WO2010040355A1 - Cooling compressor with system for reducing oil outflow - Google Patents

Cooling compressor with system for reducing oil outflow Download PDF

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Publication number
WO2010040355A1
WO2010040355A1 PCT/DK2009/000219 DK2009000219W WO2010040355A1 WO 2010040355 A1 WO2010040355 A1 WO 2010040355A1 DK 2009000219 W DK2009000219 W DK 2009000219W WO 2010040355 A1 WO2010040355 A1 WO 2010040355A1
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WO
WIPO (PCT)
Prior art keywords
oil
gas
compressor
liquid
crankcase
Prior art date
Application number
PCT/DK2009/000219
Other languages
English (en)
French (fr)
Inventor
Per Skærbæk NIELSEN
Original Assignee
Cooling Consult
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Publication date
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First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=41261392&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO2010040355(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Cooling Consult filed Critical Cooling Consult
Priority to EP09736805A priority Critical patent/EP2344766A1/en
Publication of WO2010040355A1 publication Critical patent/WO2010040355A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B43/00Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • F25B43/02Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for separating lubricants from the refrigerant
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/04Measures to avoid lubricant contaminating the pumped fluid
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/16Filtration; Moisture separation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B31/00Compressor arrangements
    • F25B31/002Lubrication

Definitions

  • the invention relates to a piston compressor for a cooling system, a liquid separating kit for retrofitting on a piston compressor and use of such a kit.
  • piston compressors used in industrial cooling systems comprises a pressure equalization connection between the crankcase of the compressor and the suction side of the compressor.
  • This pressure equalization connection serves two purposes.
  • One purpose of the pressure equalization connection is to equalize the pressure in the crankcase to the suction side of the compressor by allowing gas from the crankcase to flow to the suction side of the compressor.
  • the other purpose of the pressure equalization connection is to prevent liquid hammer by acting as a drain channel between the suction side of the compressor and the crankcase.
  • liquid refrigerant and oil which may be carried along with the refrigerant gas from the low pressure side of the cooling system and may result in a liquid hammer, is drained through the pressure equalization channel to the crankcase of the piston compressor.
  • the oil and fluid refrigerant which is transported along with the suction gas against the compressor will hereby be mixed with the oil in the oil sump in the crankcase where most of the content of refrigerant will decoct and evaporate due to the high temperature in the crankcase.
  • the evaporated refrigerant will flow through the equalization connection to the suction side of the compressor.
  • hermetic compressors mainly used in commercial cooling systems, often leads the suction gas through the electric motor which hereby gets cooled. At the same time, refrigeration fluid carried along with the suction gas will evaporate due to the heat in the electric motor. Oil carried along with the suction gas is separated and lead to the crankcase of the compressor, which often has a connection to the bottom part of the electric motor.
  • DE 1978048, DE 4214324 and DE 19628812 relates to separation of oil from gasses from a crankcase of a combustion engine to avoid pollution due to combustion of the oil. The oil separated is led back to the oil sump of the crankcase of the combustion engine.
  • oil that unintentionally enters the compression chamber of the compressor will, due to the following compression, be heated before it leaves the compressor together with the pressure gas.
  • the high temperature entails that a part of the oil evaporates and cannot subsequently be extracted from the refrigeration gas by a traditional oil separator on the pressure side of the compressor, and will therefore continue to flow as a gas into the cooling system. Therefore, it is especially advantageous that the oil carried by the gas flow from the pressure equalization connection is separated from the gas before the oil enters the compression chamber from the suction side.
  • the invention therefore relates to a piston compressor for a cooling system, the piston compressor having a crankcase with an oil sump, wherein said crankcase is connected to the suction side of said compressor by means of a pressure equalization connection, wherein the compressor comprises a liquid separator for separating oil from at least a part of a gas flow prior to entering a compression chamber of the compressor from the suction side of the compressor, wherein the liquid separator comprises at least one gas inlet and an oil outlet for the separated oil, which oil outlet is configured for discharging said separated oil into said oil sump, and wherein the liquid separator is arranged so that gas passing from the crankcase through said pressure equalization connection enters the gas inlet of said liquid separator during normal operation of the compressor.
  • the liquid separator is arranged at the suction side of the cooling compressor, it facilitates separation of liquid at a considerably lower pressure and/or temperature than if it is was arranged to separate liquid at the pressure side of the compressor. Separating the liquid at the pressure side of the compressor would increase the costs and demands to the liquid separator significantly.
  • the oil outlet discharges the oil directly to the oil sump, but I other aspects of the invention the oil may be led to a pre-chamber or the like before it is led to the oil sump.
  • the liquid separator is arranged to separate the oil from the gas from the crankcase before the gas enters from the pressure equalization connection to the suction side of the compressor during normal operational conditions.
  • the liquid separator may be arranged substantially at the suction side of the compressor to separate the oil in the gas from the pressure equalization connection.
  • the oil outlet is arranged to discharge said separated oil underneath the oil surface level of said oil sump during normal operational conditions.
  • the oil sump hereby constitutes a liquid plug preventing gas from the crankcase from being sucked from the crankcase through the oil outlet into the liquid separator.
  • one or more of the gas inlets of the liquid separator may be utilized as an oil outlet for the separated oil and is not arranged to discharge said separated oil underneath the oil surface level of the oil sump during normal operational conditions.
  • the oil outlet and the gas inlet(s) are separately arranged to prevent gas and oil flowing in opposite directions which in some cases may prevent the separated oil from draining back to the oil sump.
  • the piston compressor comprises a drain connection for draining liquid from the suction side of the compressor to the crankcase.
  • Oil, and in some cases refrigerant dissolved in the oil or not evaporated in an evaporator of a cooling system is known to be carried around in the compressor- system and result in various disadvantages in cooling compressors.
  • the oil and/or refrigerant which may accumulate in the cooling system can be led to the oil sump and it is thereby avoided that the oil is led from the suction side of the compressor, back into the cooling system, furthermore, liquid hammer which may damage the cooling compressor can be avoided.
  • the pressure equalization connection is further configured to be utilized as said drain connection for draining liquid from the suction side of said compressor.
  • the oil and liquid refrigerant accumulated in the cooling system may hereby run through the pressure equalization connection, through the liquid separator (if arranged at the inlet if the pressure equalization connection or between the inlet and outlet of the pressure equalization connection) and into the outlet of the liquid separator to the oil sump.
  • the pressure equalization connection both facilitates drainage of the liquid from the suction side of the compressor, and pressure equalization from the crankcase to the suction side of the compressor.
  • said drain connection is a drain connection being arranged separately from the pressure equalization connection, said separately arranged drain connection having an outlet arranged to discharge said liquid underneath the oil surface level of said oil sump during normal operational conditions.
  • the oil -inlet of the separately arranged drain connection is arranged at the suction side of the compressor before the gas outlet of the pressure equalization channel, to achieve that the oil carried around in the system is let back to the oil-sump before it reaches the pressure equalization channel.
  • the gas-outlet of the pressure equalization connection may be arranged above the oil- outlet of the separately arranged drain connection, at the suction side of the compressor.
  • the separately arranged drain connection may comprise an on-way valve to avoid oil and/or gas to enters the separately arranged drain connection from the crankcase. This may for example be advantageous if the outlet of the separately arranged drain connection is not arranged to discharge said liquid underneath the oil surface level of the oil sump during normal operational conditions.
  • a one-way valve may act as a safety precaution if the pressure in the crankcase unintentionally rises to an amount which results in that oil from the oil sump could be pressed from the crankcase, through the separately arranged drain connection to the suction side of the compressor.
  • the one-way valve may hereby prevent this flow due to that the one-way valve permits a flow from the suction side of the compressor towards the crankcase, but prevents a liquid flow from the crankcase towards the suction side of the compressor.
  • said liquid separator comprises a sedimentation separator for separating said oil from said gas.
  • Sedimentation separation is an advantageous and efficient way of separating oil droplets from the gas.
  • Sedimentation separation utilizes the difference in density, in this case the difference in density between gas and oil mist in the gas. Due to the larger density of the oil in relation to the gas, the oil will settle faster than the gas due to the action of a force, such as gravity.
  • the gravitational driven sedimentation separation is for some applications a relatively space consuming separation process requiring either a long distance over which the sedimentation from the flowing fluid occurs or a wide space where the flow velocity is lowered sufficiently to allow sedimentation.
