CN2867223Y - Water-cooled internal multiplex refrigerating system - Google Patents
Water-cooled internal multiplex refrigerating system Download PDFInfo
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- CN2867223Y CN2867223Y CN 200620025210 CN200620025210U CN2867223Y CN 2867223 Y CN2867223 Y CN 2867223Y CN 200620025210 CN200620025210 CN 200620025210 CN 200620025210 U CN200620025210 U CN 200620025210U CN 2867223 Y CN2867223 Y CN 2867223Y
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Abstract
The utility model discloses a water-cooling internal laminated refrigerating system, which uses water condensation method to obtain high refrigerating efficiency, short system balance time, stable operation and simple structure. The invention comprises a compressor, a water-cooling system, a water-cooling condenser, a gas-liquid separator with an internal water cooler, a condensing evaporator with inside a high-boiling-point medium evaporator, a thermal-insulated box with inside a low-boiling-point medium evaporator, a first heat regenerator and a second heat regenerator. The water-cooling condenser and the water cooler of gas-liquid separator are respectively connected with the water-cooling system. The invention utilizes the water condensation, therefore, the water cooler of the gas-liquid separator condenses the steam of the working medium with high boiling point, the water of water cooler and the condenser share one water system, to improve the utilization efficiency of high-boiling-point working medium and improve the efficiency of whole system. The invention has simple structure, short system balance time and the applied control on the refrigerating system.
Description
Technical field
The utility model relates to a kind of cascade refrigerating system, in particular, relates to adopt in a kind of water-cooled condenser and the vapour liquid separator cascade refrigerating system of water condensation mode.
Background technology
Cascade refrigerating system (auto-cascade refrigeration) has extraordinary application prospect in industries such as the energy, space flight, military project, biology, medicine, food, material.The refrigeration machine of this fabrication techniques adopts non-azeotropic mixed working medium to make cold-producing medium based on the KLEEMENKO circulation theory, and whole system only uses a compressor, and with the evaporative condenser low boiling working fluid of higher boiling working medium, the evaporation of low boiling working fluid obtains cold.Can obtain-50 ℃～-80 ℃ low temperature for two fluid system.This system is because equipment is few, and low having obtained of cost used widely.But evaporate the method for condensation higher boiling working substance steam at present in the vapour liquid separator of this system owing to employing higher boiling working medium, the utilization ratio of higher boiling working medium is lower, and the Energy Efficiency Ratio of whole system is lower.And, because the influence of the isolation technics of higher boiling working medium and low boiling working fluid, make and contain a certain proportion of higher boiling working medium in the low boiling working fluid, produce the drift of low boiling working fluid evaporating temperature, cause the stability of a system poor.
Patent publication No. is CN1363815A, denomination of invention is separated height effectively for the patent documentation of " deep refrigerating device " discloses a kind of employing rectifier unit isolation technics, the refrigerating plant of low boiling working fluid, though its separative efficiency improves, but the evaporating temperature that enters rectifier unit and condenser/evaporator owing to higher boiling working medium is different, according to this systemic circulation, can make the branch that enters rectifier unit and condenser/evaporator in higher boiling working medium mix and be difficult to control, and after vapour liquid separator top condensation higher boiling working substance steam, enter condenser/evaporator condensation low boiling working fluid again with the higher boiling working medium after the throttling, will certainly cause low boiling working fluid in vapour liquid separator, to be condensed in advance, cause the system balancing time long, Energy Efficiency Ratio is lower, is difficult to the commercialization and the industrialization of realization technology.In addition, experiment shows, the low boiling working fluid that contains ratio seldom in higher boiling working medium is very little to the influence of system, but contains the drift that the higher boiling working medium of ratio seldom can produce the low boiling working fluid evaporating temperature in the low boiling working fluid, causes the stability of a system poor.Therefore in rectifying column to the heating of higher boiling working medium to improve having little significance of higher boiling working medium purity, the stability of a system of this device is lower, and the utilization ratio of higher boiling working medium is lower, the Energy Efficiency Ratio of whole system is lower.
Patent publication No. is CN1677014A, denomination of invention is a kind of for the patent documentation of " mixed working medium cascade refrigerating system " discloses to adopt different evaporating temperatures to reach the purpose of condensation low boiling working fluid and higher boiling working medium respectively in condenser/evaporator and vapour liquid separator with higher boiling working medium, shortens the system balancing time to reach, the cascade refrigerating system of minimizing system energy consumption.But owing to adopt the air-cooled mode of coagulating, can increase the resistance of mixed working fluid in the two-phase flow of air cooled condenser, system condensing pressure can improve relatively, causes compression ratio to increase.And in vapour liquid separator in higher boiling working medium evaporator outlet and the condenser/evaporator between the higher boiling working medium evaporator outlet pipe be connected to evaporating pressure regulating valve balance sysmte back pressure, strengthened the irreversible loss of system, and system architecture is complicated.
The utility model content
The utility model is in order to overcome defective of the prior art, a kind of employing water condensation mode condensation higher boiling working substance steam is provided, to realize the better endless form of mixed working medium cascade refrigerating system, the control of realization system better, the refrigerating efficiency height, the system balancing time is short, and is stable, and be convenient to realize commercialization, water-cooling inside superposed refrigerating system simple in structure.
The utility model is achieved through the following technical solutions:
A kind of water-cooling inside superposed refrigerating system, it is characterized in that, comprise compressor, water cooling system, water-cooled condenser, vapour liquid separator and interior water cooler, condenser/evaporator and interior higher boiling working medium evaporimeter, insulation casing and interior low boiling working fluid evaporimeter, first regenerator and second regenerator thereof thereof thereof, described water-cooled condenser is connected with described water cooling system respectively with the interior water cooler of vapour liquid separator; The outlet of described compressor is connected with the inlet of described water-cooled condenser, and the outlet of described water-cooled condenser is connected to the middle part of vapour liquid separator, and the gas vent at described vapour liquid separator top is connected with the gas access at described condenser/evaporator top; The liquid outlet of described vapour liquid separator bottom is connected with the inlet of second regenerator, magnetic valve, higher boiling throttling element, higher boiling working medium evaporimeter successively, the liquid outlet of described condenser/evaporator bottom is connected with the inlet of first regenerator, magnetic valve, low boiling working fluid restricting element, low boiling working fluid evaporimeter successively, and the outlet of described low boiling working fluid evaporimeter is connected with first regenerator, second regenerator successively; The outlet of the outlet of described higher boiling working medium evaporimeter and the low boiling working fluid of second regenerator is connected to the inlet of compressor after in parallel by pipeline.
Described restricting element is one or more the combination in one section capillary, manual or automatic valve, the orifice plate type decompressor.
A kind of water-cooling inside superposed refrigerating system, it is characterized in that, comprise compressor, water cooling system, vapour liquid separator and interior first water cooler and second cooler, condenser/evaporator and interior higher boiling working medium evaporimeter, insulation casing and interior low boiling working fluid evaporimeter, first regenerator and second regenerator thereof thereof thereof, first water cooler in the described vapour liquid separator is connected with described water cooling system respectively with second cooler; The outlet of described compressor is connected to the middle part of vapour liquid separator, and the gas vent at described vapour liquid separator top is connected with the gas access at described condenser/evaporator top; The liquid outlet of described vapour liquid separator bottom is connected with the inlet of second regenerator, magnetic valve, higher boiling throttling element, higher boiling working medium evaporimeter successively, the liquid outlet of described condenser/evaporator bottom is connected with the inlet of first regenerator, magnetic valve, low boiling working fluid restricting element, low boiling working fluid evaporimeter successively, and the outlet of described low boiling working fluid evaporimeter is connected with first regenerator, second regenerator successively; The outlet of the outlet of described higher boiling working medium evaporimeter and the low boiling working fluid of second regenerator is connected to the inlet of compressor after in parallel by pipeline.
Described restricting element is one or more the combination in one section capillary, manual or automatic valve, the orifice plate type decompressor.
The utlity model has following technique effect:
1. the utility model water-cooled mixed working medium cascade refrigerating system is owing to adopted the water condensation mode, in vapour liquid separator, adopt water cooler condensation higher boiling working substance steam, the shared cover water system of water in the water cooler and condenser, thereby improved the utilization ratio of higher boiling working medium, that is improved the Energy Efficiency Ratio of total system.
2. in vapour liquid separator, adopt cooling water condensation higher boiling working substance steam, thereby make the interior overlapping system of both vapor compression more be tending towards rationalizing, can effectively control the purity and the evaporating temperature of higher boiling working medium, improve the purity of low boiling working fluid simultaneously, temperature drift when reducing the low boiling working fluid evaporation has increased entire system stability.And refrigerant system configurations of the present utility model is simple, the system balancing time is short, can well realize refrigeration system control.
3. the compressor that uses in the refrigeration system of the present utility model is the common refrigeration compressor with oil lubrication, and compression ratio is less than 10.Do not need cryogenic compressor in the refrigeration system of the present utility model, and lubricating oil also is plain oil, in other words also without limits to the use of lubricating oil, therefore not only can reduce the refrigeration system production cost, also can reduce the refrigeration system use cost, the convenient use is convenient to promote.
Description of drawings
Fig. 1 is the structural representation of the water-cooling inside superposed refrigerating system of the shared cover water system of the utility model water-cooled condenser and water cooler;
Fig. 2 is arranged in the structural representation of the water-cooling inside superposed refrigerating system of the shared cover water system of two water coolers of vapour liquid separator for the utility model.
Among the figure: 1-compressor, 2-water-cooled condenser, 3-vapour liquid separator, 4-water cooler, 4-1-first water cooler, 4-2-second water cooler, 5-higher boiling working medium evaporimeter, 7-magnetic valve, 8-higher boiling throttling element, 9-magnetic valve, 10-low boiling working fluid restricting element, 11-insulation casing, 12-low boiling working fluid evaporimeter, 13-first regenerator, 14-second regenerator, 15-water cooling system.
The specific embodiment
Below in conjunction with the drawings and specific embodiments the utility model is described in detail.
Fig. 1 is the structural representation of the water-cooling inside superposed refrigerating system of the shared cover water system of the utility model water-cooled condenser and water cooler, comprise compressor 1, water cooling system 15, water-cooled condenser 2, vapour liquid separator 3 and interior water cooler 4 thereof, condenser/evaporator 6 and interior higher boiling working medium evaporimeter 5 thereof, insulation casing 11 and interior low boiling working fluid evaporimeter 12 thereof, first regenerator 13 and second regenerator 14, water-cooled condenser 2 is connected with water cooling system 15 respectively with the interior water cooler 4 of vapour liquid separator, like this, the 4 public cover water cooling systems of the water cooler in water-cooled condenser 2 and the vapour liquid separator.The outlet of compressor 1 is connected with the inlet of water-cooled condenser 2, and the outlet of water-cooled condenser 2 is connected to the middle part of vapour liquid separator 3, and the gas vent at vapour liquid separator 3 tops is connected with the gas access at condenser/evaporator 6 tops.The liquid outlet of vapour liquid separator 3 bottoms successively with second regenerator 14, magnetic valve 7, higher boiling throttling element 8, the inlet of higher boiling working medium evaporimeter 5 connects, the liquid outlet of condenser/evaporator 6 bottoms successively with first regenerator 13, magnetic valve 9, low boiling working fluid restricting element 10, the inlet of low boiling working fluid evaporimeter 12 connects, the outlet of low boiling working fluid evaporimeter 12 successively with first regenerator 13, second regenerator 14 connects, and the outlet of higher boiling working medium evaporimeter and the low boiling working fluid of second regenerator export by pipeline the inlet that is connected to compressor 1 after in parallel.The utility model water-cooling inside superposed refrigerating system appropriate design also adopts water cooler 4 water condensation higher boiling working substance steam in vapour liquid separator 3, water in the water cooler 4 and water-cooled condenser 2 shared cover water systems, replaced the prior art cascade refrigerating system evaporates condensation higher boiling working substance steam with higher boiling working medium in vapour liquid separator method, it as patent publication No. disclosed technical scheme in two patent documentations of CN1363815A and CN1677014A, avoided the defective of prior art, improve the utilization ratio of higher boiling working medium, that is improved the Energy Efficiency Ratio of total system.
The compressor 1 that the utility model refrigeration system is used is the common refrigeration compressor with oil lubrication, and compression ratio is less than 10.Its effect is that the compression and low pressure mixed working fluid is with its pressure that raises.Do not need cryogenic compressor in the utility model refrigeration system, and lubricating oil also is plain oil, in other words also without limits to the use of lubricating oil, therefore not only can reduce the refrigeration system production cost, also can reduce the refrigeration system use cost, the convenient use is convenient to promote.
The water-cooled condenser 2 that the utility model refrigeration system is used is the water cooled condenser that common kind of refrigeration cycle is used, its effect is the heat of emitting the high pressure mixing Working medium gas after compressed machine 1 compresses, make the condensation therein of higher boiling working medium, low boiling working fluid cools off therein simultaneously.Its heat-absorbing medium that adopts can be normal-temperature water or other fluids.
Vapour liquid separator 3 described in the utility model refrigeration system and supporting pipeline can adopt material filling type rectifying column or distillation system in the chemical field extensive use.In this cascade refrigerating system, play the purpose of vapor-liquid separation, its effect is that the mixing vapour-liquid working medium that two or more boiling points are different is separated, and separates through the higher boiling working medium of condenser 2 condensations with through condenser 2 uncooled low boiling working fluids in the utility model refrigeration system.Make low boiling working fluid steam enter condenser/evaporator 6 from top, the higher boiling worker quality liquid then sinks to the bottom, by entering the higher boiling working medium evaporimeter 5 in the condenser/evaporator 6 behind second heat exchanger 14, magnetic valve 7 and the higher boiling throttling element 8.
The effect of water cooler 4 is the higher boiling working substance steam in the condensation vapour liquid separator 3, and to improve the purity of low boiling working fluid, the temperature drift when reducing the low boiling working fluid evaporation has increased entire system stability, can well realize refrigeration system control.
Magnetic valve 7, magnetic valve 9 are common electric stop valves, and its effect is that worker quality liquid no longer flows to corresponding evaporimeter after guaranteeing system-down, guarantees the pressure of compressor 1 high-low pressure both sides.
Higher boiling throttling element 8 and low boiling working fluid restricting element 10 are decompressor, and its effect is to make the decompression of high-pressure working medium liquid.The form that restricting element adopts is unrestricted, can be one section capillary, also can be manual or automatic valve, also can be orifice plate type decompressor, or their any combination.
Higher boiling working medium evaporimeter 5 is an evaporimeter, and its effect is to make low pressure higher boiling worker quality liquid evaporation flow into high pressure higher boiling steam the condenser/evaporator 6 with condensation from vapour liquid separator 3.
Low boiling working fluid evaporimeter 12 also is an evaporimeter, and the one side is evaporated heat absorption by low-pressure low-temperature low boiling working fluid fluid, and opposite side is the cooled object heat release, and cooled object can be fluid or solid.
Condenser/evaporator 6 is heat exchangers commonly used in the prior art, and main effect is the evaporative condenser low boiling working fluid that utilizes higher boiling working medium.One side process be low pressure high boiling liquid working medium, and evaporation heat absorption; The opposite side process be high pressure low-boiling point gas working medium, and condensation heat release.
The mixed working fluid that refrigeration system of the present utility model is used be the different working medium of high low boiling to or the combination of several working medium.Described working medium can be selected in following material: R134a, R22, R290, R600a, R123, R23, R13, R50, R1150, R170 etc., for example the working medium that can select is to being: R134a/R23, R600a/R170, R290/R50 or R290/R170 etc. also can be that the working medium of isolated gas composition from air or natural gas is right.
The part that the utility model mixed working medium cascade refrigerating system is not addressed is applicable to prior art.
The course of work of the utility model refrigeration system is as follows: together enter compressor 1 from the low pressure low boiling working fluid steam of second regenerator 14 and low pressure higher boiling working substance steam through higher boiling working medium evaporimeter 5, the high pressure mixing working substance steam of compressed machine 1 compression enters water-cooled condenser 2, is cooled to the high pressure liquid-vapor mixture after emitting heat.Wherein higher boiling working medium is condensed into liquid, and low boiling working fluid still is a gas.The high pressure liquid-vapor mixture enters vapour liquid separator 3, carries out the separation of two kinds of working medium.In vapour liquid separator 3, low boiling working fluid steam rises and enters the top of vapour liquid separator 3, and the liquid of higher boiling working medium sinks to its bottom.The higher boiling working substance steam of low boiling working fluid entrainment with steam that rises to vapour liquid separator 3 tops is sunk to vapour liquid separator 3 bottoms by water cooler 4 condensations.
Bottom liquid phases higher boiling working medium is cold excessively by low temperature low boiling working fluid steam through second regenerator 14, after magnetic valve 7 is by 8 step-downs of higher boiling throttling element, enter in the higher boiling working medium evaporimeter 5 in the condenser/evaporator 6, absorb the low boiling working fluid condensation heat and be evaporated to behind the low boiling steam low pressure low boiling working fluid steam with second regenerator, 14 exits and merge and get back to compressor 1.
Top high-voltage low boiling working fluid steam at vapour liquid separator 3 enters condenser/evaporator 6 after water cooler 4 coolings are purified, the purity of these low boiling working fluid steam is than the low boiling working fluid steam-purity value height that enters in the vapour liquid separator 3.Cooling through higher boiling working medium evaporimeter 5 in condenser/evaporator 6 is condensed into liquid, sink to the bottom of condenser/evaporator 6, this high pressure low boiling working fluid liquid is cold excessively by low temperature low boiling working fluid steam through first regenerator 13, the low boiling working fluid evaporimeter 12 that enters in the insulation casing 11 by magnetic valve 9,10 step-downs of low boiling working fluid restricting element evaporates absorbing and cooling temperature, has realized the refrigeration purpose.The low pressure low boiling working fluid steam that comes out from low boiling working fluid evaporimeter 12 through the heat absorption evaporation enters first regenerator 13 and second regenerator 14 successively, cool off low boiling working fluid liquid and higher boiling worker quality liquid respectively, the heat absorption back of heating up merges with low pressure higher boiling working substance steam from higher boiling working medium evaporimeter 5 exits and is back to compressor 1, mist is compressed once more, thereby finishes whole systemic circulation.
Another embodiment of the present utility model is separately installed with water cooler 4-1 for the two parts up and down at vapour liquid separator, 4-2, the shared cover water cooling system of above-mentioned two water coolers, its structural representation as shown in Figure 2, comprise compressor 1, water cooling system 15, vapour liquid separator 3 and the interior first water cooler 4-1 and the second cooler 4-2 thereof, condenser/evaporator 6 and interior higher boiling working medium evaporimeter 5 thereof, insulation casing 11 and interior low boiling working fluid evaporimeter 12 thereof, first regenerator 13 and second regenerator 14, the first water cooler 4-1 in the vapour liquid separator 3 is connected with water cooling system 15 respectively with the second cooler 4-2, a shared cover water cooling system.The outlet of compressor 1 is connected to the middle part of vapour liquid separator 3, and the gas vent at vapour liquid separator 3 tops is connected with the gas access at condenser/evaporator 6 tops.The liquid outlet of vapour liquid separator 3 bottoms successively with second regenerator 14, magnetic valve 7, higher boiling throttling element 8, the inlet of higher boiling working medium evaporimeter 5 connects, the liquid outlet of condenser/evaporator 6 bottoms successively with first regenerator 13, magnetic valve 9, low boiling working fluid restricting element 10, the inlet of low boiling working fluid evaporimeter 12 connects, the outlet of low boiling working fluid evaporimeter 12 successively with first regenerator 13, second regenerator 14 connects, and the outlet of higher boiling working medium evaporimeter 5 and the low boiling working fluid of second regenerator 14 export by pipeline the inlet that is connected to compressor 1 after in parallel.The difference of this embodiment and embodiment shown in Figure 1 is that two parts up and down of vapour liquid separator are separately installed with water cooler, has replaced water-cooled condenser with one of them water cooler, and other parts are identical with embodiment shown in Figure 1.Its course of work is: together enter compressor 1 from the low pressure low boiling working fluid steam of second regenerator 14 and low pressure higher boiling working substance steam through higher boiling working medium evaporimeter 5, the high pressure mixing working substance steam of compressed machine 1 compression enters in the vapour liquid separator 3.In vapour liquid separator 3, low boiling working fluid steam rises and enters the top of vapour liquid separator 3, and the higher boiling working substance steam is sunk to vapour liquid separator 3 bottoms by water cooler 4-1 and 4-2 condensation.
Bottom liquid phases higher boiling working medium is cold excessively by low temperature low boiling working fluid steam through second regenerator 14, after magnetic valve 7 is by 8 step-downs of higher boiling throttling element, enter in the higher boiling working medium evaporimeter 5 in the condenser/evaporator 6, absorb the low boiling working fluid condensation heat and be evaporated to behind the low boiling steam low pressure low boiling working fluid steam with second regenerator, 14 exits and merge and get back to compressor 1.
Top high-voltage low boiling working fluid steam at vapour liquid separator 3 enters condenser/evaporator 6 after water cooler 4-1 and 4-2 cooling purification, the purity of these low boiling working fluid steam is than the low boiling working fluid steam-purity value height that enters in the vapour liquid separator 3.Cooling through higher boiling working medium evaporimeter 5 in condenser/evaporator 6 is condensed into liquid, sink to the bottom of condenser/evaporator 6, this high pressure low boiling working fluid liquid is cold excessively by low temperature low boiling working fluid steam through first regenerator 13, the low boiling working fluid evaporimeter 12 that enters in the insulation casing 11 by magnetic valve 9,10 step-downs of low boiling working fluid restricting element evaporates absorbing and cooling temperature, has realized the refrigeration purpose.The low pressure low boiling working fluid steam that comes out from low boiling working fluid evaporimeter 12 through the heat absorption evaporation enters first regenerator 13 and second regenerator 14 successively, cool off low boiling working fluid liquid and higher boiling worker quality liquid respectively, the heat absorption back of heating up merges with low pressure higher boiling working substance steam from higher boiling working medium evaporimeter 5 exits and is back to compressor 1, mist is compressed once more, thereby finishes whole systemic circulation.
Although relate to a kind of water-cooling inside superposed refrigerating system and carried out special description disclosed with reference to embodiment, embodiment described above is illustrative and not restrictive, under the situation that does not break away from spirit and scope of the present utility model, all variations and modification are all within scope of the present utility model.
Claims (4)
1. water-cooling inside superposed refrigerating system, it is characterized in that, comprise compressor, water cooling system, water-cooled condenser, vapour liquid separator and interior water cooler, condenser/evaporator and interior higher boiling working medium evaporimeter, insulation casing and interior low boiling working fluid evaporimeter, first regenerator and second regenerator thereof thereof thereof, described water-cooled condenser is connected with described water cooling system respectively with the interior water cooler of vapour liquid separator; The outlet of described compressor is connected with the inlet of described water-cooled condenser, and the outlet of described water-cooled condenser is connected to the middle part of vapour liquid separator, and the gas vent at described vapour liquid separator top is connected with the gas access at described condenser/evaporator top; The liquid outlet of described vapour liquid separator bottom is connected with the inlet of second regenerator, magnetic valve, higher boiling throttling element, higher boiling working medium evaporimeter successively, the liquid outlet of described condenser/evaporator bottom is connected with the inlet of first regenerator, magnetic valve, low boiling working fluid restricting element, low boiling working fluid evaporimeter successively, and the outlet of described low boiling working fluid evaporimeter is connected with first regenerator, second regenerator successively; The outlet of the outlet of described higher boiling working medium evaporimeter and the low boiling working fluid of second regenerator is connected to the inlet of compressor after in parallel by pipeline.
2. water-cooling inside superposed refrigerating system according to claim 1 is characterized in that, described restricting element is one or more the combination in one section capillary, manual or automatic valve, the orifice plate type decompressor.
3. water-cooling inside superposed refrigerating system, it is characterized in that, comprise compressor, water cooling system, vapour liquid separator and interior first water cooler and second cooler, condenser/evaporator and interior higher boiling working medium evaporimeter, insulation casing and interior low boiling working fluid evaporimeter, first regenerator and second regenerator thereof thereof thereof, first water cooler in the described vapour liquid separator is connected with described water cooling system respectively with second cooler; The outlet of described compressor is connected to the middle part of vapour liquid separator, and the gas vent at described vapour liquid separator top is connected with the gas access at described condenser/evaporator top; The liquid outlet of described vapour liquid separator bottom is connected with the inlet of second regenerator, magnetic valve, higher boiling throttling element, higher boiling working medium evaporimeter successively, the liquid outlet of described condenser/evaporator bottom is connected with the inlet of first regenerator, magnetic valve, low boiling working fluid restricting element, low boiling working fluid evaporimeter successively, and the outlet of described low boiling working fluid evaporimeter is connected with first regenerator, second regenerator successively; The outlet of the outlet of described higher boiling working medium evaporimeter and the low boiling working fluid of second regenerator is connected to the inlet of compressor after in parallel by pipeline.
4. water-cooling inside superposed refrigerating system according to claim 3 is characterized in that, described restricting element is one or more the combination in one section capillary, manual or automatic valve, the orifice plate type decompressor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620025210 CN2867223Y (en) | 2006-01-20 | 2006-01-20 | Water-cooled internal multiplex refrigerating system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620025210 CN2867223Y (en) | 2006-01-20 | 2006-01-20 | Water-cooled internal multiplex refrigerating system |
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| CN2867223Y true CN2867223Y (en) | 2007-02-07 |
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| CN 200620025210 Expired - Lifetime CN2867223Y (en) | 2006-01-20 | 2006-01-20 | Water-cooled internal multiplex refrigerating system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100357674C (en) * | 2006-01-20 | 2007-12-26 | 天津商学院 | Water-cooling inside superposed refrigerating system |
| CN104298257A (en) * | 2014-09-24 | 2015-01-21 | 上海空间推进研究所 | Gas micro-flow throttler |
-
2006
- 2006-01-20 CN CN 200620025210 patent/CN2867223Y/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100357674C (en) * | 2006-01-20 | 2007-12-26 | 天津商学院 | Water-cooling inside superposed refrigerating system |
| CN104298257A (en) * | 2014-09-24 | 2015-01-21 | 上海空间推进研究所 | Gas micro-flow throttler |
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| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Effective date of abandoning: 20071226 |
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| C25 | Abandonment of patent right or utility model to avoid double patenting |