 A1 US 20100154467A1 US 8787307 A US8787307 A US 8787307A US 2010154467 A1 US2010154467 A1 US 2010154467A1
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Prior art keywords
gas
liquid
vessel body
refrigerant
liquid separator
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US12/087,873
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English (en)
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Shuuji Fujimoto
Takahiro Yamaguchi
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Daikin Industries Ltd
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Daikin Industries Ltd
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Assigned to DAIKIN INDUSTRIES, LTD. reassignment DAIKIN INDUSTRIES, LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: FUJIMOTO, SHUUJI, YAMAGUCHI, TAKAHIRO
Publication of US20100154467A1 publication Critical patent/US20100154467A1/en
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    • 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
    • F25B1/00—Compression machines, plants or systems with non-reversible cycle
    • F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
    • 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
    • F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • 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
    • F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/13—Economisers
    • 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
    • F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/23—Separators
    • 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
    • F25B41/00—Fluid-circulation arrangements

Definitions

  • This invention relates to gas-liquid separators for separating gas-liquid two-phase fluid into liquid fluid and gaseous fluid and refrigeration systems including a refrigerant circuit with such a gas-liquid separator.
  • Conventional refrigeration systems include those including a refrigerant circuit operating in a two-stage compression and two-stage expansion refrigeration cycle. Furthermore, among such refrigeration systems include those including a gas-liquid separator for separating gas-liquid two-phase fluid into liquid fluid and gaseous fluid (see, for example, Patent Document 1).
  • the refrigeration system disclosed in the above Patent Document 1 is an air conditioning system including a refrigerant circuit operating in a two-stage compression and two-stage expansion refrigeration cycle during a heating operation.
  • the refrigerant circuit is provided with a gas-liquid separator for separating gas-liquid two-phase refrigerant into gas refrigerant and liquid refrigerant.
  • refrigerant discharged from a high-pressure stage compressor condenses in an indoor heat exchanger to heat room air.
  • the condensed refrigerant passes through an intermediate expansion valve to reach an intermediate-pressure, gas-liquid two-phase state, is then introduced into the gas-liquid separator and is separated therein into gas refrigerant and liquid refrigerant.
  • the evaporated refrigerant is sucked into a low-pressure stage compressor and compressed therein into intermediate-pressure discharge refrigerant.
  • the intermediate-pressure discharge refrigerant is joined with gas refrigerant coming from the gas-liquid separator and the refrigerant mixture is sucked into the high-pressure stage compressor and compressed therein to a high pressure.
  • the gas-liquid separator includes, as specifically shown in FIG. 8 , a cylindrical vessel body (a).
  • the vessel body (a) is connected at its top to an inflow pipe (b), a liquid outflow pipe (c) and a gas outflow pipe (d) that pass through the top.
  • the interior of the vessel body (a) is divided into a liquid refrigerant pool (e) located in an upper side thereof and a gas refrigerant pool (f) located in a lower side thereof.
  • an opening end of the liquid outflow pipe (c) is located in the liquid refrigerant pool (e)
  • an opening end of the gas outflow pipe (d) is located in the gas refrigerant pool (f)
  • an opening end of the inflow pipe (b) is located at a height between the opening end of the liquid outflow pipe (c) and the opening end of the gas outflow pipe (d).
  • FIG. 9 Another example of the gas-liquid separator is shown in FIG. 9 .
  • a gas outflow pipe (d) is connected to the top of a vertically long vessel body (a) to pass through the top.
  • An inflow pipe is connected to an upper part of the peripheral wall of the vessel body (a) to pass through it.
  • a liquid outflow pipe is connected to a lower part of the peripheral wall of the vessel body (a) to pass through it.
  • Patent Document 1 Published Japanese Patent Application No. 2001-235245
  • refrigerant flowing through the inflow pipe (b) is gas-liquid two-phase refrigerant and, therefore, may cause a slug flow in which large gas bubbles of gas refrigerant and masses of liquid refrigerant irregularly flow. If such a slug flow is introduced through the inflow pipe (b) into the vessel body (a), a problem arises that the liquid level of the liquid refrigerant pool (e) is disturbed and the disturbance of the liquid level incurs spattering of the liquid refrigerant, resulting in mixing of the liquid refrigerant into gas refrigerant flowing out of the vessel body (a) and through the gas outflow pipe (d). In addition, another problem arises that gas bubbles are mixed into the liquid refrigerant pool (e) and, therefore, gas refrigerant is mixed into liquid refrigerant flowing out of the vessel body (a) and through the liquid outflow pipe (c).
  • the vessel body (a) is vertically long and the opening end of the inflow pipe (b) is close to opposite part of the inside wall of the vessel body (a). Therefore, if large gas bubbles in a slug flow flow through the inflow pipe (b) so that refrigerant therein temporarily reaches a high flow rate, the gas-liquid two-phase refrigerant having flowed through the inflow pipe (b) into the vessel body (a) hits the inside wall of the vessel body (a) and spatters, as shown in the arrows in FIG. 9 . This causes a problem that spattered refrigerant directly flows out through the gas outflow pipe (d). In addition, another problem arises that the spattered refrigerant falls into the liquid refrigerant pool (e), thereby disturbing the liquid level and mixing gas bubbles into the liquid refrigerant pool (e).
  • the known gas-liquid separators have a problem that if gas-liquid two-phase refrigerant flowing through the inflow pipe forms a slug flow, they deteriorate its performance of separation of the gas-liquid two-phase refrigerant or deteriorate the reliability as a gas-liquid separator. Furthermore, if the gas-liquid separator in a refrigeration system varies its refrigerant separation performance because of flow conditions of gas-liquid two-phase refrigerant, this causes variations in evaporation capacity of the evaporator and variations in condensation capacity of the condenser. As a result, a problem arises that the refrigeration system cannot perform a stable operation.
  • the present invention has been made in view of the foregoing points and, therefore, an object thereof is to enhance the refrigerant separation performance of a gas-liquid separator for separating gas-liquid two-phase fluid into gaseous fluid and liquid fluid and stabilize the operation of a refrigeration system including the gas-liquid separator.
  • a first aspect of the invention is directed to a gas-liquid separator including: a vessel body ( 16 ) for separating gas-liquid two-phase fluid into liquid fluid and gaseous fluid; an inflow pipe ( 20 ) through which the gas-liquid two-phase fluid flows into the vessel body ( 16 ); a liquid outflow pipe ( 30 ) through which liquid fluid in the vessel body ( 16 ) flows out of the vessel body ( 16 ); and a gas outflow pipe ( 40 ) through which gaseous fluid in the vessel body ( 16 ) flows out of the vessel body ( 16 ). Furthermore, the inflow pipe ( 20 ) is provided with a fragmentation device ( 50 ) for fragmentizing gas bubbles in the gas-liquid two-phase fluid.
  • the inflow pipe ( 20 ) is provided with a fragmentation device ( 50 ), even if gas-liquid two-phase fluid flowing through the inflow pipe ( 20 ) forms a slug flow, gas bubbles of gaseous fluid are fragmentized to homogenize the gas-liquid two-phase fluid.
