CN112303958A - High-efficiency refrigerating and heating equipment - Google Patents
High-efficiency refrigerating and heating equipment Download PDFInfo
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- CN112303958A CN112303958A CN202011488580.5A CN202011488580A CN112303958A CN 112303958 A CN112303958 A CN 112303958A CN 202011488580 A CN202011488580 A CN 202011488580A CN 112303958 A CN112303958 A CN 112303958A
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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
- F25B31/00—Compressor arrangements
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B37/00—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00
- F04B37/10—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for special use
- F04B37/12—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for special use to obtain high pressure
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B39/00—Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
- F04B39/06—Cooling; Heating; Prevention of freezing
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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
- F25B39/00—Evaporators; Condensers
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Structures Of Non-Positive Displacement Pumps (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Abstract
The invention relates to high-efficiency refrigerating and heating equipment, which comprises an isenthalpic compressor, a regenerator, an evaporator, a throttle valve and a condenser, wherein the outlet of the evaporator is connected with the inlet of the low-temperature end of the regenerator, the outlet of the low-temperature end of the regenerator is connected with the inlet of the low-pressure end of the isenthalpic compressor, the outlet of the high-pressure end of the isenthalpic compressor is connected with the inlet of the condenser, the outlet of the condenser is connected with the inlet of the high-temperature end of the regenerator, the outlet of the high-temperature end of the regenerator is connected with the inlet of the throttle valve, and the outlet of the throttle; its working method is also disclosed. The invention has the advantages that: the isenthalpic compressor separates the tasks of hot compression and potential energy lifting, the heat exchanger completes hot compression, and the compressor completes potential energy lifting; the energy efficiency ratio is improved by 10 times, and one-degree electric energy is used for exchanging heat energy or cold energy of more than ten degrees to thirty degrees; a heat regenerator is added to increase the refrigerating and heating capacity of the unit working medium, so that the energy efficiency ratio is further improved; the split type compressor is beneficial to improving the temperature resistance degree of the compressor.
Description
Technical Field
The invention relates to the field of artificial environment, in particular to a high-efficiency refrigerating and heating device which consists of an isenthalpic compressor, a heat regenerator, an evaporator, a throttle valve and a condenser.
Background
The existing air conditioner and water heater all adopt an isentropic compressor, the larger the compression ratio is, the more the power consumption is, the ratio of heat or cold generated by the air conditioner to the power consumption is called as an energy efficiency ratio, the normal condition is about three points, and the cold condition is only a little, namely, the direct use of the electric heater is equivalent.
In order to ensure that satisfactory heating and hot water can be obtained in an environment below 20 ℃ below zero, the pressure ratio of the compressor needs to be increased to about 11-13.
Disclosure of Invention
The invention aims to overcome the defects of the prior art, and provides high-efficiency refrigerating and heating equipment consisting of an isenthalpic compressor, a regenerator, an evaporator, a throttle valve and a condenser on the basis of theoretical research and experimental experience in the field for many years, wherein the isenthalpic compressor is named as an isenthalpic compressor under the application number of 2020114762843, and the equipment is combined with the regenerator, so that the energy efficiency ratio is changed from one point to three points to one dozen to thirty points at present, one-time electric energy is used for changing heat energy or cold energy of more than ten to thirty degrees, the quantity is changed to generate qualitative change, the most basic and most extensive rigid demand cost of global refrigeration and heating and artificial climate control in industrial and agricultural production is greatly reduced due to the great improvement of the energy efficiency ratio, and the problems of energy, carbon emission, air pollution and the like are solved.
The purpose of the invention is realized by the following technical scheme:
the high-efficiency refrigerating and heating equipment consists of an equal enthalpy compressor, a heat regenerator, an evaporator, a throttle valve and a condenser:
an enthalpy compressor is used for replacing a common compressor;
A. in a cold working condition, the outlet of the evaporator is connected with the inlet of the low-temperature end of the heat regenerator, the outlet of the low-temperature end of the heat regenerator is connected with the inlet of the low-pressure end of the isenthalpic compressor, the outlet of the high-pressure end of the isenthalpic compressor is connected with the inlet of the condenser, the outlet of the condenser is connected with the inlet of the high-temperature end of the heat regenerator, the outlet of the high-temperature end of the heat regenerator is connected with the inlet of the throttle valve, and the outlet of the throttle valve is connected with the inlet;
B. when the compressor is in a common working condition, the outlet of the evaporator is connected with the inlet of the low-pressure end of the isenthalpic compressor, the outlet of the high-pressure end of the isenthalpic compressor is connected with the inlet of the condenser, the outlet of the condenser is connected with the inlet of the throttling valve, and the outlet of the throttling valve is connected with the inlet of the evaporator.
Further, the isenthalpic compressor which is changed from a common compressor into the isenthalpic compressor is a high-temperature-resistant or split-type compressor. And the ordinary compressor and the heat exchanger which form the isenthalpic compressor need to adopt heat preservation measures, and the heat preservation layer is wrapped outside the ordinary compressor and the heat exchanger.
Furthermore, the application range of the scheme is various artificial environment equipment needing the compressor, including air conditioners, water heaters, heat pumps, water chilling units, freezing and refrigerating warehouses, municipal heating and the like.
The scheme is that the high-efficiency refrigerating and heating equipment consists of an isenthalpic compressor, a heat regenerator, an evaporator, a throttle valve and a condenser; when the equipment works, the isenthalpic compressor separates the tasks of hot compression and potential energy lifting, the heat exchanger completes the hot compression, the potential energy lifting is completed by the compressor, and then the heat regenerator increases the refrigerating and heating capacity of the unit working medium.
In addition, under the condition of smaller refrigerating and heating temperature difference, a heat regenerator can be removed; the throttle valve is connected with the input end of the evaporator, the output end of the evaporator is connected with the inlet of the low-pressure end of the isenthalpic compressor, the outlet of the high-pressure end of the isenthalpic compressor is connected with the inlet of the condenser, and the output end of the condenser is connected with the throttle valve.
The high-efficiency refrigerating and heating equipment consists of an equal enthalpy compressor, a heat regenerator, an evaporator, a throttle valve and a condenser, and the working method comprises the following steps:
A. in cold working conditions, high-pressure high-temperature gas flows out of the high-pressure end outlet of the isenthalpic compressor 1, the high-pressure high-temperature gas enters the condenser 5 to release heat to form high-pressure medium-temperature gas, and the high-pressure medium-temperature gas enters the heat regenerator 2 to be cooled
The high-pressure normal-temperature liquid enters a throttle valve 4 to be throttled and decompressed to form a medium-high-pressure normal-temperature gas-liquid mixture, the gas-liquid mixture enters an evaporator 3 to be gasified to form low-pressure low-temperature gas, the low-pressure low-temperature gas enters a heat regenerator 2 to be subjected to heat exchange to form low-pressure normal-temperature gas, and the low-pressure normal-temperature gas enters an isenthalpic compressor 1 to be isenthalpic compressed to form high-pressure normal-temperature gas;
B. under the ordinary working condition, the high-pressure high-temperature gas flows out of the high-pressure end outlet of the isenthalpic compressor 1, the high-pressure high-temperature gas enters the condenser 5 to release heat to form high-pressure medium-temperature gas, the high-pressure medium-temperature gas enters the throttle valve 4 to be throttled and depressurized to form a medium-pressure normal-temperature gas-liquid mixture, the gas-liquid mixture enters the evaporator 3 to be gasified to form low-pressure low-temperature gas, and the low-pressure low-temperature gas enters the isenthalpic compressor 1 to be isenthalpic compressed to form high-pressure normal-temperature.
The invention has the following advantages:
1. the isenthalpic compressor is combined with a heat regenerator, and then forms high-efficiency refrigerating and heating equipment together with an evaporator, a throttle valve and a condenser, the energy efficiency ratio is changed from one point to three points to ten and several tens of points at present, one-degree electric energy is used for exchanging heat energy or cold energy with more than ten to thirty degrees, the quantity and the quantity change generate quality change, the most basic and most extensive rigidity requirement cost of the human in global refrigerating and heating and artificial climate control in industrial and agricultural production is greatly reduced due to the great improvement of the energy efficiency ratio, the problems of energy source, carbon emission, air pollution and the like are solved, and the significance of the equipment is immeasurable;
2. when the equipment works, firstly, a heat compression task and a potential energy lifting task are separated in an isenthalpic compressor, the heat compression is completed by a heat exchanger, the potential energy lifting is completed by the compressor, and the energy efficiency ratio is greatly improved; and then the heat regenerator increases the refrigerating and heating capacity of the unit working medium, thereby further improving the energy efficiency ratio.
Drawings
FIG. 1 is a first schematic structural diagram of the present invention; FIG. 2 is a second schematic structural view of the present invention;
in the figure: 1-an isenthalpic compressor, 2-a heat regenerator, 3-an evaporator, 4-a throttle valve and 5-a condenser.
Detailed Description
The invention will be further described with reference to the accompanying drawings, but the scope of the invention is not limited to the following. As shown in fig. 1, the high-efficiency refrigerating and heating device is composed of an isenthalpic compressor 1, a heat regenerator 2, an evaporator 3, a throttle valve 4 and a condenser 5;
the export of evaporimeter 3 is connected with the low temperature end entry of regenerator 2, and the low temperature end export of regenerator 2 is connected with the low-pressure end entry of isenthalpic compressor 1, and the high-pressure end export of isenthalpic compressor 1 is connected with the entry of condenser 5, and the export of condenser 5 is connected with regenerator 2 high temperature end entry, and the high temperature end export of regenerator 2 is connected with the entry of choke valve 4, and the export of choke valve 4 is connected with the entry of evaporimeter 3.
The device comprises an isenthalpic compressor 1, a heat regenerator 2, an evaporator 3, a throttle valve 4 and a condenser 5, wherein the isenthalpic compressor 1 separates the tasks of thermal compression and potential energy lifting, the heat exchanger completes the thermal compression, and the potential energy lifting is completed by the compressor; then the heat regenerator increases the refrigerating and heating capacity of the unit working medium.
The isenthalpic heat exchange means heat exchange with a constant enthalpy value. The enthalpy compressor in the scheme is essentially a combination of a common heat exchanger and a common compressor, namely, the enthalpy heat exchange of the heat exchanger + the compression formed by the gas compressor = the enthalpy compression in the common sense. Isenthalpic compression is a thought controlled compression process, and adopts ideal gas (i.e. molecules are elastic particles which do not occupy volume, no force is generated between molecules except collision, and the ideal gas is an abstraction of actual gas at low pressure and high temperature), which cannot absolutely reach isenthalpic and only tends to isenthalpic.
Further, the isenthalpic compressor 1, which is a modified form of a general compressor, is a high temperature resistant or split type compressor. And the ordinary compressor and the heat exchanger which form the isenthalpic compressor 1 need to adopt heat preservation measures, and the heat preservation layer is wrapped outside the ordinary compressor and the heat exchanger.
Furthermore, the application range of the scheme is various artificial environment equipment needing the compressor, including air conditioners, water heaters, heat pumps, water chilling units, freezing and refrigerating warehouses, municipal heating and the like.
The high-efficiency refrigerating and heating equipment consists of an isenthalpic compressor 1, a heat regenerator 2, an evaporator 3, a throttle valve 4 and a condenser 5, and the working method comprises the following steps:
A. in a cold working condition, high-pressure high-temperature gas flows out of an outlet at a high-pressure end of the isenthalpic compressor 1, the high-pressure high-temperature gas enters the condenser 5 to release heat to form high-pressure medium-temperature gas, the high-pressure medium-temperature gas enters the heat regenerator 2 to be cooled to form high-pressure normal-temperature liquid, the high-pressure normal-temperature liquid enters the throttle valve 4 to be throttled and depressurized to form a medium-pressure and high-pressure normal-temperature gas-liquid mixture, the gas-liquid mixture enters the evaporator 3 to be gasified to form low-pressure low-temperature gas, the low-pressure low-temperature gas enters the heat regenerator 2 to be subjected to heat exchange to form low-pressure normal-temperature gas, and the low-pressure;
B. under the common working condition, high-pressure high-temperature gas flows out of the high-pressure end outlet of the isenthalpic compressor 1, the high-pressure high-temperature gas enters the condenser 5 to release heat so as to form high-pressure medium-temperature gas, and the high-pressure medium-temperature gas enters the throttle valve 4 to be throttled and reduced
And (3) pressing to form a gas-liquid mixture with medium and high pressure and normal temperature, wherein the gas-liquid mixture enters the evaporator (3) to be gasified to form low-pressure and low-temperature gas, and the low-pressure and low-temperature gas enters the isenthalpic compressor (1) to be isenthalpic compressed to form high-pressure and normal-temperature gas.
Example 1, ultra-high energy efficiency air conditioner:
in severe cold areas with the temperature lower than minus 20 ℃, ordinary air-conditioning heating cannot be used, the auxiliary heating of enhanced vapor injection and electricity is adopted in a small amount, the power consumption is high, and the effect is not ideal. In this embodiment 1, an efficient cooling and heating apparatus is proposed, which is not only suitable for severe cold regions, but also widely applicable to cooling and heating air conditioners, ground source heat pumps, water source heat pumps, air source water heaters, and water chilling units under various climatic conditions, and the specific method is as follows: the original compressor in the system is replaced by an isenthalpic compressor which is formed by a high-temperature-resistant compressor connected with a heat exchanger in series, as shown in figure 1, a throttle valve 4 is connected with the input end of an evaporator 3, the output end of the evaporator 3 is connected with the low-temperature end inlet of a heat regenerator 2, the low-temperature end outlet of the heat regenerator 2 is connected with the low-pressure end inlet of the isenthalpic compressor 1, the high-pressure end outlet of the isenthalpic compressor 1 is connected with the inlet of a condenser 5, the output end of the condenser 5 is connected with the high-temperature end inlet of the heat regenerator 2, and the high-temperature end outlet of the heat regenerator 2 is connected with the; because the common compressor is changed into the isenthalpic compressor, the tasks of hot compression and potential energy lifting are separated, the hot compression is completed by the heat exchanger, and the potential energy lifting is completed by the compressor.
Taking a super heating air conditioner as an example, working in a severe cold area with 20 ℃ below zero, a refrigerant R134a is adopted as a working medium, the temperature of a condenser is set to be 60 ℃, the supercooling degree is 5 ℃, the corresponding condensation pressure of a pressure-enthalpy diagram is 1.8MPa at the condensation temperature of 60 ℃, the outlet pressure of an evaporator is 0.135MPa at the outlet temperature of-20 ℃, in order to further improve the heating efficiency, a regenerator is added, the inlet of the high-temperature end of the regenerator is connected with the output end of the condenser, the outlet of the high-temperature end of the regenerator is connected with the inlet end of a throttle valve 4, the inlet of the low-temperature end of the regenerator is connected with the outlet of the evaporator, the outlet of the low-temperature end of the regenerator is connected with the inlet of an isenthalpic compressor, the regenerator mainly increases the superheat degree of the outlet of the evaporator, the refrigeration and heating capacity of the unit refrigerant is, the outlet of the low temperature end of the heat regenerator is 50 ℃, if an isenthalpic compressor is not adopted, the inlet temperature of the compressor is the inlet temperature of the compressor, the compressor needs to lift gas with 0.135MPa, 50 ℃ and 450KJ/kg of enthalpy to 1.8MPa, 140 ℃ and 520KJ/kg of enthalpy, electric power consumption of each 1kg of the compressor is 70KJ, under the working condition, the heating capacity of each 1kg of working medium is 240KJ, and according to the definition of energy efficiency ratio, the heating capacity is divided by the power consumption of electricityThe rate 240KJ ÷ 70KW =3.43, which is a result achieved only with the use of a regenerator, but the compressor temperature has reached 140 ℃, exceeding the compressor protection temperature. After the isenthalpic compressor is adopted, the inlet of the isenthalpic compressor is still 0.135MPa, the temperature is 50 ℃, the outlet temperature of the compressor body is still 140 ℃, but the outlet temperature of the isenthalpic compressor, namely the outlet temperature of the heat exchanger is 80 ℃, the heating capacity is reduced to 170KJ/Kg, the increase value of the pressure is 1.8MPa-0.135MPa =1.665MPa, the increase value is converted into Kg and is equal to 16.65Kg, and 1KW =102 N.m, so the increase potential energy = mg/102 =16.65Kg × 9.8m/s2÷102=1.6KW。
From the above data, it is clear that, when the same supercharging function is realized, the energy efficiency ratio of consumption of the isenthalpic compression is 170KW/1.6KW =106, the compressor efficiency is 0.5, the energy efficiency ratio can also reach 50, and the energy saving effect is extremely remarkable.
Of course, to achieve this effect, a very rigorous process is necessary: because 18KW ÷ 1.35KW =13, need to raise the pressure ratio of the compressor to about 11-13, because of using the heat regenerator and increasing the compression ratio, the temperature of the compressor will obviously raise, and need to take the heat-insulating measure in order to guarantee very high energy efficiency ratio compressor and heat exchanger, this will exceed its protective temperature to making the apparatus that integrates motor and compressor into at present, so compressor and motor must make split type, make the integration into compressor and motor at present, the purpose is to reduce the noise and facilitate the lubrication, after making the split type, the compressor only needs to adopt appropriate material and lubricating oil can bear the higher temperature, the motor lubricates very common things independently, because the pressure and motor power that the compressor bears actually reduce a lot, as long as the problem of dealing with the noise is very good to solve, while the compressor takes the heat-insulating treatment, the noise thereof is also reduced;
also, to ensure an improvement in the energy efficiency ratio, the connecting piping between the heat exchanger of the isenthalpic compressor and the compressor must be shortened as much as possible.
The regenerator and the isenthalpic compressor are the best isenthalpic enthalpy increasing technology, so the enhanced vapor injection compressor is not needed.
The power of the corresponding compressor motor can be greatly reduced.
The heating air conditioner is used for refrigeration, the working condition is greatly improved, and the refrigeration energy efficiency ratio is similar to that of heating.
On the basis of the scheme of the embodiment, under the condition that the refrigerating and heating temperature difference is small, a heat regenerator can be omitted, as shown in fig. 2, a throttle valve 4 is connected with the input end of an evaporator 3, the output end of the evaporator 3 is connected with the inlet of the low-pressure end of an isenthalpic compressor 1, the outlet of the high-pressure end of the isenthalpic compressor 1 is connected with the inlet of a condenser 5, and the output end of the condenser 5 is connected with the throttle valve 4; because the common compressor is changed into the isenthalpic compressor, the tasks of hot compression and potential energy lifting are separated, the hot compression is completed by the heat exchanger, and the potential energy lifting is completed by the compressor.
Example 2, ultra-efficient water heater:
the structure is the same as that of a heating air conditioner, as shown in figure 1, except that a condenser in the air conditioner is replaced by a condenser in a water storage tank;
the national standard stipulates that the hot water temperature is not lower than 55 ℃, so the condensation temperature of the ultra-efficient water heater is set to be 60 ℃, and the condensation temperature is equal to the condensation temperature of the ultra-efficient water heater
The condensing temperature set by the heating air conditioner is the same, so the working condition is also suitable for the ultra-high efficiency water heater, when the water temperature is close to 60 ℃, the compressor stops working, and when the water temperature is reduced to 45 ℃, the compressor resumes working, thereby keeping stable hot water supply.
The life hot water is needed all the year round, and the hot water can be used for heating in winter, so that the water heater has wide application.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (5)
1. High-efficient refrigeration heating installation of constituteing by isenthalpic compressor (1), regenerator (2), evaporimeter (3), choke valve (4) and condenser (5), its characterized in that:
an isenthalpic compressor (1) is used for replacing a common compressor;
when the refrigeration cycle is in a cold working condition, the outlet of the evaporator (3) is connected with the inlet of the low-temperature end of the heat regenerator (2), the outlet of the low-temperature end of the heat regenerator (2) is connected with the inlet of the low-pressure end of the isenthalpic compressor (1), the outlet of the high-pressure end of the isenthalpic compressor (1) is connected with the inlet of the condenser (5), the outlet of the condenser (5) is connected with the inlet of the high-temperature end of the heat regenerator (2), the outlet of the high-temperature end of the heat regenerator (2) is connected with the inlet of the throttle valve (4), and the outlet of the throttle valve (4) is connected with the inlet of the;
under the ordinary working condition, the outlet of the evaporator (3) is connected with the inlet of the low-pressure end of the isenthalpic compressor (1), the outlet of the high-pressure end of the isenthalpic compressor (1) is connected with the inlet of the condenser (5), the outlet of the condenser (5) is connected with the inlet of the throttle valve (4), and the outlet of the throttle valve (4) is connected with the inlet of the evaporator (3).
2. The working method of the high-efficiency refrigerating and heating equipment consisting of the isenthalpic compressor (1), the heat regenerator (2), the evaporator (3), the throttle valve (4) and the condenser (5) is characterized in that:
A. in a cold working condition, high-pressure high-temperature gas flows out of an outlet at a high-pressure end of the isenthalpic compressor (1), the high-pressure high-temperature gas enters a condenser (5) to release heat so as to form high-pressure medium-temperature gas, the high-pressure medium-temperature gas enters a heat regenerator (2) to be cooled so as to form high-pressure normal-temperature liquid, the high-pressure normal-temperature liquid enters a throttle valve (4) to be throttled and decompressed so as to form a medium-pressure normal-temperature gas-liquid mixture, the gas-liquid mixture enters an evaporator (3) to be gasified so as to form low-pressure low-temperature gas, the low-pressure low-temperature gas enters the heat regenerator (2) to be subjected to heat exchange so as to form low-pressure normal-temperature gas, and the;
B. when the constant-temperature constant-pressure gas-liquid separator is in a common working condition, high-pressure high-temperature gas flows out of a high-pressure end outlet of the constant-enthalpy compressor (1), the high-pressure high-temperature gas enters the condenser (5) to release heat to form high-pressure medium-temperature gas, the high-pressure medium-temperature gas enters the throttle valve (4) to be throttled and depressurized to form a medium-high-pressure normal-temperature gas-liquid mixture, the gas-liquid mixture enters the evaporator (3) to be gasified to form low-pressure low-temperature gas, and the low-pressure low-temperature gas enters the constant-enthalpy compressor (1) to be compressed by.
3. The high efficiency refrigerating and heating apparatus as claimed in claim 1 or 2, wherein: the isenthalpic compressor (1) is a high-temperature-resistant or split compressor.
4. The high temperature resistant or split compressor as set forth in claim 3, wherein: the isenthalpic compressor (1) comprises a common compressor and a heat exchanger, and heat insulation layers are arranged outside the common compressor and the heat exchanger.
5. The high efficiency refrigerating and heating apparatus as claimed in claim 1 or 2, wherein: the application range of the compressor is various artificial environment equipment needing the compressor, including air conditioners, water heaters, heat pumps, water chilling units, freezing and refrigerating warehouses, municipal heating and the like.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011016916.8A CN112013570A (en) | 2020-09-24 | 2020-09-24 | Isenthalpic compressor |
| CN2020110169168 | 2020-09-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112303958A true CN112303958A (en) | 2021-02-02 |
Family
ID=73527229
Family Applications (5)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011016916.8A Pending CN112013570A (en) | 2020-09-24 | 2020-09-24 | Isenthalpic compressor |
| CN202011488580.5A Withdrawn CN112303958A (en) | 2020-09-24 | 2020-12-16 | High-efficiency refrigerating and heating equipment |
| CN202011488616.XA Withdrawn CN112303960A (en) | 2020-09-24 | 2020-12-16 | Cold power engine |
| CN202011488575.4A Withdrawn CN112283978A (en) | 2020-09-24 | 2020-12-16 | Cold power generation refrigeration container |
| CN202011488581.XA Withdrawn CN112303959A (en) | 2020-09-24 | 2020-12-16 | Gas precooling power generation equal enthalpy compressor |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011016916.8A Pending CN112013570A (en) | 2020-09-24 | 2020-09-24 | Isenthalpic compressor |
Family Applications After (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011488616.XA Withdrawn CN112303960A (en) | 2020-09-24 | 2020-12-16 | Cold power engine |
| CN202011488575.4A Withdrawn CN112283978A (en) | 2020-09-24 | 2020-12-16 | Cold power generation refrigeration container |
| CN202011488581.XA Withdrawn CN112303959A (en) | 2020-09-24 | 2020-12-16 | Gas precooling power generation equal enthalpy compressor |
Country Status (1)
| Country | Link |
|---|---|
| CN (5) | CN112013570A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023040189A1 (en) * | 2021-09-18 | 2023-03-23 | 成都佳灵绿色能源有限责任公司 | Zero-carbon reefer container refrigerating unit and refrigerating method |
-
2020
- 2020-09-24 CN CN202011016916.8A patent/CN112013570A/en active Pending
- 2020-12-16 CN CN202011488580.5A patent/CN112303958A/en not_active Withdrawn
- 2020-12-16 CN CN202011488616.XA patent/CN112303960A/en not_active Withdrawn
- 2020-12-16 CN CN202011488575.4A patent/CN112283978A/en not_active Withdrawn
- 2020-12-16 CN CN202011488581.XA patent/CN112303959A/en not_active Withdrawn
Also Published As
| Publication number | Publication date |
|---|---|
| CN112283978A (en) | 2021-01-29 |
| CN112303960A (en) | 2021-02-02 |
| CN112013570A (en) | 2020-12-01 |
| CN112303959A (en) | 2021-02-02 |
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