CN203964421U - A kind of single stage compress cryogenic refrigerating system - Google Patents

A kind of single stage compress cryogenic refrigerating system Download PDF

Info

Publication number
CN203964421U
CN203964421U CN201420323977.2U CN201420323977U CN203964421U CN 203964421 U CN203964421 U CN 203964421U CN 201420323977 U CN201420323977 U CN 201420323977U CN 203964421 U CN203964421 U CN 203964421U
Authority
CN
China
Prior art keywords
output
input
heat exchanger
gas
liquid separator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201420323977.2U
Other languages
Chinese (zh)
Inventor
沈学明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wuxi Institute of Commerce
Original Assignee
Wuxi Institute of Commerce
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wuxi Institute of Commerce filed Critical Wuxi Institute of Commerce
Priority to CN201420323977.2U priority Critical patent/CN203964421U/en
Application granted granted Critical
Publication of CN203964421U publication Critical patent/CN203964421U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Separation By Low-Temperature Treatments (AREA)

Abstract

The utility model has been announced a kind of single stage compress cryogenic refrigerating system, comprises compressor, and the input of described compressor is connected with the output of the first gas-liquid separator, and its output is connected with condenser; The output of described condenser is connected with the input of the second gas-liquid separator, the first output of described the second gas-liquid separator is connected to the first input end of the first heat exchanger by the first expansion valve, the first output of described the first heat exchanger is connected to the input of described the first gas-liquid separator.Single stage compress cryogenic refrigerating system of the present utility model, belongs to the refrigeration system of single stage compress, one-level separation, and this system architecture is simple, can reach-40 ℃ of following low temperature.In addition, in this system, only need to use a compressor, comprehensive energy consumption is lower, and reliable operation, and maintenance is few, little to atmosphere environment impact, meets environmental requirement.

Description

A kind of single stage compress cryogenic refrigerating system
Technical field
The utility model relates to a kind of single stage compress cryogenic refrigerating system.
Background technology
At present, along with scientific technological advance, the occasion (below 40 ℃) that needs cryogenic conditions at some, traditional cryogenic system major part is two-stage compression system, or folding type cooling system.Although these refrigeration systems can reach the low temperature needing, the structure relative complex of refrigeration system, and need two above refrigeration compressor associated working.So not only system complex, difficult in maintenance, and efficiency is also lower.
Utility model content
The utility model object is that the defect existing for prior art provides a kind of single stage compress cryogenic refrigerating system.
The utility model for achieving the above object, adopts following technical scheme: a kind of single stage compress cryogenic refrigerating system,
Comprise compressor, the input of described compressor is connected with the output of the first gas-liquid separator, and its output is connected with condenser; The output of described condenser is connected with the input of the second gas-liquid separator, the first output of described the second gas-liquid separator is connected to the first input end of the first heat exchanger by the first expansion valve, the first output of described the first heat exchanger is connected to the input of described the first gas-liquid separator;
The second output of described the second gas-liquid separator is connected with the second input of described the first heat exchanger, the second output of described the first heat exchanger is connected to the first input end of the second heat exchanger by the second expansion valve, the first output of described the second heat exchanger is connected to the input of described the first gas-liquid separator;
Also comprise low temperature refrigerating medium container, its input is connected with the second output of described the second heat exchanger, and its output is connected to the second input of described the second heat exchanger by coolant pump.
Further, the input of described compressor is provided with inlet valve, and its output is provided with air bleeding valve; On described inlet valve, be provided with low-pressure meter, on described air bleeding valve, be provided with high pressure gauge, between described low-pressure meter and described high pressure gauge, be connected with high-low pressure relay.
Further, on described condenser, be provided with ventilating fan.
The beneficial effects of the utility model: single stage compress cryogenic refrigerating system of the present utility model, belong to the refrigeration system of single stage compress, one-level separation, this system architecture is simple, can reach-40 ℃ of following low temperature.In addition, in this system, only need to use a compressor, comprehensive energy consumption is lower, and reliable operation, and maintenance is few, little to atmosphere environment impact, meets environmental requirement.
Accompanying drawing explanation
Fig. 1 structural principle schematic diagram of the present utility model.
The specific embodiment
Shown in Fig. 1, for a kind of single stage compress cryogenic refrigerating system, comprise compressor 1, the input of described compressor 1 is connected with the output of the first gas-liquid separator 17, and its output is connected with condenser 2; The output of described condenser 2 is connected with the input of the second gas-liquid separator 3, the first output of described the second gas-liquid separator 3 is connected to the first input end of the first heat exchanger 4 by the first expansion valve 6, the first output of described the first heat exchanger 4 is connected to the input of described the first gas-liquid separator 17;
The second output of described the second gas-liquid separator 3 is connected with the second input of the first heat exchanger 4, the second output of described the first heat exchanger 4 is connected to the first input end of the second heat exchanger 5 by the second expansion valve 7, the first output of described the second heat exchanger 5 is connected to the input of described the first gas-liquid separator 17; In single stage compress cryogenic refrigerating system of the present utility model, also comprise low temperature refrigerating medium container 16, its input is connected with the second output of described the second heat exchanger 5, and its output is connected to the second input of described the second heat exchanger 5 by coolant pump 15.
Wherein, the input of described compressor 1 is provided with inlet valve 9, and its output is provided with air bleeding valve 10; On described inlet valve 9, be provided with low-pressure meter 12, on described air bleeding valve 10, be provided with high pressure gauge 13, between described low-pressure meter 12 and described high pressure gauge 13, be connected with high-low pressure relay 11.In addition, on described condenser 1, can also be provided with ventilating fan 14, can accelerate so cooling.
Its operation principle is as follows:
During compressor 1 work, first the mixed refrigerant vapor of HTHP enters into carries out cooling and condensation process in condenser 2.Wherein, high temperature refrigerant A in the mixed refrigerant vapor of HTHP is condensed into liquid and enters the second gas-liquid separator 3, and become low pressure liquid through the first expansion valve 6 reducing pressure by regulating flows, then in the first heat exchanger 4, carry out evaporation endothermic, make the second heat exchanger 4 become low temperature environment, then the steam producing, after the first gas-liquid separator 17 separation, is reuptaked compression by compressor 1 again.
Meanwhile, due to the low-temperature refrigerant B in the mixed refrigerant vapor of HTHP, because do not meet condensing condition in condenser 2, although its pressure is promoted, low-temperature refrigerant B can not be condensed into liquid in condenser 2.Like this, the low-temperature refrigerant B after boosting, after the separation of the second gas-liquid separator 3, enters the second heat exchanger 4 and is condensed into highly pressurised liquid; Highly pressurised liquid, by after the second expansion valve 7 reducing pressure by regulating flows, becomes low pressure liquid, and then enters the interior evaporation endothermic of the second heat exchanger 5.Now, refrigerating medium in low temperature refrigerating medium container 16 is by the effect of coolant pump 15, enter in the second heat exchanger 5 and the generation of the low-temperature refrigerant B after step-down heat exchange, obtain-40 ℃ of following low-temperature refrigerants, the steam producing after the low-temperature refrigerant B obtaining evaporates, absorbs heat in the second heat exchanger 5, equally also, through the first gas-liquid separator 8 separation, finally by compressor 1, reuptaked compression again, so iterative cycles.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.

Claims (3)

1. a single stage compress cryogenic refrigerating system, is characterized in that,
Comprise compressor, the input of described compressor is connected with the output of the first gas-liquid separator, and its output is connected with condenser; The output of described condenser is connected with the input of the second gas-liquid separator, the first output of described the second gas-liquid separator is connected to the first input end of the first heat exchanger by the first expansion valve, the first output of described the first heat exchanger is connected to the input of described the first gas-liquid separator;
The second output of described the second gas-liquid separator is connected with the second input of described the first heat exchanger, the second output of described the first heat exchanger is connected to the first input end of the second heat exchanger by the second expansion valve, the first output of described the second heat exchanger is connected to the input of described the first gas-liquid separator;
Also comprise low temperature refrigerating medium container, its input is connected with the second output of described the second heat exchanger, and its output is connected to the second input of described the second heat exchanger by coolant pump.
2. a kind of single stage compress cryogenic refrigerating system as claimed in claim 1, is characterized in that, the input of described compressor is provided with inlet valve, and its output is provided with air bleeding valve; On described inlet valve, be provided with low-pressure meter, on described air bleeding valve, be provided with high pressure gauge, between described low-pressure meter and described high pressure gauge, be connected with high-low pressure relay.
3. a kind of single stage compress cryogenic refrigerating system as claimed in claim 1, is characterized in that, on described condenser, is provided with ventilating fan.
CN201420323977.2U 2014-06-12 2014-06-12 A kind of single stage compress cryogenic refrigerating system Expired - Fee Related CN203964421U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420323977.2U CN203964421U (en) 2014-06-12 2014-06-12 A kind of single stage compress cryogenic refrigerating system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420323977.2U CN203964421U (en) 2014-06-12 2014-06-12 A kind of single stage compress cryogenic refrigerating system

Publications (1)

Publication Number Publication Date
CN203964421U true CN203964421U (en) 2014-11-26

Family

ID=51924995

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420323977.2U Expired - Fee Related CN203964421U (en) 2014-06-12 2014-06-12 A kind of single stage compress cryogenic refrigerating system

Country Status (1)

Country Link
CN (1) CN203964421U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104142032A (en) * 2014-06-12 2014-11-12 无锡商业职业技术学院 Single-stage compression low-temperature refrigeration system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104142032A (en) * 2014-06-12 2014-11-12 无锡商业职业技术学院 Single-stage compression low-temperature refrigeration system

Similar Documents

Publication Publication Date Title
CN107521698B (en) Environment control system waste heat refrigerating device
CN204254921U (en) The low-temperature cold water unit structure of single machine two-stage
CN103486754A (en) Energy-saving middle temperature refrigerant/middle temperature refrigerant cascade refrigeration system
CN110375455B (en) Compressed air energy refrigeration air conditioning system
CN103398485A (en) Steam compression refrigerating system device and supercooling method
CN204115285U (en) A kind of falling film type double parallel Screw chiller
CN206803544U (en) Refrigeration experiment double-machine two-stage compression refrigerating system
CN103615824B (en) A kind of many warm areas cold acquisition methods and device reclaiming driving based on expansion work
CN102410664A (en) Novel air energy refrigeration device
CN104792052A (en) Novel ultralow-temperature compression refrigerating system
CN203964421U (en) A kind of single stage compress cryogenic refrigerating system
CN207487165U (en) Superposition type air-cooled condensing group
CN204730505U (en) A kind of novel three stage compression ultra-low temperature refrigerating device
CN204100637U (en) A kind of twice decompression carbon dioxide household electric refrigerator
CN204438359U (en) Air-conditioner outdoor unit
CN204494900U (en) A kind of refrigeration system of mechanical temperature-control frequency conversion refrigerator
CN203928493U (en) Earth source heat pump
CN103123179B (en) Multi-heat-source absorption refrigeration device
CN104142032A (en) Single-stage compression low-temperature refrigeration system
CN202119155U (en) Open economizer utilizing double-pressure circulating principle
CN204202232U (en) A kind of high temperature heat pump dryer group using non-azeotropic working medium
CN201163118Y (en) Novel refrigeration unit
CN204854065U (en) Novel cascade refrigeration device
CN205655518U (en) Air -cooled cold water or heat pump set with cross cold type structural system
CN201425385Y (en) Fluid cooling device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20141126

Termination date: 20150612

EXPY Termination of patent right or utility model