US20100251750A1 - Economized refrigerant system with flow control - Google Patents

Economized refrigerant system with flow control Download PDF

Info

Publication number
US20100251750A1
US20100251750A1 US12/599,888 US59988807A US2010251750A1 US 20100251750 A1 US20100251750 A1 US 20100251750A1 US 59988807 A US59988807 A US 59988807A US 2010251750 A1 US2010251750 A1 US 2010251750A1
Authority
US
United States
Prior art keywords
refrigerant
economizer
flow
line
recited
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US12/599,888
Inventor
Alexander Lifson
Michael F. Taras
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Carrier Corp
Original Assignee
Carrier Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Carrier Corp filed Critical Carrier Corp
Assigned to CARRIER CORPORATION reassignment CARRIER CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: LIFSON, ALEXANDER, TARAS, MICHAEL F.
Publication of US20100251750A1 publication Critical patent/US20100251750A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • F25B1/10Compression machines, plants or systems with non-reversible cycle with multi-stage compression
    • 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
    • F25B2400/00General 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
    • F25B2400/13Economisers
    • 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
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2509Economiser valves
    • 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
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2513Expansion valves

Definitions

  • This invention relates generally to refrigerant vapor compression systems and, more particularly, to refrigerant vapor compression systems equipped with an economizer cycle.
  • Refrigerant vapor compression systems are well known in the art and commonly used for conditioning air (or other secondary media) to be supplied to a climate-controlled comfort zone within a residence, office building, hospital, school, restaurant or other facility.
  • Refrigerant vapor compression systems are also commonly used in transport refrigeration for refrigerating air supplied to a temperature-controlled cargo space of a truck, trailer, container or the like for transporting perishable items, and in commercial refrigeration for cooling air supplied to a temperature-controlled space in a cold room, a beverage cooler, a diary case or a refrigerated merchandiser for displaying perishable foods item in a chilled or frozen state, as appropriate.
  • these refrigerant vapor compression systems include: a compressor, a condenser, an evaporator; and an expansion device.
  • the expansion device typically a fixed orifice, a capillary tube, a thermostatic expansion valve (TXV) or an electronic expansion valve (EXV), is disposed in the refrigerant line upstream, with respect to refrigerant flow, of the evaporator and downstream of the condenser.
  • TXV thermostatic expansion valve
  • EXV electronic expansion valve
  • the economizer heat exchanger is generally disposed hi the refrigerant circuit intermediate the condenser and the evaporator. In operation, a portion of the refrigerant leaving the condenser is diverted from the primary refrigerant circuit, expanded to an intermediate pressure and then passed through the economizer heat exchanger in heat exchange relationship with the main portion of the refrigerant leaving the condenser.
  • any liquid in the economized expanded refrigerant flow is evaporated, and then the evaporated refrigerant is typically superheated, while the refrigerant passing through the primary refrigerant circuit from the condenser to the evaporator is further cooled.
  • the expanded refrigerant vapor is injected into an intermediate stage in the compression process, either through an injection port or ports opening into an intermediate pressure stage of the compression chamber (or chambers) of a single compressor or, in the case of a multiple compressor system, into a refrigerant line extending between the discharge outlet of the upstream compressor and the suction inlet of the downstream compressor.
  • U.S. Pat. No. 6,571,576 discloses a refrigerant vapor compression system operating in a subcritical cycle and equipped with an economizer heat exchanger, wherein vapor refrigerant and liquid refrigerant are returned to, an intermediate stage of the compression process through one or more economizer injection ports opening into the compression chambers of a scroll compressor.
  • a portion of liquid refrigerant is taken from the primary refrigerant circuit at a location downstream of the condenser, expanded to an intermediate pressure and lower temperature by means of an expansion device, such as a valve, to form a refrigerant liquid/vapor mixture which is thereafter passed through the economizer heat exchanger in heat exchange relationship with the main flow of refrigerant liquid.
  • this refrigerant liquid/vapor mixture extracts heat from the main flow of refrigerant liquid, further cooling this liquid, thereby evaporating any remaining liquid component in the two-phase mixture and typically further heating the vapor.
  • the refrigerant vapor leaving the economizer heat exchanger is then injected into the compressor through the economizer injection ports at the intermediate (between suction and discharge) pressure. Additionally, liquid refrigerant is selectively taken from the refrigerant circuit at a location downstream of the condenser and mixed into the refrigerant vapor being passed from the economizer to the compressor and injected into an intermediate pressure stage of the compression chambers of the scroll compressor together with the refrigerant vapor through the same economizer injection ports.
  • U.S. Pat. No. 7,114,349 discloses a refrigerant vapor compression system with a refrigerant-to-refrigerant heat exchanger interdisposed in the refrigerant circuit downstream of the condenser, with respect to refrigerant flow, and upstream of the evaporator, with respect to refrigerant flow.
  • the common heat exchanger may be operated either as an economizer heat exchanger or as a liquid-suction heat exchanger.
  • refrigerant is passed from the primary refrigerant circuit through an economizer expansion device and thence through the refrigerant-to-refrigerant heat exchanger in heat exchange relationship with the remainder of the refrigerant passing through the primary refrigerant circuit from the condenser to the evaporator.
  • the expanded refrigerant is injected into an intermediate pressure stage of the compressor or returned to the primary refrigerant circuit at a point downstream, with respect to refrigerant flow, of the evaporator and upstream of the suction inlet of the compressor.
  • U.S. Pat. No. 6,058,729 discloses a subcritical refrigerant vapor compression system for a transport refrigeration unit incorporating a refrigerant-to-refrigerant heat exchanger into the refrigerant circuit as an economizer.
  • the disclosed system also includes a suction modulation valve (SMV) for throttling refrigerant flow to the suction inlet of the compressor and an intermediate pressure-to-suction pressure unload circuit for compressor capacity control.
  • SMV suction modulation valve
  • the refrigerant vapor compression system of the invention includes a primary refrigerant circuit, an economizer circuit, a bypass line, a bypass flow control device, and an economizer/compressor unload flow control apparatus.
  • the primary refrigerant circuit includes a refrigerant compression device, a refrigerant heat rejection heat exchanger, a refrigerant heat absorption heat exchanger, and a primary expansion device interdisposed in the primary refrigerant circuit downstream of the refrigerant heat rejection heat exchanger and upstream of the refrigerant heat absorption heat exchanger.
  • the economizer circuit includes an economizer refrigerant line extending in refrigerant flow communication between the economizer and an intermediate pressure stage of the compression device.
  • a bypass line extends in refrigerant flow communication from the economizer refrigerant line to the primary refrigerant circuit at a location downstream, with respect to refrigerant flow, of the refrigerant heat absorption heat exchanger.
  • a bypass flow control device is disposed in the bypass line.
  • the bypass flow control device has a first open position whereat refrigerant may flow through the bypass line and a second closed position whereat refrigerant is blocked from flowing through the bypass line.
  • the bypass flow control device may comprise a solenoid valve having a first open position and a second closed position.
  • a flow control apparatus disposed in the economizer refrigerant line provides a first flow path through the economizer refrigerant line in a first direction from the intermediate pressure stage of the compression device to the bypass line and a second flow path through the economizer refrigerant line in a second direction from the economizer into the intermediate pressure stage of the compression device.
  • the first flow path has a first hydraulic resistance to refrigerant flow through the first flow path and the second flow path has a second hydraulic resistance to refrigerant flow through the second flow path, the first hydraulic resistance being different from the second hydraulic resistance.
  • the first hydraulic resistance is relatively lower and the second hydraulic resistance is relatively higher.
  • flow control apparatus comprises a “fluid diode” device interdisposed in the economizer refrigerant line at a location intermediate the intermediate pressure stage of the compression device and the bypass line.
  • the “fluid diode” device has different flow resistance depending on the direction of the flow through the “fluid diode”.
  • a check valve with two position openings is one embodiment of such a “fluid diode” device. The check valve is used to illustrate this embodiment; however, other types of “fluid diodes” known in the art would fall within the scope of this invention.
  • the check valve has a first position wherein refrigerant may flow therethrough in a first direction from the intermediate pressure stage of the compression device to the bypass line and a second flow path through the economizer refrigerant line in a second direction from the second refrigerant pass of the refrigerant-to-refrigerant heat exchanger into the intermediate pressure stage of the compression device.
  • the flow control apparatus comprises a first branch refrigerant line in refrigerant flow communication with the economizer refrigerant line, a second branch refrigerant line in refrigerant flow communication with the economizer refrigerant line and disposed in parallel with the first branch refrigerant line, and a check valve disposed in the first branch refrigerant line and having a first position wherein refrigerant may flow through the first branch refrigerant line and a second position wherein refrigerant flow through the first branch refrigerant line is blocked and refrigerant may flow through the second branch refrigerant line.
  • the economizer may be a heat exchanger economizer or a flash tank economizer.
  • the economizer comprises a refrigerant-to-refrigerant heat exchanger including a first refrigerant pass and a second refrigerant pass disposed in heat exchange relationship with said first refrigerant pass.
  • the first refrigerant pass interdisposed in the primary refrigerant circuit and the second refrigerant pass interdisposed in the economizer refrigerant line.
  • the economizer refrigerant line extends in fluid communication from the primary refrigerant circuit through the second refrigerant pass to an intermediate pressure stage of the compression device.
  • an economizer expansion device is interdisposed in the economizer refrigerant line upstream with respect to refrigerant flow of the second refrigerant pass of the refrigerant-to-refrigerant heat exchanger.
  • the invention may be equally applied to flash tank type economized systems.
  • the control of the bypass flow and economizer vapor flow is accomplished in a similar fashion by controlling flow through the refrigerant economizer line.
  • the flash tank economizer is interdisposed in the primary refrigerant circuit downstream, with respect to refrigerant flow, of the refrigerant heat rejection heat exchanger and upstream, with respect to refrigerant flow, of the primary expansion device.
  • the economizer refrigerant line extends in refrigerant vapor flow communication from the flash tank economizer to an intermediate pressure stage of the compression device and an economizer expansion device is interdisposed in the primary refrigerant circuit upstream with respect to refrigerant flow of the flash tank economizer.
  • FIG. 1 is a schematic diagram illustrating an exemplary embodiment of a refrigerant vapor compression system in accord with the invention.
  • FIG. 2 is a schematic diagram illustrating another exemplary embodiment of a refrigerant vapor compression system in accord with the invention.
  • the refrigerant vapor compression system 20 includes a compression device 22 , a heat rejection heat exchanger 24 , an evaporator expansion device 26 , and an evaporator 28 , interconnected by various refrigerant lines 3 , 5 and 7 in serial refrigerant flow communication in a conventional refrigeration cycle in a primary refrigerant circuit.
  • the refrigerant vapor compression system 20 is suitable for use in a transport refrigeration system for refrigerating the air or other gaseous atmosphere within the temperature-controlled cargo space of a truck, trailer, container or the like for transporting perishable/frozen goods.
  • the refrigerant vapor compression system 20 is also suitable for use in conditioning air to be supplied to a climate-controlled comfort zone within a residence, office building, hospital, school, restaurant or other facility.
  • the refrigerant vapor compression system 20 could also be employed in refrigerating air supplied to display cases, merchandisers, freezer cabinets, cold rooms or other perishable/frozen product storage areas in commercial establishments.
  • the compression device 22 may comprise a single refrigerant compressor having at least a first compression stage and a second compression stage, such as, for example, a scroll compressor, such as illustrated in FIG. 1 , or a screw compressor having staged compression pockets, or a reciprocating compressor having at least a first bank and a second bank of cylinders, or a pair of compressors 22 A and 228 connected in series refrigerant flow relationship as illustrated in FIG. 2 , such as, for example, a pair of scroll compressors, screw compressors, centrifugal compressors, reciprocating compressors (or separate cylinders of a single reciprocating compressor) or rotary compressors, with the discharge outlet port of the upstream compressor connected in serial refrigerant flow communication with the suction inlet port of the downstream compressor.
  • a single refrigerant compressor having at least a first compression stage and a second compression stage
  • a scroll compressor such as illustrated in FIG. 1
  • a reciprocating compressor having at least a first bank and
  • refrigerant vapor is compressed from a suction pressure at which the refrigerant vapor enters the suction inlet port of the compression device 22 to a discharge pressure, substantially higher than the suction pressure.
  • the hot, high pressure refrigerant vapor passes from the discharge outlet port of the compression device 22 through refrigerant fine 3 of the primary refrigerant circuit to and through the heat rejection heat exchanger 24 .
  • the hot, high pressure refrigerant passes in heat exchange relationship with a cooling medium to cool and, in a subcritical cycle, condense the refrigerant vapor.
  • the heat rejection heat exchanger 24 may comprise, for example, a finned tube heat exchanger, such as for example a plate fin and round tube heat exchanger or a fin and minichannel flat tube heat exchanger, wherein the refrigerant passes through the heat exchanger tubes in heat exchange relationship with ambient (typically outdoor) air being drawn through the finned tube heat exchanger by an air mover, such as one or more fans (not shown) operatively associated with the heat rejection heat exchanger 24 .
  • a finned tube heat exchanger such as for example a plate fin and round tube heat exchanger or a fin and minichannel flat tube heat exchanger, wherein the refrigerant passes through the heat exchanger tubes in heat exchange relationship with ambient (typically outdoor) air being drawn through the finned tube heat exchanger by an air mover, such as one or more fans (not shown) operatively associated with the heat rejection heat exchanger 24 .
  • the refrigerant leaving the heat rejection heat exchanger 24 passes through refrigerant line 5 of the primary refrigerant circuit to the evaporator 28 .
  • the refrigerant traverses the evaporator expansion device 26 interdisposed in refrigerant line 5 and expands to a lower temperature, lower pressure liquid refrigerant or more commonly a liquid/vapor refrigerant mixture, before entering the evaporator 28 .
  • the evaporator expansion device 26 may be a restriction type expansion device, such as a capillary tube or a fixed plate orifice, a thermostatic expansion valve or an electronic expansion valve.
  • the evaporator 28 constitutes a refrigerant heat absorbing heat exchanger through which the liquid or liquid/vapor refrigerant mixture passes in heat exchange relationship with a secondary fluid to be cooled, and typically dehumidified, and delivered to a conditioned environment.
  • the refrigerant is heated thereby evaporating the liquid component and typically superheating the resultant vapor.
  • the secondary fluid typically air to be supplied to a climate-controlled environment, in the conditioned, cooled and typically dehumidified, state.
  • the evaporator 28 may comprise a finned tube heat exchanger through which refrigerant passes in heat exchange relationship with air that may be drawn from and returned to a climate-controlled environment by the one or more fans (not shown) operatively associated with the evaporator 28 .
  • the finned tube heat exchanger may comprise, for example, a plate fin and round tube heat exchanger or a fin and minichannel flat tube heat exchanger.
  • the refrigerant vapor leaving the evaporator 28 passes through the refrigerant line 7 of the primary refrigerant circuit to reenter the compression device 22 through the suction inlet port of the compression device.
  • the refrigerant vapor compression system 20 further includes an economizer circuit comprising an economizer refrigerant line 9 , an economizer heat exchanger 30 and an associated economizer expansion device 32 interdisposed in the economizer refrigerant line 9 .
  • the economizer heat exchanger 30 comprises a refrigerant-to-refrigerant heat exchanger having a first refrigerant pass 31 and a second refrigerant pass 33 disposed in heat exchange relationship.
  • the first refrigerant pass 31 is interdisposed in refrigerant line 5 of the primary refrigerant circuit downstream, with respect to refrigerant flow, of the heat rejection heat exchanger 24 and upstream, with respect to refrigerant flow, of the evaporator expansion device 26 .
  • the second refrigerant pass 33 is interdisposed in the economizer refrigerant line 9 downstream, with respect to refrigerant flow, of the economizer expansion device 32 .
  • Refrigerant passing through the refrigerant line 5 of the primary refrigerant circuit passes through the first refrigerant pass 31 of the economizer heat exchanger 30 in heat exchange relationship with a flow of refrigerant tapped off the refrigerant line 5 into the economizer refrigerant line 9 to pass through the second refrigerant pass 33 of the economizer heat exchanger 30 .
  • the economizer refrigerant line 9 establishes refrigerant flow communication between the refrigerant line 5 of the primary refrigerant circuit and an intermediate pressure stage of the compression process.
  • the economizer refrigerant line 9 may tap a portion of refrigerant from the refrigerant line 5 at a location upstream with respect to refrigerant flow of the first refrigerant pass 31 of the economizer heat exchanger 30 , as depicted in FIG. 1 , or at a location downstream with respect to refrigerant flow of the first refrigerant pass 31 of the economizer heat exchanger 30 , as depicted in FIG. 2 .
  • the economizer refrigerant line 9 communicates in refrigerant flow communication via an injection port 25 that opens into an intermediate pressure stage of the compression chambers of the compressor 22 . If the compression device 22 of the refrigerant vapor compression system 20 is a pair of compressors 22 A and 22 B, the economizer refrigerant line 9 communicates in refrigerant flow communication with a refrigerant line 11 connecting the outlet of the first compressor 22 A with the inlet to the second compressor 22 B as illustrated in FIG. 2 .
  • the refrigerant vapor compression system 20 also includes a compressor unloading circuit comprising a bypass line 17 , which establishes refrigerant flow communication between the economizer refrigerant, line 9 and the suction refrigerant line 7 of the primary refrigerant circuit, and a flow control device such as valve 50 interdisposed in the bypass line 17 .
  • the flow control device 50 has at least a first open position and a second closed position.
  • the flow control device may comprise a two-position solenoid valve having a first open position and a second closed position.
  • the bypass line 17 taps into the economizer refrigerant line 9 at a location downstream, with respect to refrigerant flow, of the second refrigerant pass 33 of the economizer heat exchanger 30 and upstream, with respect to refrigerant flow, of the terminus of the economizer refrigerant line 9 at an intermediate compression stage of the compression device 22 .
  • the refrigerant bypass line 17 taps into the refrigerant suction line 7 of the primary refrigerant circuit at a location downstream, with respect to refrigerant flow, of the outlet of the evaporator 28 and upstream, with respect to refrigerant flow, of the suction inlet port of the compression device 22 .
  • bypass line 17 provides a refrigerant flow path through which intermediate pressure refrigerant may pass from an intermediate pressure stage in the compression process into the primary refrigerant circuit, in a region thereof where the refrigerant is at suction pressure, in order to unload the compressor.
  • downstream portion with reference to the economizer refrigerant line 9 refers to that part of the economizer refrigerant line 9 extending between the junction of the bypass line 17 with the economizer refrigerant line 9 and the terminus of the economizer refrigerant line 9 at an intermediate stage of the compression device 22
  • upstream portion with reference to the economizer refrigerant line 9 refers to that part of the economizer refrigerant line 9 extending between refrigerant line 5 of the primary refrigerant circuit and the junction of the bypass line 17 with the economizer refrigerant line 9 .
  • the refrigerant vapor compression system 20 further includes a check valve 40 interdisposed in a downstream portion of the economizer refrigerant line 9 .
  • the check, valve 40 has a first position wherein the check valve opens to refrigerant vapor flow through the downstream portion of the economizer refrigerant line 9 in a direction from an intermediate stage of the compression process with the compression device 22 , and a second position wherein the check valve 40 restricts refrigerant flow through the downstream portion of the economizer refrigerant line 9 in a direction from the upstream portion of the economizer refrigerant line 9 into an intermediate stage of the compression process within the compression device 22 .
  • a flow metering device 42 is disposed in parallel flow arrangement with the check valve 40 .
  • the flow metering device 42 and the check valve 40 may be interdisposed respectively in parallel branches 9 a and 9 b of the downstream portion of the economizer refrigerant line 9 such as depicted in FIG. 1 .
  • the flow control device 50 in the bypass line 17 is closed and the flow of refrigerant from the upstream portion of the economizer refrigerant line 9 into the downstream portion of the economizer refrigerant line 9 sets the check valve 40 in branch line 9 b in its second position, which, in this embodiment, completely closes the check valve.
  • the check valve 40 With the check valve 40 fully closed, refrigerant from the economizer passes from the upstream portion of the refrigerant line 9 through the flow metering device 42 in the branch 9 b of the downstream portion of the economizer refrigerant line 9 to enter into an intermediate pressure stage of the compression process of the compression device 22 .
  • the flow metering device 42 may comprise, but is not limited to, a fixed flow area orifice.
  • the flow metering function desired in the economized mode of operation may be provided by an appropriate sizing of the branch line 9 a , whereby the branch line 9 a itself provides the desired flow restriction thereby eliminating the need for a fixed area orifice or other form of flow metering device 42 in the branch line 9 a.
  • the bypass flow control valve 50 in the bypass line 17 is open, whereby refrigerant vapor flows from an intermediate stage of the compression process of the compression device 22 through the branch 9 a of the downstream portion of the economizer refrigerant line 9 , setting the check valve 40 in its open position, and flowing into and through the bypass line 17 and thence the refrigerant line 7 of the primary refrigerant circuit to reenter the compression device 22 through the suction inlet port thereof.
  • the refrigerant passing through the upstream portion of the economizer refrigerant line 9 passes into the bypass 17 and also passes therethrough into refrigerant line 7 of the primary refrigerant circuit to reenter the compression device 22 through the suction inlet port thereof.
  • the check valve 40 interdisposed in the downstream portion of the economizer refrigerant line 9 has a first full open position and a second partially open position.
  • the flow control device 50 in the bypass line 17 is closed and the flow of refrigerant from the upstream portion of the economizer refrigerant line 9 into the downstream portion of the economizer refrigerant line 9 sets the check valve 40 in its second partially open position, which in this embodiment meters the refrigerant flow passing therethrough into an intermediate pressure stage of the compression process of the compression device 22 .
  • the bypass flow control device 50 in the bypass line 17 is open, whereby refrigerant vapor flows from an intermediate stage of the compression process of the compression device 22 through the downstream portion of the economizer refrigerant line 9 , setting the cheek valve 40 in its first fully open position, and flowing into and through the bypass line 17 and thence the refrigerant line 7 of the primary refrigerant circuit to reenter the compression device 22 through the suction inlet port thereof.
  • the refrigerant passing through the upstream portion of the economizer refrigerant line 9 passes into the bypass line 17 and also passes therethrough into the refrigerant line 7 of the primary refrigerant circuit to reenter the compression device 22 through the suction inlet port thereof.
  • the portion of the refrigerant having traversed the second refrigerant pass 33 of the economizer heat exchanger 30 flows through the economizer refrigerant line 9 to return to the compression device 22 at an intermediate pressure state in the compression process.
  • the compression device is a single refrigerant compressor 22 , such as for example a scroll compressor as illustrated in FIG. 1 , or a screw compressor or a multi-bank reciprocating compressor, the refrigerant from the second refrigerant pass 33 of the economizer heat exchanger 30 enters the compressor 22 through at least one injection port opening at an intermediate pressure state of compression process within the compressor 22 . If, as depicted in FIG.
  • the compression device is a pair of compressors 20 A and 20 B connected in series relationship, with respect to refrigerant flow, the refrigerant having traversed the second refrigerant pass 33 of the economizer heat exchanger 30 is injected into the refrigerant line ii interconnecting the discharge outlet of the first stage compressor 20 A in refrigerant flow communication with the suction inlet of the second stage compressor 20 B.
  • the positioning of the bypass flow control device 50 may be controlled by a controller 80 operatively associated with the refrigerant vapor compression system 20 .
  • the controller 80 may constitute the main system controller and may receive operating data regarding various system operating parameters as in conventional practice, such as for purposes of illustration but not limitation, the refrigerant temperature and/or pressure at the compressor discharge, at the compressor suction inlet, at the evaporator outlet, and other locations, as desired, provided by appropriately disposed sensors (not shown).
  • the primary expansion device 26 is an electronic expansion valve
  • the controller 80 may also control the operation of the primary expansion device in response to selected operating parameters.
  • the economizer expansion device 32 is an electronic expansion valve
  • the controller 80 may also control the operation of the economizer expansion device in response to selected operating parameters.
  • the refrigerant line can not be optimally sized for each of the flow control conditions.
  • the optimal flow area of a refrigerant line for unloading the compression device is significantly larger, for example, by as much an order of magnitude, than the optimal flow area of a refrigerant line for injecting, refrigerant into an intermediate pressure stage of the compression device.
  • a flow control apparatus having a first flow path through the economizer refrigerant line in a first direction from the intermediate pressure stage of the compression device to the bypass line and a second flow path through the economizer refrigerant line in a second direction from the second refrigerant pass of the refrigerant-to-refrigerant economizer heat exchanger into the intermediate pressure stage of the compression device.
  • the first flow path has a first hydraulic resistance to refrigerant flow through the first flow path and the second flow path has a second hydraulic resistance to refrigerant flow through the second flow path, with the first hydraulic resistance being different from the second hydraulic resistance.
  • the first hydraulic resistance is relatively lower and the second hydraulic resistance is relatively higher. Therefore, the flow area of each of these flow paths may be optimally sized for the respective refrigerant vapor flows therethrough, which may improve compressor efficiency by as much as 10%.
  • the check valve 40 in its open position, provides a relatively lower hydraulic resistance to refrigerant flow through the branch refrigerant line 9 b , while the flow restrictor 42 provides a relatively higher hydraulic resistance to refrigerant flow through the branch refrigerant line 9 a .
  • the flow restrictor 42 in its open position, provides a relatively lower hydraulic resistance to refrigerant flow through the branch refrigerant line 9 a .
  • the check valve 40 provides a relatively lower hydraulic resistance to refrigerant flow through the economizer refrigerant line 9 in the direction of flow from the intermediate pressure stage of the compression device 22 to the bypass line 17 and provides a relatively higher hydraulic resistance to refrigerant flow through the economizer refrigerant line 9 in the direction of flow from the economizer 30 into the port 25 opening into the intermediate stage of the compression device 22 .
  • the invention may be equally applied to flash tank type economized systems.
  • the control of the bypass flow and economizer vapor flow is accomplished in a similar fashion by controlling flow through the refrigerant economizer line.
  • the flash tank economizer is interdisposed in the primary refrigerant circuit downstream, with respect to refrigerant flow, of the refrigerant, heat rejection heat exchanger and upstream, with respect to refrigerant flow, of the primary expansion device.
  • the economizer refrigerant line extends in refrigerant vapor flow communication from the flash tank economizer to an intermediate pressure stage of the compression device and an economizer expansion device is interdisposed in the primary refrigerant circuit upstream, with respect to refrigerant flow, of the flash tank economizer.
  • the check valve 40 of the FIG. 2 embodiment may be positioned externally or internally, in relation to the shell of the compression device 22 .
  • the check valve 40 may be substituted by a solenoid valve that would be controlled by the controller 80 .