  • An alterative force to be used for sedimentation separation is a centrifugal force applied in a cyclone separator, where the magnitude of the force may be increased as compared to gravitational sedimentation, so that the space requirements can be reduced.
  • Sedimentation separation is especially advantageous for separating small oil droplets of the oil mist in the gas, rather than impingement separation which has the largest effect on larger oil droplets in the oil mist.
  • the sedimentation separator is designed to utilise centrifugal separation to separate said oil from said gas. This may be advantageous in that centrifugal separation is an efficient and well-tested way of separating liquid from gas.
  • the sedimentation separator is designed to utilise gravitational separation to separate said oil from said gas.
  • Gravitational separation is advantageous in that it may be a cost efficient solution. Furthermore gravitational separation may be especially advantageous in embodiments where the liquid separator is arranged inside the crankcase since it is reliable solution which works during the demanding environment in the crankcase. Furthermore, a sedimentation separator utilizing gravitational separation may be advantageous in that it facilitates a low pressure loss in the liquid separator.
  • the sedimentation separator during normal operation of the compressor separates at least 30%, preferably at least 50% of the liquid oil in the gas passing the pressure equalization connection.
  • the sedimentation separator comprises a housing enclosing a liquid separation chamber for separating said oil from said gas, the gas being led from said gas inlet through the liquid separation chamber to a gas outlet.
  • the liquid separator is arranged inside said crankcase, where a gas outlet of the liquid separator is connected to a gas inlet of the pressure equalization connection.
  • said liquid separator is arranged outside said crankcase between a gas inlet and a gas outlet of said pressure equalization connection.
  • the liquid separator may be arranged at any suitable location between the gas inlet and the gas outlet of the pressure equalization connection.
  • the liquid separator maybe arranged substantially at the gas inlet of the pressure equalization connection, substantially at the gas outlet of the pressure equalization connection, or somewhere between the gas inlet and the gas outlet of the pressure equalization connection.
  • said liquid separator comprises at least one impingement separation part.
  • Impingement separation relates to a method of separation which utilizes the difference in inertia of the gas and the oil mist in the gas.
  • the gas is due to its lower inertia capable of changing its direction of motion more abruptly than the oil droplets of the mist.
  • the inertia of the oil droplets causes them to collide with the collectors to which they become attached.
  • the impingement separating part may e.g. comprise a plurality of collectors arranged to intercept oil in the flow of gas in the pressure equalization connection, it may comprise a sudden bend, the bend making oil droplets of the gas strike the wall of the pipe due to the larger inertia of the oil droplets, while the gas continues at the direction of the flow, or the like.
  • the impingement separation part is arranged before the liquid separation chamber of the liquid separator, e.g. substantially at the gas inlet(s) of the liquid separator.
  • the pressure difference between the crankcase and the suction side of the compressor is less than 5000 Pa such as less than 3000 Pa during normal operation of the cooling compressor.
  • the pressure difference between the crankcase and the suction side of the compressor during normal operation has a magnitude allowing a flow of pressure equalizing gas from the crankcase to the suction side of the compressor, and at the same time allows drainage of liquid refrigerant and oil from the suction side of the compressor to the oil sump in the crankcase.
  • the compressor comprises a separately arranged drain channel, it is advantageous to have a low pressure difference between the crankcase and the suction side of the compressor, so that oil from the oil sump is not forced by the pressure in the crank case through the separately arranged drain channel into the suction side of the compressor.
  • the invention also relates to a liquid separating kit for retrofitting on a piston compressor of a cooling system, which piston compressor comprises a crankcase with an oil sump, which crankcase is connected to the suction side of said compressor by means of a pressure equalization connection, wherein said liquid separating kit is configured to be arranged to separate oil from at least a part of a gas flow prior to entering a compression chamber of the compressor from the suction side of the compressor, and wherein the liquid separating kit comprises at least one gas-inlet for receiving gas from said crankcase, a liquid separator for separating oil from the gas received from said gas-inlet, an oil outlet for oil separated by means of said liquid separator, and a gas-outlet for discharging gas from said liquid separator after the liquid separator during normal operation has separated said oil from said gas.
  • the liquid separator may be advantageously be retrofitted to existing cooling compressors at the suction side of the compressor.
  • the kit may be fitted to a new cooling compressor without having to make significant structural changes of the design of the cooling compressor.
  • said oil outlet comprises a drain channel part enabling said separated oil to be discharged underneath the oil surface level of said oil sump during normal operational conditions.
  • the drain channel part preferably comprises a pipe connection having an outlet underneath the oil surface level of the oil sump.
  • the gas inlet(s) may be utilized as an oil outlet.
  • said liquid separator comprises a sedimentation separator for separating said oil from said gas.
  • the sedimentation separator comprises a housing enclosing a liquid separation chamber for separating said oil from said gas, the gas being led from said gas inlet through the liquid separation chamber to the gas outlet of the liquid separator during normal operation.
  • said sedimentation separator is designed to utilise centrifugal separation to separate said oil from said gas.
  • said gas-outlet is further configured to be utilized as a part of a drain connection for draining liquid from the suction side of said compressor.
  • the kit is configured to be arranged inside said crankcase, and the gas outlet is configured to be connected to a gas inlet of the pressure equalization connection.
  • the kit is configured to be arranged outside said crankcase between a gas inlet and a gas outlet of said pressure equalization connection.
  • said liquid separator comprises at least one impingement separation part.
  • the invention furthermore relates to use of a liquid separating kit according to any of claims 16-24 for retrofitting to a piston compressor having a crankcase with an oil sump, which crankcase is connected to the suction side of said compressor by means of a pressure equalization connection.
  • the invention relates to use of a liquid separating kit according to claim 25, wherein said kit is arranged so to separate the oil from the gas from the crankcase before the gas enters the suction side of the compressor.
  • fig. 1 illustrates an embodiment of a piston compressor comprising a liquid separator according to the invention, where the liquid separator is arranged inside the crankcase of the piston compressor,
  • fig. Ia illustrates an example of a liquid separator for arranging inside the crankcase of the cooling compressor.
  • fig. Ib illustrates an embodiment of the invention, wherein gas-inlets of the liquid separator are utilized as oil-outlets.
  • fig. 2 illustrates an embodiment of a piston compressor comprising a liquid separator according to the invention, where the liquid separator is arranged external to the crankcase of the compressor fig. 3 illustrates an embodiment of the invention wherein the compressor comprises a separately arranged drain connection.
  • fig. 4 illustrates an embodiment of the invention wherein oil from the pressure equalization gas is separated after the gas from the pressure equalization connection has entered the suction side of the compressor
  • fig. 5 illustrates another embodiment of the invention wherein oil from the pressure equalization gas is separated after the gas from the pressure equalization connection has entered the suction side of the compressor, and
  • fig. 6 illustrates an embodiment of the invention wherein the liquid-outlet of a separately arranged drain connection is connected to an oil-outlet of the liquid separator.
  • Fig 1 illustrates a cooling compressor for cooling systems according to the invention.
  • the cooling compressor which is a piston compressor, comprises a crankcase 8, comprising an oil-sump 5 with oil for lubricating movable parts of the compressor.
  • the piston compressor comprises a compression chamber 19 for compressing the gas from the suction side 9 of the compressor.
  • the cooling compressor furthermore comprises a pressure equalization connection 1 comprising a gas inlet 13 and a gas outlet 14, where the pressure equalization connection 1 connects the crankcase 8 to the suction side 9 of the compressor.
  • the cooling compressor comprises a liquid separator 11, in the embodiment of fig. 1 arranged inside the crankcase 8, for separating oil from the gas in/from the pressure equalization connection 1.
  • the liquid separator 11 may be arranged outside the crankcase between the gas-inlet 13 and the gas-outlet 14 of the pressure equalization connection, or at the suction side 9 of the compressor as explained later on with reference to figs. 2 and 6.
  • the liquid separator 11 comprises at least one gas inlet 2 for receiving gas from the crankcase 8.
  • the liquid separator 11 is illustrated with two gas inlets 11 , but it is understood that the liquid separator in other embodiments may comprise one, three, four or even more gas inlets 2.
  • the liquid separator comprises a gas-outlet 12 for discharging gas from the liquid separator 11 after the liquid separator 11 has separated the oil mist from the gas received from the crankcase 8.
  • the liquid separator 11 comprises an oil-outlet 4 for the separated oil, preferably arranged at the bottom of the housing 15 of the liquid separator 11.
  • the oil outlet 4 is preferably as illustrated in fig. 1 arranged to discharge the separated oil into the oil sump 5 below the surface level of the oil in the oil sump 5, so as to prevent a couterflow of gas through the oil outlet 4.
  • liquid separator 11 may be arranged at the cooling compressor during manufacturing of the compressor, or it may be retrofitted to an existing cooling compressor e.g. as liquid separating kit for retrofitting.
  • the liquid separator 11 is arranged to separate the oil from the gas from the crankcase 8 before the gas enters the suction side (9) of the compressor.
  • the liquid separator 11 is arranged inside the crankcase 8 so that the gas outlet 12 of the liquid separator 11 is connected to the inlet 13 of the pressure equalization connection 1.
  • the oil outlet 4 comprises a piping leading the separated oil from the liquid separator 11 to be discharged underneath the surface level of the oil sump 5.
  • the housing of the liquid separator 11 may instead comprise a bottom part being a part adapted to be arranged underneath the oil surface level of the oil sump 5 so that a liquid plug is created.
  • the separation of oil droplets from the gas by means of the liquid separator 11 may in general be achieved in different ways.
  • the liquid separator 11 comprises a sedimentation separator as explained earlier, for separating the oil from the gas.
  • a sedimentation separator may be a separator designed to utilize centrifugal separation (not illustrated in any figures) to separate the oil from the gas, preferably by means of a cyclone separator.
  • a cyclone separator utilizing centrifugal separation is described in the following.
  • the gas from the crankcase 8 may be let into a gas inlet 2 in the top part of a cyclone separator, where the gas inlet 2 is located tangentially to the cylindrical portion of the cyclone separator.
  • the gas containing the oil droplets then moves downward in a whirling motion forming a peripheral vortex giving rise to centrifugal forces.
  • centrifugal forces results in that the oil droplets in the gas is thrown against the walls of the separator.
  • the oil hereby runs down the inner walls of the cyclone separator and out of the oil outlet 4.
  • the gas changes direction to an upward flow after reaching the end of a conical portion of the cyclone separator, and moves towards the gas outlet 12, forming an inner vortex, hi this movement of gases, more oil droplets may be separated and let into the oil outlet 4 due to gravity.
  • the preferred liquid separator is a gravitational sedimentation separator 11 as illustrated in the figures.
  • the gravitational separator is a liquid separator 11 configured for utilizing the gravitational force for separating the oil droplets from the gas.
  • Such a gravitational separator preferably comprises a housing 15 enclosing one or more liquid separation chambers 3 for separating the oil from the gas. hi this configuration, the gas is led from the gas inlet(s) 2 through the liquid separation chamber 3 to the gas outlet 12, and the separation chamber 3 is preferably designed to facilitate a low gas flow velocity during normal operation of the compressor.
  • the velocity of the gas flow in a sedimentation separator utilizing gravitational forces is less than 5 m/s, preferably less than 3 m/s during normal operation of the compressor, but it is understood that the velocity may of vary dependent of e.g. the compressor configuration the type and size of the liquid separator 11, the type of refrigerant, the temperature and pressure and the like.
  • the lower velocity may e.g. be achieved by increasing the flow cross section (e.g. by making a separation chamber larger than the outlet of the liquid separator 11) and/or by dividing the gas flow by means of two or more inlets, e.g. as illustrated in figs. 1 , Ia and Ib.
  • a sedimentation separation may also be achieved by extending the pressure equalization channel 1 so that the gas has to travel a longer horizontal distance to reach the suction side 9 of the compressor, giving the oil droplets in the gas a better opportunity to settle in the pressure equalization channel 1 and run back to the oil sump 5 in the crankcase 8.
  • the pressure equalization channel 1 may at least partly act as the liquid separator 11.
  • the pressure equalization connection may comprise one or more impingement separation parts 6, e.g. sudden bends of at least 90° such as of at least 135° on the pressure equalization channel, to achieve impingement separation.
  • the pressure equalization connection 1 may also comprise one or more impingement separation parts 6, such as collectors arranged in an angle to the flow of the gas in the pressure equalization connection 1, e.g. a mesh.
  • the liquid separator 11 during normal operation separates at least 30%, such as at least 50%, preferably at least 80% of the liquid oil in the gas passing the pressure equalization connection 1 by means of impingement separation and/or sedimentation separation such as gravitational separation, before the gas enters the compression chamber of the compressor.
  • Fig. Ia illustrates an example of the liquid separator 11 illustrated in fig. 1, arranged inside the crankcase 8.
  • the liquid separator 11 in fig. Ia is sedimentation separator utilizing the gravitational force for separating the oil from the gas.
  • the liquid separator 11 comprises a housing 15 and two gas inlets 2 for receiving the gas from the crankcase 8.
  • the housing 15 helps to shield the separation chamber 3 from outside disturbances in the crankcase 8 so that the gas from the gas inlets 2 can settle in the separation chamber 3, helping the oil droplets in the gas to settle faster.
  • the sedimentation separator 11 may in a further embodiment of the invention comprise one or more impingement separation parts 6 assisting to separate especially larger droplets of oil from the gas and oil splash from the crankcase.
  • the impingement separation part(s) 6 may comprise one or more impingement elements, preferably one or more meshes, e.g. arranged at the gas inlet(s) 2, it may comprise one or more other filter elements, one or more plates arranged in an angle in relation to the gas flow or the like.
  • the liquid separator 11 in fig. 1 and Ia is especially advantageous in that it requires a minimum of structural changes of the cooling compressor in order to achieve the separation of liquid.
  • the gas outlet 12 of the liquid separator 11 is connected to the gas inlet 13 of the pressure equalization connection 1, and the outlet of the oil outlet 4 may as illustrated be arranged underneath the surface level of the oil sump 5.
  • liquid separator 11 may also in another embodiment be configured for utilizing impingement separation alone.
  • Fig. Ib illustrates another embodiment of the liquid separator 11 for arranging inside the crankcase 8, wherein the gas-inlet(s) 2 of the liquid separator 11 are further utilized as oil-outlets 4 for the oil separated by means of the liquid separator 11.
  • fig. Ib illustrates an embodiment wherein a part of the housing 15 of the liquid separation chamber 3 is arranged in an angle ⁇ in relation to horizontal.
  • This may be advantageous in that the separated liquid may be more effectively led back to the oil-sump 5 by means of the gas-inlet(s) 2, if the housing 15 is angled towards the oil sump 5.
  • it may be advantageous to arrange the housing 15 in an angle ⁇ in relation to horizontal (even towards the oil sump 5 as illustrated or away from the oil sump 5) due to the design of the crankcase 8.
  • the design of the crankcase may vary, and it may be possible to achieve a larger separation area 3 and/or a more space saving liquid separator 11 in the sideway direction, if the housing 15 is angled in relation to horizontal.
  • the liquid separator 11 comprises an oil-outlet 4, preferably at the lowest point of the bottom of the liquid separator 4.
  • the inlet(s) 2 of the liquid separator 11 is arranged at the location in the crankcase 8 which is identified to be exposed to the less amount of oil mist and/or oil splash caused due to e.g. the movement of the crank.
  • at least one gas-inlet 2 of the liquid separator 11 is arranged at a location in the crankcase 8 wherein the amount of oil mist and/or oil splash is identified to be at least 20% lower such as at least 40% lower, e.g. at least 60% lower than the amount of oil mist and/or oil splash at another location in the crankcase 8. This area may e.g.
  • FIG. 2 illustrates another embodiment of the invention wherein the liquid separator 11 which in this case is a gravitational sedimentation separator, is arranged to separate the oil from the gas from the crankcase 8 before the gas enters the suction side 9 of the compressor by means of the pressure equalization connection 1.
  • the liquid separator 11 is arranged external to the crankcase 8 between the gas inlet 13 and the gas outlet 14 of the pressure equalization connection 1.
  • the gas inlet 13 of the pressure equalization connection 1 is as illustrated connected to the gas inlet 2 of the liquid separator 11, for example by means of a pipe connection, and the gas outlet 12 of the liquid separator 11 is connected to the gas outlet 14 of the pressure equalization connection 1, also for example by means of a pipe connection.
  • the fluid separator 11 in fig. 2 further comprises an oil outlet 4 which discharges the separated oil into the oil sump 5 of the crankcase 8, in the illustrated example underneath the oil surface level of the oil sump 5.
  • the gas from the crankcase 8 is sucked into the inlet 13 of the pressure equalization connection 1, through the inlet 2 of the liquid separator 11 into the liquid separator 11 for separation of the oil from the gas.
  • the gas enters the gas outlet 12 of the liquid separator 11 and is discharged at the gas outlet 14 of the pressure equalization connection 1, to enter the suction side 9 of the compressor.
  • the gas-inlet 2 of the liquid separator 11 arranged external to the crankcase 8 may be utilized as oil outlet 4.
  • the liquid separator 11 may comprise one or more separation chambers 3, 7 for sedimentation separation of the oil from the gas.
  • the liquid separator 11 comprises a pre-chamber 7 performing a first sedimentation separation before the gas is let through an impingement separation part 6 to a second liquid separation chamber 3, and further into the gas outlet 12 of the liquid separator 11.
  • the pressure equalization connection 1 may in embodiments of the invention be arranged as a drain connection to drain oil and liquid refrigerant from the suction side 9 of the compressor to the oil sump 5.
  • the oil from the suction side 9 of the compressor may originate from oil unintentionally transported around in the cooling system, and the liquid refrigerant may e.g. originate from non-evaporated refrigerant from the evaporator.
  • the pressure difference between the crankcase 8 and the suction side 9 of the compressor, during normal operation of the compressor is large enough to allow a gas flow from the crankcase 8 to the suction side 9 of the compressor by means of the pressure equalization connection, and at the same time allow a flow of liquid from the suction side 9 to the crankcase 8 towards the gas flow from the crankcase 8.
  • the pressure difference is limited to the pressure of the oil column practically possible in the compressor construction.
  • the oil and liquid refrigerant may hereby be let through the gas-outlet 14 of the pressure equalization connection 1, against the flow direction of the pressure equalization gas from the crankcase 8, towards the gas inlet 13 of the pressure equalization connection 1.
