KR20100078074A - System of heat pump for cooling and heating of middle pressure cycle for air heat source - Google Patents
System of heat pump for cooling and heating of middle pressure cycle for air heat source Download PDFInfo
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- KR20100078074A KR20100078074A KR1020080136218A KR20080136218A KR20100078074A KR 20100078074 A KR20100078074 A KR 20100078074A KR 1020080136218 A KR1020080136218 A KR 1020080136218A KR 20080136218 A KR20080136218 A KR 20080136218A KR 20100078074 A KR20100078074 A KR 20100078074A
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- heat exchanger
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- refrigerant
- plate heat
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B13/00—Compression machines, plants or systems, with reversible cycle
-
- 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
- F25B2400/05—Compression system with heat exchange between particular parts of the system
- F25B2400/051—Compression system with heat exchange between particular parts of the system between the accumulator and another part of the cycle
-
- 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
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- 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)
Abstract
The present invention relates to a device having excellent cooling and heating efficiency in a cold district.
The discharge part and seal of the booster compressor 11 which compresses the medium-medium pressure refrigerant evaporated from the tank 5.
Discharge part of the main compressor (1) for compressing the low temperature low pressure refrigerant evaporated in the outer heat exchanger (9)
Are connected to each other and the refrigerant condenser of the plate heat exchanger (3) by mutual extrusion action
It is a device that increases heating rate and improves heating efficiency.
The low temperature low pressure liquid refrigerant passing through the second expansion side (8) is evaporated using the external air of
When cooling, the condenser is converted to a condenser to condense the refrigerant of high temperature and high pressure gas.
An outdoor side heat exchanger 9 on which the fan 10 is mounted; Hot water tank
Hot water is heated to supply hot water, and when cooled, it is switched to an evaporator
And plate heat exchanger (3) to supply; The plate heat exchanger (3) outlet pipe heat and the first
Hue produces medium-temperature medium pressure by evaporation by heat exchange with liquid refrigerant passing through expansion valve (7)
A tank (5); The medium-pressure medium pressure refrigerant vapor evaporated from the flash tank (5) is a medium pressure pipe (MP)
A medium pressure side booster compressor (11) for sucking through and supplying the plate to the plate heat exchanger (3); The second
After passing through the expansion valve (8) of low temperature low pressure evaporated in the outdoor heat exchanger (9) by the outside air
A low pressure side main compressor (1) for sucking gas and supplying it to the plate heat exchanger (3); The outdoor side
The liquid refrigerant which has not been evaporated in the heat exchanger (9) is overheated in the fresh tank (5) again, and the main pressure
After preventing the liquid compression of the accumulator (1), it is a cooling and heating device to increase the heating efficiency by increasing the amount of refrigerant supplied to the plate heat exchanger (3).
Description
In the present invention, even if the outside temperature is lower than about 15 ℃, cold inside the system
Maintain hot water temperature of 60 ℃ or higher and keep hot water
Keeping the temperature at a high temperature ensures stability and efficiency at heating and cooling
To overcome the medium pressure cycle heating and cooling heat pump system
Invention.
In general, heating and cooling heat pump systems are characterized by selective bidirectional flow of refrigerant.
During the summer season, the heat from the high pressure side (condenser) is used to provide heating and hot water.
During the cooling season, ambient heat absorption at the low pressure side (evaporator) can be used to provide cold air.
To ensure that
Such heating and cooling heat pump system has various structures depending on the application environment.
But basically 4 compressors, condenser, expansion valve, evaporator
The refrigerant in the system consists of the elements from the compressor to the condenser and from the condenser to the expansion valve.
Cycles from the expansion valve to the evaporator and from the evaporator back to the compressor.
And this cycle uses the second law of thermodynamics to cause the compressor to
High heat source with high temperature by absorbing heat from low heat source by performing positive work
It aims to transfer heat to (高 熱源).
At this time, the refrigerant is evaporated at a low temperature in the evaporator to absorb the surrounding heat, the compressor
In the low pressure gas flowing from the evaporator to compress the high pressure gas
It is heated up and sent to a condenser, and the condenser is heated at a high temperature from the compressor.
Heats the pressurized gas and hot water flowing from the hot water tank to heat it up.
It is phase-converted to medium temperature liquid refrigerant and sent to the expansion valve.
And, the expansion valve expands the medium-temperature liquid refrigerant flowing from the condenser
Is converted into a refrigerant and then supplied to an evaporator, in which the condenser
Heat exchanged with cold water tank and circulating water piping
It will produce cold and cold water.
On the other hand, cooling by switching the flow direction of the refrigerant to the combination of the circulation cycle as described above
Or by including a four-way valve to allow selective use as a heating device, the evaporator
If it is used to absorb the heat of the high temperature part, it is possible to perform cooling operation such as air conditioner or refrigerator.
Can be used as a cooling device, and the condenser is activated to discharge heat to the low temperature part.
It can also be used as a heating device that can perform heating operation.
As such, the evaporator and condenser are a kind of heat exchanger, so the compressor, evaporator, condenser
And expansion valves, and by selectively changing the flow of refrigerant, cooling and heating operations
It will be possible to implement a heating and cooling heat pump system that combines into a single device.
As such, the heat pump may be selectively cooled and heated.
As an air conditioner, refrigerant flows slowly as the cooling mode or heating mode is selected.
In the reverse direction, cooling or heating is performed depending on the selected mode.
It is to be.
On the other hand, conventional heating and cooling heat in air-conditioning equipment using a refrigerant directly to date
The pump system includes an electric compressor driving method and an engine port using gas, oil, etc. as a fuel.
Homogeneous compression has been released and is in use.
However, these conventional products and currently released products have an outside temperature during heating operation.
Becomes lower, the heating load increases, and the consumption of energy (electricity, gas, oil, etc.) increases.
According to the difference in product performance, the outside temperature is outside from 3 ℃ to -15 ℃
The side evaporator prevents the evaporation of the refrigerant liquid from occurring smoothly.
Refrigerant circulation to high pressure side because it cannot absorb latent heat of evaporation
As the amount of heat decreases, the heating value of the condenser is lowered, causing a sudden decrease in heating efficiency.
The noise generated by the load operation is large and the compression ratio in the outdoor unit compressor is increased.
Is an inefficient phenomenon in which the amount of heat obtained indoors is relatively small compared to the operating energy.
There was a problem that led to the driving of the device.
The present invention relates to a medium pressure cycle air-conditioning heat pump system for cold cooling,
In particular, the hot water temperature inside the system can be maintained at
Maintain high temperature water above ℃ and keep hot water temperature high
To maintain stability and efficiency at the same time for heating and cooling.
The purpose is to do so.
The booster compressor that compresses the medium to medium pressure refrigerant evaporated from the flash tank
Interaction with main compressor that compresses low temperature low pressure refrigerant evaporated from heat exchanger
To increase the heating efficiency of condenser refrigerant in plate heat exchanger
The low temperature that passes through the second expansion valve using external air of low temperature
Evaporate the low-temperature liquid refrigerant and convert it to a condenser during cooling to cool the high-temperature and high-pressure gas.
An outdoor heat exchanger configured to condense the medium, and having a blower fan mounted on the outside thereof; Condenser during heating
To absorb the heat of condensation of the high-temperature and high-pressure gas, and then add hot water from a hot water tank (not shown).
It supplies heat to hot water, and when cooled, it is converted to an evaporator to supply cold water.
Plate heat exchanger; The heat of the outlet heat of the plate heat exchanger and the liquid refrigerant passing through the first expansion valve
A fresh tank for generating a medium temperature pressure by evaporation by exchange; Increase in the flash tank
Medium pressure booster compression to supply plate heat exchanger by compressing the medium-temperature medium pressure refrigerant vapor
tile; Low evaporated from the outdoor heat exchanger by outside air after passing through the second expansion valve
Low pressure side for sucking the gas of low and low pressure through the low pressure pipe and supplying it to the plate heat exchanger
A main compressor; The liquid refrigerant that has not been evaporated in the outdoor heat exchanger is returned to the fresh tank.
After overheating to prevent liquid compression of the main compressor, the amount of refrigerant supplied to the plate heat exchanger 3 is increased.
The present invention as described above is the refrigerant liquid evaporation of the outdoor evaporator in the cold cold place
The amount of heat dissipation in the condenser is reduced due to the decrease in the amount of refrigerant circulation to the high pressure side.
Temperature is reduced by using a fresh tank to prevent the heating efficiency from decreasing.
Generates medium pressure gas and compresses it with a booster compressor to increase the heat dissipation of the condenser.
Is evaporated in the outdoor heat exchanger, and the remaining liquid refrigerant is
After preventing the liquid compression of the main compressor by overheating, it is an invention that is effective to increase the efficiency of the refrigerant supply to the plate heat exchanger (3) to increase the heating and cooling efficiency and to reduce the cost.
1 and 2 is a medium pressure cycle air-conditioning heat pump system for cold cooling of the present invention
1 is a view showing a heating mode, Figure 2 is a cooling mode or defrost mode
It is a figure which shows. When described in detail with reference to the accompanying drawings of the present invention as follows.
All. Toe of the booster compressor (11) for compressing the medium-temperature medium pressure refrigerant evaporated in the flash tank (5)
Main compressor (1) for compressing the low temperature low pressure refrigerant evaporated from the outlet and outdoor heat exchanger (9)
The discharge parts of the plate heat exchanger are mutually extruded to increase the condenser refrigerant circulation of the plate heat exchanger (3) to increase the heating efficiency, the heating is switched to the evaporator when the second expansion valve using low-temperature external air (8) the low-temperature low-pressure liquid refrigerant is evaporated, and during cooling is converted to a condenser to condense the refrigerant of the high-temperature high-pressure gas, the outer side heat exchanger (9) equipped with a blowing fan (10); When the heating is converted to a condenser to absorb the heat of condensation of the high temperature and high pressure gas, and then heated hot water in the hot water tank (not shown) to supply the hot water, when cooling the plate heat exchanger is converted to the evaporator to supply cold water (3) Wow; A fresh tank (5) for generating a medium temperature pressure by evaporation by heat exchange between the plate heat exchanger (3) outlet pipe heat and the liquid refrigerant passing through the first expansion valve (7); The upper portion of the flash tank (5) through the electronic valve (4) provided in the middle of the medium pressure pipe (MP) and the medium pressure pipe
Connected to the booster compressor (11), the medium pressure medium pressure of the gas evaporated in the flash tank (5)
A medium pressure side booster compressor (11) which sucks through the pipe (MP) and supplies it to the plate heat exchanger (3);
After passing through the second expansion side (8) low evaporation in the outdoor heat exchanger (9) by the outside air
The low pressure side menu that sucks the gas of low temperature through the low pressure pipe and supplies it to the plate heat exchanger (3).
After the overheating in the main compressor (1) the superheated steam is sucked in to prevent liquid compression
Therefore, in low temperature cold district, the refrigerant liquid evaporation of the outdoor evaporator is not smooth.
As the amount of refrigerant circulated to the gas decreases,
By operating the medium pressure cycle to prevent this from happening,
At the same time, the efficiency can be increased to increase cooling and heating efficiency while reducing costs.
It is a technical basic feature.
Each sphere for the medium-pressure cycle air-conditioning heat pump system for cold cooling of the present invention
Looking at the components one by one with reference to the accompanying drawings as follows.
First, the present invention, a part for compressing the medium-temperature medium pressure refrigerant evaporated in the flash tank (5)
A compressor for compressing the low temperature low pressure refrigerant evaporated from the ster compressor (11) and the outdoor heat exchanger (9).
In-compressor (1), converted to evaporator during heating to increase liquid refrigerant using low-temperature external air
The outdoor heat exchanger (9), which converts into a condenser upon cooling, and a condenser when heating
When cooling, the plate heat exchanger (3) is converted to the evaporator, and
It consists of a fresh tank (5) for generating a medium temperature and medium pressure by cooling.
Plate heat exchanger (3) is the production of cold or hot water according to the temperature and operating conditions of the outside air
It is made to be possible, and when heated, it is converted to a condenser to heat the condensation of high temperature and high pressure gas.
After absorbing, supply hot water by heating hot water from hot water tank (not shown) from 55 ℃ to 60 ℃.
When cooling, it is converted to an evaporator to supply cold water.
In addition, the upper portion of the flash tank (5) is the electron provided in the middle of the medium pressure pipe (MP) and
It is connected to the
Is connected to the outdoor side evaporator (9), one side of the fresh tank (5) is the plate heat
It is connected to the exchanger (3), the other side is connected to the main compressor (1) and the four sides (2)
From the outlet pipe heat of the plate heat exchanger (3), the medium pressure is reduced by evaporation and subcooling by heat exchange.
The 3-
One side of is connected to the plate heat exchanger (3) and the other side is connected to the first expansion edge (7), the center
One side of 1way is connected to the first expansion side (7) and the other side proceeds to the bottom of the fresh tank (5), the right
One side of the side 1way is connected to the four sides (2) and the other side is connected to the main compressor (1),
The heat exchange from the shaft outlet pipe heat is to be made smoothly.
For example, the outdoor evaporator (9) is a low temperature outside air of about 15 ℃ below
The side heat exchanger (9) is used to evaporate the liquid refrigerant.
In this case, a
Make sure
At this time, the suction side of the booster compressor (11) is connected to the upper portion of the fresh tank (5) of medium temperature and medium pressure
The discharge side of the
It is fed to the plate heat exchanger (3) through a pressure pipe.
As a result, the amount of refrigerant circulating to the plate heat exchanger 3 increases, so that the condensation capacity is remarkably increased.
This increases the heating capacity.
The
The medium-temperature high-pressure supercooling liquid passed through the exchanger 3 is expanded to medium-temperature medium pressure (evaporation pressure
7kg / cm2, evaporation temperature 15 ℃).
The
1.5kg / cm2, evaporation temperature -20 ℃) is transmitted to the outdoor heat exchanger (9).
In addition, the outdoor side heat exchanger (9) is provided with a blowing fan (10), the outdoor side heat exchanger
One side of the machine (9) is connected to the main compressor (1) and the other side is connected to the fresh tank (5), the
The suction part of the
Four-way valve (2) is a high temperature and high pressure gas discharged from the main compressor (1)
It is provided in the interruption of the high pressure pipe that is pumped to the machine (3), the flow path of the refrigerant according to the cooling and heating
Name can be switched.
At this time, the plate heat exchanger 3 is switched to a condenser or an evaporator according to heating and cooling.
Or conversion of the outdoor
As a technology, the above switching operation is a heating and cooling switching selector provided by the user outside
Is implemented through a switch (not shown) operation.
S / V (4) provided at the stop of booster compressor (11) and medium pressure pipe (MP) during cooling or defrosting
(The part marked with ------ (silver line) in Fig. 2) is turned OFF, and
The S / V 4 provided at the interruption of the
Hereinafter, an embodiment of the present invention will be described.
As shown in Figure 1 and 2, when converted to a condenser upon heating and cooling or
Plate heat exchanger (3) which is always switched to the evaporator, and evaporation and supercooling by heat exchange
Fresh tank (5) for generating medium-temperature and medium pressure
Is the heating of the outdoor heat exchanger (9) and the plate heat exchanger (3) which is converted into a condenser at the time of defrosting
It consists of a
As such, the present invention can be switched to the desired mode when the cooling and heating operation
The heating effect is not reduced even in a cold place where the outside air temperature is minus 15 ℃.
The medium pressure cycle air-conditioning heat pump system of the present inventors
Hereinafter, an embodiment of the heating mode operation and the cooling mode operation will be described.
First, as shown in Figure 1, the medium pressure during the heating mode of the heat pump system
Looking at the action on the cycle, the
It is connected to the tank (5), the discharge portion of the plate heat exchanger (3) on the outlet side and the high pressure side of the main compressor (1)
Connected with
At this time, the condenser acts in the heating mode of the plate heat exchanger 3 on the high pressure side.
The medium and high pressure refrigerant liquid, which has passed through the outlet pipe of the plate heat exchanger 3 on the high pressure side, is fresh.
Inflated through the first expansion valve (7) while passing through a three-way heat exchanger (6) embedded in the tank (5)
It exchanges heat with the refrigerant liquid at moderate pressure (evaporation pressure 7kg / cm2, evaporation temperature 15 ℃).
On the other hand, the coolant liquid that has passed through the
Heat exchange occurs in the vent (6), resulting in a first evaporation of 7 kg / cm2 (R-22 evaporation temperature
FIG.: 15 ° C.) generates a medium-temperature medium pressure gas in the
Through the solenoid valve (4) provided at the middle of the medium pressure pipe (MP) and the middle
The suction side of the ster compressor (11) is sucked into the medium temperature medium pressure gas and compressed by the booster compressor (11)
The high pressure tube is compressed with the high temperature and high pressure gas compressed and the high temperature and high pressure gas compressed by the main compressor (1).
It is sent to the plate heat exchanger (3) acting as a condenser through the two compressors
Due to the increase in the circulation of the refrigerant is to increase the heat radiation of the condenser.
At this time, the second expansion edge (8) due to the evaporation of the primary refrigerant by the heat exchange in the flash tank (5)
The temperature of the high pressure liquid pipe connected to the supercooling is up to 15 ° C.
After the second pressure reduction to 1.5kg / cm2 (evaporation temperature -20 ℃) in the second expansion side (8) is sent to the outdoor evaporator (9), the liquid refrigerant sent to the outdoor evaporator (9) is a low temperature After evaporation takes place in the outdoor heat exchanger (9) using outside air (zero below 15 ° C), the remaining liquid refrigerant is overheated in the fresh tank (5) again, and then the main compressor (through 1) inhaled in gaseous state.
Therefore, low temperature low pressure liquid cooling to be evaporated in the outdoor side heat exchanger (9)
Since the quantity is greatly reduced, it reduces the incidence rate of sex, increasing the coefficient of performance and heating effect.
The rate can be improved.
In addition, as shown in Figure 1, during the heating mode operation of the heat pump system
Looking at the action on the compressor (1), the suction portion of the main compressor (1) is an outdoor thermal bridge
It is connected with the ventilation (9), the discharge portion discharge portion of the booster compressor (11) and the plate heat exchange
Is connected to the machine 3, the high temperature and high pressure gas discharged from the main compressor (1) is everywhere
Along the flow path of the bar (2), while passing through the plate heat exchanger (3), which is converted to a condenser upon heating,
The temperature rises from the water inlet temperature of 50 ° C to the hot water outlet temperature of 55 ° C.
And, the condensation temperature of the plate heat exchanger (reference numeral 3, or condenser) is 55 ℃
The temperature of the outlet pipe of the plate heat exchanger (ref. 3, or condenser) is 45 ° C.
In order to utilize the outlet pipe heat, the plate heat exchanger (reference 3, or condensation)
And a fresh tank (5) between the first expansion edge (7) and the first expansion valve (7).
Medium temperature liquid cooling through the medium-temperature liquid refrigerant (45 ° C) and the first expansion valve (7) at the outlet of No. 3, or condenser)
The liquid pipe to which the medium (15 ° C) exchanges with each other and goes to the second expansion side (8) is subcooled from 45 ° C to 15 ° C.
At the same time as the angle, the first evaporation takes place to become a gas of medium pressure.
On the other hand, the supercooled refrigerant liquid (evaporation pressure 1.5kg / cm2, evaporation temperature through the second expansion side 8)
-20 ° C.) After the expansion, heat exchange with the outdoor air (-15 ° C.) occurs in the
After that, the cycle is sucked back into the main compressor (1) through the suction pipe and compressed again to high pressure
Keep it circulating.
When there is a drop in the outdoor heat exchanger (9), the air conditioner is switched to the cooling mode.
It acts.
In addition, as shown in Figure 2, the cooling mode (defrost mode) operation of the heat pump system
Looking at the action on the copper, the high temperature and high pressure gas discharged from the main compressor (1)
By switching the
Is transferred to the outdoor heat exchanger (9), which is converted to a condenser.
Accordingly, the first expansion after condensation occurs in the outdoor heat exchanger (9)
On the side (8), the gas of high temperature and high pressure expands to medium temperature and medium pressure, and the low temperature low pressure of the second expansion side
After expansion, the cold water and heat exchange in the plate heat exchanger (3) converted to the evaporator during cooling
After the engine is sucked back into the main compressor (1) and compressed again to high pressure,
At this time, the
(The part indicated by ------ (silver line) in Fig. 2) The operation is turned off.
Medium pressure cycle air-conditioning heat pump sheath for cold storage of the present invention configured as described above
The system of the booster compressor and the main compressor interact with each other.
When cooling, the plate heat exchanger is switched to the evaporator, and evaporation and supercooling
Flash tank that generates medium pressure and evaporator when heated and condenser when cooled
It consists of an outdoor side heat exchanger that is switched, and the refrigerant of the outdoor side evaporator in a cold district of low temperature
The condenser is reduced due to the reduction of refrigerant circulation to the high pressure side due to no liquid evaporation.
The low heat dissipation rate of the heat sink prevents the heating efficiency from being reduced.
, The amount of refrigerant circulating to the outdoor evaporator is reduced, which reduces the incidence rate
Increase the efficiency and increase the heating efficiency while lowering the heating cost
It is an invention that has an excellent advantage in reducing.
The above embodiment is an example for explaining the technical spirit of the present invention in detail.
The scope of the present invention is not limited to the above drawings and examples.
1 is a view showing a heating mode of the medium-pressure cycle heating and cooling heat pump system for cold cooling of the present invention;
2 is a medium pressure cycle air-conditioning heat pump system for cold storage of the present invention
Fig. Showing the cooling mode (defrost mode).
(Part marked with ------ line is OFF)
<Explanation of symbols for the main parts of the drawings>
1: main compressor 2: four-way valve
3: plate heat exchanger 4: solenoid valve (for medium pressure pipe)
5: fresh tank 6: 3way heat exchanger
7: first expansion valve 8: second expansion valve
9: outdoor side heat exchanger 10: outdoor side heat exchanger fan
11: booster compressor MP: medium pressure pipe
Claims (5)
Priority Applications (1)
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KR1020080136218A KR101015307B1 (en) | 2008-12-30 | 2008-12-30 | System of heat pump for cooling and heating of middle pressure cycle for air heat source |
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KR1020080136218A KR101015307B1 (en) | 2008-12-30 | 2008-12-30 | System of heat pump for cooling and heating of middle pressure cycle for air heat source |
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KR20100078074A true KR20100078074A (en) | 2010-07-08 |
KR101015307B1 KR101015307B1 (en) | 2011-02-15 |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
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KR101050253B1 (en) * | 2010-11-23 | 2011-07-19 | (주)세원센추리 | Heat pump type thermo-hygrostat for cold districts |
CN110145883A (en) * | 2019-05-23 | 2019-08-20 | 青岛澳柯玛智慧冷链有限公司 | A kind of multi-stage heat exchanger water cooling system for built-in showcase |
CN110220303A (en) * | 2019-02-26 | 2019-09-10 | 华北电力大学 | A kind of low * damage heat exchanger |
CN110594923A (en) * | 2019-10-16 | 2019-12-20 | 上海热翼智能科技有限公司 | Anti-frosting heat pump air conditioning system |
CN110671836A (en) * | 2019-11-11 | 2020-01-10 | 恒量电器(厦门)有限公司 | Integrated supply device based on temperature and humidity control and hot water heating |
CN114103587A (en) * | 2021-11-10 | 2022-03-01 | 上海同心济世工程技术有限公司 | Integrated thermal management control system based on heat pump air conditioning technology and control method thereof |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
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US5899091A (en) | 1997-12-15 | 1999-05-04 | Carrier Corporation | Refrigeration system with integrated economizer/oil cooler |
EP2078178B1 (en) | 2006-10-26 | 2016-05-18 | Johnson Controls Technology Company | Economized refrigeration system |
CN101688697B (en) | 2007-04-24 | 2012-10-03 | 开利公司 | Refrigerant vapor compression system with dual economizer circuits |
-
2008
- 2008-12-30 KR KR1020080136218A patent/KR101015307B1/en not_active IP Right Cessation
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101050253B1 (en) * | 2010-11-23 | 2011-07-19 | (주)세원센추리 | Heat pump type thermo-hygrostat for cold districts |
CN110220303A (en) * | 2019-02-26 | 2019-09-10 | 华北电力大学 | A kind of low * damage heat exchanger |
CN110220303B (en) * | 2019-02-26 | 2024-03-29 | 华北电力大学 | Low exergy -loss heat exchanger |
CN110145883A (en) * | 2019-05-23 | 2019-08-20 | 青岛澳柯玛智慧冷链有限公司 | A kind of multi-stage heat exchanger water cooling system for built-in showcase |
CN110594923A (en) * | 2019-10-16 | 2019-12-20 | 上海热翼智能科技有限公司 | Anti-frosting heat pump air conditioning system |
CN110671836A (en) * | 2019-11-11 | 2020-01-10 | 恒量电器(厦门)有限公司 | Integrated supply device based on temperature and humidity control and hot water heating |
CN114103587A (en) * | 2021-11-10 | 2022-03-01 | 上海同心济世工程技术有限公司 | Integrated thermal management control system based on heat pump air conditioning technology and control method thereof |
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