Abstract

A refrigerant vapor compression system has a primary refrigerant circuit including a compression device, a refrigerant heat rejection heat exchanger and a refrigerant heat absorption heat exchanger, and an economizer circuit including an economizer refrigerant line. A bypass flow control device controls refrigerant vapor flow through a bypass line extending between the economizer refrigerant line and a suction pressure portion of the primary refrigerant circuit. A flow control apparatus operatively associated with the economizer refrigerant line provides different flow resistance to refrigerant flow through the economizer refrigerant line in a first direction from an intermediate stage of the compression device to the suction portion of the primary refrigerant circuit and in a second direction from the economizer into an intermediate pressure stage of the compression device.

Description

    FIELD OF THE INVENTION
  • This invention relates generally to refrigerant vapor compression systems and, more particularly, to refrigerant vapor compression systems equipped with an economizer cycle.
  • BACKGROUND OF THE INVENTION
  • Refrigerant vapor compression systems are well known in the art and commonly used for conditioning air (or other secondary media) to be supplied to a climate-controlled comfort zone within a residence, office building, hospital, school, restaurant or other facility. Refrigerant vapor compression systems are also commonly used in transport refrigeration for refrigerating air supplied to a temperature-controlled cargo space of a truck, trailer, container or the like for transporting perishable items, and in commercial refrigeration for cooling air supplied to a temperature-controlled space in a cold room, a beverage cooler, a diary case or a refrigerated merchandiser for displaying perishable foods item in a chilled or frozen state, as appropriate. Typically, these refrigerant vapor compression systems include: a compressor, a condenser, an evaporator; and an expansion device. Commonly, the expansion device, typically a fixed orifice, a capillary tube, a thermostatic expansion valve (TXV) or an electronic expansion valve (EXV), is disposed in the refrigerant line upstream, with respect to refrigerant flow, of the evaporator and downstream of the condenser. These basic refrigerant vapor compression system components are serially interconnected by refrigerant lines in a closed-loop refrigerant circuit, arranged in accord with known refrigerant vapor compression cycles.
  • To improve performance of the refrigerant vapor compression system and to control the temperature of the refrigerant vapor discharged from the final stage of the compressor over a wide range of operating conditions, it is known to equip such systems with an economizer cycle incorporating a refrigerant-to-refrigerant economizer heat exchanger. The economizer heat exchanger is generally disposed hi the refrigerant circuit intermediate the condenser and the evaporator. In operation, a portion of the refrigerant leaving the condenser is diverted from the primary refrigerant circuit, expanded to an intermediate pressure and then passed through the economizer heat exchanger in heat exchange relationship with the main portion of the refrigerant leaving the condenser. In this manner, any liquid in the economized expanded refrigerant flow is evaporated, and then the evaporated refrigerant is typically superheated, while the refrigerant passing through the primary refrigerant circuit from the condenser to the evaporator is further cooled. Typically, the expanded refrigerant vapor is injected into an intermediate stage in the compression process, either through an injection port or ports opening into an intermediate pressure stage of the compression chamber (or chambers) of a single compressor or, in the case of a multiple compressor system, into a refrigerant line extending between the discharge outlet of the upstream compressor and the suction inlet of the downstream compressor.
  • For example, U.S. Pat. No. 6,571,576 discloses a refrigerant vapor compression system operating in a subcritical cycle and equipped with an economizer heat exchanger, wherein vapor refrigerant and liquid refrigerant are returned to, an intermediate stage of the compression process through one or more economizer injection ports opening into the compression chambers of a scroll compressor. To provide the refrigerant vapor for injection into the compressor, a portion of liquid refrigerant is taken from the primary refrigerant circuit at a location downstream of the condenser, expanded to an intermediate pressure and lower temperature by means of an expansion device, such as a valve, to form a refrigerant liquid/vapor mixture which is thereafter passed through the economizer heat exchanger in heat exchange relationship with the main flow of refrigerant liquid. In traversing the economizer heat exchanger, this refrigerant liquid/vapor mixture extracts heat from the main flow of refrigerant liquid, further cooling this liquid, thereby evaporating any remaining liquid component in the two-phase mixture and typically further heating the vapor. The refrigerant vapor leaving the economizer heat exchanger is then injected into the compressor through the economizer injection ports at the intermediate (between suction and discharge) pressure. Additionally, liquid refrigerant is selectively taken from the refrigerant circuit at a location downstream of the condenser and mixed into the refrigerant vapor being passed from the economizer to the compressor and injected into an intermediate pressure stage of the compression chambers of the scroll compressor together with the refrigerant vapor through the same economizer injection ports.
  • U.S. Pat. No. 7,114,349 discloses a refrigerant vapor compression system with a refrigerant-to-refrigerant heat exchanger interdisposed in the refrigerant circuit downstream of the condenser, with respect to refrigerant flow, and upstream of the evaporator, with respect to refrigerant flow. Through various bypass lines and manipulation of various open/closed solenoid valves associated with the bypass lines, the common heat exchanger may be operated either as an economizer heat exchanger or as a liquid-suction heat exchanger. When the system is operating with the refrigerant-to-refrigerant heat exchanger functioning as an economizer, refrigerant is passed from the primary refrigerant circuit through an economizer expansion device and thence through the refrigerant-to-refrigerant heat exchanger in heat exchange relationship with the remainder of the refrigerant passing through the primary refrigerant circuit from the condenser to the evaporator. After traversing the refrigerant-to-refrigerant heat exchanger, the expanded refrigerant is injected into an intermediate pressure stage of the compressor or returned to the primary refrigerant circuit at a point downstream, with respect to refrigerant flow, of the evaporator and upstream of the suction inlet of the compressor.
  • U.S. Pat. No. 6,058,729 discloses a subcritical refrigerant vapor compression system for a transport refrigeration unit incorporating a refrigerant-to-refrigerant heat exchanger into the refrigerant circuit as an economizer. The disclosed system also includes a suction modulation valve (SMV) for throttling refrigerant flow to the suction inlet of the compressor and an intermediate pressure-to-suction pressure unload circuit for compressor capacity control.
  • SUMMARY OF THE INVENTION
  • The refrigerant vapor compression system of the invention includes a primary refrigerant circuit, an economizer circuit, a bypass line, a bypass flow control device, and an economizer/compressor unload flow control apparatus. The primary refrigerant circuit includes a refrigerant compression device, a refrigerant heat rejection heat exchanger, a refrigerant heat absorption heat exchanger, and a primary expansion device interdisposed in the primary refrigerant circuit downstream of the refrigerant heat rejection heat exchanger and upstream of the refrigerant heat absorption heat exchanger. The economizer circuit includes an economizer refrigerant line extending in refrigerant flow communication between the economizer and an intermediate pressure stage of the compression device.
  • A bypass line extends in refrigerant flow communication from the economizer refrigerant line to the primary refrigerant circuit at a location downstream, with respect to refrigerant flow, of the refrigerant heat absorption heat exchanger. A bypass flow control device is disposed in the bypass line. The bypass flow control device has a first open position whereat refrigerant may flow through the bypass line and a second closed position whereat refrigerant is blocked from flowing through the bypass line. In an embodiment, the bypass flow control device may comprise a solenoid valve having a first open position and a second closed position.
  • Additionally, a flow control apparatus disposed in the economizer refrigerant line provides a first flow path through the economizer refrigerant line in a first direction from the intermediate pressure stage of the compression device to the bypass line and a second flow path through the economizer refrigerant line in a second direction from the economizer into the intermediate pressure stage of the compression device. The first flow path has a first hydraulic resistance to refrigerant flow through the first flow path and the second flow path has a second hydraulic resistance to refrigerant flow through the second flow path, the first hydraulic resistance being different from the second hydraulic resistance. In an embodiment, the first hydraulic resistance is relatively lower and the second hydraulic resistance is relatively higher.
  • In an embodiment, flow control apparatus comprises a “fluid diode” device interdisposed in the economizer refrigerant line at a location intermediate the intermediate pressure stage of the compression device and the bypass line. The “fluid diode” device has different flow resistance depending on the direction of the flow through the “fluid diode”. A check valve with two position openings is one embodiment of such a “fluid diode” device. The check valve is used to illustrate this embodiment; however, other types of “fluid diodes” known in the art would fall within the scope of this invention. The check valve has a first position wherein refrigerant may flow therethrough in a first direction from the intermediate pressure stage of the compression device to the bypass line and a second flow path through the economizer refrigerant line in a second direction from the second refrigerant pass of the refrigerant-to-refrigerant heat exchanger into the intermediate pressure stage of the compression device.
  • In an embodiment, the flow control apparatus comprises a first branch refrigerant line in refrigerant flow communication with the economizer refrigerant line, a second branch refrigerant line in refrigerant flow communication with the economizer refrigerant line and disposed in parallel with the first branch refrigerant line, and a check valve disposed in the first branch refrigerant line and having a first position wherein refrigerant may flow through the first branch refrigerant line and a second position wherein refrigerant flow through the first branch refrigerant line is blocked and refrigerant may flow through the second branch refrigerant line.
  • The economizer may be a heat exchanger economizer or a flash tank economizer. In an embodiment, the economizer comprises a refrigerant-to-refrigerant heat exchanger including a first refrigerant pass and a second refrigerant pass disposed in heat exchange relationship with said first refrigerant pass. The first refrigerant pass interdisposed in the primary refrigerant circuit and the second refrigerant pass interdisposed in the economizer refrigerant line. The economizer refrigerant line extends in fluid communication from the primary refrigerant circuit through the second refrigerant pass to an intermediate pressure stage of the compression device. In this embodiment, an economizer expansion device is interdisposed in the economizer refrigerant line upstream with respect to refrigerant flow of the second refrigerant pass of the refrigerant-to-refrigerant heat exchanger.
  • The invention may be equally applied to flash tank type economized systems. In such systems, the control of the bypass flow and economizer vapor flow is accomplished in a similar fashion by controlling flow through the refrigerant economizer line. In such an embodiment, the flash tank economizer is interdisposed in the primary refrigerant circuit downstream, with respect to refrigerant flow, of the refrigerant heat rejection heat exchanger and upstream, with respect to refrigerant flow, of the primary expansion device. The economizer refrigerant line extends in refrigerant vapor flow communication from the flash tank economizer to an intermediate pressure stage of the compression device and an economizer expansion device is interdisposed in the primary refrigerant circuit upstream with respect to refrigerant flow of the flash tank economizer.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • For a further understanding of the invention, reference will be made to the following detailed description of the invention which is to be read in connection with the accompanying drawing, where:
  • FIG. 1 is a schematic diagram illustrating an exemplary embodiment of a refrigerant vapor compression system in accord with the invention; and
  • FIG. 2 is a schematic diagram illustrating another exemplary embodiment of a refrigerant vapor compression system in accord with the invention.
  • DETAILED DESCRIPTION OF THE INVENTION
  • The invention will be described further herein with respect to the exemplary embodiments of the refrigerant vapor compression system 20 depicted in FIGS. 1-2. As in conventional systems, the refrigerant vapor compression system 20 includes a compression device 22, a heat rejection heat exchanger 24, an evaporator expansion device 26, and an evaporator 28, interconnected by various refrigerant lines 3, 5 and 7 in serial refrigerant flow communication in a conventional refrigeration cycle in a primary refrigerant circuit. The refrigerant vapor compression system 20 is suitable for use in a transport refrigeration system for refrigerating the air or other gaseous atmosphere within the temperature-controlled cargo space of a truck, trailer, container or the like for transporting perishable/frozen goods. The refrigerant vapor compression system 20 is also suitable for use in conditioning air to be supplied to a climate-controlled comfort zone within a residence, office building, hospital, school, restaurant or other facility. The refrigerant vapor compression system 20 could also be employed in refrigerating air supplied to display cases, merchandisers, freezer cabinets, cold rooms or other perishable/frozen product storage areas in commercial establishments.
  • The compression device 22 may comprise a single refrigerant compressor having at least a first compression stage and a second compression stage, such as, for example, a scroll compressor, such as illustrated in FIG. 1, or a screw compressor having staged compression pockets, or a reciprocating compressor having at least a first bank and a second bank of cylinders, or a pair of compressors 22A and 228 connected in series refrigerant flow relationship as illustrated in FIG. 2, such as, for example, a pair of scroll compressors, screw compressors, centrifugal compressors, reciprocating compressors (or separate cylinders of a single reciprocating compressor) or rotary compressors, with the discharge outlet port of the upstream compressor connected in serial refrigerant flow communication with the suction inlet port of the downstream compressor.
  • In the compression device 22, refrigerant vapor is compressed from a suction pressure at which the refrigerant vapor enters the suction inlet port of the compression device 22 to a discharge pressure, substantially higher than the suction pressure. The hot, high pressure refrigerant vapor passes from the discharge outlet port of the compression device 22 through refrigerant fine 3 of the primary refrigerant circuit to and through the heat rejection heat exchanger 24. In the heat rejection heat exchanger 24, the hot, high pressure refrigerant passes in heat exchange relationship with a cooling medium to cool and, in a subcritical cycle, condense the refrigerant vapor. The heat rejection heat exchanger 24 may comprise, for example, a finned tube heat exchanger, such as for example a plate fin and round tube heat exchanger or a fin and minichannel flat tube heat exchanger, wherein the refrigerant passes through the heat exchanger tubes in heat exchange relationship with ambient (typically outdoor) air being drawn through the finned tube heat exchanger by an air mover, such as one or more fans (not shown) operatively associated with the heat rejection heat exchanger 24.
  • The refrigerant leaving the heat rejection heat exchanger 24 passes through refrigerant line 5 of the primary refrigerant circuit to the evaporator 28. In doing so, the refrigerant traverses the evaporator expansion device 26 interdisposed in refrigerant line 5 and expands to a lower temperature, lower pressure liquid refrigerant or more commonly a liquid/vapor refrigerant mixture, before entering the evaporator 28. The evaporator expansion device 26 may be a restriction type expansion device, such as a capillary tube or a fixed plate orifice, a thermostatic expansion valve or an electronic expansion valve. The evaporator 28 constitutes a refrigerant heat absorbing heat exchanger through which the liquid or liquid/vapor refrigerant mixture passes in heat exchange relationship with a secondary fluid to be cooled, and typically dehumidified, and delivered to a conditioned environment. The refrigerant is heated thereby evaporating the liquid component and typically superheating the resultant vapor. The secondary fluid, typically air to be supplied to a climate-controlled environment, in the conditioned, cooled and typically dehumidified, state. In an embodiment, the evaporator 28 may comprise a finned tube heat exchanger through which refrigerant passes in heat exchange relationship with air that may be drawn from and returned to a climate-controlled environment by the one or more fans (not shown) operatively associated with the evaporator 28. The finned tube heat exchanger may comprise, for example, a plate fin and round tube heat exchanger or a fin and minichannel flat tube heat exchanger. The refrigerant vapor leaving the evaporator 28 passes through the refrigerant line 7 of the primary refrigerant circuit to reenter the compression device 22 through the suction inlet port of the compression device.
  • The refrigerant vapor compression system 20 further includes an economizer circuit comprising an economizer refrigerant line 9, an economizer heat exchanger 30 and an associated economizer expansion device 32 interdisposed in the economizer refrigerant line 9. The economizer heat exchanger 30 comprises a refrigerant-to-refrigerant heat exchanger having a first refrigerant pass 31 and a second refrigerant pass 33 disposed in heat exchange relationship. The first refrigerant pass 31 is interdisposed in refrigerant line 5 of the primary refrigerant circuit downstream, with respect to refrigerant flow, of the heat rejection heat exchanger 24 and upstream, with respect to refrigerant flow, of the evaporator expansion device 26. The second refrigerant pass 33 is interdisposed in the economizer refrigerant line 9 downstream, with respect to refrigerant flow, of the economizer expansion device 32. Refrigerant passing through the refrigerant line 5 of the primary refrigerant circuit passes through the first refrigerant pass 31 of the economizer heat exchanger 30 in heat exchange relationship with a flow of refrigerant tapped off the refrigerant line 5 into the economizer refrigerant line 9 to pass through the second refrigerant pass 33 of the economizer heat exchanger 30.
  • The economizer refrigerant line 9 establishes refrigerant flow communication between the refrigerant line 5 of the primary refrigerant circuit and an intermediate pressure stage of the compression process. The economizer refrigerant line 9 may tap a portion of refrigerant from the refrigerant line 5 at a location upstream with respect to refrigerant flow of the first refrigerant pass 31 of the economizer heat exchanger 30, as depicted in FIG. 1, or at a location downstream with respect to refrigerant flow of the first refrigerant pass 31 of the economizer heat exchanger 30, as depicted in FIG. 2. If the compression device 22 of the refrigerant vapor compression system 20 is a single compressor, such as a scroll compressor as illustrated in FIG. 1, the economizer refrigerant line 9 communicates in refrigerant flow communication via an injection port 25 that opens into an intermediate pressure stage of the compression chambers of the compressor 22. If the compression device 22 of the refrigerant vapor compression system 20 is a pair of compressors 22A and 22B, the economizer refrigerant line 9 communicates in refrigerant flow communication with a refrigerant line 11 connecting the outlet of the first compressor 22A with the inlet to the second compressor 22B as illustrated in FIG. 2.
  • The refrigerant vapor compression system 20 also includes a compressor unloading circuit comprising a bypass line 17, which establishes refrigerant flow communication between the economizer refrigerant, line 9 and the suction refrigerant line 7 of the primary refrigerant circuit, and a flow control device such as valve 50 interdisposed in the bypass line 17. The flow control device 50 has at least a first open position and a second closed position. In an embodiment, the flow control device may comprise a two-position solenoid valve having a first open position and a second closed position. At its inlet, the bypass line 17 taps into the economizer refrigerant line 9 at a location downstream, with respect to refrigerant flow, of the second refrigerant pass 33 of the economizer heat exchanger 30 and upstream, with respect to refrigerant flow, of the terminus of the economizer refrigerant line 9 at an intermediate compression stage of the compression device 22. At its outlet end, the refrigerant bypass line 17 taps into the refrigerant suction line 7 of the primary refrigerant circuit at a location downstream, with respect to refrigerant flow, of the outlet of the evaporator 28 and upstream, with respect to refrigerant flow, of the suction inlet port of the compression device 22. In this manner, the bypass line 17 provides a refrigerant flow path through which intermediate pressure refrigerant may pass from an intermediate pressure stage in the compression process into the primary refrigerant circuit, in a region thereof where the refrigerant is at suction pressure, in order to unload the compressor. As used in herein, the term “downstream portion” with reference to the economizer refrigerant line 9 refers to that part of the economizer refrigerant line 9 extending between the junction of the bypass line 17 with the economizer refrigerant line 9 and the terminus of the economizer refrigerant line 9 at an intermediate stage of the compression device 22, and the term “upstream portion” with reference to the economizer refrigerant line 9 refers to that part of the economizer refrigerant line 9 extending between refrigerant line 5 of the primary refrigerant circuit and the junction of the bypass line 17 with the economizer refrigerant line 9.
  • The refrigerant vapor compression system 20 further includes a check valve 40 interdisposed in a downstream portion of the economizer refrigerant line 9. The check, valve 40 has a first position wherein the check valve opens to refrigerant vapor flow through the downstream portion of the economizer refrigerant line 9 in a direction from an intermediate stage of the compression process with the compression device 22, and a second position wherein the check valve 40 restricts refrigerant flow through the downstream portion of the economizer refrigerant line 9 in a direction from the upstream portion of the economizer refrigerant line 9 into an intermediate stage of the compression process within the compression device 22.
  • Referring now to FIG. 1, in the exemplary embodiment of the refrigerant vapor compression system 20 depicted therein, a flow metering device 42 is disposed in parallel flow arrangement with the check valve 40. For example, the flow metering device 42 and the check valve 40 may be interdisposed respectively in parallel branches 9 a and 9 b of the downstream portion of the economizer refrigerant line 9 such as depicted in FIG. 1. In this embodiment, when the refrigerant vapor compression system 20 is operating in an economized mode without compressor unloading, the flow control device 50 in the bypass line 17 is closed and the flow of refrigerant from the upstream portion of the economizer refrigerant line 9 into the downstream portion of the economizer refrigerant line 9 sets the check valve 40 in branch line 9 b in its second position, which, in this embodiment, completely closes the check valve. With the check valve 40 fully closed, refrigerant from the economizer passes from the upstream portion of the refrigerant line 9 through the flow metering device 42 in the branch 9 b of the downstream portion of the economizer refrigerant line 9 to enter into an intermediate pressure stage of the compression process of the compression device 22. The flow metering device 42 may comprise, but is not limited to, a fixed flow area orifice. For example, in an embodiment, the flow metering function desired in the economized mode of operation may be provided by an appropriate sizing of the branch line 9 a, whereby the branch line 9 a itself provides the desired flow restriction thereby eliminating the need for a fixed area orifice or other form of flow metering device 42 in the branch line 9 a.
  • However, when the refrigerant vapor compression system 20 is operating with compressor unloading, the bypass flow control valve 50 in the bypass line 17 is open, whereby refrigerant vapor flows from an intermediate stage of the compression process of the compression device 22 through the branch 9 a of the downstream portion of the economizer refrigerant line 9, setting the check valve 40 in its open position, and flowing into and through the bypass line 17 and thence the refrigerant line 7 of the primary refrigerant circuit to reenter the compression device 22 through the suction inlet port thereof. If the refrigerant vapor compression system 20 is operating in the economized mode when the compressor is unloaded, the refrigerant passing through the upstream portion of the economizer refrigerant line 9 passes into the bypass 17 and also passes therethrough into refrigerant line 7 of the primary refrigerant circuit to reenter the compression device 22 through the suction inlet port thereof.
  • Referring now to FIG. 2, in the exemplary embodiment of the refrigerant vapor compression system 20 depicted therein, the check valve 40 interdisposed in the downstream portion of the economizer refrigerant line 9 has a first full open position and a second partially open position. In this embodiment, when the refrigerant vapor compression system 20 is operating in a economized mode without compressor unloading, the flow control device 50 in the bypass line 17 is closed and the flow of refrigerant from the upstream portion of the economizer refrigerant line 9 into the downstream portion of the economizer refrigerant line 9 sets the check valve 40 in its second partially open position, which in this embodiment meters the refrigerant flow passing therethrough into an intermediate pressure stage of the compression process of the compression device 22. However, in this embodiment, when the refrigerant vapor compression system 20 is operating with compressor unloading, the bypass flow control device 50 in the bypass line 17 is open, whereby refrigerant vapor flows from an intermediate stage of the compression process of the compression device 22 through the downstream portion of the economizer refrigerant line 9, setting the cheek valve 40 in its first fully open position, and flowing into and through the bypass line 17 and thence the refrigerant line 7 of the primary refrigerant circuit to reenter the compression device 22 through the suction inlet port thereof. Again, if the refrigerant vapor compression system 20 is operating in the economized mode when the compressor is unloaded, the refrigerant passing through the upstream portion of the economizer refrigerant line 9 passes into the bypass line 17 and also passes therethrough into the refrigerant line 7 of the primary refrigerant circuit to reenter the compression device 22 through the suction inlet port thereof.
  • In either embodiment of the invention, in the economized mode of operation without bypass, the portion of the refrigerant having traversed the second refrigerant pass 33 of the economizer heat exchanger 30 flows through the economizer refrigerant line 9 to return to the compression device 22 at an intermediate pressure state in the compression process. If the compression device is a single refrigerant compressor 22, such as for example a scroll compressor as illustrated in FIG. 1, or a screw compressor or a multi-bank reciprocating compressor, the refrigerant from the second refrigerant pass 33 of the economizer heat exchanger 30 enters the compressor 22 through at least one injection port opening at an intermediate pressure state of compression process within the compressor 22. If, as depicted in FIG. 2, the compression device is a pair of compressors 20A and 20B connected in series relationship, with respect to refrigerant flow, the refrigerant having traversed the second refrigerant pass 33 of the economizer heat exchanger 30 is injected into the refrigerant line ii interconnecting the discharge outlet of the first stage compressor 20A in refrigerant flow communication with the suction inlet of the second stage compressor 20B.
  • The positioning of the bypass flow control device 50 may be controlled by a controller 80 operatively associated with the refrigerant vapor compression system 20. In an embodiment, the controller 80 may constitute the main system controller and may receive operating data regarding various system operating parameters as in conventional practice, such as for purposes of illustration but not limitation, the refrigerant temperature and/or pressure at the compressor discharge, at the compressor suction inlet, at the evaporator outlet, and other locations, as desired, provided by appropriately disposed sensors (not shown). If the primary expansion device 26 is an electronic expansion valve, the controller 80 may also control the operation of the primary expansion device in response to selected operating parameters. Similarly, if the economizer expansion device 32 is an electronic expansion valve, the controller 80 may also control the operation of the economizer expansion device in response to selected operating parameters.
  • In prior art refrigerant vapor compression systems using a common portion of the economizer refrigerant line through which refrigerant passes in a first direction into, an intermediate pressure stage of the compression device from the economizer heat exchanger, during an economized mode operation, but in a second direction from an intermediate pressure stage of the compression device to return to the suction inlet of the compression device, during an unload mode of operation, the refrigerant line can not be optimally sized for each of the flow control conditions. Typically, the optimal flow area of a refrigerant line for unloading the compression device is significantly larger, for example, by as much an order of magnitude, than the optimal flow area of a refrigerant line for injecting, refrigerant into an intermediate pressure stage of the compression device.
  • However, in the refrigerant vapor compression system 20 of the invention, a flow control apparatus is provided having a first flow path through the economizer refrigerant line in a first direction from the intermediate pressure stage of the compression device to the bypass line and a second flow path through the economizer refrigerant line in a second direction from the second refrigerant pass of the refrigerant-to-refrigerant economizer heat exchanger into the intermediate pressure stage of the compression device. The first flow path has a first hydraulic resistance to refrigerant flow through the first flow path and the second flow path has a second hydraulic resistance to refrigerant flow through the second flow path, with the first hydraulic resistance being different from the second hydraulic resistance. In an embodiment, the first hydraulic resistance is relatively lower and the second hydraulic resistance is relatively higher. Therefore, the flow area of each of these flow paths may be optimally sized for the respective refrigerant vapor flows therethrough, which may improve compressor efficiency by as much as 10%.
  • In the exemplary embodiment depicted in FIG. 1, in its open position, the check valve 40 provides a relatively lower hydraulic resistance to refrigerant flow through the branch refrigerant line 9 b, while the flow restrictor 42 provides a relatively higher hydraulic resistance to refrigerant flow through the branch refrigerant line 9 a. In the exemplary embodiment depicted in FIG. 2, The check valve 40 provides a relatively lower hydraulic resistance to refrigerant flow through the economizer refrigerant line 9 in the direction of flow from the intermediate pressure stage of the compression device 22 to the bypass line 17 and provides a relatively higher hydraulic resistance to refrigerant flow through the economizer refrigerant line 9 in the direction of flow from the economizer 30 into the port 25 opening into the intermediate stage of the compression device 22.
  • The invention may be equally applied to flash tank type economized systems. In such systems, the control of the bypass flow and economizer vapor flow is accomplished in a similar fashion by controlling flow through the refrigerant economizer line. In such an embodiment, the flash tank economizer is interdisposed in the primary refrigerant circuit downstream, with respect to refrigerant flow, of the refrigerant, heat rejection heat exchanger and upstream, with respect to refrigerant flow, of the primary expansion device. The economizer refrigerant line extends in refrigerant vapor flow communication from the flash tank economizer to an intermediate pressure stage of the compression device and an economizer expansion device is interdisposed in the primary refrigerant circuit upstream, with respect to refrigerant flow, of the flash tank economizer.
  • While the present invention has been particularly, shown and described with reference to the exemplary embodiments as illustrated in the drawings, it will be understood by one skilled in the art that various changes in detail may be effected therein without departing from the spirit and scope of the invention as defined by the claims. For example, the check valve 40 of the FIG. 2 embodiment may be positioned externally or internally, in relation to the shell of the compression device 22. Also, the check valve 40 may be substituted by a solenoid valve that would be controlled by the controller 80.

Claims (21)

1. A refrigerant vapor compression system comprising:
a primary refrigerant circuit including a refrigerant compression device, a refrigerant heat rejection heat exchanger, a refrigerant heat absorption heat exchanger, and a primary expansion device interdisposed in the primary refrigerant circuit downstream of said refrigerant heat rejection heat exchanger and upstream of said refrigerant heat absorption heat exchanger;
an economizer circuit including an economizer and an economizer refrigerant line in refrigerant vapor flow communication between said economizer and an intermediate pressure stage of said compression device;
a bypass line in refrigerant flow communication between said economizer refrigerant line at a location intermediate said economizer and an intermediate stage of said compression device and said primary refrigerant circuit at a location downstream with respect to refrigerant flow of said refrigerant heat absorption heat exchanger;
a bypass flow control device disposed in said bypass line, said bypass flow control device having a first open position whereat refrigerant may flow through said bypass line and a second closed position whereat refrigerant is blocked from flowing through said bypass line; and
a flow control apparatus disposed in said economizer refrigerant line providing a first flow path through said economizer refrigerant line in a first direction from the intermediate pressure stage of said compression device to said bypass line and a second flow path through said economizer refrigerant line in a second direction from said economizer into the intermediate pressure stage of said compression device, said first flow path having a first hydraulic resistance to refrigerant flow through said first flow path and said second flow path having a second hydraulic resistance to refrigerant flow through said second flow path, the first and second hydraulic resistances being different.
2. A refrigerant vapor compression system as recited in claim 1 wherein said bypass flow control device comprises a solenoid valve having a first open position and a second closed position.
3. A refrigerant vapor compression system as recited in claim 1 wherein said flow control apparatus comprises a fluid diode device interdisposed in said economizer refrigerant fine at a location intermediate said bypass line and the intermediate pressure stage of said compression device, said fluid diode device providing a first flow path through said economizer refrigerant line in the first direction from the intermediate pressure stage of said compression device to said bypass line having a first relatively lower hydraulic resistance to refrigerant flow therethrough, and a second flow path through said economizer refrigerant line in a second direction from said economizer into the intermediate pressure stage of said compression device having a second relatively higher hydraulic resistance to refrigerant flow therethrough.
4. A refrigerant vapor compression system as recited in claim 3 wherein said fluid diode device comprises a check valve interdisposed in said economizer refrigerant line at a location intermediate the intermediate pressure stage of said compression device and said bypass line, said check valve having a first position wherein refrigerant may flow therethrough in the first direction through said first flow path from the intermediate pressure stage of said compression device to said bypass line and the second position wherein refrigerant may flow therethrough in a second direction through said economizer refrigerant line in a second direction from said economizer into the intermediate pressure stage of said compression device.
5. A refrigerant vapor compression system as recited in claim 1 wherein said flow control apparatus comprises a first branch refrigerant line in refrigerant flow communication with said first flow path through said economizer refrigerant line, a second branch refrigerant line in refrigerant flow communication with said second flow path through said economizer refrigerant line and disposed in parallel with said first branch refrigerant line, and a check valve disposed in the first branch refrigerant line, said check valve having a first position wherein refrigerant may flow through said first branch refrigerant line and said first flow path and a second position wherein refrigerant flow through said first branch refrigerant line and said first flow path is blocked.
6. A refrigerant vapor compression system as recited in claim 5 wherein said first branch refrigerant line has a relatively lower hydraulic resistance to refrigerant flow therethrough and said second branch refrigerant line has a relatively higher hydraulic resistance to refrigerant flow therethrough.
7. A refrigerant vapor compression system as recited in claim 5 further comprising a fixed restriction flow control device disposed in said second branch refrigerant line.
8. A refrigerant vapor compression system as recited in claim 7 wherein said cheek valve in its first position provides a relatively lower hydraulic resistance to refrigerant flow through said first branch refrigerant line and said fixed restriction flow control device provides a relatively higher hydraulic resistance to refrigerant flow through said second branch refrigerant line.
9. A refrigerant vapor compression system as recited in claim 1 wherein said flow control apparatus comprises a first branch refrigerant line in refrigerant flow communication with said first flow path through said economizer refrigerant line, a second branch refrigerant line in refrigerant flow communication with said second flow path through said economizer refrigerant line and disposed in parallel with said first branch refrigerant line, and a solenoid valve disposed in said first branch refrigerant line, said solenoid valve having a first position wherein refrigerant may flow through said first branch refrigerant line and a second position wherein refrigerant flow through said first branch refrigerant line is blocked and refrigerant may flow only through said second branch refrigerant line.
10. A refrigerant vapor compression system as recited in claim 9 further comprising a fixed restriction flow control device disposed in said second branch refrigerant line.
11. A refrigerant, vapor compression system as recited in claim 1 wherein said economizer comprises a refrigerant-to-refrigerant heat exchanger.
12. A refrigerant vapor compression system as recited in claim 1 wherein said refrigerant-to-refrigerant heat exchanger includes a first refrigerant pass and a second refrigerant pass disposed in heat exchange relationship with said first refrigerant pass, said first refrigerant pass interdisposed in said primary refrigerant circuit and said second refrigerant pass interdisposed in said economizer refrigerant line, said economizer refrigerant line extending in fluid communication from said primary refrigerant circuit through said second refrigerant pass to an intermediate pressure stage of said compression device.
13. A refrigerant vapor compression system as recited in claim 12 further comprising an economizer expansion device interdisposed in said economizer refrigerant line upstream with respect to refrigerant flow of the second refrigerant pass of said refrigerant-to-refrigerant heat exchanger.
14. A refrigerant vapor compression system as recited in claim 13 wherein said economizer expansion device comprises an expansion device selected from the group comprising electronic expansion valves, thermostatic expansion valves and fixed orifice flow restriction devices.
15. A refrigerant vapor compression system as recited in claim 1 wherein said economizer heat exchanger is a flash tank interdisposed in said primary refrigerant circuit downstream with respect to refrigerant flow of said refrigerant heat rejection heat exchanger and upstream with respect to refrigerant flow of said primary expansion device.
16. A refrigerant vapor compression system as recited in claim 15 further comprising an economizer expansion device interdisposed in said primary refrigerant circuit upstream with respect to refrigerant flow of said flash tank.
17. A refrigerant vapor compression system as recited in claim 16 wherein said economizer expansion device comprises an expansion device selected from the group comprising electronic expansion valves, thermostatic expansion valves and fixed orifice flow restriction devices.
18. A refrigerant vapor compression system as recited in claim 1 wherein said primary expansion device comprises an expansion device selected from the group comprising electronic expansion valves, thermostatic expansion valves and fixed orifice flow restriction devices.
19. A refrigerant vapor compression system as recited in claim 1 wherein said compression device comprises a single compressor having at least two compression stages.
20. A refrigerant vapor compression system as recited in claim 1 wherein said compression device comprises at least two compressors disposed in said primary refrigerant circuit in a series relationship with respect to refrigerant flow.
21. A refrigerant vapor compression system as recited in claim 1 wherein said compression device comprises at least one compressor selected from the group of compressors comprising scroll compressors, reciprocating compressors, screw compressors, centrifugal compressors and rotary compressors.
US12/599,888 2007-05-17 2007-05-17 Economized refrigerant system with flow control Abandoned US20100251750A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US2007/011797 WO2008143611A1 (en) 2007-05-17 2007-05-17 Economized refrigerant system with flow control

Publications (1)

Publication Number Publication Date
US20100251750A1 true US20100251750A1 (en) 2010-10-07

Family

ID=40032179

Family Applications (1)

Application Number Title Priority Date Filing Date
US12/599,888 Abandoned US20100251750A1 (en) 2007-05-17 2007-05-17 Economized refrigerant system with flow control

Country Status (3)

Country Link
US (1) US20100251750A1 (en)
CN (1) CN101755177A (en)
WO (1) WO2008143611A1 (en)

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012137207A (en) * 2010-12-24 2012-07-19 Mitsubishi Electric Corp Refrigerating cycle apparatus
US20120266624A1 (en) * 2011-04-21 2012-10-25 Denso Corporation Heat pump cycle
JP2013076532A (en) * 2011-09-30 2013-04-25 Daikin Industries Ltd Refrigerator
US20130240180A1 (en) * 2012-03-14 2013-09-19 Kist Europe-Korea Institute of Science and Technologie Europe Forschungsgesellschaft mbh System and method for superheating and/or supercooling of liquids and use of the system and/or method
US20140047852A1 (en) * 2012-08-14 2014-02-20 Samsung Electronics Co., Ltd. Air conditioner and control method thereof
EP2910872A4 (en) * 2012-10-22 2016-10-19 Mitsubishi Electric Corp Freezing device
WO2017147391A1 (en) 2016-02-26 2017-08-31 Daikin Applied Americas Inc. Economizer used in chiller system
WO2018026757A1 (en) 2016-08-05 2018-02-08 Daikin Applied Americas Inc. Centrifugal compressor, impeller clearance control apparatus for centrifugal compressor, and impeller clearance control method for centrifugal compressor
WO2018053067A1 (en) 2016-09-15 2018-03-22 Daikin Applied Americas Inc. Centrifugal compressor
US10107536B2 (en) 2009-12-18 2018-10-23 Carrier Corporation Transport refrigeration system and methods for same to address dynamic conditions
US10119738B2 (en) 2014-09-26 2018-11-06 Waterfurnace International Inc. Air conditioning system with vapor injection compressor
US10337767B2 (en) 2014-01-08 2019-07-02 Carrier Corporation Adaptive control of multi-compartment transport refrigeration system
USD887788S1 (en) 2017-05-17 2020-06-23 Dometic Sweden Ab Cooler
USD888503S1 (en) 2017-05-17 2020-06-30 Dometic Sweden Ab Cooler
US10866002B2 (en) 2016-11-09 2020-12-15 Climate Master, Inc. Hybrid heat pump with improved dehumidification
US10871314B2 (en) 2016-07-08 2020-12-22 Climate Master, Inc. Heat pump and water heater
US10935260B2 (en) 2017-12-12 2021-03-02 Climate Master, Inc. Heat pump with dehumidification
USD933449S1 (en) 2016-11-22 2021-10-19 Dometic Sweden Ab Latch
US11300341B2 (en) 2017-06-08 2022-04-12 Carrier Corporation Method of control for economizer of transport refrigeration units
US11365916B2 (en) 2015-11-25 2022-06-21 Carrier Corporation Refrigeration system and throttle control method therefor
US11414238B2 (en) 2016-11-22 2022-08-16 Dometic Sweden Ab Cooler
CN115038869A (en) * 2020-01-10 2022-09-09 江森自控泰科知识产权控股有限责任合伙公司 Economizer control system and method
US11506430B2 (en) 2019-07-15 2022-11-22 Climate Master, Inc. Air conditioning system with capacity control and controlled hot water generation
US11592215B2 (en) 2018-08-29 2023-02-28 Waterfurnace International, Inc. Integrated demand water heating using a capacity modulated heat pump with desuperheater
US11725851B2 (en) 2017-03-31 2023-08-15 Carrier Corporation Multiple stage refrigeration system and control method thereof

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103673145B (en) * 2012-09-05 2016-03-23 苏州必信空调有限公司 The air-conditioning system of compact handpiece Water Chilling Units and skyscraper
CN105008820B (en) * 2013-03-12 2017-03-08 三菱电机株式会社 Air-conditioning device
JP5855312B2 (en) * 2013-03-12 2016-02-09 三菱電機株式会社 Air conditioner
CN103322717A (en) * 2013-06-17 2013-09-25 江苏科立德制冷设备有限公司 Low-temperature vortex parallel compression condensing unit with enhanced vapor injection
ITVI20130257A1 (en) * 2013-10-18 2015-04-19 Carel Ind Spa METHOD OF DRIVING A REFRIGERATED MACHINE EQUIPPED WITH AN ECONOMISER SYSTEM
WO2016092512A1 (en) * 2014-12-11 2016-06-16 Angelantoni Cleantech S.R.L. Refrigeration device
KR101702736B1 (en) 2015-01-12 2017-02-03 엘지전자 주식회사 An air conditioner
CN104896813B (en) * 2015-06-29 2018-06-05 广东美的暖通设备有限公司 For the multi-line system of air-conditioning

Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4141708A (en) * 1977-08-29 1979-02-27 Carrier Corporation Dual flash and thermal economized refrigeration system
US4144717A (en) * 1977-08-29 1979-03-20 Carrier Corporation Dual flash economizer refrigeration system
US4207749A (en) * 1977-08-29 1980-06-17 Carrier Corporation Thermal economized refrigeration system
US5431026A (en) * 1994-03-03 1995-07-11 General Electric Company Refrigerant flow rate control based on liquid level in dual evaporator two-stage refrigeration cycles
US5553457A (en) * 1994-09-29 1996-09-10 Reznikov; Lev Cooling device
US6202438B1 (en) * 1999-11-23 2001-03-20 Scroll Technologies Compressor economizer circuit with check valve
US6250099B1 (en) * 1998-07-31 2001-06-26 Zexel Corporation Refrigerating device
US6276148B1 (en) * 2000-02-16 2001-08-21 David N. Shaw Boosted air source heat pump
US6385980B1 (en) * 2000-11-15 2002-05-14 Carrier Corporation High pressure regulation in economized vapor compression cycles
US6658867B1 (en) * 2002-07-12 2003-12-09 Carrier Corporation Performance enhancement of vapor compression system
US6718781B2 (en) * 2001-07-11 2004-04-13 Thermo King Corporation Refrigeration unit apparatus and method
US6772600B2 (en) * 2002-06-12 2004-08-10 Lg Electronics Inc. Multi-unit air conditioner and method for controlling the same
US6883341B1 (en) * 2003-11-10 2005-04-26 Carrier Corporation Compressor with unloader valve between economizer line and evaporator inlet
US6938438B2 (en) * 2003-04-21 2005-09-06 Carrier Corporation Vapor compression system with bypass/economizer circuits
US6955058B2 (en) * 2004-01-30 2005-10-18 Carrier Corporation Refrigerant cycle with tandem economized and conventional compressors
US7000423B2 (en) * 2003-10-24 2006-02-21 Carrier Corporation Dual economizer heat exchangers for heat pump
US20060037336A1 (en) * 2004-08-20 2006-02-23 Bush James W Compressor loading control
US7114349B2 (en) * 2004-12-10 2006-10-03 Carrier Corporation Refrigerant system with common economizer and liquid-suction heat exchanger
US7137270B2 (en) * 2004-07-14 2006-11-21 Carrier Corporation Flash tank for heat pump in heating and cooling modes of operation
US20100115975A1 (en) * 2007-04-24 2010-05-13 Carrier Corporation Refrigerant vapor compression system and method of transcritical operation

Patent Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4141708A (en) * 1977-08-29 1979-02-27 Carrier Corporation Dual flash and thermal economized refrigeration system
US4144717A (en) * 1977-08-29 1979-03-20 Carrier Corporation Dual flash economizer refrigeration system
US4207749A (en) * 1977-08-29 1980-06-17 Carrier Corporation Thermal economized refrigeration system
US5431026A (en) * 1994-03-03 1995-07-11 General Electric Company Refrigerant flow rate control based on liquid level in dual evaporator two-stage refrigeration cycles
US5553457A (en) * 1994-09-29 1996-09-10 Reznikov; Lev Cooling device
US6250099B1 (en) * 1998-07-31 2001-06-26 Zexel Corporation Refrigerating device
US6202438B1 (en) * 1999-11-23 2001-03-20 Scroll Technologies Compressor economizer circuit with check valve
US6276148B1 (en) * 2000-02-16 2001-08-21 David N. Shaw Boosted air source heat pump
US6385980B1 (en) * 2000-11-15 2002-05-14 Carrier Corporation High pressure regulation in economized vapor compression cycles
US6718781B2 (en) * 2001-07-11 2004-04-13 Thermo King Corporation Refrigeration unit apparatus and method
US6772600B2 (en) * 2002-06-12 2004-08-10 Lg Electronics Inc. Multi-unit air conditioner and method for controlling the same
US6658867B1 (en) * 2002-07-12 2003-12-09 Carrier Corporation Performance enhancement of vapor compression system
US6938438B2 (en) * 2003-04-21 2005-09-06 Carrier Corporation Vapor compression system with bypass/economizer circuits
US7000423B2 (en) * 2003-10-24 2006-02-21 Carrier Corporation Dual economizer heat exchangers for heat pump
US6883341B1 (en) * 2003-11-10 2005-04-26 Carrier Corporation Compressor with unloader valve between economizer line and evaporator inlet
US6955058B2 (en) * 2004-01-30 2005-10-18 Carrier Corporation Refrigerant cycle with tandem economized and conventional compressors
US7137270B2 (en) * 2004-07-14 2006-11-21 Carrier Corporation Flash tank for heat pump in heating and cooling modes of operation
US20060037336A1 (en) * 2004-08-20 2006-02-23 Bush James W Compressor loading control
US7114349B2 (en) * 2004-12-10 2006-10-03 Carrier Corporation Refrigerant system with common economizer and liquid-suction heat exchanger
US20100115975A1 (en) * 2007-04-24 2010-05-13 Carrier Corporation Refrigerant vapor compression system and method of transcritical operation

Cited By (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10107536B2 (en) 2009-12-18 2018-10-23 Carrier Corporation Transport refrigeration system and methods for same to address dynamic conditions
JP2012137207A (en) * 2010-12-24 2012-07-19 Mitsubishi Electric Corp Refrigerating cycle apparatus
US8671707B2 (en) * 2011-04-21 2014-03-18 Denso Corporation Heat pump cycle
US20120266624A1 (en) * 2011-04-21 2012-10-25 Denso Corporation Heat pump cycle
JP2013076532A (en) * 2011-09-30 2013-04-25 Daikin Industries Ltd Refrigerator
US20130240180A1 (en) * 2012-03-14 2013-09-19 Kist Europe-Korea Institute of Science and Technologie Europe Forschungsgesellschaft mbh System and method for superheating and/or supercooling of liquids and use of the system and/or method
US20140047852A1 (en) * 2012-08-14 2014-02-20 Samsung Electronics Co., Ltd. Air conditioner and control method thereof
EP2910872A4 (en) * 2012-10-22 2016-10-19 Mitsubishi Electric Corp Freezing device
US10337767B2 (en) 2014-01-08 2019-07-02 Carrier Corporation Adaptive control of multi-compartment transport refrigeration system
US11927377B2 (en) 2014-09-26 2024-03-12 Waterfurnace International, Inc. Air conditioning system with vapor injection compressor
US11480372B2 (en) 2014-09-26 2022-10-25 Waterfurnace International Inc. Air conditioning system with vapor injection compressor
US10753661B2 (en) 2014-09-26 2020-08-25 Waterfurnace International, Inc. Air conditioning system with vapor injection compressor
US10119738B2 (en) 2014-09-26 2018-11-06 Waterfurnace International Inc. Air conditioning system with vapor injection compressor
US11761695B2 (en) 2015-11-25 2023-09-19 Carrier Corporation Refrigeration system and throttle control method therefor
US11365916B2 (en) 2015-11-25 2022-06-21 Carrier Corporation Refrigeration system and throttle control method therefor
US10539350B2 (en) 2016-02-26 2020-01-21 Daikin Applied Americas Inc. Economizer used in chiller system
WO2017147391A1 (en) 2016-02-26 2017-08-31 Daikin Applied Americas Inc. Economizer used in chiller system
US10871314B2 (en) 2016-07-08 2020-12-22 Climate Master, Inc. Heat pump and water heater
US11448430B2 (en) 2016-07-08 2022-09-20 Climate Master, Inc. Heat pump and water heater
WO2018026757A1 (en) 2016-08-05 2018-02-08 Daikin Applied Americas Inc. Centrifugal compressor, impeller clearance control apparatus for centrifugal compressor, and impeller clearance control method for centrifugal compressor
US10724546B2 (en) 2016-08-05 2020-07-28 Daikin Applied Americas Inc. Centrifugal compressor having a casing with an adjustable clearance and connections for a variable flow rate cooling medium, impeller clearance control apparatus for centrifugal compressor, and impeller clearance control method for centrifugal compressor
WO2018053067A1 (en) 2016-09-15 2018-03-22 Daikin Applied Americas Inc. Centrifugal compressor
US11435095B2 (en) 2016-11-09 2022-09-06 Climate Master, Inc. Hybrid heat pump with improved dehumidification
US10866002B2 (en) 2016-11-09 2020-12-15 Climate Master, Inc. Hybrid heat pump with improved dehumidification
USD995264S1 (en) 2016-11-22 2023-08-15 Dometic Sweden Ab Latch
USD985359S1 (en) 2016-11-22 2023-05-09 Dometic Sweden Ab Latch
USD933449S1 (en) 2016-11-22 2021-10-19 Dometic Sweden Ab Latch
US11414238B2 (en) 2016-11-22 2022-08-16 Dometic Sweden Ab Cooler
US11535425B2 (en) 2016-11-22 2022-12-27 Dometic Sweden Ab Cooler
US11725851B2 (en) 2017-03-31 2023-08-15 Carrier Corporation Multiple stage refrigeration system and control method thereof
USD887788S1 (en) 2017-05-17 2020-06-23 Dometic Sweden Ab Cooler
USD888503S1 (en) 2017-05-17 2020-06-30 Dometic Sweden Ab Cooler
US11300341B2 (en) 2017-06-08 2022-04-12 Carrier Corporation Method of control for economizer of transport refrigeration units
US10935260B2 (en) 2017-12-12 2021-03-02 Climate Master, Inc. Heat pump with dehumidification
US11592215B2 (en) 2018-08-29 2023-02-28 Waterfurnace International, Inc. Integrated demand water heating using a capacity modulated heat pump with desuperheater
US11953239B2 (en) 2018-08-29 2024-04-09 Waterfurnace International, Inc. Integrated demand water heating using a capacity modulated heat pump with desuperheater
US11506430B2 (en) 2019-07-15 2022-11-22 Climate Master, Inc. Air conditioning system with capacity control and controlled hot water generation
CN115038869A (en) * 2020-01-10 2022-09-09 江森自控泰科知识产权控股有限责任合伙公司 Economizer control system and method

Also Published As

Publication number Publication date
WO2008143611A1 (en) 2008-11-27
CN101755177A (en) 2010-06-23

Similar Documents

Publication Publication Date Title
US20100251750A1 (en) Economized refrigerant system with flow control
US7997092B2 (en) Refrigerant vapor compression system operating at or near zero load
US8424326B2 (en) Refrigerant vapor compression system and method of transcritical operation
US8671703B2 (en) Refrigerant vapor compression system with flash tank economizer
US8528359B2 (en) Economized refrigeration cycle with expander
EP2257748B1 (en) Refrigerant vapor compression system
US20100132399A1 (en) Transcritical refrigerant vapor compression system with charge management
US9360237B2 (en) Transcritical refrigerant vapor system with capacity boost
US9068765B2 (en) Refrigeration storage in a refrigerant vapor compression system
DK2417406T3 (en) Coolant vapor compression system with hot gas bypass
US20160272047A1 (en) Capacity modulation of transport refrigeration system
CN112424542A (en) Refrigerant vapor compression system

Legal Events

Date Code Title Description
AS Assignment

Owner name: CARRIER CORPORATION, CONNECTICUT

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:LIFSON, ALEXANDER;TARAS, MICHAEL F.;REEL/FRAME:023508/0445

Effective date: 20070516

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION