The present invention relates to a cooling cycle suited for use in automotive air-conditioning systems, and more particularly, to a cooling cycle using supercritical or transcritical refrigerant such as CO2.
The cooling cycle for automotive air conditioners uses fluorocarbon refrigerant such as CFC12, HFC134a or the like. When released into the atmosphere, fluorocarbon can destroy an ozone layer to cause environmental problems such as global warming. On this account, the cooling cycle has been proposed which uses CO2, ethylene, ethane, nitrogen oxide or the like in place of fluorocarbon.
The cooling cycle using CO2 refrigerant, is similar in operating principle to the cooling cycle using fluorocarbon refrigerant except the following. Since the critical temperature of CO2 is about 31° C., which is remarkably lower than that of fluorocarbon (e.g. 112° C. for CFC12), the temperature of CO2 in a gas cooler or condenser becomes higher than the critical temperature thereof in the summer months where the outside-air temperature rises, for example, CO2 does not condense even at the outlet of the gas cooler.
The conditions of the outlet of the gas cooler are determined in accordance with the compressor discharge pressure and the CO2 temperature at the gas-cooler outlet. And the CO2 temperature at the gas-cooler outlet is determined in accordance with the heat-radiation capacity of the gas cooler and the outside-air temperature. However, since the outside-air temperature cannot be controlled, the CO2 temperature at the gas-cooler outlet cannot be controlled practically. On the other hand, since the gas-cooler-outlet conditions can be controlled by regulating the compressor discharge pressure, i.e. the refrigerant pressure at the gas-cooler outlet, the refrigerant pressure at the gas-cooler outlet is increased to secure sufficient cooling capacity or enthalpy difference during the summer months where the outside-air temperature is higher.
Specifically, the cooling cycle using fluorocarbon refrigerant has 0.2-1.6 Mpa refrigerant pressure in the cycle, whereas the cooling cycle using CO2 refrigerant has 3.5-10.0 Mpa refrigerant pressure in the cycle, which is remarkably higher than in the fluorocarbon cooling cycle.
An attempt has been made in the cooling cycle using supercritical refrigerant to enhance the ratio of the cooling capacity of an evaporator to the workload of a compressor, i.e. coefficient of performance (COP). U.S. Pat. No. 5,245,836 issued Sep. 21, 1993 to Lorentzen, et al. proposes enhancement in COP by carrying out heat exchange between refrigerant that has passed through the evaporator and supercritical-area refrigerant that is present in a high-pressure line. In the cooling cycle including such internal heat exchanger, refrigerant is further cooled by the heat exchanger to reach a throttling valve. This leads to still lower temperature of refrigerant at the inlet of the throttling valve, which provides maximum COP.
Even in the cooling cycle including such internal heat exchanger, when the cooling cycle is in the high-load state where the outside-air temperature is higher than, for example, 30° C., and the vehicle is at a standstill where the velocity of cooling air for the gas cooler is low, the radiation performance of the gas cooler is remarkably degraded. As a result, the temperature of refrigerant at the gas-cooler outlet is not sufficiently lowered, thus degrading the cooling performance of the evaporator.
It is, therefore, an object of the present invention to provide a cooling cycle which can provide sufficient cooling performance even when the radiation effect of the gas cooler is lower.
The present invention provides generally a cooling cycle, which comprises: a compressor that compresses a refrigerant; a gas cooler that cools the compressed refrigerant; a throttling device that throttles flow of the cooled refrigerant; an evaporator that cools intake air by a heat absorbing action of the cooled refrigerant; and a heat exchanger arranged between the compressor and the throttling device, the heat exchanger carrying out heat exchange through the compressed refrigerant.
The other objects and features of the present invention will become apparent from the following description with reference to the attached drawings, wherein:
Referring to the drawings, a description is made with regard to preferred embodiments of the cooling cycle according to the present invention.
Referring to
The compressor 1 is driven by a prime mover such as engine or motor to compress a CO2 refrigerant in the gaseous phase and discharge the high-temperature high-pressure refrigerant to the gas cooler 2. The compressor 1 may be of any type such as variable-displacement type wherein automatic control of the discharge quantity and pressure of refrigerant is carried out internally or externally in accordance with the conditions of refrigerant in a cooling cycle, constant-displacement type with rotational-speed control capability or the like.
The heat exchanger 10 carries out heat exchange between the high-temperature high-pressure refrigerant discharged from the compressor 1 and a coolant or cooling water of an engine or automotive prime mover 11. The coolant is provided by a water pump, not shown, to the heat exchanger 10 through a coolant line 12, which is led to a heater core or heating device 13 arranged in the vehicle cabin, then returned to the engine 11. Note that the direction of flow of the coolant is shown by dotted arrow in
The gas cooler 2 carries out heat exchange between the high-temperature high-pressure CO2 refrigerant compressed by the compressor 1 and subjected to passage through the heat exchanger 10 and the outside air or the like for cooling of the refrigerant. The gas cooler 2 is provided with a cooling fan 6 for allowing acceleration of heat exchange or implementation thereof even when the vehicle is at a standstill. In order to cool the refrigerant within the gas cooler 2 up to the outside-air temperature as closely as possible, the gas cooler 2 is arranged at the front of the vehicle, for example.
The internal heat exchanger 9 carries out heat exchange between the CO2 refrigerant flowing from the gas cooler 2 and the refrigerant flowing from the trap 5. During operation, heat is dissipated from the former refrigerant to the latter refrigerant.
The pressure control valve or pressure-reducing valve 3 reduces the pressure of CO2 refrigerant by making the high-pressure (about 10 Mpa) refrigerant flowing from the internal heat exchanger 9 pass through a pressure-reducing hole. The pressure control valve 3 caries out not only pressure reduction of the refrigerant, but pressure control thereof at the outlet of the gas cooler 2. The refrigerant with the pressure reduced by the pressure control valve 3, which is in the two-phase (gas-liquid) state, flows into the evaporator 4. The pressure control valve 3 may be of any type such as duty-ratio control type wherein the opening/closing duty ratio of the pressure-reducing hole is controlled by an electric signal, etc.
The evaporator 4 is accommodated in a casing of an automotive air-conditioning unit, for example, to provide cooling for air vented into the vehicle cabin. Air taken in from the outside or the cabin by a fan 7 is cooled by the passage through the evaporator 4, which is discharged from a vent, not shown, to a desired position in the cabin. Specifically, when evaporating or vaporizing in the evaporator 4, the two-phase CO2 refrigerant flowing from the pressure control valve 3 absorbs latent heat of vaporization from introduced air for cooling thereof. The heater core 13 is arranged downstream of the evaporator 4, at the front of which an air mixing door 15 is arranged rotatably. When heating intake air, the air mixing door 15 is rotated in a position shown by broken line in
The trap 5 separates the CO2 refrigerant that has passed through the evaporator 4 into a gaseous-phase portion and a liquid-phase portion. Only the gaseous-phase portion is returned to the compressor 1, and the liquid-phase portion is temporarily accumulated in the trap 5.
Referring to
The refrigerant precooled by the heat exchanger 10 is cooled further by the gas cooler 2(c-d). Then, the refrigerant is reduced in pressure by the pressure control valve 3(d-e), which makes the refrigerant fall in the two-phase (gas-liquid) state. The two-phase refrigerant is evaporated in the evaporator 4(e-f) to absorb latent heat of vaporization from introduced air for cooling thereof. Such operation of the cooling cycle allows cooling of air introduced in the air-conditioning unit, which is vented into the cabin for cooling thereof.
In the trap 5, the refrigerant that has passed through the evaporator 4 is separated into a gaseous-phase portion and a liquid-phase portion. Only the gaseous-phase portion passes through the internal heat exchanger 9 to absorb heat (f-a), and is inputted again to the compressor 1.
In such a way, the heat exchanger 10 is arranged at the outlet of the compressor 1 to precool the high-temperature refrigerant to be provided to the gas cooler 2. Thus, even when the cooling capacity of the gas cooler 2 is degraded temporarily due to higher outside-air temperature and vehicle standstill, the refrigerant that has passed through the gas cooler 2 is sufficiently low in temperature, allowing preservation of the cooling capacity of the evaporator 4.
On the other hand, fulfillment of sufficient heating capacity is desired due to lower outside-air temperature, the air mixing door 15 arranged in front of the heater core 13 is rotated in the position shown by broken line in
In the first embodiment, the heat exchanger 10 is arranged in the refrigerant line 8 at the position between the compressor 1 and the gas cooler 2. Optionally, when a space for the heat exchanger 10 is difficult to secure in the engine room, it is recommended to adopt the following embodiment.
Specifically, in the second embodiment, referring to
Referring to
In this embodiment, the heat exchanger 10 is constructed by arranging the refrigerant line 8 between the compressor 1 and the gas cooler 2 through the upper tank 171 of the radiator 17, i.e. it is of the double-tube structure having the refrigerant line 8 arranged inside the upper tank 171. The heat exchanger 10 may be constructed by arranging the refrigerant line 8 through the lower tank 174. However, arrangement in the upper tank 171, i.e. at the inlet of the radiator 17 is preferable to arrangement in the lower tank 174, i.e. at the outlet of the radiator 17 in view of easy control of the coolant at an optimum temperature. Note that the present invention is applicable to the cooling cycle having the heat exchanger 10 arranged at the outlet of the radiator 17.
In view of the efficiency of heat exchange, it is preferable to oppose the direction of the coolant flowing into the upper tank 171 to that of the refrigerant flowing down therein, i.e. to form counter flow. Note that the present invention is applicable not only to the cooling cycle having counter flow, but the cooling cycle having forward flow.
Referring to
Referring to
As shown in
Having described the present invention in connection with the preferred embodiments, it is to be understood that the present invention is not limited thereto, and various changes and modifications can be made without departing from the scope of the present invention.
By way of example, in the illustrative embodiments, the heat exchanger 10 is arranged between the compressor 1 and gas cooler 2. Alternatively, the heat exchanger 10 may be arranged between the compressor 1 and the pressure control valve 3. Moreover, in the illustrative embodiments, the pressure control valve 3 is of the electric type. Alternatively, the pressure control valve 3 may be of the mechanical expansion type wherein the valve opening degree is adjusted by detecting the pressure and temperature of the high-pressure side refrigerant. In this alternative, a high-pressure side refrigerant pressure detecting part and a high-pressure side refrigerant temperature detecting part are arranged to ensure communication between a valve main body and the gas cooler 2 and internal heat exchanger 9. Further, the internal heat exchanger 9, which is arranged in the illustrative embodiments, can be eliminated if required. Furthermore, the coolant may be a coolant for a drive motor for electric vehicles or a coolant for a generating unit for fuel cell powered vehicles.
As described above, according to the present invention, the heat exchanger is arranged between the compressor and the pressure control valve for carrying out heat exchange through the refrigerant. With this, the temperature of the refrigerant provided to the gas cooler is reduced in advance, so that even when the radiation effect of the gas cooler is low, the temperature of the refrigerant at the outlet of the gas cooler is lowered relatively, resulting in securing of the cooling performance of the evaporator.
Moreover, according to the present invention, the heat exchanger is constructed to allow circulation of an engine coolant therethrough. Since the engine-coolant system is indispensable for the vehicle, the requirement is only extension of its line without any arrangement of additional cooling means, having an advantage in terms of manufacturing cost and space. Further, at engine start, the engine coolant is heated by the high-temperature refrigerant at the outlet of the compressor, contributing to shortening of an engine worm up time.
Furthermore, according to the present invention, the heat exchanger is integrated with an automotive radiator. This allows arrangement of the heat exchanger with practically no taking-up of a space in the engine room.
Number | Date | Country | Kind |
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2001-212274 | Jul 2001 | JP | national |
2002-193065 | Jul 2002 | JP | national |
The present application is a divisional of U.S. application Ser. No. 11/221,986, filed Sep. 9, 2005, which is a divisional of U.S. application Ser. No. 10/191,809, filed Jul. 10, 2002, the entire contents of which is incorporated herein by reference.
Number | Date | Country | |
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Parent | 11221986 | Sep 2005 | US |
Child | 11452222 | Jun 2006 | US |
Parent | 10191809 | Jul 2002 | US |
Child | 11221986 | Sep 2005 | US |