  • the gas-liquid two-phase fluid is introduced in a regular and stable flow condition into the vessel body ( 16 ).
  • the gas-liquid two-phase fluid is separated into liquid fluid and gaseous fluid.
  • a pool ( 23 ) of liquid fluid is formed in a lower side of the interior of the vessel body ( 16 ), while a pool ( 24 ) of gaseous fluid is formed in an upper side thereof. Since regularly flowing gas-liquid two-phase fluid is introduced into the vessel body ( 16 ), this reduces the disturbance of the liquid level of the pool ( 23 ) of liquid fluid, the spattering of the liquid fluid due to the disturbance and the mixing of gas bubbles into the pool ( 23 ) of liquid fluid.
  • a second aspect of the invention is the gas-liquid separator according to the first aspect of the invention, wherein the fragmentation device ( 50 ) comprises a mesh member ( 50 ).
  • the fragmentation device ( 50 ) comprises a mesh member ( 50 )
  • gas bubbles are surely fragmentized and the resistance that gas-liquid two-phase fluid meets on the fragmentation device ( 50 ) becomes relatively small.
  • a third aspect of the invention is the gas-liquid separator according to the first aspect of the invention, wherein an opening end ( 21 ) of the inflow pipe ( 20 ) and an opening end ( 41 ) of the gas outflow pipe ( 40 ) are placed in an upper part of the vessel body ( 16 ) and arranged to face each other at opposite sides of the vessel body ( 16 ), and an opening end ( 31 ) of the liquid outflow pipe ( 30 ) is placed in a lower part of the vessel body ( 16 ).
  • an opening end ( 21 ) of the inflow pipe ( 20 ) and an opening end ( 41 ) of the gas outflow pipe ( 40 ) are placed to face each other in an upper part of the vessel body ( 16 ) and at opposite sides of the vessel body ( 16 ). Therefore, the opening end ( 21 ) of the inflow pipe ( 20 ) is free from being immersed in the pool ( 23 ) of liquid fluid in a lower part of the vessel body ( 16 ). As a result, it is prevented that gas-liquid two-phase fluid is directly introduced into the pool ( 23 ) of liquid fluid to mix gas bubbles into the pool ( 23 ) of liquid fluid and disturb the liquid level of the pool ( 23 ).
  • the opening end ( 21 ) of the inflow pipe ( 20 ) is prevented from being close to opposite part of the inside wall of the vessel body ( 16 ). This reduces the likelihood of hitting of gas-liquid two-phase fluid having flowed into the vessel body ( 16 ) through the inflow pipe ( 20 ) against the inside wall of the vessel body ( 16 ) and in turn the likelihood of the resultant spattering of the gas-liquid two-phase fluid.
  • the opening end ( 41 ) of the gas outflow pipe ( 40 ) is placed a certain distance away from the opening end ( 21 ) of the inflow pipe ( 20 ) in the vessel body ( 16 ), gas-liquid two-phase fluid flowing through the inflow pipe ( 20 ) into the vessel body ( 16 ) is free from directly flowing out through the opening end ( 41 ) of the gas outflow pipe ( 40 ). Furthermore, the opening end ( 31 ) of the liquid outflow pipe ( 30 ) is placed in the pool ( 23 ) of liquid fluid in a lower part of the interior of the vessel body ( 16 ).
  • a ninth aspect of the invention is directed to a gas-liquid separator including: a vessel body ( 16 ) for separating gas-liquid two-phase fluid into liquid fluid and gaseous fluid; an inflow pipe ( 20 ) through which the gas-liquid two-phase fluid flows into the vessel body ( 16 ); a liquid outflow pipe ( 30 ) through which liquid fluid in the vessel body ( 16 ) flows out of the vessel body ( 16 ); and a gas outflow pipe ( 40 ) through which gaseous fluid in the vessel body ( 16 ) flows out of the vessel body ( 16 ).
  • the vessel body ( 16 ) is formed to have a longer horizontal dimension than the vertical dimension.
  • an opening end ( 21 ) of the inflow pipe ( 20 ) and an opening end ( 41 ) of the gas outflow pipe ( 40 ) are placed in an upper part of the vessel body ( 16 ) and arranged to face each other at longitudinally opposite sides of the vessel body ( 16 ). Furthermore, an opening end ( 31 ) of the liquid outflow pipe ( 30 ) is placed in a lower part of the vessel body ( 16 ).
  • an opening end ( 21 ) of the inflow pipe ( 20 ) and an opening end ( 41 ) of the gas outflow pipe ( 40 ) are placed in an upper part of the vessel body ( 16 ) and arranged to face each other at longitudinally opposite sides of the vessel body ( 16 ). Therefore, the distance between the opening end ( 21 ) of the inflow pipe ( 20 ) and the opposite part of the inside wall of the vessel body ( 16 ) becomes long. Thus, gas-liquid two-phase fluid flowing through the inflow pipe ( 20 ) into the vessel body ( 16 ) is surely prevented from hitting the inside wall of the vessel body ( 16 ) and thereby spattering.
  • the opening end ( 41 ) of the gas outflow pipe ( 40 ) is surely spaced apart from the opening end ( 21 ) of the inflow pipe ( 20 ), gas-liquid two-phase fluid flowing through the inflow pipe ( 20 ) into the vessel body ( 16 ) is prevented from directly flowing out through the opening end ( 41 ) of the gas outflow pipe ( 40 ).
  • a fourth aspect of the invention is the gas-liquid separator according to the first aspect of the invention, wherein the vessel body ( 16 ) is installed so that the under surface ( 16 d) thereof inclines downward towards a point thereof corresponding to the opening end ( 31 ) of the liquid outflow pipe ( 30 ).
  • a tenth aspect of the invention is the gas-liquid separator according to the ninth aspect of the invention, wherein the vessel body ( 16 ) is installed so that the under surface ( 16 d) thereof inclines downward towards a point thereof corresponding to the opening end ( 31 ) of the liquid outflow pipe ( 30 ).
  • the under surface ( 16 d ) of the vessel body ( 16 ) means a surface located on the under side of the vessel body ( 16 ) and includes not only a flat surface but also, for example, a curved surface portion formed continuously with the other surface portions of the vessel body ( 16 ). According to the fourth and tenth aspects of the invention, even if the amount of liquid fluid in the vessel body ( 16 ) is small, the vessel body ( 16 ) surely has a pool of liquid fluid around the opening end ( 31 ) of the liquid outflow pipe ( 30 ) and thereby allows the liquid fluid to flow out through the liquid outflow pipe ( 30 ).
  • a fifth aspect of the invention is the gas-liquid separator according to the first aspect of the invention, wherein the inflow pipe ( 20 ) is horizontally extended to the interior of the vessel body ( 16 ) and the opening end ( 21 ) of the inflow pipe ( 20 ) opens obliquely downward.
  • An eleventh aspect of the invention is the gas-liquid separator according to the ninth aspect of the invention, wherein the inflow pipe ( 20 ) is horizontally extended to the interior of the vessel body ( 16 ) and the opening end ( 21 ) of the inflow pipe ( 20 ) opens obliquely downward.
  • gas-liquid two-phase fluid is free from hitting the inside wall of the vessel body ( 16 ) and thereby spattering.
  • the gas-liquid two-phase fluid falls more gently to the liquid level of liquid fluid in the vessel body ( 16 ) than the case of vertically falling, this reduces the disturbance of the liquid level of the pool ( 23 ) of liquid fluid and the mixing of gas bubbles into the pool ( 23 ) of liquid fluid.
  • a sixth aspect of the invention is the gas-liquid separator according to the first aspect of the invention, wherein the inflow pipe ( 20 ) is installed to horizontally extend.
  • a twelfth aspect of the invention is the gas-liquid separator according to the ninth aspect of the invention, wherein the inflow pipe ( 20 ) is installed to horizontally extend.
  • the inflow pipe ( 20 ) is installed to horizontally extend. Therefore, even if gas-liquid two-phase fluid forms a slug flow, large bubble masses of gaseous fluid in the slug flow are likely to be broken.
  • a seventh aspect of the invention is the gas-liquid separator according to the third aspect of the invention, wherein the opening end ( 41 ) of the gas outflow pipe ( 40 ) is placed above the opening end ( 21 ) of the inflow pipe ( 20 ).
  • a thirteenth aspect of the invention is the gas-liquid separator according to the ninth aspect of the invention, wherein the opening end ( 41 ) of the gas outflow pipe ( 40 ) is placed above the opening end ( 21 ) of the inflow pipe ( 20 ).
  • An eighth aspect of the invention is a refrigeration system including a refrigerant circuit ( 10 ) including the gas-liquid separator ( 18 ) according to the first aspect of the invention. Furthermore, a fourteenth aspect of the invention is a refrigeration system including a refrigerant circuit ( 10 ) including the gas-liquid separator ( 18 ) according to the ninth aspect of the invention.
  • the refrigerant circuit ( 10 ) is configured so that a first expansion mechanism ( 17 ), an evaporator ( 13 ), a low-pressure stage compressor ( 11 ), a high-pressure stage compressor ( 12 ), a condenser ( 14 ) and a second expansion mechanism ( 15 ) are connected in this order therein to operate in a two-stage compression and two-stage expansion refrigeration cycle.
  • the inflow pipe ( 20 ) of the gas-liquid separator ( 18 ) is connected to the downstream side of the second expansion valve ( 15 ) so that gas-liquid two-phase refrigerant flowing through the condenser ( 14 ) and then reduced to an intermediate pressure in the second expansion mechanism ( 15 ) flows into the vessel body ( 16 ) of the gas-liquid separator ( 18 ). Furthermore, the liquid outflow pipe ( 30 ) of the gas-liquid separator ( 18 ) is connected to the upstream side of the first expansion mechanism ( 17 ) so that liquid refrigerant separated by the gas-liquid separator ( 18 ) is fed to the first expansion mechanism ( 17 ).
  • gas outflow pipe ( 40 ) of the gas-liquid separator ( 18 ) is connected to the suction side of the high-pressure stage compressor ( 12 ) so that gas refrigerant separated by the gas-liquid separator ( 18 ) is fed to the suction side of the high-pressure,stage compressor ( 12 ).
  • the refrigerant circuit ( 10 ) including the gas-liquid separator ( 18 ) operates in a two-stage compression and two-stage expansion refrigeration cycle, gas-liquid two-phase refrigerant reduced to an intermediate pressure by the second expansion mechanism ( 15 ) is surely separated into liquid refrigerant and gas refrigerant by the gas-liquid separator ( 18 ).
  • gas refrigerant to be fed to the suction side of the high-pressure stage compressor ( 12 ) is prevented from mixing-in of liquid refrigerant and liquid refrigerant to be fed through the first expansion mechanism ( 17 ) to the evaporator ( 13 ) is prevented from mixing-in of gas refrigerant.
  • the evaporation capacity of the evaporator ( 13 ) and the condensation capacity of the condenser ( 14 ) are stabilized, thereby stabilizing the operation of the system.
  • the inflow pipe ( 20 ) is provided with a fragmentation device ( 50 ), even if gas-liquid two-phase fluid flowing through the inflow pipe ( 20 ) forms a slug flow, large gas bubbles of gaseous fluid can be fragmentized to homogenize the gas-liquid two-phase fluid. As a result, the gas-liquid two-phase fluid can be introduced in a regular and stable flow condition into the vessel body ( 16 ).
  • the gas-liquid two-phase fluid is separated into liquid fluid and gaseous fluid.
  • a pool ( 23 ) of liquid fluid is formed in a lower side of the interior of the vessel body ( 16 ), while a pool ( 24 ) of gaseous fluid is formed in an upper side thereof. Since gas-liquid two-phase fluid is introduced in a regular flow condition into the vessel body ( 16 ), this reduces the disturbance of the liquid level of the pool ( 23 ) of liquid fluid, the spattering of the liquid fluid due to the disturbance and the mixing of gas bubbles into the pool ( 23 ) of liquid fluid.
  • liquid fluid flowing from the pool ( 23 ) of liquid fluid to the liquid outflow pipe ( 30 ) can be prevented from mixing-in of gas refrigerant and gaseous fluid flowing from the pool ( 24 ) of gaseous fluid to the gas outflow pipe ( 40 ) can be prevented from mixing-in of liquid fluid. Therefore, the gas-liquid separation performance can be enhanced.
  • the fragmentation device ( 50 ) comprises a mesh member ( 50 )
  • gas bubbles can surely be fragmentized and the resistance that gas-liquid two-phase fluid meets on the fragmentation device ( 50 ) can be relatively small.
  • the gas-liquid two-phase fluid flowing into the vessel body ( 16 ) reaches a further regular and stable flow condition.
  • the opening end ( 21 ) of the inflow pipe ( 20 ) and the opening end ( 41 ) of the gas outflow pipe ( 40 ) are placed to face each other in an upper part of the vessel body ( 16 ) and at opposite sides of the vessel body ( 16 ), gas-liquid two-phase fluid can be prevented from being directly introduced from the opening end ( 21 ) of the inflow pipe ( 20 ) to the pool ( 23 ) of liquid fluid in a lower part of the vessel body ( 16 ).
  • gas-liquid two-phase fluid flowing through the opening end ( 21 ) of the inflow pipe ( 20 ) into the vessel body ( 16 ) can be prevented from hitting the inside wall of the vessel body ( 16 ) and thereby spattering. As a result, it can surely be prevented that gas bubbles are mixed into the pool ( 23 ) of liquid fluid and that the liquid level of the pool ( 23 ) gets disturbed.
  • the opening end ( 41 ) of the gas outflow pipe ( 40 ) can be placed a certain distance away from the opening end ( 21 ) of the inflow pipe ( 20 ) in the vessel body ( 16 ), gas-liquid two-phase fluid flowing through the inflow pipe ( 20 ) into the vessel body ( 16 ) can be prevented from directly flowing out through the opening end ( 41 ) of the gas outflow pipe ( 40 ).