  • the liquid separator 11 is arranged inside the crankcase 8 as illustrated in figs. 1, Ia and Ib or if it is arranged as illustrated in fig. 2 outside the crankcase 8 between the gas inlet 13 and the gas outlet 14 of the pressure equalization connection, the gas outlet 12 of the liquid separator 11 may be used as an inlet for the liquid oil/refrigerant, and the oil outlet 4 of the liquid separator 11 may be used as outlet for the oil and/or refrigerant liquid drained from the suction side of the compressor.
  • Fig. 3 illustrates an embodiment of the invention wherein the cooling compressor comprises a drain connection 16 separately arranged from the pressure equalization connection 1.
  • the separately arranged drain connection 16 is intended for draining oil and fluid refrigerant from the suction side 9 of the compressor to the crankcase 8, and comprises an liquid-inlet 17 connected to the suction side 9 of the compressor, and a liquid-outlet 18 arranged to discharge the liquid underneath the oil surface level of the oil sump 5.
  • the liquid separator 11 may be arranged to separate the oil from the gas from the crankcase 8, after the gas from the pressure equalization connection 1 enters the suction side 9 of the compressor.
  • Fig. 4 illustrates such an embodiment where the liquid separator 11 is arranged before the compression chamber 19 of the compressor, at the suction side 9 of the compressor.
  • the liquid separator 11 separates the oil droplets from the pressure equalization gas received from the pressure equalization connection 1.
  • the gas outlet 12 of the liquid separator 11 may release both the gas received from the suction side 9 of the compressor and the gas received from the pressure equalization connection 1.
  • the gas outlet 14 of the pressure equalization connection 1 is in the embodiment of fig. 4 arranged at the suction side 9 of the compressor before the gas- inlet 2 of the liquid separator 11.
  • Fig. 5 illustrates another embodiment of the invention wherein the liquid separator 11 is arranged at the suction side 9 of the compressor to separate the oil from the pressure equalization gas received from the pressure equalization connection 1.
  • the gas-outlet 14 of the pressure equalization connection 1 is connected directly to the liquid separator 11 and is mixed with the gas from the suction side 9 of the compressor, e.g. inside the liquid separator 11.
  • the liquid separator illustrated in fig. 5 may in an embodiment of the invention which is not illustrated in the figure comprise more than one separation chamber for separating the oil droplets from the gas.
  • the liquid separator 11 illustrated in fig. 5 may comprise one separation chamber for separating oil droplets from the gas received from the pressure equalization connection 1 and another chamber for receiving the gas from the suction side 9 of the compressor.
  • Fig. 6 illustrates a liquid separator 11 arranged to separate oil from the crankcase 8, where the liquid separator 11 is arranged external to the crankcase 8 as illustrated in fig. 2.
  • the cooling compressor comprises a separately arranged drain connection 16 comprising a liquid-inlet 17 and a liquid outlet 18.
  • the liquid-inlet 17 is in this embodiment connected to the suction side 9 of the compressor, and the liquid-outlet 18 is connected to the oil-outlet 4 of the liquid separator 11.
  • the separately arranged drain connection 16, where suitable may comprise a one-way valve (not illustrated in any figures) to avoid that oil and/or gas from the crankcase 8 enters the separately arranged drain connection 16.
  • the oil outlet 4 of the liquid separator 11 where suitable, may comprise a one-way valve (not illustrated in any figures) to prevent gas and/or oil from the crankcase 8 to enter the separately arranged drain connection 16.
  • the liquid separator 11 may be a part of a liquid separating kit comprising the above mentioned gas inlet(s) 2, gas outlet 12 and oil outlet(s) 4.
  • This liquid separating kit may e.g. be utilized for retrofitting a liquid separator 11 to existing cooling compressors, as described above in relation to the description of the figures.
  • Oil density foil 900 - - ⁇ r m
  • Oil surface tension ⁇ oil 0.030 — m
  • the Froude number should be larger than one (worse case scenario):
  • the 90% is a safety factor to assure advantageous liquid separation.
  • Maximum speed in the separation chamber 3 is the one that holds the flow in the separation zone for at least the droplet fall time (substantially horizontal flow):
  • the Froude number above is chosen to be one so that substantially all oil mist would be carried along, including oil adhering to the inside of the pressure equalization connection 1. hi practice, oil will be carried along by the flow at much lower Froude numbers. Therefore, the performance factor by utilizing the liquid separator 11 in practice would be significantly larger.
  • the parameters in the calculation example above may vary dependent of e.g. the type of liquid separator 11, the location of the liquid separator 11, the dimension of the gas-inlet 13, the dimensions of the liquid separator 11, the type of refrigerant and the like.
  • Liquid-inlet of separately arranged drain connection 17.
  • Liquid-outlet of separately arranged drain connection 19.
  • Compression chamber of piston compressor 19.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Power Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Compressor (AREA)
  • Cyclones (AREA)
PCT/DK2009/000219 2008-10-10 2009-10-12 Cooling compressor with system for reducing oil outflow WO2010040355A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP09736805A EP2344766A1 (en) 2008-10-10 2009-10-12 Cooling compressor with system for reducing oil outflow

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DKPA200801425 2008-10-10
DKPA200801425A DK177037B1 (da) 2008-10-10 2008-10-10 Kølekompressor med system til minimering af olieudkast

Publications (1)

Publication Number Publication Date
WO2010040355A1 true WO2010040355A1 (en) 2010-04-15

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PCT/DK2009/000219 WO2010040355A1 (en) 2008-10-10 2009-10-12 Cooling compressor with system for reducing oil outflow

Country Status (3)

Country Link
EP (1) EP2344766A1 (da)
DK (1) DK177037B1 (da)
WO (1) WO2010040355A1 (da)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2538157A2 (de) 2011-06-24 2012-12-26 Viessmann Werke GmbH & Co. KG Periodisch arbeitende Sorptionsvorrichtung
WO2020072083A1 (en) * 2018-10-02 2020-04-09 Vilter Manufacturing Llc 3d-printed oil separation for reciprocating compressors
US11859603B2 (en) 2018-10-02 2024-01-02 Copeland Industrial Lp 3D-printed oil separation for reciprocating compressors

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE696906C (de) * 1938-09-03 1951-08-16 Willy Hirche Kompressionskaeltemaschine
JPH07146035A (ja) * 1993-11-19 1995-06-06 Mitsubishi Electric Corp 油分離装置
DE19525461A1 (de) * 1995-07-14 1997-01-16 Knorr Bremse Systeme Kolbenkompressor

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2233168A (en) 1939-04-19 1941-02-25 Gen Electric Compressor

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE696906C (de) * 1938-09-03 1951-08-16 Willy Hirche Kompressionskaeltemaschine
JPH07146035A (ja) * 1993-11-19 1995-06-06 Mitsubishi Electric Corp 油分離装置
DE19525461A1 (de) * 1995-07-14 1997-01-16 Knorr Bremse Systeme Kolbenkompressor

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP2344766A1 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2538157A2 (de) 2011-06-24 2012-12-26 Viessmann Werke GmbH & Co. KG Periodisch arbeitende Sorptionsvorrichtung
DE102011105742A1 (de) 2011-06-24 2012-12-27 Viessmann Werke Gmbh & Co Kg Periodisch arbeitende Sorptionsvorrichtung
WO2020072083A1 (en) * 2018-10-02 2020-04-09 Vilter Manufacturing Llc 3d-printed oil separation for reciprocating compressors
US11859603B2 (en) 2018-10-02 2024-01-02 Copeland Industrial Lp 3D-printed oil separation for reciprocating compressors

Also Published As

Publication number Publication date
DK200801425A (da) 2009-10-15
DK177037B1 (da) 2011-02-21
EP2344766A1 (en) 2011-07-20

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