CN204757428U - Four control double evaporation ware refrigerating system - Google Patents
Four control double evaporation ware refrigerating system Download PDFInfo
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- CN204757428U CN204757428U CN201520453042.0U CN201520453042U CN204757428U CN 204757428 U CN204757428 U CN 204757428U CN 201520453042 U CN201520453042 U CN 201520453042U CN 204757428 U CN204757428 U CN 204757428U
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- evaporimeter
- refrigerant
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- low pressure
- oil return
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Abstract
The utility model discloses a four control double evaporation ware refrigerating system, including compressor, oil separator, condenser, second evaporimeter, system ice evaporate ware, low -pressure circulation barrel, oil return jet pump and refrigerant solution feed pump, oil separator's gas outlet links to each other with the air inlet that deices air inlet and oil return jet pump of the high -pressure air inflow mouth of the air inlet of condenser, second evaporimeter, system ice evaporate ware simultaneously, the refrigerant solution feed pump is continuous with the refrigerant import of system ice evaporate ware after supplying the liquid check valve, the refrigerant export of system ice evaporate ware is continuous with low -pressure circulation barrel's gas -liquid import behind refrigerant discharge solenoid valve, and it deices the gas outlet and links to each other with the second evaporimeter after deicing steam discharge check valve and deice steam discharge solenoid valve. The utility model discloses it is simple to make the heat transfer area configuration to system's operation is stable, and the energy consumption is low.
Description
Technical field
The utility model relates to refrigeration system, particularly relates to a kind of four-pipe system Dual-evaporator refrigeration system.
Background technology
At present, board-like ice machine or refrigeration system are adopt single evaporimeter at air conditioning condition and ice making operating mode, operating point difference causes the configuration of single evaporator heat exchanger heat exchange area to there is certain difficulty, can not directly to end cooling during refrigeration system air conditioning condition, need by intermediate heat transfer process terminad cooling, cause the stability of a system poor, and refrigeration system efficiency reduce.
Usually, ice machine or refrigeration system are divided into cooling condition and deice operating mode, and wherein cooling condition is divided into chilled water operating mode and ice making operating mode.When hot-gas deicing operating mode, the high-temperature high-pressure refrigerant gas of compressor outlet enters evaporimeter through hot-gas deicing magnetic valve and deices, become the gas liquid mixture of low-temp low-pressure, through hot-gas deicing dump valve check valve get back to low pressure recycle bucket or compressor suction duct overheated after (increase heat exchanger) enter compressor.The gas liquid mixture temperature compared with cold-producing medium in low pressure recycle bucket entering low pressure recycle bucket through hot-gas deicing discharge check valve is higher, cause gaseous refrigerant physical property change in low pressure recycle bucket liquid fluctuating and low pressure recycle bucket, make compressor and whole system fluctuation of service; Discharge after check valve enters heat exchanger heat exchange through hot-gas deicing and enter compressor, cause compressor air suction band liquid to make pressure of inspiration(Pi) too low because liquid in gas liquid mixture is more, cause compressor and system works unstable, even there will be refrigeration system and can not normally to run and liquid hit phenomenon causes the damage of compressor; Affect unit ice making, deice efficiency, reduce whole system efficiency.
Utility model content
For prior art above shortcomings, it is difficult that the purpose of this utility model is how to solve the configuration of existing ice-making system heat exchange area, operation stability is poor, the problem that system energy consumption is high, a kind of four-pipe system Dual-evaporator refrigeration system is provided, heat exchange area can be made to configure simple, and system run all right, energy consumption is low.
In order to solve the problems of the technologies described above, the technical solution adopted in the utility model is such: a kind of four-pipe system Dual-evaporator refrigeration system, is characterized in that: comprise refrigeration compressor, oil eliminator, condenser, the second evaporimeter, ice making evaporator, low pressure recycle bucket, oil return jet pump and refrigerant feed liquid pump;
The gas outlet of described refrigeration compressor is connected with the air inlet of oil eliminator, the oil return opening of described oil eliminator is connected with the air entry of refrigeration compressor after oil eliminator oil return solenoid valve, is connected the while of its gas outlet with the air inlet of condenser, the high pressure admission mouth of the second evaporimeter, the air inlet deicing air inlet and oil return jet pump of ice making evaporator; Wherein, hot gas bypass solenoid valve is provided with between the gas outlet of oil eliminator and the high pressure admission mouth of the second evaporimeter, between the gas outlet and the air inlet of ice making evaporator of oil eliminator, be provided with hot-gas deicing magnetic valve, between the gas outlet of oil eliminator and the air inlet of oil return jet pump, be provided with injection magnetic valve;
The refrigerant outlet of described condenser through in press electric expansion valve after be connected with compression refrigerant import in the second evaporimeter, the economizer tonifying Qi outlet of the second evaporimeter is connected with the economizer tonifying Qi interface of refrigeration compressor through economizer tonifying Qi magnetic valve, and its gas returning port is connected with the air entry of refrigeration compressor through the second evaporimeter return-air motor-driven valve; The oil return opening of this second evaporimeter is connected with the ejecting port of oil return jet pump through the second evaporimeter oil return solenoid valve;
The refrigerant outlet of the second evaporimeter is connected with the low pressure refrigerant import of low pressure recycle bucket after Low-voltage Electronic expansion valve; The refrigerant outlet of described low pressure recycle bucket is connected with refrigerant feed liquid pump, and refrigerant feed liquid pump is connected with the refrigerant inlet of ice making evaporator after feed flow check valve; The gas returning port of this low pressure recycle bucket is connected with the air entry of refrigeration compressor after low pressure recycle bucket return-air motor-driven valve, and its oil return opening is connected with the ejecting port of oil return jet pump through low pressure recycle bucket oil return solenoid valve; The described outlet of oil return jet pump is connected with the air entry of refrigeration compressor;
The refrigerant outlet of described ice making evaporator is discharged after magnetic valve through cold-producing medium and is connected with the gas-liquid import of low pressure recycle bucket, and it deices gas outlet and is connected with the second evaporimeter with deicing after hot gas discharges magnetic valve through deicing hot gas discharge check valve.
Further, be provided with differential pressure controller with refrigerant feed liquid parallel connection of pumps, for detecting the pressure reduction of refrigerant feed liquid pump inlet and liquid outlet; Liquid pump bypass solenoid valve is provided with between the liquid outlet and the gas-liquid import of low pressure recycle bucket of refrigerant feed liquid pump.
Further, liquid pump oil returning tube is provided with between refrigerant feed liquid pump and the air entry of refrigeration compressor, one end of described liquid pump oil returning tube is connected with the liquid outlet of refrigeration solution feed pump, and the other end is connected with the air inlet of refrigeration compressor, and liquid pump oil returning tube is provided with liquid pump oil return solenoid valve.
Further, low pressure recycle bucket and the second evaporimeter are respectively equipped with low pressure recycle bucket liquid level sensor and the second evaporimeter liquid level sensor.
Further, between the gas returning port and refrigeration compressor of low pressure recycle bucket, be provided with heat exchanger, the refrigerant outlet of condenser also through heat exchanger cross cold after be connected to middle pressure electric expansion valve again.
Further, described ice making evaporator for organize plate-type evaporator more.
Further, described second evaporimeter is the full liquid evaporimeter of shell-tube type.
Compared with prior art, the utility model tool has the following advantages:
1, double evaporators structure (ice making evaporator and the second evaporimeter) is adopted, different evaporators can be utilized to realize air conditioning condition and ice making operating mode, eliminate the problem that the configuration of single evaporator heat exchange area is difficult, and improve refrigeration system operation stability and comprehensive energy efficiency further.
2, ice making evaporator is connected with four pipelines, and every root pipeline is connected from different equipment, make cooling condition and deice operating mode to be circulated by different pipeline, eliminate the impact of making on system run all right and efficiency when deicing operating mode, thus the stability of further raising system, reduce the operation energy consumption of system.
3, liquid pump oil return system adopts initiatively (pressure) formula liquid pump oil return, efficiently solves refrigeration compressor oil level unstable problem when refrigeration system is run, thus the stability that raising refrigeration system is run; And solve because refrigeration compressor oil level is unstable and system loses the oily warning phenomenon produced.
Accompanying drawing explanation
Fig. 1 is structural principle block diagram of the present utility model.
In figure: 1-refrigeration compressor, 2-oil eliminator, 3-condenser, 4-the second evaporimeter, 5-ice making evaporator, 6-low pressure recycle bucket, 7-oil return jet pump, 8-refrigerant feed liquid pump, 9-oil eliminator oil return solenoid valve, 10-hot gas bypass solenoid valve, 11-hot-gas deicing magnetic valve, 12-injection magnetic valve, 13-middle pressure electric expansion valve, 14-economizer tonifying Qi magnetic valve, 15-the second evaporimeter return-air motor-driven valve, 16-the second evaporimeter oil return solenoid valve, 17-Low-voltage Electronic expansion valve, 18-feed flow check valve, 19-low pressure recycle bucket return-air motor-driven valve, 20-low pressure recycle bucket oil return solenoid valve, magnetic valve discharged by 21-cold-producing medium, 22-deice hot gas to discharge check valve, 23-deice hot gas to discharge magnetic valve, 24-differential pressure controller, 25-liquid pump bypass solenoid valve, 26-liquid pump oil returning tube, 27-liquid pump oil return solenoid valve, 28-low pressure recycle bucket liquid level sensor, 29-the second evaporimeter liquid level sensor.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is described in further detail.
Embodiment: see Fig. 1, a kind of four-pipe system Dual-evaporator refrigeration system, comprises refrigeration compressor 1, oil eliminator 2, condenser 3, second evaporimeter 4, ice making evaporator 5, low pressure recycle bucket 6, oil return jet pump 7 and refrigerant feed liquid pump 8; During concrete enforcement, whole system is controlled by system controller.Described ice making evaporator 5 is many group plate-type evaporators or other vertical type evaporators by hot-gas deicing; Described second evaporimeter 4 is the full liquid evaporimeter of shell-tube type.
The gas outlet of described refrigeration compressor 1 is connected with the air inlet of oil eliminator 2, the oil return opening of described oil eliminator 2 is connected with the air entry of refrigeration compressor 1 after oil eliminator oil return solenoid valve 9, gaseous refrigerant compresses through refrigeration compressor 1 and forms high temperature and high pressure gaseous refrigerant, access oil eliminator 2 carries out Oil-gas Separation, and the lubricating oil of separation gets back to refrigeration compressor 1 through oil eliminator oil return solenoid valve 9.The gas outlet of oil eliminator 2 is connected with the air inlet of condenser 3, the high pressure admission mouth of the second evaporimeter 4, the air inlet deicing air inlet and oil return jet pump 7 of ice making evaporator 5 simultaneously.Wherein, hot gas bypass solenoid valve 10 is provided with between the gas outlet of oil eliminator 2 and the high pressure admission mouth of the second evaporimeter 4, in work, system controller is by detection second evaporimeter 4 refrigerant pressure and control the keying of the second evaporimeter 4 hot gas bypass solenoid valve 10.Between the gas outlet of oil eliminator 2 and the air inlet of ice making evaporator 5, be provided with hot-gas deicing magnetic valve 11, between the gas outlet of oil eliminator 2 and the air inlet of oil return jet pump 7, be provided with injection magnetic valve 12.Like this; the gaseous refrigerant after oil eliminator 2 is separated is made to divide four tunnels: a road connects hot-gas deicing magnetic valve 11 in order to deicing; one tunnel takes back oily jet pump 7 in order to ejecting scavenge return; one road is accessed the second evaporimeter 4 and is condensed into liquid refrigerant in order to protection second evaporimeter 4, tunnel access (water-cooled) condenser 3.
The refrigerant outlet of described condenser 3 through in press electric expansion valve 13 after be connected with compression refrigerant import in the second evaporimeter 4, formed after condenser 3 condensation the liquid refrigerant of pressing in high temperature through in press electric expansion valve 13 throttling to lower the temperature after (in formation warm cold-producing medium) to enter the second evaporimeter 4.The economizer tonifying Qi outlet of the second evaporimeter 4 is connected with the economizer tonifying Qi interface of refrigeration compressor 1 through economizer tonifying Qi magnetic valve 14, and its gas returning port is connected with the air entry of refrigeration compressor 1 through the second evaporimeter return-air motor-driven valve 15.The oil return opening of this second evaporimeter 4 is connected with the ejecting port of oil return jet pump 7 through the second evaporimeter oil return solenoid valve 16.During air conditioning condition, the second evaporimeter 4 freezes with external agents heat exchange, and the gaseous refrigerant formed after evaporation is back to refrigeration compressor 1 through the second evaporimeter return-air motor-driven valve 15, realizes air conditioner refrigerating circulation.
The refrigerant outlet of the second evaporimeter 4 is connected with the low pressure refrigerant import of (have liquid storage with gas-liquid separating function) low pressure recycle bucket 6 after Low-voltage Electronic expansion valve 17.The refrigerant outlet of described low pressure recycle bucket 6 is connected with refrigerant feed liquid pump 8, and refrigerant feed liquid pump 8 is connected with the refrigerant inlet of ice making evaporator 5 after feed flow check valve 18; The gas returning port of this low pressure recycle bucket 6 is connected with the air entry of refrigeration compressor 1 after low pressure recycle bucket return-air motor-driven valve 19, and its oil return opening is connected with the ejecting port of oil return jet pump 7 through low pressure recycle bucket oil return solenoid valve 20; The outlet of described oil return jet pump 7 is connected with the air entry of refrigeration compressor 1.The refrigerant outlet of described ice making evaporator 5 is discharged after magnetic valve 21 through cold-producing medium and is connected with the gas-liquid import of low pressure recycle bucket 6, and it deices gas outlet and is connected with the second evaporimeter 4 with deicing after hot gas discharges magnetic valve 23 through deicing hot gas discharge check valve 22.Such ice making evaporator 5 is connected with four pipelines, that is: the refrigerant inlet of ice making evaporator 5 is connected with refrigerant feed liquid pump 8 by input duct, and its refrigerant outlet is connected with the gas-liquid import of low pressure recycle bucket 6; The air inlet that deices of refrigerating evaporator is connected with oil eliminator 2 by pipeline, and it is deiced gas outlet and is connected with the second evaporimeter 4 by pipeline.During ice making operating mode, close the second evaporimeter return-air motor-driven valve 15, and keep passing into the second evaporimeter 4 and refrigerant heat exchanger without external agents, make the middle temperature cold-producing medium in the second evaporimeter 4 enter low pressure recycle bucket 6 after Low-voltage Electronic expansion valve 17 throttling cooling (formation low-temperature refrigerant).Low-temperature refrigerant enters ice making evaporator 5 after refrigerant feed liquid pump 8 and feed flow check valve 18, with medium heat exchange ice making outside ice making evaporator 5; The cold-producing medium that low-temperature refrigerant forms gas-liquid mixed after evaporator heat exchange is discharged through refrigeration and is accessed low pressure recycle bucket 6 after magnetic valve and carry out gas-liquid separation.Gaseous refrigerant in low pressure recycle bucket 6 is back to refrigeration compressor 1 after low pressure recycle bucket return-air motor-driven valve 19, and liquid refrigerant is stored in low pressure recycle bucket 6 and continues cooled dose of industrial pumping and realize ice-make cycle to evaporimeter.In this process, second evaporimeter 4 is made economizer and is used, after oil is separated, high-temperature high-pressure refrigerant accesses the second evaporimeter 4 (system controller is by detection second evaporimeter 4 refrigerant pressure and control the keying of hot gas bypass solenoid valve 10) through hot gas bypass solenoid valve 10, and gaseous refrigerant is connected to the economizer tonifying Qi interface of refrigeration compressor 1 after economizer tonifying Qi magnetic valve 14.When deicing work, HTHP hot gas enters ice making evaporator 5 through the air inlet that deices of ice making evaporator 5, then enters in the second evaporimeter 4 from deicing after gas outlet is discharged of ice making evaporator 5; Eliminate the impact of making on system run all right and efficiency when deicing operating mode, thus the stability of further raising system, reduce the operation energy consumption of system.
During concrete enforcement, liquid pump oil returning tube 26 is provided with between refrigerant feed liquid pump 8 and the air entry of refrigeration compressor 1, one end of described liquid pump oil returning tube 26 is connected with the liquid outlet of refrigeration solution feed pump, the other end is connected with the air inlet of refrigeration compressor 1, and liquid pump oil returning tube 26 is provided with liquid pump oil return solenoid valve 27.Adopt initiatively (pressure) formula liquid pump oil return, efficiently solve refrigeration compressor 1 oil level unstable problem when refrigeration system is run, thus the stability that raising refrigeration system is run.
In parallelly with refrigerant feed liquid pump 8 be provided with differential pressure controller 24, for detecting the pressure reduction of refrigerant feed liquid pump 8 inlet and liquid outlet; Liquid pump bypass solenoid valve 25 is provided with between the liquid outlet and the gas-liquid import of low pressure recycle bucket 6 of refrigerant feed liquid pump 8; During for controlling that pressure reduction is lower before and after the refrigerant feed liquid pump 8 that differential pressure controller 24 detects, cold-producing medium direct bypass enters gas in low pressure recycle bucket 6 excavationg pump.
Low pressure recycle bucket 6 and the second evaporimeter 4 are respectively equipped with low pressure recycle bucket liquid level sensor 28 and the second evaporimeter liquid level sensor 29.Second evaporimeter liquid level sensor 29 forms the second evaporimeter 4 tank level control system with middle pressure electric expansion valve 13, and adopts PID regulable control liquid level.Low pressure recycle bucket liquid level sensor 28 and Low-voltage Electronic expansion valve 17 form low pressure recycle bucket 6 tank level control system, and adopt PID regulable control level stability.
Between the gas returning port and refrigeration compressor 1 of low pressure recycle bucket 6, be provided with heat exchanger, the refrigerant outlet of condenser 3 also through heat exchanger cross cold after be connected to middle pressure electric expansion valve 13 again.This heat exchanger is also shell and tube exchanger, and low pressure recycle bucket 6 gaseous refrigerant connects refrigeration compressor 1 air entry after this heat exchanger heats, the refrigerant outlet liquid refrigerant of condenser 3 also through heat exchanger cross cold after be connected to middle pressure electric expansion valve 13 again; Thus improve the operating efficiency of whole system, and reduce operating power consumption.
In whole refrigeration system, the oil return circulatory system divides three tunnels: a road is that oil eliminator 2 gets back to refrigeration compressor 1 through oil return pipe and oil eliminator oil return solenoid valve 9, all works when air conditioning condition and ice making operating mode; One tunnel is the ejecting port of the oil return opening access jet pump of low pressure recycle bucket 6, and oil leads back to refrigeration compressor 1 with communicating after compressor air suction by jet pump outlet, works during ice making operating mode; One tunnel is the ejecting port of the oil return opening access jet pump of the second evaporimeter 4, and oil to lead back to refrigeration compressor 1 with communicating after compressor air suction by jet pump outlet, works during air conditioning condition.
In the course of work, refrigerant flow direction is as follows:
1, air conditioning condition cooling system runs: refrigeration compressor → oil eliminator → water-cooled condenser → middle pressure electric expansion valve → the second evaporimeter → the second evaporimeter return-air motor-driven valve → refrigeration compressor.Wherein, Low-voltage Electronic expansion valve, low pressure recycle bucket, refrigerant feed liquid pump, feed flow check valve, ice making evaporator etc. do not participate in work.
2, ice making operating mode cooling system runs: refrigeration compressor → oil eliminator → water-cooled condenser → middle pressure electric expansion valve → the second evaporimeter → Low-voltage Electronic expansion valve → low pressure recycle bucket → refrigerant feed liquid pump → feed flow check valve → ice making evaporator → refrigeration discharges magnetic valve → low pressure recycle bucket → refrigeration compressor.
3, operation need be deiced: refrigeration compressor → oil eliminator → hot-gas deicing magnetic valve → ice making evaporator → hot-gas deicing is discharged check valve → hot-gas deicing and discharged magnetic valve → the second evaporimeter.
Finally it should be noted that, above embodiment is only in order to illustrate the technical solution of the utility model but not restriction technologies scheme, those of ordinary skill in the art is to be understood that, those are modified to the technical solution of the utility model or equivalent replacement, and do not depart from aim and the scope of the technical program, all should be encompassed in the middle of right of the present utility model.
Claims (7)
1. a four-pipe system Dual-evaporator refrigeration system, is characterized in that: comprise refrigeration compressor, oil eliminator, condenser, the second evaporimeter, ice making evaporator, low pressure recycle bucket, oil return jet pump and refrigerant feed liquid pump;
The gas outlet of described refrigeration compressor is connected with the air inlet of oil eliminator, the oil return opening of described oil eliminator is connected with the air entry of refrigeration compressor after oil eliminator oil return solenoid valve, is connected the while of its gas outlet with the air inlet of condenser, the high pressure admission mouth of the second evaporimeter, the air inlet deicing air inlet and oil return jet pump of ice making evaporator; Wherein, hot gas bypass solenoid valve is provided with between the gas outlet of oil eliminator and the high pressure admission mouth of the second evaporimeter, between the gas outlet and the air inlet of ice making evaporator of oil eliminator, be provided with hot-gas deicing magnetic valve, between the gas outlet of oil eliminator and the air inlet of oil return jet pump, be provided with injection magnetic valve;
The refrigerant outlet of described condenser through in press electric expansion valve after be connected with compression refrigerant import in the second evaporimeter, the economizer tonifying Qi outlet of the second evaporimeter is connected with the economizer tonifying Qi interface of refrigeration compressor through economizer tonifying Qi magnetic valve, and its gas returning port is connected with the air entry of refrigeration compressor through the second evaporimeter return-air motor-driven valve; The oil return opening of this second evaporimeter is connected with the ejecting port of oil return jet pump through the second evaporimeter oil return solenoid valve;
The refrigerant outlet of the second evaporimeter is connected with the low pressure refrigerant import of low pressure recycle bucket after Low-voltage Electronic expansion valve; The refrigerant outlet of described low pressure recycle bucket is connected with refrigerant feed liquid pump, and refrigerant feed liquid pump is connected with the refrigerant inlet of ice making evaporator after feed flow check valve; The gas returning port of this low pressure recycle bucket is connected with the air entry of refrigeration compressor after low pressure recycle bucket return-air motor-driven valve, and its oil return opening is connected with the ejecting port of oil return jet pump through low pressure recycle bucket oil return solenoid valve; The described outlet of oil return jet pump is connected with the air entry of refrigeration compressor;
The refrigerant outlet of described ice making evaporator is discharged after magnetic valve through cold-producing medium and is connected with the gas-liquid import of low pressure recycle bucket, and it deices gas outlet and is connected with the second evaporimeter with deicing after hot gas discharges magnetic valve through deicing hot gas discharge check valve.
2. four-pipe system Dual-evaporator refrigeration system according to claim 1, is characterized in that: be provided with differential pressure controller with refrigerant feed liquid parallel connection of pumps, for detecting the pressure reduction of refrigerant feed liquid pump inlet and liquid outlet; Liquid pump bypass solenoid valve is provided with between the liquid outlet and the gas-liquid import of low pressure recycle bucket of refrigerant feed liquid pump.
3. four-pipe system Dual-evaporator refrigeration system according to claim 1, it is characterized in that: between refrigerant feed liquid pump and the air entry of refrigeration compressor, be provided with liquid pump oil returning tube, one end of described liquid pump oil returning tube is connected with the liquid outlet of refrigeration solution feed pump, the other end is connected with the air inlet of refrigeration compressor, and liquid pump oil returning tube is provided with liquid pump oil return solenoid valve.
4. four-pipe system Dual-evaporator refrigeration system according to claim 1, is characterized in that: on low pressure recycle bucket and the second evaporimeter, be respectively equipped with low pressure recycle bucket liquid level sensor and the second evaporimeter liquid level sensor.
5. four-pipe system Dual-evaporator refrigeration system according to claim 1, it is characterized in that: between the gas returning port and refrigeration compressor of low pressure recycle bucket, be provided with heat exchanger, the refrigerant outlet of condenser also through heat exchanger cross cold after be connected to middle pressure electric expansion valve again.
6. four-pipe system Dual-evaporator refrigeration system according to claim 1, is characterized in that: described ice making evaporator for organize plate-type evaporator more.
7. four-pipe system Dual-evaporator refrigeration system according to claim 1, is characterized in that: described second evaporimeter is the full liquid evaporimeter of shell-tube type.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520453042.0U CN204757428U (en) | 2015-06-29 | 2015-06-29 | Four control double evaporation ware refrigerating system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520453042.0U CN204757428U (en) | 2015-06-29 | 2015-06-29 | Four control double evaporation ware refrigerating system |
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| Publication Number | Publication Date |
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| CN204757428U true CN204757428U (en) | 2015-11-11 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520453042.0U Withdrawn - After Issue CN204757428U (en) | 2015-06-29 | 2015-06-29 | Four control double evaporation ware refrigerating system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104864621A (en) * | 2015-06-29 | 2015-08-26 | 中机西南能源科技有限公司 | Four-pipe double- evaporator refrigeration system |
-
2015
- 2015-06-29 CN CN201520453042.0U patent/CN204757428U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104864621A (en) * | 2015-06-29 | 2015-08-26 | 中机西南能源科技有限公司 | Four-pipe double- evaporator refrigeration system |
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| C14 | Grant of patent or utility model | ||
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| AV01 | Patent right actively abandoned |
Granted publication date: 20151111 Effective date of abandoning: 20171114 |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20151111 Effective date of abandoning: 20171114 |
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| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |