[go: up one dir, main page]

US20070295025A1 - Engine Heat Pump - Google Patents

Engine Heat Pump Download PDF

Info

Publication number
US20070295025A1
US20070295025A1 US11/569,429 US56942905A US2007295025A1 US 20070295025 A1 US20070295025 A1 US 20070295025A1 US 56942905 A US56942905 A US 56942905A US 2007295025 A1 US2007295025 A1 US 2007295025A1
Authority
US
United States
Prior art keywords
heat exchanger
refrigerant
compressor
supercooling
engine
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
US11/569,429
Other languages
English (en)
Inventor
Ken-ichi Minami
Jirou Fukudome
Hiroshi Azuma
Keishi Yamanaka
Eita Kureha
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.)
Yanmar Co Ltd
Original Assignee
Yanmar Co Ltd
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 Yanmar Co Ltd filed Critical Yanmar Co Ltd
Assigned to YANMAR CO., LTD. reassignment YANMAR CO., LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: AZUMA, HIROSHI, FUKUDOME, JIROU, KUREHA, EITA, MINAMI, KEN-ICHI, YAMANAKA, KEISHI
Publication of US20070295025A1 publication Critical patent/US20070295025A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00—Fluid-circulation arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B27/00—Machines, plants or systems, using particular sources of energy
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00—Compression machines, plants or systems with non-reversible cycle
    • F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/07—Details of compressors or related parts
    • F25B2400/075—Details of compressors or related parts with parallel compressors
    • F25B2400/0751—Details of compressors or related parts with parallel compressors the compressors having different capacities
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/13—Economisers

Definitions

  • the invention relates to a system of an engine heat pump. Particularly, the invention relates to a technology for reducing the total compression work of the engine heat pump without increase of consumed electric power.
  • the reference document discloses an electromotive compressor serving as the compressor (sub compressor) subjected to the higher evaporation pressure.
  • the engine heat pump is provided with an additional device (i.e., the electromotive compressor) requiring electric power.
  • the electromotive compressor serving as the compressor (sub compressor) subjected to the higher evaporation pressure.
  • An object of the invention is to provide an engine heat pump whose compression work is reduced without increase of consumed electric power, thereby improving its driving efficiency (energy efficiency).
  • An engine heat pump comprises: an engine; a main compressor driven by the engine; a sub compressor delivering a refrigerant to be joined to a refrigerant delivered from the main compressor; an indoor heat exchanger; an outdoor heat exchanger; an expansion valve for the indoor heat exchanger; an expansion valve for the outdoor heat exchanger; and a supercooling heat exchanger disposed on a liquid refrigerant passage of a connection passage between the indoor heat exchanger and the outdoor heat exchanger.
  • a supercooling liquid refrigerant branched into a branching passage supercools a liquid refrigerant before being branched.
  • the sub compressor is driven by the engine so as to compress the supercooling liquid refrigerant.
  • a ratio of a capacity of the sub compressor to a total capacity of the main compressor and the sub compressor ranges between 20% and 29%.
  • an engine exhaust heat recovery unit is disposed in parallel to the outdoor heat exchanger.
  • the supercooling liquid refrigerant is evaporated by the engine exhaust heat recovery unit and compressed by the sub compressor.
  • the sub compressor is driven by the engine so as to compress the supercooling refrigerant subjected to a higher evaporation pressure (refrigerant suction pressure) than the evaporation pressure of refrigerant compressed by the main compressor. Therefore, the engine heat pump requires no additional electric power required for an electromotive sub compressor, so that the total compression work in a refrigeration cycle is reduced while ensuring or improving the cooling capacity by the supercooling performance of the supercooling heat exchanger.
  • a capacity ratio of the sub compressor relative to a total capacity of the main compressor and the sub compressor the sub compressor is set within a certain range. Therefore, while the cooling efficiency for the cooling operation is ensured or improved, the capacity of the supercooling heat exchanger for the heating operation is ensured. That is, in the present invention, since the common engine drives the main compressor and the sub compressor, sufficient driving efficiency (energy efficiency) is ensured whether the engine heat pump is operated for cooling or for heating.
  • the liquid refrigerant is supercooled so as to improve the capacity of refrigerant per unit mass and unit flow rate for absorbing heat from an outdoor air, thereby reducing the total amount of refrigerant flowing in the refrigeration cycle.
  • the total compression work is reduced so as to improve the driving efficiency (energy efficiency) of the engine heat pump.
  • FIG. 1 is a diagram of a refrigerant circuit of an engine heat pump according to the invention.
  • FIG. 2 is a block diagram of control units for the refrigerant circuit of the engine heat pump.
  • FIG. 3 is a Moliere chart due to the refrigerant circuit.
  • FIG. 4 is a graph of COP relative to the capacity share of a sub compressor.
  • FIG. 5 is a graph of temperature of refrigerant in a supercooling exchanger relative to the capacity share of a sub compressor.
  • FIG. 1 A refrigerant circuit system and a refrigeration cycle of an engine heat pump according to the invention will be described with reference to FIG. 1 .
  • the engine heat pump of the invention comprises: an engine 4 ; a main compressor 2 driven by engine 4 ; a sub compressor 3 driven by engine 4 ; an indoor heat exchanger 8 ; an outdoor heat exchanger 5 ; an expansion valve 23 for the indoor heat exchanger 8 ; an expansion valve 21 for the outdoor heat exchanger; and a supercooling heat exchanger 15 .
  • Supercooling heat exchanger 15 is disposed on a main passage 26 serving as a liquid refrigerant passage of a connection passage between indoor heat exchanger 8 and outdoor heat exchanger 5 , so that, in supercooling heat exchanger 15 , a supercooling liquid refrigerant branched into a branching passage 27 (including passages 27 a and 27 b ) supercools a liquid refrigerant before being branched.
  • the engine heat pump uses a refrigeration cycle caused by these components.
  • Supercooling heat exchanger 15 includes connection points 15 a and 15 b to be connected to main passage 26 , and connection points 15 c and 15 d to be connected to branching passage 27 .
  • a plurality of indoor heat exchangers 8 may be provided to the engine heat pump.
  • Main compressor 2 driven by engine 4 , absorbs and compresses a vapor refrigerant separated from a liquid refrigerant by an accumulator (not shown), and delivers vapor refrigerant having a high temperature and a high pressure.
  • a four-way valve 24 introduces the vapor refrigerant delivered from main compressor 2 into a predetermined direction.
  • Four-way valve 24 also receives a vapor refrigerant to be supplied to main compressor 2 . Therefore, a passage 32 , serving as a suction line of main compressor 2 , is interposed between a refrigerant inlet of main compressor 2 and four-way valve 24 , so as to introduce the vapor refrigerant from four-way valve 24 into main compressor 2 .
  • a supercooling liquid refrigerant is separated into branching passage 27 and passed through supercooling heat exchanger 15 .
  • An accumulator (not shown) separates a vapor refrigerant from the supercooling liquid refrigerant passed through supercooling heat exchanger 15 .
  • Sub compressor 3 driven by engine 4 , absorbs and compresses the vapor refrigerant separated from the supercooling liquid refrigerant, and delivers a vapor refrigerant having a high temperature and a high pressure.
  • An expansion valve 22 for the supercooling heat exchanger is provided on branching passage 27 , so as to cool a refrigerant as the supercooling liquid refrigerant supplied to supercooling heat exchanger 15 for supercooling the liquid refrigerant before being branched.
  • Sub compressor 3 absorbs the supercooling liquid refrigerant whose heat has been exchanged by supercooling heat exchanger 15 . Therefore, a passage 33 , serving as a suction line of sub compressor 3 , is interposed between supercooling heat exchanger 15 and a refrigerant inlet of sub compressor 3 .
  • Branching passage 27 connected to main passage 26 includes branching passage 27 a between indoor heat exchanger 8 and supercooling heat exchanger 15 .
  • Branching passage 27 also includes branching passage 27 b between outdoor heat exchanger 5 and supercooling heat exchanger 15 .
  • An on-off valve 28 a is interposed between branching passage 27 a and expansion valve 22
  • an on-off valve 28 b is interposed between branching passage 27 b and expansion valve 22 .
  • the refrigerant delivered from sub compressor 3 is joined to the refrigerant delivered from main compressor 2 at a confluence point 65 before four-way valve 24 .
  • Four-way valve 24 changes the flow direction of the joined refrigerant from confluence point 65 , so as to perform either the cooling cycle or the heating cycle.
  • An oil separator (not shown) is interposed between confluence point 65 and four-way valve 24 .
  • the oil separator separates a refrigerator oil from the high-temperature and high-pressurized vapor refrigerant, and returns the refrigerator oil to suction sides of main compressor 2 and sub compressor 3 , so as to smoothly lubricate compressors 2 and 3 .
  • the above construction makes a refrigeration cycle, which is switched between the cooling cycle and the heating cycle depending on the change of the flow direction of refrigerant by four-way valve 24 .
  • the respective refrigerants compressed by main compressor 2 and sub compressor 3 join each other at confluence point 65 , and the joined refrigerant is sent to outdoor heat exchanger 5 through four-way valve 24 .
  • the refrigerant is radiated and condensed by outdoor heat exchanger 5 , and sent to supercooling heat exchanger 15 .
  • the refrigerant flows into supercooling heat exchanger 15 through connection point 15 b, and flows out from supercooling heat exchanger 15 through connection point 15 a.
  • the liquid refrigerant supercooled by supercooling heat exchanger 15 is expanded by expansion valve 23 , and evaporated by the endothermic action of indoor heat exchanger 8 .
  • the vapor refrigerant is supplied to main compressor 2 through four-way valve 24 , and compressed by main compressor 2 to be delivered again.
  • a part of the liquid refrigerant flowing from outdoor heat exchanger 5 through main passage 26 is branched into branching passage 27 a so as to serve as the supercooling liquid refrigerant.
  • the branched refrigerant is expanded and cooled by expansion valve 22 so as to be changed into a wet low-temperature refrigerant.
  • the wet low-temperature refrigerant flows into supercooling heat exchanger 15 through connection point 15 c, supercools the refrigerant flowing in main passage 26 , and flows out from supercooling heat exchanger 15 through connection point 15 d.
  • on-off valve 28 a is opened and on-off valve 28 b is closed, so that the refrigerant flowing in main passage 26 is not branched into branching passage 27 b, but into branching passage 27 a.
  • the supercooling refrigerant branched into branching passage 27 a supercools the undivided liquid refrigerant before being branched.
  • liquid refrigerant flowing through main passage 26 is supercooled so as to improve the efficiency of the refrigeration cycle.
  • the supercooling liquid refrigerant is supplied to sub compressor 3 so as to be compressed and delivered again.
  • the respective refrigerants compressed by main compressor 2 and sub compressor 3 join each other at confluence point 65 , and the joined refrigerant is sent to indoor heat exchanger 8 through four-way valve 24 .
  • the refrigerant is radiated and condensed (liquefied) by indoor heat exchanger 8 , and sent to supercooling heat exchanger 15 .
  • the refrigerant flows into supercooling heat exchanger 15 through connection point 15 a, and flows out from supercooling heat exchanger 15 through connection point 15 b.
  • the liquid refrigerant supercooled by supercooling heat exchanger 15 is expanded by expansion valve 21 , and evaporated by the endothermic action of outdoor heat exchanger 5 .
  • the vapor refrigerant is supplied to main compressor 2 through four-way valve 24 , and compressed by main compressor 2 to be delivered again.
  • a part of the liquid refrigerant flowing from indoor heat exchanger 8 through main passage 26 is branched into branching passage 27 b so as to serve as the supercooling liquid refrigerant.
  • the branched refrigerant is expanded and cooled by expansion valve 22 so as to be changed into a wet low-temperature refrigerant.
  • the wet low-temperature refrigerant flows into supercooling heat exchanger 15 through connection point 15 c, supercools the refrigerant flowing in main passage 26 , and flows out from super cooling heat exchanger 15 through connection point 15 d.
  • on-off valve 28 a is closed and on-off valve 28 b is opened, so that the refrigerant flowing in main passage 26 is not branched into branching passage 27 a, but into branching passage 27 b.
  • the supercooling refrigerant branched into branching passage 27 b supercools the undivided liquid refrigerant before being branched.
  • the liquid refrigerant flowing out from supercooling heat exchanger 15 is radiated and evaporated by engine exhaust heat recovery unit 6 , and supplied to sub compressor 3 so as to be compressed and delivered again.
  • a system for controlling the engine heat pump of the present invention will be described with reference to FIG. 2 .
  • a controller 25 serves as a control unit provided in the engine heat pump of the present invention. Controller 25 is connected to expansion valve 21 for the outdoor heat exchanger, expansion valve 22 for the supercooling heat exchanger, and expansion valve 23 for the indoor heat exchanger, so as to control the respective expansion valves.
  • Controller 25 is also connected to on-off valves 28 a and 28 b provided on respective branching passages 27 a and 27 b.
  • On-off valves 28 a and 28 b are controlled as follows: On-off valve 28 a is opened for supercooling the liquid refrigerant in the cooling cycle, and closed in the other cases. On-off valve 28 b is opened for supercooling the liquid refrigerant in the heating cycle, and closed in the other cases.
  • the liquid refrigerant is branched at the downstream side of supercooling heat exchanger 15 , and the undivided whole liquid refrigerant before being branched is supercooled by supercooling heat exchanger 15 .
  • Controller 25 is connected to engine 4 (or a control circuit of engine 4 ), so as to control the on-off operation of engine 4 for driving main compressor 2 and sub compressor 3 .
  • controller 25 controls the opening of expansion valve 22 so that the wet refrigerant expanded by expansion valve 22 is overheated in passage 33 serving as the suction line of sub compressor 3 .
  • sub compressor 3 is selected (or configured) so that the refrigerant suction pressure of sub compressor 3 becomes higher than the refrigerant suction pressure of main compressor 2 , that is, as shown in the Moliere chart of FIG. 3 , a compression work ⁇ Ws by sub compressor 3 becomes smaller than a compression work ⁇ Wm by main compressor 2 , thereby reducing the total compression work of the engine heat pump in comparison with only the compression work ⁇ Wm for the whole refrigerant.
  • the Moliere chart of the refrigeration cycle due to the above refrigerant circuit system will be described with reference to the flow of refrigerant in the refrigerant circuit system.
  • the Moliere chart indicates a change of condition of refrigerant having a unit mass and a unit flow rate.
  • the axis of abscissas indicates a specific enthalpy (kJ/kg), which is an energy of 1 kg refrigerant.
  • the axis of ordinate indicates a (absolute) pressure (MPa abs).
  • a point Am on the Moliere chart defines a condition of the refrigerant flowing in passage 32 serving as the suction line of main compressor 2 .
  • the refrigerant is set to have a specific enthalpy h 2 (kJ/kg) and a pressure p 2 (MPa abs), and have a flow rate Gm.
  • a point As on the Moliere chart defines a condition of the refrigerant flowing in passage 33 serving as the suction line of sub compressor 3 .
  • the refrigerant is set to have a specific enthalpy h 1 (kJ/kg) and a pressure p 1 (MPa abs), and have a flow rate Gs.
  • the refrigerants set to have the above conditions at the respective points are supplied to respective compressors 2 and 3 , so as to be compressed.
  • Main compressor 2 performs compression work ⁇ Wm relative to the refrigerant having the unit mass and the unit flow rate (a compression process AmB).
  • Sub compressor 3 performs compression work ⁇ Ws relative to the refrigerant having the unit mass and the unit flow rate (a compression process AsB).
  • Go total flow rate
  • the joined high-pressurized vapor refrigerant is sent to outdoor heat exchanger 5 so as to be condensed and radiated, i.e., cooled, thereby being changed into the liquid refrigerant (a condensation process BC).
  • a point B defines a condition of the refrigerant flowing in the passage from confluence point 65 to outdoor heat exchanger 5 .
  • the refrigerant is set to have a specific enthalpy h 0 (kJ/kg).
  • the liquid refrigerant discharged from outdoor heat exchanger 5 is supercooled by the supercooling liquid refrigerant which has been branched into branching passage 27 a at the downward side of supercooling heat exchanger 15 (a supercooling process CD).
  • isothermal lines T 1 , T 2 and T 3 are set at respective constant temperatures t1(° C.), t2(° C.) and t3(° C.) (t1>t2>t3).
  • the chart indicates that supercooling heat exchanger 15 supercools the liquid refrigerant flowing in main passage 26 so as to reduce the temperature of the liquid refrigerant flowing in main passage 26 from t1(° C.) to t2(° C.).
  • the supercooled liquid refrigerant has a pressure p 0 (MPa abs) at a point D.
  • a part of the supercooled liquid refrigerant flowing in main passage 26 is branched, and the remaining supercooled liquid refrigerant is expanded by expansion valve 23 for the indoor heat exchanger, so as to be changed into a liquid refrigerant whose temperature and pressure are lower than those of an indoor air to be cooled (an expansion process DEm).
  • the low-temperature and low-pressurized liquid refrigerant is set to have a pressure p 2 (MPa abs) at a point Em.
  • the liquid refrigerant having gotten pressure p 2 at point Em is sent to indoor heat exchanger 8 , and indoor heat exchanger 8 absorbs heat from the indoor air so as to evaporate the refrigerant (an evaporation process EmAm).
  • the evaporated refrigerant flows through passage 32 serving as the suction line of main compressor 2 so as to be supplied to main compressor 2 .
  • pressure p 2 of the refrigerant is equaled to a refrigerant suction pressure Pm of main compressor 2 , and the flow rate of refrigerant absorbed into main compressor 2 becomes Gm.
  • the supercooling liquid refrigerant branched into the branching passage is expanded so as to have the pressure and temperature which are lower than those of the liquid refrigerant at point C (an evaporation process DEs).
  • the temperature of the supercooling refrigerant is reduced from t2(° C.) to t3(° C.).
  • a part of this supercooled liquid refrigerant by supercooling heat exchanger 15 is branched into branching passage 27 a so as to serve as the supercooling liquid refrigerant.
  • the liquid refrigerant branched into branching passage 27 a is set to have flow rate Gs.
  • the evaporation scale of the branched liquid refrigerant by expansion valve 22 is smaller than that of the liquid refrigerant by expansion valve 23 (evaporation process Dem) because of the following reason.
  • the only requirement for supercooling the liquid refrigerant flowing in main passage 26 by the supercooling refrigerant branched into branching passage 27 a is that the temperature of the supercooling refrigerant is lower than the liquid refrigerant (having the condition at point C) before being supplied to expansion valve 22 . That is, the supercooling effect is ensured even when the pressure drop of the refrigerant having the condition at point D is such a small degree between pressure p 0 and pressure p 1 .
  • the supercooling refrigerant having the condition at point Es absorbs heat from the liquid refrigerant flowing in main passage 26 , so as to supercool the liquid refrigerant flowing in main passage 26 (an evaporation process EsAs).
  • the supercooling refrigerant, having finished supercooling flows through passage 33 serving as the suction line of sub compressor 3 so as to be supplied to sub compressor 3 .
  • the evaporation scale of expansion valve 22 for expanding the liquid refrigerant having flow rate Gs branched into branching passage 27 a is smaller than that of expansion valve 23 for expanding the remaining liquid refrigerant having flow rate Gm remaining after being branched, so as to ensure a small pressure drop of the supercooling liquid refrigerant from pressure p 0 to pressure p 1 , thereby ensuring a high evaporation pressure p 1 in evaporation process EsAs.
  • the evaporation pressure of the branched supercooling liquid refrigerant having flow rate Gs is higher than the evaporation pressure of the remaining refrigerant having flow rate Gm after being branched, thereby greatly reducing compression work ⁇ Ws required for compression process AsB in comparison with compression work ⁇ Wm required for compression process AmB.
  • the compression work by sub compressor 3 is very small relative to the compression work by main compressor 2 , thereby reducing the total compression work of the engine heat pump.
  • the reduction of the compression work will be detailed.
  • the basis of comparison is the total compression work of the engine heat pump with the whole refrigerant having flow rate Go under only compression work ⁇ Wm.
  • this is a total compression work in a refrigerant circuit with no sub compressor, i.e., with only a single compressor performing compression work ⁇ Wm for the whole refrigerant having flow rate Go.
  • This compression work is equal to the total compression work when the pressure drop of the supercooling liquid refrigerant having flow rate Gs branched into branching passage 27 a in evaporation process DEs is set between pressure p 0 and p 2 .
  • sub compressor 3 is driven by engine 4 so as to compress the supercooling refrigerant subjected to evaporation pressure (pressure of refrigerant to be supplied to the compressor) which is higher than that for the refrigerant compressed by main compressor 2 . Therefore, the engine heat pump requires no additional electric power that is required for a conventional engine heat pump with an electromotive sub compressor. Therefore, the total compression work in the refrigeration cycle is reduced while ensuring or improving the cooling capacity due to the supercooling performance of supercooling heat exchanger 15 .
  • a capacity ratio between main compressor 2 and sub compressor 3 in the engine heat pump of the invention will now be described.
  • the capacity ratio between main compressor 2 and sub compressor 3 is referred to as a ratio between a delivery capacity of main compressor 2 and a delivery capacity of sub compressor 3 .
  • the delivery capacity of each of compressors 2 and 3 is determined based on its volumetric capacity and rotary speed.
  • the volumetric capacity is a volume of refrigerant supplied to each of compressors 2 and 3 per cycle of a rotor of corresponding compressor 2 or 3 (cc/cycle). Since main compressor 2 and sub compressor 3 are driven by common engine 4 , the rotary speed of each of compressors 2 and 3 is determined by a pulley ratio (speed ratio) of corresponding compressor 2 or 3 relative to a pulley of engine 4 .
  • the delivery capacity of each of compressors 2 and 3 is produced by multiplying the volumetric capacity and the pulley ratio.
  • main compressor 2 has a volumetric capacity Vm and a pulley ratio Um
  • sub compressor 3 has a volumetric capacity Vs and a pulley ratio Us
  • the delivery capacity of main compressor 2 is produced by Vm*Um
  • the delivery capacity of sub compressor 3 is produced by Vs*Us.
  • the capacity ratio of sub compressor 3 to the total capacity of main compressor 2 and sub compressor 3 (hereinafter, referred to as a sub compressor capacity ratio R) is calculated by the following formula.
  • R (Vs*Us)/ ⁇ (Vm*Um)+(Vs*Us) ⁇
  • sub compressor capacity ratio R is determined according to pulley ratios Um and Us of respective compressors 2 and 3 to engine 4 .
  • sub compressor capacity ratio R is determined according to volumetric capacities Vm and Vs.
  • the delivery capacity of sub compressor 3 is smaller than that of main compressor 2 .
  • Sub compressor capacity ratio R(%) ranges between 20% and 29%. Description will be given of this range of sub compressor capacity ratio R.
  • variation of sub compressor capacity ratio R is reflected in variation of the ratio of flow rate Gs of the supercooling liquid refrigerant branched from main passage 26 into branching passage 27 a (in the cooling cycle) or 27 b (in the heating cycle) to flow rate Go of the whole liquid refrigerant.
  • sub compressor capacity ratio R increases, the ratio of flow rate Gs to flow rate Go increases.
  • sub compressor capacity ratio R decreases, the ratio of flow rate Gs to flow rate Go decreases.
  • the upper limit 29% is determined based on variation of driving efficiency (energy efficiency) in the cooling cycle (for cooling).
  • driving efficiency energy efficiency
  • flow rate Gs of the branched liquid refrigerant increases i.e., the amount of the supercooling liquid refrigerant for supercooling the undivided liquid refrigerant having flow rate Go flowing in main passage 26 increases so as to enhance the cooling capacity of the main liquid refrigerant per unit mass and unit flow rate.
  • flow rate Gm of the main liquid refrigerant decreases so as to reduce the cooling capacity of indoor heat exchanger 8 .
  • This phenomenon defines the variation of driving efficiency (energy efficiency) for defining the upper limit of sub compressor capacity ratio R.
  • the upper limit 29% of sub compressor capacity ratio R is determined based on measurement data indicated as graphs of FIG. 4 .
  • the graphs of FIG. 4 are defined by the axis of abscissas indicating sub compressor capacity ratio R and the axis of ordinate indicating coefficient of performance (COP) in the refrigeration cycle.
  • COP is obtained by dividing the cooling or heating capacity by the quantity of consumed fuel. As COP increases, the driving efficiency (energy efficiency) is enhanced.
  • a dotted graph indicates COP of a refrigerant circuit system with no sub compressor, i.e., with only a single compressor.
  • sub compression capacity ratio R when sub compression capacity ratio R is smaller than approximate 30%, COP under the cooling operation is kept larger than COP by the conventional system. This is the reason why the upper limit of sub compressor capacity ratio R is set to 29% according to the present invention. Incidentally, COP under the heating operation is constantly larger than COP by the conventional system regardless of sub compression capacity ratio R.
  • connection point 15 a serves as a refrigerant inlet for introducing the refrigerant from main passage 26 to supercooling heat exchanger 15
  • connection point 15 b serves as a refrigerant outlet for discharging the refrigerant from supercooling heat exchanger 15 to main passage 26 .
  • the lower limit 20% of sub compressor capacity ratio R is determined based on the relation of the refrigerant temperature at connection point 15 a (hereinafter referred to as “inlet temperature”) to the refrigerant temperature at connection point 15 b (hereinafter referred to as “outlet temperature”) during the heating operation.
  • flow rate Gs of the branched liquid refrigerant branched into branching passage 27 b decreases, i.e., the amount of the supercooling liquid refrigerant for supercooling the undivided liquid refrigerant having flow rate Go flowing in main passage 26 decreases so as to reduce the supercooling effect of supercooling heat exchanger 15 . Accordingly, the branched liquid refrigerant tends to be easily evaporated.
  • flow rate Gs of branched liquid refrigerant decreases
  • flow rate Gm of the main liquid refrigerant increases so that the undivided liquid refrigerant having flow rate Go is insufficiently supercooled by supercooling heat exchanger 15 . That is, in supercooling heat exchanger 15 , the outlet temperature rises while the inlet temperature is kept constant. This outlet temperature rising relative to the inlet temperature in supercooling heat exchanger 15 is obstacle to the sufficient supercooling action of supercooling heat exchanger 15 .
  • sub compressor 3 has to be selected (or configured) in its capacity for ensuring the enough supercooling degree, i.e., a difference of the inlet temperature of the supercooling refrigerant from the outlet temperature of the supercooling refrigerant after supercooling has to be not lower than a certain level (e.g., 5° C.).
  • the lower limit of sub compression capacity range R is set so as to ensure the enough supercooling degree.
  • the lower limit 20% of sub compressor capacity ratio R is determined based on measurement data indicated as graphs of FIG. 5 .
  • the graphs of FIG. 5 are defined by the axis of abscissas indicating sub compressor capacity ratio R and the axis of ordinate indicating the inlet or outlet temperature (° C.) of supercooling heat exchanger 15 under the heating operation.
  • the inlet temperature of supercooling heat exchanger 15 is substantially kept constant (32-33° C.) regardless of sub compressor capacity ratio R.
  • the outlet temperature of supercooling heat exchanger 15 increases from a value lower than the inlet temperature to a value higher than the inlet temperature.
  • the relation between the inlet temperature and the outlet temperature is preferably set so that the outlet temperature is lower than the inlet temperature by a temperature difference that is not less than approximate 5° C.
  • a critic value (lower limit) of sub compressor capacity ratio R for reducing the outlet temperature lower than the inlet temperature by the difference that is not less than approximate 5° C. is 20%. This is the reason why the lower limit of sub compressor capacity ratio R is set to 20% according to the present invention.
  • the upper limit of sub compressor capacity ratio R is determined in due consideration of the cooling operation, and the lower limit of sub compressor capacity ratio R is determined in due consideration of the heating operation, so that sub compressor capacity ratio R ranges between 20% and 29%, thereby ensuring or improving the cooling capacity during the cooling operation, and thereby ensure the performance of supercooling heat exchanger 15 during the heating operation.
  • the engine heat pump according to the present invention ensures a good driving efficiency (energy efficiency) because common engine 4 drives main compressor 2 and sub compressor 3 , and because sub compressor capacity range R ranges between 20% and 29%.
  • a continuously variable transmission can be adapted to transmit power from engine 4 to main compressor 2 and sub compressor 3 .
  • the CVT is set so as to change a speed ratio between main compressor 2 and sub compressor 3 in due consideration of the critic values of sub compressor capacity ratio R in the respective cases of cooling operation and heating operation.
  • any sub compressor ratio R is allowed only if it does not exceed the upper limit, and during the heating operation, any sup compressor ratio R is allowed only if it is not smaller than the lower limit. Therefore, the CVT is configured so as to change the speed ratio due to whether the engine heat pump is operated for cooling or heating, so that sub compressor capacity ratio R under the cooling operation is less than approximate 30%, and sub compressor capacity ratio R under the heating operation is not less than 20%.
  • the engine heat pump of the invention is provided with engine exhaust recovery unit 6 in parallel to outdoor heat exchanger 5 .
  • the supercooling liquid refrigerant branched from main passage 26 is evaporated by engine exhaust heat recovery unit 6 , and compressed by sub compressor 3 .
  • Engine exhaust heat recovery unit 6 is adapted to evaporate the endothermic branched liquid refrigerant having passed through supercooling heat exchanger 15 under the heating operation.
  • the branched liquid refrigerant exchanges heat with engine cooling water CW having a higher temperature than the branched liquid refrigerant, i.e., absorbs heat from engine cooling water CW so as to be evaporated.
  • point B defines the condition of refrigerant on the way from confluence point 65 to indoor heat exchanger 8 .
  • the liquid refrigerant discharged from indoor heat exchanger 8 is supercooled in supercooling heat exchanger 15 by the supercooling refrigerant branched into branching passage 27 b at the downstream side of supercooling heat exchanger 15 (a supercooling process CD).
  • a part of the supercooled liquid refrigerant flowing in main passage 26 is branched, and the remaining supercooled liquid refrigerant is expanded by expansion valve 21 so as to be changed into a low-temperature and low-pressurized liquid refrigerant (an expansion process DEm).
  • the liquid refrigerant having the condition at point Em is sent to outdoor heat exchanger 5 .
  • the refrigerant absorbs heat from an outdoor air so as to be evaporated (an evaporation process EmAm).
  • the vapor refrigerant flows in passage 32 serving as the suction line of main compressor 2 so as to be sucked to main compressor 2 again.
  • the supercooling liquid refrigerant branched into branching passage 27 b is expanded by expansion valve 22 so as to have pressure and temperature lower than the pressure and temperature of the refrigerant at point C (an expansion process DEs).
  • a part of the liquid refrigerant supercooled by supercooling heat exchanger 15 is branched into branching passage 27 b so as to serve as the supercooling refrigerant having flow rate Gs.
  • the supercooling liquid refrigerant having the condition at point Es absorbs heat from the liquid refrigerant flowing in main passage 26 so as to supercool the liquid refrigerant flowing in main passage 26 .
  • the supercooling liquid refrigerant having passed through supercooling heat exchanger 15 is sent to engine exhaust heat recovery unit 6 .
  • the supercooling liquid refrigerant exchanges heat with engine cooling water CW, i.e., absorbs heat from engine cooling water CW so as to be evaporated (an evaporation process EsAs).
  • the evaporated refrigerant flows in passage 33 serving as the suction line of sub compressor 3 so as to be sucked into sub compressor 3 again.
  • the supercooling is performed so as to improve the driving efficiency (energy efficiency) by the following action.
  • the undivided liquid refrigerant having the total flow rate Go flowing in main passage 26 is supercooled by supercooling heat exchanger 15 .
  • the supercooled liquid refrigerant increases its endothermic reaction capacity per unit mass and unit flow rate (kJ/kg). Therefore, when the supercooled liquid refrigerant reaches outdoor heat exchanger 5 , the supercooled liquid refrigerant has an increased capacity per unit mass and unit flow rate for absorbing heat from the outdoor air. That is, the supercooled refrigerant can absorb heat as much as that absorbed by a non-supercooled refrigerant even if the supercooled refrigerant is less than the non-supercooled refrigerant.
  • flow rate Gm of the main liquid refrigerant sent into outdoor heat exchanger 5 under the heating operation can be reduced so as to reduce total flow rate Go of the refrigerant circulating in the refrigeration cycle.
  • the total compression work in the refrigeration cycle can be reduced so as to improve the driving efficiency (energy efficiency).
  • main compressor 2 and sub compressor 3 which are driven by engine 4 , may be operable individually. Due to this configuration, one or both of main compressor 2 and sub compressor 3 is/are selectively driven in correspondence to the rate of air-conditioning load, thereby improving the driving efficiency (energy efficiency).
  • a main compressor clutch 42 is interposed between main compressor 2 and engine 4 so as to selectively drivingly connect or disconnect main compressor 2 to and from engine 4
  • a sub compressor clutch 43 is interposed between sub compressor 3 and engine 4 , so as to selectively drivingly connect or disconnect sub compressor 3 to and from engine 4 .
  • Passage 33 serving as the suction line of sub compressor 3 to passage 32 serving as the suction of main compressor 2 through a connection passage 34 with an on-off valve 35 .
  • On-off valve 35 on connection passage 34 is opened to connect passages 32 and 33 to each other, and closed to separate passages 32 and 33 from each other, thereby forming a refrigerant circuit in correspondence to each of a low air-conditioning load rate, a middle air-conditioning load rate and a high air-conditioning load rate.
  • controller 25 is connected to main compressor clutch 42 and sub compressor clutch 43 so as to control the engagement and disengagement operation of each of clutches 42 and 43 , and is connected to on-off valve 35 so as to control the opening and closing operation of on-off valve 35 .
  • the low air-conditioning load rate ranges between 0% and 15%
  • the middle air-conditioning load rate ranges between 15% and 60%
  • the high air-conditioning load rate ranges between 60% and 100%.
  • the engine heat pump is controlled for cooing as follows:
  • controller 25 disengages main compressor clutch 42 , and opens on-off valve 35 . Therefore, the driving power of engine 4 is transmitted to only sub compressor 3 , and passage 32 serving as the suction line of main compressor 2 is connected to passage 33 serving as the suction line of sub compressor 3 , so that sub compressor 3 compresses the whole refrigerant having flow rate Go.
  • Supercooling heat exchanger 15 is exercised or not depending on the control of opening and closing operation of expansion valve 22 for the supercooling heat exchanger. To exercise supercooling heat exchanger 15 for the supercooling, the pressure relation at a confluence point 64 (see FIG. 1 ) is considered to reduce the pressure loss. Controller 25 controls the opening degrees of respective expansion valves 22 and 23 so as to substantially equalize the pressure of refrigerant from passage 33 to the pressure of refrigerant from passage 32 .
  • controller 25 When the air-conditioning load rate is middling, only main compressor 2 is driven. In this case, controller 25 disengages sub compressor clutch 43 , so as to transmit the driving power of engine 4 to only main compressor 2 , so that main compressor 2 compresses the whole refrigerant having flow rate Go. To exercise supercooling heat exchanger 15 for the supercooling, controller 25 opens on-off valve 35 and controls the opening degrees of respective expansion valves 22 and 23 , so that, at a confluence point 63 (see FIG. 1 ), the pressure of refrigerant from passage 33 is substantially equal to the pressure of refrigerant from passage 32 .
  • controller 25 engages main compressor clutch 42 and sub compressor clutch 43 , and closes on-off valve 35 . Therefore, the driving power of engine 4 is transmitted to main and sub compressors 2 and 3 , and simultaneously, passages 32 and 33 are separated from each other, so that main compressor 2 compresses the refrigerant having flow rate Gm, and sub compressor 3 compresses the supercooling refrigerant having flow rate Gs.
  • the engine heat pump is controlled for heating as follows:
  • control pattern with controller 25 is similar to the control during the cooling operation under the low air-conditioning load rate.
  • controller 25 disengages sub compressor clutch 43 to transmit the driving power of engine 4 to only main compressor 2 , and opens on-off valve 35 to exercise engine exhaust heat recovery unit 6 for the heat exchange, so that main compressor 2 compresses the whole refrigerant having flow rate Go joined at confluence point 63 .
  • controller 25 opens on-off valve 35 and controls the opening degrees of respective expansion valves 22 and 23 , so that, at confluence point 63 , the pressure of refrigerant from passage 33 is substantially equal to the pressure of refrigerant from passage 32 .
  • controller 25 engages main compressor clutch 42 and sub compressor clutch 43 , and closes on-off valve 35 . Therefore, the driving power of engine 4 is transmitted to main and sub compressors 2 and 3 , and simultaneously, passages 32 and 33 are separated from each other, so that main compressor 2 compresses the refrigerant having flow rate Gm, and sub compressor 3 compresses the supercooling refrigerant having flow rate Gs under the heat exchanging by engine exhaust heat recovery unit 6 .
  • main and sub compressors 2 and 3 is/are selectively driven in correspondence to the rate of required air-conditioning load, so as to reduce a load part of the engine heat pump where the fuel efficiency of engine 4 is reduced, thereby improving the driving efficiency (energy efficiency) of the engine heat pump.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
US11/569,429 2004-05-20 2005-04-18 Engine Heat Pump Abandoned US20070295025A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2004150371A JP4336619B2 (ja) 2004-05-20 2004-05-20 エンジンヒートポンプ
JP2004-150371 2004-05-20
PCT/JP2005/007411 WO2005114064A1 (ja) 2004-05-20 2005-04-18 エンジンヒートポンプ

Publications (1)

Publication Number Publication Date
US20070295025A1 true US20070295025A1 (en) 2007-12-27

Family

ID=35428465

Family Applications (1)

Application Number Title Priority Date Filing Date
US11/569,429 Abandoned US20070295025A1 (en) 2004-05-20 2005-04-18 Engine Heat Pump

Country Status (5)

Country Link
US (1) US20070295025A1 (ja)
EP (1) EP1762792A4 (ja)
JP (1) JP4336619B2 (ja)
CN (1) CN100470165C (ja)
WO (1) WO2005114064A1 (ja)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2009230171B2 (en) * 2008-03-24 2012-02-02 Yanmar Power Technology Co., Ltd Engine-driven heat pump
JP2013142487A (ja) * 2012-01-10 2013-07-22 Hitachi Appliances Inc 冷凍装置及び冷凍機ユニット
US20160265815A1 (en) * 2013-12-12 2016-09-15 Johnson Controls Technology Company Steam turbine driven centrifugal heat pump

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008145002A (ja) * 2006-12-07 2008-06-26 Sanyo Electric Co Ltd 空気調和装置
JP5163161B2 (ja) * 2008-02-01 2013-03-13 ダイキン工業株式会社 暖房用補助ユニットおよび空気調和装置
FR2956190B1 (fr) * 2010-02-08 2012-04-13 Muller & Cie Soc Pompe a chaleur a etages de puissance
KR101212681B1 (ko) * 2010-11-08 2012-12-17 엘지전자 주식회사 공기조화기
KR101497813B1 (ko) * 2013-06-27 2015-03-04 한국교통대학교산학협력단 증기분사 히트펌프 시스템 및 그 작동방법
CN105466063A (zh) * 2015-12-16 2016-04-06 珠海格力电器股份有限公司 一种热泵系统
CN105588357B (zh) * 2015-12-16 2019-04-16 珠海格力电器股份有限公司 一种热泵系统
CN106766327A (zh) * 2016-11-29 2017-05-31 珠海格力电器股份有限公司 空调器
CN106801953A (zh) * 2016-11-29 2017-06-06 珠海格力电器股份有限公司 空调器
KR102105706B1 (ko) * 2017-12-12 2020-04-28 브이피케이 주식회사 히트펌프 시스템, 이의 양방향 인젝션 운전 방법
US11906226B2 (en) * 2018-04-16 2024-02-20 Carrier Corporation Dual compressor heat pump
CN110173912B (zh) * 2019-04-29 2020-10-02 同济大学 一种带机械热回收的混合工质压缩循环系统及工作方法

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2242588A (en) * 1938-02-07 1941-05-20 Honeywell Regulator Co Heating system
US2273281A (en) * 1938-07-11 1942-02-17 Honeywell Regulator Co Control system

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60226669A (ja) * 1984-04-24 1985-11-11 三洋電機株式会社 冷凍装置
JPS62293066A (ja) * 1986-06-12 1987-12-19 ヤンマーディーゼル株式会社 エンジン駆動型ヒ−トポンプ式空調機
JPH0618121A (ja) * 1992-06-30 1994-01-25 Nippondenso Co Ltd エンジン駆動ヒートポンプ空調装置
CN1205073A (zh) * 1996-08-14 1999-01-13 大金工业株式会社 空调机
JPH11193966A (ja) * 1997-12-28 1999-07-21 Tokyo Gas Co Ltd ガスヒートポンプ装置
JPH11248264A (ja) * 1998-03-04 1999-09-14 Hitachi Ltd 冷凍装置
JP4214021B2 (ja) * 2003-08-20 2009-01-28 ヤンマー株式会社 エンジンヒートポンプ

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2242588A (en) * 1938-02-07 1941-05-20 Honeywell Regulator Co Heating system
US2273281A (en) * 1938-07-11 1942-02-17 Honeywell Regulator Co Control system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2009230171B2 (en) * 2008-03-24 2012-02-02 Yanmar Power Technology Co., Ltd Engine-driven heat pump
JP2013142487A (ja) * 2012-01-10 2013-07-22 Hitachi Appliances Inc 冷凍装置及び冷凍機ユニット
US20160265815A1 (en) * 2013-12-12 2016-09-15 Johnson Controls Technology Company Steam turbine driven centrifugal heat pump
KR101816656B1 (ko) 2013-12-12 2018-01-09 존슨 컨트롤스 테크놀러지 컴퍼니 증기터빈 구동식 원심형 히트펌프
US10704810B2 (en) * 2013-12-12 2020-07-07 Johnson Controls Technology Company Steam turbine driven centrifugal heat pump

Also Published As

Publication number Publication date
EP1762792A4 (en) 2008-05-07
EP1762792A1 (en) 2007-03-14
JP4336619B2 (ja) 2009-09-30
JP2005331177A (ja) 2005-12-02
CN100470165C (zh) 2009-03-18
CN1957211A (zh) 2007-05-02
WO2005114064A1 (ja) 2005-12-01

Similar Documents

Publication Publication Date Title
US11320170B2 (en) Heat pump cycle
CN203249455U (zh) 空调装置
US9341393B2 (en) Refrigerating cycle apparatus having an injection circuit and operating with refrigerant in supercritical state
US20070295025A1 (en) Engine Heat Pump
EP3217121B1 (en) Outdoor unit for air conditioner and method for controlling air conditioner
JP2020183857A (ja) 電気自動車用ヒートポンプシステム及びその制御方法
EP2792974B1 (en) Air conditioner and method for controlling the same
WO2009147826A1 (ja) 冷凍サイクル装置
US11448433B2 (en) Refrigeration apparatus
CN113891635A (zh) 冷站单元、集成冷站系统及其控制方法和相关设备
EP3217120B1 (en) Outdoor unit for air conditioner
US20100000248A1 (en) Refrigeration system
EP3770532A1 (en) Air-conditioning apparatus
JP2024043209A (ja) 車両用の温調システムおよび温調方法
JP2016138715A (ja) ヒートポンプ
US12460852B2 (en) Heat pump
JP5018020B2 (ja) 冷凍サイクル装置
KR100743753B1 (ko) 냉장고 및 냉장고의 제어 방법
JP2012207866A (ja) 空気調和機
JP2006234321A (ja) 室外ユニットおよび空気調和装置
JP2017156050A (ja) 空気調和機
CN114729767A (zh) 用于制冷装置的中间机组及制冷装置
KR102895359B1 (ko) 가스 히트펌프 시스템 및 그 제어방법
EP3217122B1 (en) Outdoor unit for air conditioner
JP6569081B2 (ja) 空気調和機

Legal Events

Date Code Title Description
AS Assignment

Owner name: YANMAR CO., LTD., JAPAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:MINAMI, KEN-ICHI;FUKUDOME, JIROU;AZUMA, HIROSHI;AND OTHERS;REEL/FRAME:018962/0931

Effective date: 20061113

STCB Information on status: application discontinuation

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