  • liquid fluid flowing from the pool ( 23 ) of liquid fluid to the liquid outflow pipe ( 30 ) can surely be prevented from mixing-in of gaseous fluid and gaseous fluid flowing from the pool ( 24 ) of gaseous fluid to the gas outflow pipe can surely be prevented from mixing-in of liquid fluid.
  • the opening end ( 21 ) of the inflow pipe ( 20 ) and the opening end ( 41 ) of the gas outflow pipe ( 40 ) are placed in an upper part of the vessel body ( 16 ) and arranged to face each other at longitudinally opposite sides of the vessel body ( 16 ), the distance between the opening end ( 21 ) of the inflow pipe ( 20 ) and the opposite part of the inside wall of the vessel body ( 16 ) can be long.
  • gas-liquid two-phase fluid flowing through the inflow pipe ( 20 ) into the vessel body ( 16 ) can surely be prevented from hitting the inside wall of the vessel body ( 16 ) and thereby spattering.
  • the pool ( 23 ) of liquid fluid in a lower side of the interior of the vessel body ( 16 ) can be prevented from disturbance of its liquid level and mixing-in of gas bubbles. In addition, it can be prevented that fluid spattered by the hitting flows out through the gas outflow pipe ( 40 ).
  • the opening end ( 41 ) of the gas outflow pipe ( 40 ) can surely be spaced apart from the opening end ( 21 ) of the inflow pipe ( 20 ). Therefore, gas-liquid two-phase fluid flowing through the inflow pipe ( 20 ) into the vessel body ( 16 ) can be prevented from directly flowing out through the opening end ( 41 ) of the gas outflow pipe ( 40 ).
  • pipe ( 30 ) can surely be prevented from mixing-in of gaseous fluid.
  • gaseous fluid flowing from the pool ( 24 ) of gaseous fluid to the gas outflow pipe ( 40 ) can surely be prevented from mixing-in of liquid fluid. As a result, the gas-liquid separation performance can be enhanced.
  • the vessel body ( 16 ) since the under surface ( 16 d) of the vessel body ( 16 ) is inclined downward towards a point thereof corresponding to the opening end ( 31 ) of the liquid outflow pipe ( 30 ), even if the amount of liquid fluid in the vessel body ( 16 ) is small, the vessel body ( 16 ) can surely have a pool of liquid fluid around the opening end ( 31 ) of the liquid outflow pipe ( 30 ). This ensures that liquid fluid flows out through the liquid outflow pipe ( 30 ), and prevents that during the outflow of liquid fluid, gaseous fluid is mixed into the liquid fluid flowing out therethrough.
  • the inflow pipe ( 20 ) is horizontally extended to the interior of the vessel body ( 16 ) and the opening end ( 21 ) of the inflow pipe ( 20 ) opens obliquely downward, gas-liquid two-phase fluid can be prevented from hitting the inside wall of the vessel body ( 16 ) and thereby spattering.
  • the gas-liquid two-phase fluid can fall more gently to the liquid level of liquid fluid in the vessel body ( 16 ) than the case of vertically falling, this reduces the disturbance of the liquid level of the pool ( 23 ) of liquid fluid and the mixing of gas bubbles into the pool ( 23 ).
  • the inflow pipe ( 20 ) since the inflow pipe ( 20 ) is installed to horizontally extend, even if gas-liquid two-phase fluid forms a slug flow, large bubble masses of gaseous fluid in the slug flow are likely to be broken.
  • the opening end ( 41 ) of the gas outflow pipe ( 40 ) is placed above the opening end ( 21 ) of the inflow pipe. ( 20 ), gas-liquid two-phase fluid having flowed through the inflow pipe ( 20 ) into the vessel body ( 16 ) can be prevented from falling towards the opening end ( 41 ) of the gas outflow pipe ( 40 ) and directly flowing out through it.
  • the refrigerant circuit ( 10 ) including the gas-liquid separator ( 18 ) according to the first or ninth aspect of the invention operates in a two-stage compression and two-stage expansion refrigeration cycle, gas-liquid two-phase refrigerant reduced to an intermediate pressure by the second expansion mechanism ( 15 ) can surely be separated into liquid refrigerant and gas refrigerant by the gas-liquid separator ( 18 ).
  • gas refrigerant to be fed to the suction side of the high-pressure stage compressor ( 12 ) can be prevented from mixing-in of liquid refrigerant and liquid refrigerant to be fed through the first expansion mechanism ( 17 ) to the evaporator ( 13 ) can be prevented from mixing-in of gas refrigerant.
  • the evaporation capacity of the evaporator ( 13 ) and the condensation capacity of the condenser ( 14 ) are stabilized, thereby stabilizing the operation of the system. Therefore, the reliability of the system can be enhanced.
  • FIG. 1 is a piping diagram of a refrigerant circuit of a refrigeration system according to Embodiment 1.
  • FIG. 2 is a longitudinal cross-sectional view of a gas-liquid separator according to Embodiment 1.
  • FIG. 3 is a longitudinal cross-sectional view of a gas-liquid separator according to Modification 1 of Embodiment 1.
  • FIG. 4 is a longitudinal cross-sectional view of a gas-liquid separator according to Modification 2 of Embodiment 1 .
  • FIG. 5 is a longitudinal cross-sectional view of a gas-liquid separator according to Embodiment 2.
  • FIG. 6 is a longitudinal cross-sectional view of a gas-liquid separator according to Modification 1 of Embodiment 2.
  • FIG. 7 is a longitudinal cross-sectional view of a gas-liquid separator according to Modification 2 of Embodiment 2.
  • FIG. 8 is a longitudinal cross-sectional view of a known gas-liquid separator.
  • FIG. 9 is a longitudinal cross-sectional view of another known gas-liquid separator.
  • a refrigeration system ( 1 ) is used to perform an operation of refrigerating the interior of a storage.
  • the refrigeration system ( 1 ) includes a refrigerant circuit ( 10 ) operating in a two-stage compression and two-stage expansion refrigeration cycle.
  • the refrigerant circuit ( 10 ) includes a low-pressure stage compressor ( 11 ), a high-pressure stage compressor ( 12 ), a refrigeration heat exchanger ( 13 ), an outdoor heat exchanger ( 14 ), a main expansion valve ( 17 ), an intermediate expansion valve ( 15 ) and a gas-liquid separator ( 18 ) as a feature of the present invention.
  • the discharge side of the low-pressure stage compressor ( 11 ) is connected to the suction side of the high-pressure stage compressor ( 12 ).
  • Each of the low-pressure stage compressor ( 11 ) and high-pressure stage compressor ( 12 ) is constituted, for example, by a scroll compressor.
  • the refrigeration heat exchanger ( 13 ) is placed in the storage and configured as an evaporator in which refrigerant can evaporate to cool the interior of the storage.
  • the refrigeration heat exchanger ( 13 ) is connected at its exit side to the suction side of the low-pressure stage compressor ( 11 ).
  • the refrigeration heat exchanger ( 13 ) is constituted, for example, by a fin-and-tube heat exchanger.
  • the refrigeration heat exchanger ( 13 ) is connected at its entrance side to the exit side of the main expansion valve ( 17 ).
  • the main expansion valve ( 17 ) is an electronic expansion valve controllable in opening and is configured as a first expansion mechanism.
  • the outdoor heat exchanger ( 14 ) is placed outside the storage and configured as a condenser in which refrigerant can condense.
  • the outdoor heat exchanger ( 14 ) is connected at its entrance side to the discharge side of the high-pressure stage compressor ( 12 ).
  • the outdoor heat exchanger ( 14 ) is constituted, for example, by a fin-and-tube heat exchanger.
  • the outdoor heat exchanger ( 14 ) is connected at its exit side to the entrance side of the intermediate expansion valve ( 15 ).
  • the intermediate expansion valve ( 15 ) is an electronic expansion valve controllable in opening and is configured as a second expansion mechanism.
  • the gas-liquid separator ( 18 ) includes a vessel body ( 16 ), an inflow pipe ( 20 ), a liquid outflow pipe ( 30 ) and a gas outflow pipe ( 40 ).
  • the vessel body ( 16 ) is connected via the inflow pipe ( 20 ) to the exit side of the intermediate expansion valve ( 15 ), which is the downstream side thereof, connected via the liquid outflow pipe ( 30 ) to the entrance side of the main expansion valve ( 17 ), which is the upstream side thereof, and connected via the gas outflow pipe ( 40 ) to the suction side of the high-pressure stage compressor ( 12 ).
  • the exit side of the intermediate expansion valve ( 15 ) is connected via the gas-liquid separator ( 18 ) to the entrance side of the main expansion valve ( 17 ), which is the upstream side thereof, and the suction side of the high-pressure stage compressor ( 12 ).
  • the vessel body ( 16 ) of the gas-liquid separator ( 18 ) is formed in an axially long, substantially cylindrical shape and disposed to match its axial direction with the vertical direction.
  • the vessel body ( 16 ) has a first through hole ( 16 a ), a second through hole ( 16 b ) and a third through hole ( 16 c ) all in the peripheral wall forming the side surface of the cylinder.
  • the first through hole ( 16 a ) is formed in an upper part of the peripheral wall of the vessel body ( 16 )
  • the second through hole ( 16 b ) is formed on the opposite side of the peripheral wall of the vessel body ( 16 ) to the first through hole ( 16 a ) and at a higher point than the first through hole ( 16 a )
  • the third through hole ( 16 c ) is formed in a lower part of the peripheral wall of the vessel body ( 16 ).
  • a pool ( 23 ) of liquid refrigerant is formed in a lower side thereof and a pool ( 24 ) of gas refrigerant is formed above the pool ( 23 ) of liquid refrigerant.
  • the inflow pipe ( 20 ) is disposed to horizontally extend over the length thereof. Furthermore, the inflow pipe ( 20 ) is extended to the interior of the vessel body ( 16 ) by passing through the first through hole ( 16 a ) of the vessel body ( 16 ) and is disposed substantially perpendicularly to the peripheral wall of the vessel body ( 16 ).
  • the opening end ( 21 ) of the inflow pipe ( 20 ) is placed in the vessel body ( 16 ) closer to part of the peripheral wall having the first through hole ( 16 a ) than the horizontal center of the vessel body ( 16 ). Furthermore, the opening end ( 21 ) of the inflow pipe ( 20 ) opens obliquely downward at an angle of approximately 45° to the vertical direction.
  • the inflow pipe ( 20 ) is provided with a mesh member ( 50 ) as a feature of the present invention. Specifically, a through part of the inflow pipe ( 20 ) at which the inflow pipe ( 20 ) passes through the first through hole ( 16 a) of the vessel body ( 16 ) is brazed to the vessel body ( 16 ), and the mesh member ( 50 ) is placed in the inflow pipe ( 20 ) in the close vicinity of the through part.
  • the mesh member ( 50 ) is composed of a wire mesh formed in a hollow conical shape, opening at the bottom of the cone and having the periphery of the cone netted with metal wires.
  • the mesh member ( 50 ) is disposed so that its cone point is directed to the opening end ( 21 ).
  • the inflow pipe ( 20 ) is configured so that refrigerant having flowed through the intermediate expansion valve ( 15 ) flows through the opening at the bottom of the mesh member ( 50 ) towards the cone point and, during the flow through the mesh member ( 50 ), passes through the wire mesh at the periphery of the cone.
  • the gas outflow pipe ( 40 ) is extended to the interior of the vessel body ( 16 ) by passing through the second through hole ( 16 b ) of the vessel body ( 16 ) and is disposed substantially perpendicularly to the peripheral wall of the vessel body ( 16 ).
  • the opening end ( 41 ) of the gas outflow pipe ( 40 ) is placed in the vessel body ( 16 ) closer to part of the peripheral wall having the second through hole ( 16 b ) than the horizontal center of the vessel body ( 16 ).
  • the opening end ( 21 ) of the inflow pipe ( 20 ) and the opening end ( 41 ) of the gas outflow pipe ( 40 ) are placed in the pool ( 24 ) of gas refrigerant in an upper part of the vessel body ( 16 ) and arranged to face each other at opposite sides of the vessel body ( 16 ). Furthermore, the opening end ( 41 ) of the gas outflow pipe ( 40 ) is placed above the opening end ( 21 ) of the inflow pipe ( 20 ).
  • the liquid outflow pipe ( 30 ) passes through the third through hole ( 16 c ) of the vessel body ( 16 ) and is disposed substantially perpendicularly to the peripheral wall of the vessel body ( 16 ).
  • the opening end ( 31 ) of the liquid outflow pipe ( 30 ) is placed in the pool ( 23 ) of liquid refrigerant in a lower part of the vessel body ( 16 ).
  • the compressors ( 11 , 12 ) Upon startup of the refrigeration system ( 1 ), in the refrigerant circuit ( 10 ), the compressors ( 11 , 12 ) start to operate, the openings of the expansion valves ( 15 , 17 ) are appropriately set and refrigerant circulates through the refrigerant circuit ( 10 ) in a direction of the arrows in FIG. 1 .
  • the refrigerant in a gas-liquid two-phase state flows through the inflow pipe ( 20 ) of the gas-liquid separator ( 18 ) and passes through the mesh member ( 50 ).
  • gas bubbles in the refrigerant in a gas-liquid two-phase state are fragmentized.
  • gas-liquid two-phase refrigerant in the inflow pipe ( 20 ) forms a slug flow so that gas bubbles ( 80 ) formed by large masses of gas refrigerant flow through the inflow pipe ( 20 ).
  • gas bubbles ( 80 ) pass through the mesh member ( 50 ) and are thereby fragmentized into fine gas bubbles ( 81 ).
  • the gas-liquid two-phase refrigerant becomes a homogeneous state in which fine gas bubbles ( 81 ) are dispersed in liquid refrigerant.
  • the gas-liquid two-phase refrigerant is introduced into the interior of the vessel body ( 16 ) while being kept in its homogeneous state.
  • the gas-liquid two-phase refrigerant is introduced into the interior of the vessel body ( 16 ) to gently fall from the opening end ( 21 ) opening downward at 45° to the vertical direction towards the pool ( 23 ) of liquid refrigerant.
  • the gas-liquid two-phase refrigerant is thus introduced in a stable flow condition into the interior of the vessel body ( 16 ), this reduces the bubbling of the pool ( 23 ) of liquid refrigerant and resultant production of gas bubbles and reduces the disturbance of the liquid level of the pool ( 23 ) of liquid refrigerant and resultant spattering of liquid refrigerant. Then, the gas-liquid two-phase refrigerant introduced in the vessel body ( 16 ) is separated into liquid refrigerant and gas refrigerant.
  • the gas refrigerant is accumulated in the gas refrigerant pool ( 24 ) in an upper part of the vessel body ( 16 ), while the liquid refrigerant is accumulated in the liquid refrigerant pool ( 23 ) in a lower part of the vessel body ( 16 ).
  • the liquid refrigerant in the vessel body ( 16 ) then flows through the liquid outflow pipe ( 30 ), then passes through the main expansion valve ( 17 ) and is thereby reduced to a low pressure to expand.
  • the expanded refrigerant takes heat from in-storage air during flow through the refrigeration heat exchanger ( 13 ), thereby evaporating and cooling the in-storage air.
  • the evaporated refrigerant is sucked into the low-pressure stage compressor ( 11 ), compressed therein to an intermediate-pressure and then discharged therefrom. Then, the gas refrigerant in the vessel body ( 16 ) of the gas-liquid separator ( 18 ) is fed through the gas outflow pipe ( 40 ) to the discharged refrigerant of intermediate pressure and the refrigerant mixture is sucked into the high-pressure stage compressor ( 11 ).
  • gas bubbles ( 80 ) of gas refrigerant in gas-liquid two-phase refrigerant flowing through the inflow pipe ( 20 ) can surely be fragmentized, whereby the gas-liquid two-phase refrigerant can be homogenized.
  • the gas-liquid two-phase refrigerant is introduced in a regular and stable flow condition into the vessel body ( 16 ).
  • the inflow pipe ( 20 ) is disposed to horizontally extend over the length thereof, large bubble masses of gas refrigerant in the gas-liquid two-phase fluid are likely to be broken, which restrains the production of large gas bubbles ( 80 ) in advance of the passage of the gas-liquid two-phase fluid through the mesh member ( 50 ).
  • the opening end ( 21 ) of the inflow pipe ( 20 ) and the opening end ( 41 ) of the gas outflow pipe ( 40 ) are placed in the pool ( 24 ) of gas refrigerant in an upper part of the vessel body ( 16 ) and arranged to face each other at opposite sides of the vessel body ( 16 ).
  • the gas-liquid two-phase refrigerant can be prevented from being directly introduced from the opening end ( 21 ) of the inflow pipe ( 20 ) to the pool ( 23 ) of liquid refrigerant and the gas-liquid two-phase refrigerant flowing through the opening end ( 21 ) of the inflow pipe ( 20 ) into the vessel body ( 16 ) can be prevented from hitting the inside wall of the vessel body ( 16 ) and thereby spattering. Hence, it can be prevented that gas bubbles are mixed into the pool ( 23 ) of liquid refrigerant and that the liquid level of the pool ( 23 ) gets disturbed.
  • the opening end ( 21 ) of the inflow pipe ( 20 ) opens obliquely downward by bending at approximately 45°, this surely prevents the gas-liquid two-phase refrigerant from hitting the peripheral wall of the vessel body ( 16 ). Furthermore, since the gas-liquid two-phase refrigerant falls more gently to the liquid level of the pool ( 23 ) of liquid refrigerant in the vessel body ( 16 ) than the case of vertically falling, this reduces the disturbance of the liquid level of the pool ( 23 ) of liquid refrigerant and the bubbling of the pool ( 23 ) of liquid refrigerant.
  • the opening end ( 41 ) of the gas outflow pipe ( 40 ) is placed at an opposite side of the vessel body ( 16 ) to the opening end ( 21 ) of the inflow pipe ( 20 ) and above the opening end ( 21 ) of the inflow pipe ( 20 ). Therefore, the gas-liquid two-phase refrigerant having flowed through the inflow pipe ( 20 ) into the vessel body ( 16 ) can be prevented from directly flowing out through the gas outflow pipe ( 40 ).
  • the opening end ( 31 ) of the liquid outflow pipe ( 30 ) is placed in the pool ( 23 ) of liquid refrigerant in a lower part of the vessel body ( 16 ), this prevents that during the outflow of liquid refrigerant through the liquid outflow pipe ( 30 ), gas refrigerant is mixed into the liquid refrigerant.
  • liquid refrigerant flowing from the pool ( 23 ) of liquid refrigerant to the liquid outflow pipe ( 30 ) can be prevented from mixing-in of gas refrigerant.
  • gas refrigerant flowing from the pool ( 24 ) of gas refrigerant to the gas outflow pipe ( 40 ) can be prevented from mixing-in of liquid refrigerant.
  • the gas-liquid separation performance can be enhanced.
  • the gas-liquid separator ( 18 ) of the refrigerant circuit ( 10 ) can be enhanced in gas-liquid separation performance, this stabilizes the evaporation capacity of the refrigeration heat exchanger ( 13 ) and the condensation capacity of the outdoor heat exchanger ( 14 ), thereby stabilizing the operation of the refrigeration system ( 1 ). As a result, the reliability of the refrigeration system ( 1 ) can be enhanced.
  • This embodiment has a configuration that, although in Embodiment 1 the inflow pipe ( 20 ) of the gas-liquid separator ( 18 ) is composed of a single pipe, the inflow pipe ( 20 ) is, as shown in FIG. 3 , composed of a main pipe part ( 20 a ), a mesh pipe part ( 20 b ) and a brazing pipe part ( 20 c ) instead.
  • the brazing pipe part ( 20 c ) is brazed to the first through hole ( 16 a ) in the vessel body ( 16 ).
  • the mesh pipe part ( 20 b ) is formed with a larger pipe diameter than the brazing pipe part ( 20 c ) and the main pipe part ( 20 a ) and includes a conically shaped mesh member ( 50 ) placed therein like Embodiment 1.
  • the main pipe part ( 20 a) is connected through the mesh pipe part ( 20 b ) to the brazing pipe part ( 20 c ).
  • main pipe part ( 20 a ), the mesh pipe part ( 20 b ) and the brazing pipe part ( 20 c ) are connected in this order.
  • the inflow pipe ( 20 ) is composed of the three pipe parts ( 20 a, 20 b, 20 c ), maintenance and replacement of the mesh member ( 50 ) can be easily performed. Furthermore, although in the mesh pipe part ( 20 b ) the mesh member ( 50 ) resists the flow of refrigerant in a gas-liquid two-phase state, the resistance can be reduced by the formation of the mesh pipe part ( 20 b ) with a slightly larger diameter than the other parts.
  • This embodiment has a configuration that, although in Embodiment 1 the vessel body ( 16 ) of the gas-liquid separator ( 18 ) is formed in a substantially cylindrical shape, the under surface ( 16 d ) of the vessel body ( 16 ) is, as shown in FIG. 4 , inclined downward towards a point thereof corresponding to the opening end ( 31 ) of the liquid outflow pipe ( 30 ).
  • the vessel body ( 16 ) since the under surface ( 16 d ) of the vessel body ( 16 ) inclines downward towards a point thereof corresponding to the opening end ( 31 ) of the liquid outflow pipe ( 30 ), even if the amount of liquid refrigerant in the vessel body ( 16 ) is small, the vessel body ( 16 ) can surely have a pool of liquid refrigerant around the opening end ( 31 ) of the liquid outflow pipe ( 30 ). As a result, liquid refrigerant can surely flow out through the liquid outflow pipe ( 30 ). In addition, the opening end ( 31 ) of the liquid outflow pipe ( 30 ) is free from being exposed to the gas refrigerant pool ( 24 ). This prevents gas refrigerant from flowing out through the liquid outflow pipe ( 30 ).
  • This embodiment is, like Embodiment 1, a refrigeration system that includes a refrigerant circuit operating in a two-stage compression and two-stage expansion refrigeration cycle and performs an operation of refrigerating the interior of a storage, but is different from Embodiment 1 only in the configuration of the gas-liquid separator ( 18 ) in the refrigerant circuit.
  • the vessel body ( 16 ) is formed to have a longer horizontal dimension than the vertical dimension. Furthermore, the inflow pipe ( 20 ) of the gas-liquid separator ( 18 ) does not include a mesh member ( 50 ) serving as a fragmentation device.
  • the vessel body ( 16 ) of the gas-liquid separator ( 18 ) is horizontally installed to match the axial direction of the cylindrical vessel body ( 16 ) in Embodiment 1 with the horizontal direction.
  • the vessel body ( 16 ) is formed to have a longer horizontal dimension than the vertical dimension.
  • one of two end surfaces of the cylinder of the vessel body ( 16 ) has a first through hole ( 16 a ) formed in an upper part thereof and a third through hole ( 16 c ) formed in a lower part thereof.
  • the inflow pipe ( 20 ) and a liquid outflow pipe ( 30 ) are connected to the vessel body ( 16 ) to pass through the first through hole ( 16 a ) and the third through hole ( 16 c ), respectively, substantially perpendicular to the associated end surfaces of the vessel body ( 16 ).
  • the other end surface of the vessel body ( 16 ) has a second through hole ( 16 b ) formed above a point thereof corresponding to the first through hole ( 16 a ).
  • a gas outflow pipe ( 40 ) is connected to the vessel body ( 16 ) to pass through the second hole ( 16 b ).
  • the opening end ( 21 ) of the inflow pipe ( 20 ) and the opening end ( 31 ) of the liquid outflow pipe ( 30 ) are placed in the vessel body ( 16 ) closer to the end surface having the first through hole ( 16 a ) and the third through hole ( 16 c ) than the horizontal center of the vessel body ( 16 ).
  • the opening end ( 41 ) of the gas outflow pipe ( 40 ) is placed in the vessel body ( 16 ) closer to the end surface having the second through hole ( 16 b ) than the horizontal center of the vessel body ( 16 ).
  • the opening end ( 21 ) of the inflow pipe ( 20 ) and the opening end ( 41 ) of the gas outflow pipe ( 40 ) are placed in the pool ( 24 ) of gas refrigerant in an upper part of the vessel body ( 16 ) and arranged to face each other at longitudinally opposite sides of the vessel body ( 16 ). Furthermore, the opening end ( 41 ) of the gas outflow pipe ( 40 ) is placed above the opening end ( 21 ) of the inflow pipe ( 20 ). On the other hand, the opening end ( 31 ) of the liquid outflow pipe ( 30 ) is placed in the pool ( 23 ) of liquid refrigerant in a lower part of the vessel body ( 16 ).
  • this embodiment exhibits the following effects since the vessel body ( 16 ) is installed to match its horizontal direction ( 16 ) with its longitudinal direction.
  • the distance between the opening end ( 21 ) of the inflow pipe ( 20 ) and an opposite part of the inside wall of the vessel body ( 21 ) i.e., the end surface having the second through hole ( 16 b )
  • the gas-liquid two-phase refrigerant flowing through the inflow pipe ( 20 ) forms a slug flow to temporarily reaches a high flow rate the gas-liquid two-phase refrigerant having flowed through the inflow pipe ( 20 ) into the vessel body ( 16 ) can be prevented from hitting the inside wall of the vessel body ( 16 ).
  • the opening end ( 21 ) of the inflow pipe ( 20 ) and the opening end ( 41 ) of the gas outflow pipe ( 40 ) can surely be spaced apart from each other, gas-liquid two-phase refrigerant having flowed through the inflow pipe ( 20 ) into the vessel body ( 16 ) can surely be prevented from directly flowing out through the gas outflow pipe ( 40 ).
  • the gas-liquid separator ( 18 ) can prevent gas refrigerant flowing out through the gas outflow pipe ( 40 ) from mixing-in of liquid refrigerant and prevent liquid refrigerant flowing out through the liquid outflow pipe ( 30 ) from mixing-in of gas refrigerant.
  • the gas-liquid separation performance of the gas-liquid separator ( 18 ) can be enhanced.
  • gas-liquid two-phase refrigerant having flowed through the inflow pipe ( 20 ) into the vessel body ( 16 ) is prevented from hitting the inside wall of the vessel body ( 16 ) by matching the longitudinal direction of the vessel body ( 16 ) with the horizontal direction.
  • the gas-liquid two-phase refrigerant having flowed through the inflow pipe ( 20 ) into the vessel body ( 16 ) can be further surely prevented from hitting the inside wall of the vessel body ( 16 ) by configuring the inflow pipe ( 20 ) so that the opening end ( 21 ) thereof opens obliquely downward like Embodiment 1.
  • This embodiment is configured, as shown in FIG. 6 , by placing a mesh member ( 50 ) in the inflow pipe ( 20 ) of the gas-liquid separator ( 18 ) according to Embodiment 2.
  • gas-liquid two-phase refrigerant introduced through the inflow pipe ( 20 ) into the vessel body ( 50 ) is homogenized, whereby the flow condition of the gas-liquid two-phase refrigerant becomes regular and stable.
  • the gas-liquid separation performance of the gas-liquid separator ( 18 ) can be further enhanced.
  • This embodiment is configured, as shown in FIG. 7 , by installing the vessel body ( 16 ) of the gas-liquid separator ( 18 ) according to Embodiment 2 to incline it downward from its one end surface through which the gas outflow pipe ( 40 ) passes towards its other end surface through which the liquid outflow pipe ( 30 ) passes.
  • an under part ( 16 d ) of the peripheral surface of the cylindrical vessel body ( 16 ) inclines downward towards a point thereof corresponding to the opening end ( 31 ) of the liquid outflow pipe ( 30 ) and is thereby constituted as the under surface of the vessel body ( 16 ).
  • only the vessel body ( 16 ) is placed at an angle but the pipes ( 20 , 30 , 40 ) are horizontally placed in and around the vessel body ( 16 ).
  • the vessel body ( 16 ) can surely have a pool of liquid refrigerant around the opening end ( 31 ) of the liquid outflow pipe ( 30 ) even if the amount of liquid refrigerant therein is small. This ensures that liquid refrigerant flows out through the liquid outflow pipe ( 30 ).
  • the opening end ( 31 ) of the liquid outflow pipe ( 30 ) can be prevented from being exposed to the gas refrigerant pool ( 24 ). This prevents gas refrigerant from flowing out through the liquid outflow pipe ( 30 ).
  • the under part ( 16 d ) of the peripheral surface of the cylindrical vessel body ( 16 ) is inclined downward towards the point thereof corresponding to the opening end ( 31 ) of the liquid outflow pipe ( 30 ) by inclining the entire vessel body ( 16 ).
  • the vessel body ( 16 ) may have a shape in which only its under part ( 16 d ) inclines downward towards the point thereof corresponding to the opening end ( 31 ) of the liquid outflow pipe ( 30 ).
  • the pipes ( 20 , 30 , 40 ) may be placed to incline in the same direction as the vessel body ( 16 ) by extending them to the interior of the vessel body ( 16 ) substantially vertically with respect to the end surfaces of the vessel body ( 16 ).
  • the above embodiments may have the following configurations.
  • the refrigeration system ( 1 ) is a refrigeration system performing an operation of refrigerating the interior of a storage
  • the refrigeration system of the present invention is sufficient if it includes a refrigerant circuit including a gas-liquid separator and operating in a two-stage compression and two-stage expansion refrigeration cycle.
  • the refrigeration system ( 1 ) may be, for example, a refrigeration system performing either one of cooling and heating operations for a room, or may be a refrigeration system switchable between the cooling and heating operations, or may be a refrigeration system switchable between a single-stage compression and single-stage expansion operation and a two-stage compression and two-stage expansion operation.
  • the configurations of the compressors ( 11 , 21 ) and heat exchangers ( 13 , 14 ) in the refrigerant circuit are not particularly limited.
  • the mesh member ( 50 ) placed in the inflow pipe ( 20 ) of the gas-liquid separator ( 18 ) is conically shaped
  • the shape and configuration of the mesh member ( 50 ) are not particularly limited.
  • the mesh member ( 50 ) may comprise a single or a plurality of overlaid mesh plates placed in the inflow pipe ( 20 ).
  • the vessel body ( 16 ) of the gas-liquid separator ( 18 ) has a cylindrical shape
  • the shape of the vessel body ( 16 ) is not particularly limited and may be a rectangular parallelepiped, for example.
  • the present invention is useful for a gas-liquid separator and a refrigeration system including a refrigerant circuit with the gas-liquid separator.

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  • Degasification And Air Bubble Elimination (AREA)
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US12/087,873 2006-01-17 2007-01-16 Gas-Liquid Separator and Refrigeration System With Gas-Liquid Seperator Abandoned US20100154467A1 (en)

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JP2006008897A JP2007192433A (ja) 2006-01-17 2006-01-17 気液分離器及び該気液分離器を備えた冷凍装置
JP206-008897 2006-01-17
PCT/JP2007/050492 WO2007083624A1 (ja) 2006-01-17 2007-01-16 気液分離器及び該気液分離器を備えた冷凍装置

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US20100300143A1 (en) * 2007-11-05 2010-12-02 Bjorn Sollie Liquid Separator For An Evaporator System
WO2012109057A3 (en) * 2011-02-08 2012-10-11 Carrier Corporation Brazed plate heat exchanger for water-cooled heat rejction in a refrigeration cycle
WO2014031728A1 (en) * 2012-08-23 2014-02-27 Shell Oil Company System and method for separating fluid produced from a wellbore
CN103765124A (zh) * 2011-09-01 2014-04-30 大金工业株式会社 制冷装置
US9261298B2 (en) 2010-07-23 2016-02-16 Carrier Corporation Ejector cycle refrigerant separator
EP4036512A1 (de) * 2021-01-29 2022-08-03 Airbus Operations GmbH System zum bereitstellen einer druckbeaufschlagten flüssigkeit
US20220333829A1 (en) * 2021-04-20 2022-10-20 Carrier Corporation Economizer and air conditioning system
US12076672B2 (en) 2021-01-29 2024-09-03 Airbus Operations Gmbh System for providing a pressurized liquid

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CN103375953B (zh) * 2012-04-27 2016-02-10 珠海格力电器股份有限公司 气液分离器及具有其的空调系统
JP5729359B2 (ja) * 2012-07-09 2015-06-03 株式会社デンソー 冷凍サイクル装置
JP6029879B2 (ja) * 2012-07-10 2016-11-24 シャープ株式会社 ヒートポンプ式加熱装置
CN104697249A (zh) * 2013-12-09 2015-06-10 马兴国 新型氟冷风机分布器
CN105928270B (zh) * 2016-06-06 2018-12-28 大连冷冻机股份有限公司 汽液分离型分液器
CN107945892B (zh) * 2017-09-29 2024-06-25 中广核研究院有限公司 一体化气态氧控装置以及铅基快中子反应堆
CN109373657B (zh) * 2018-11-19 2023-05-23 珠海格力节能环保制冷技术研究中心有限公司 空调系统及其控制方法
CN115516259A (zh) * 2020-05-11 2022-12-23 三菱电机株式会社 储蓄器和制冷循环装置
KR102144916B1 (ko) * 2020-05-19 2020-08-14 주식회사 케이. 씨. 이 메카니칼씰의 수냉식 냉각 시스템
WO2023053513A1 (ja) * 2021-09-30 2023-04-06 株式会社島津製作所 気液分離器、全有機体炭素計および分析システム

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US20100300143A1 (en) * 2007-11-05 2010-12-02 Bjorn Sollie Liquid Separator For An Evaporator System
US10036583B2 (en) * 2007-11-05 2018-07-31 Alfa Laval Corporated Ab Liquid separator for an evaporator system
US9261298B2 (en) 2010-07-23 2016-02-16 Carrier Corporation Ejector cycle refrigerant separator
WO2012109057A3 (en) * 2011-02-08 2012-10-11 Carrier Corporation Brazed plate heat exchanger for water-cooled heat rejction in a refrigeration cycle
US10401094B2 (en) 2011-02-08 2019-09-03 Carrier Corporation Brazed plate heat exchanger for water-cooled heat rejection in a refrigeration cycle
CN103765124A (zh) * 2011-09-01 2014-04-30 大金工业株式会社 制冷装置
WO2014031728A1 (en) * 2012-08-23 2014-02-27 Shell Oil Company System and method for separating fluid produced from a wellbore
EP4036512A1 (de) * 2021-01-29 2022-08-03 Airbus Operations GmbH System zum bereitstellen einer druckbeaufschlagten flüssigkeit
US12076672B2 (en) 2021-01-29 2024-09-03 Airbus Operations Gmbh System for providing a pressurized liquid
US20220333829A1 (en) * 2021-04-20 2022-10-20 Carrier Corporation Economizer and air conditioning system

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JP2007192433A (ja) 2007-08-02
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WO2007083624A1 (ja) 2007-07-26
CN101371085A (zh) 2009-02-18
AU2007206437A1 (en) 2007-07-26

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