CN207280082U - Low temperature on-condensible gas cold recovery system - Google Patents
Low temperature on-condensible gas cold recovery system Download PDFInfo
- Publication number
- CN207280082U CN207280082U CN201721344455.0U CN201721344455U CN207280082U CN 207280082 U CN207280082 U CN 207280082U CN 201721344455 U CN201721344455 U CN 201721344455U CN 207280082 U CN207280082 U CN 207280082U
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- low temperature
- heat exchanger
- condensible gas
- condensible
- recovery system
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Abstract
A kind of low temperature on-condensible gas cold recovery system, including double rectification column and heat exchanger, pressure nitrogen gas pipeline and low temperature on-condensible gas pipeline are connected with heat exchanger, low temperature on-condensible gas pipeline is connected with the waste gas outlet of the condenser/evaporator in the middle part of double rectification column, and pressure nitrogen gas pipeline and the pressure nitrogen gas outlet of tower under double rectification column connect.The utility model provides a kind of low temperature on-condensible gas cold recovery system, and by the recycling of on-condensible gas cold, cold recovery is carried out on the premise of energy consumption is not increased, high-purity liquid nitrogen yield is added, reduces product energy consumption.
Description
Technical field
The utility model belongs to gas separation technique field, refers in particular to a kind of low temperature on-condensible gas cold recovery system.
Background technology
Full liquid space division has several strands of not solidifying cryogenic gases to be discharged into air, such as neon helium, is continuously drained into equipment running process
Air, causes very High cooling power loss.
Utility model content
The purpose of this utility model is to provide a kind of low temperature on-condensible gas cold recovery system, passes through on-condensible gas cold
Recycling, cold recovery is carried out on the premise of energy consumption is not increased, high-purity liquid nitrogen yield is added, reduces product energy consumption.
What the purpose of this utility model was realized in：A kind of low temperature on-condensible gas cold recovery system, including twin-stage essence
Evaporate tower and heat exchanger, be connected with pressure nitrogen gas pipeline and low temperature on-condensible gas pipeline on heat exchanger, low temperature on-condensible gas pipeline with it is double
The waste gas outlet connection of condenser/evaporator in the middle part of level rectifying column, the pressure nitrogen gas of pressure nitrogen gas pipeline and tower under double rectification column
Outlet connection.
Preferably, low temperature on-condensible gas pipeline connects the heat exchanger, and the heat exchanger is aluminium-made plate type heat exchanger.
Preferably, cold is exchanged heat and is lowered temperature to pressure nitrogen gas, pressure nitrogen gas by low temperature on-condensible gas by heat exchanger
After become liquid nitrogen.
The utility model is prominent and beneficial compared with prior art to be had the technical effect that：
The exhaust gas such as the low temperature neon helium discharged in space division condenser/evaporator are separated through aluminium-made plate type heat exchanger with air separation plant
The middle pressure high pure nitrogen gone out carries out heat exchange, and middle pressure high pure nitrogen is liquefied, and obtains the exhaust gas such as high-purity liquid nitrogen product, low temperature neon helium
Air is discharged into after re-heat to room temperature.The technology is carried out cold by the recycling of on-condensible gas cold on the premise of energy consumption is not increased
Amount recycling, adds high-purity liquid nitrogen yield, reduces product energy consumption.
Brief description of the drawings
Fig. 1 is the schematic diagram of the utility model.
Embodiment
The utility model is further described with specific embodiment below in conjunction with the accompanying drawings, referring to Fig. 1：
A kind of low temperature on-condensible gas cold recovery system, including double rectification column and heat exchanger, are connected with pressure on heat exchanger
Nitrogen pipeline and low temperature on-condensible gas pipeline, the exhaust gas of low temperature on-condensible gas pipeline and the condenser/evaporator in the middle part of double rectification column
Outlet connection, pressure nitrogen gas pipeline and the pressure nitrogen gas outlet of tower under double rectification column connect.
Preferably, low temperature on-condensible gas pipeline connects the heat exchanger, and the heat exchanger is aluminium-made plate type heat exchanger.
Preferably, cold is exchanged heat and is lowered temperature to pressure nitrogen gas, pressure nitrogen gas by low temperature on-condensible gas by heat exchanger
After become liquid nitrogen.
The utility model is prominent and beneficial compared with prior art to be had the technical effect that：
The exhaust gas such as the low temperature neon helium discharged in space division condenser/evaporator are separated through aluminium-made plate type heat exchanger with air separation plant
The middle pressure high pure nitrogen gone out carries out heat exchange, and middle pressure high pure nitrogen is liquefied, and obtains the exhaust gas such as high-purity liquid nitrogen product, low temperature neon helium
Air is discharged into after re-heat to room temperature.The technology is carried out cold by the recycling of on-condensible gas cold on the premise of energy consumption is not increased
Amount recycling, adds high-purity liquid nitrogen yield, reduces product energy consumption.
Above-described embodiment is only the preferred embodiment of the utility model, not limits the protection model of the utility model according to this
Enclose, therefore：The equivalence changes that all structures, shape, principle according to the utility model are done, should all be covered by the protection of the utility model
Within the scope of.
Claims (3)
- A kind of 1. low temperature on-condensible gas cold recovery system, it is characterised in that：Including double rectification column and heat exchanger, on heat exchanger It is connected with pressure nitrogen gas pipeline and low temperature on-condensible gas pipeline, low temperature on-condensible gas pipeline and the condensation evaporation in the middle part of double rectification column The waste gas outlet connection of device, pressure nitrogen gas pipeline and the pressure nitrogen gas outlet of tower under double rectification column connect.
- 2. low temperature on-condensible gas cold recovery system according to claim 1, it is characterised in that：Low temperature on-condensible gas pipeline The heat exchanger is connected, the heat exchanger is aluminium-made plate type heat exchanger.
- 3. low temperature on-condensible gas cold recovery system according to claim 1, it is characterised in that：Low temperature on-condensible gas passes through Heat exchanger exchanges heat cold to pressure nitrogen gas, and pressure nitrogen gas becomes liquid nitrogen after being lowered temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721344455.0U CN207280082U (en) | 2017-10-18 | 2017-10-18 | Low temperature on-condensible gas cold recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721344455.0U CN207280082U (en) | 2017-10-18 | 2017-10-18 | Low temperature on-condensible gas cold recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207280082U true CN207280082U (en) | 2018-04-27 |
Family
ID=61980616
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721344455.0U Expired - Fee Related CN207280082U (en) | 2017-10-18 | 2017-10-18 | Low temperature on-condensible gas cold recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207280082U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109297261A (en) * | 2018-10-17 | 2019-02-01 | 浙江海天气体有限公司 | A kind of neon helium cryogenic gas cold energy recyclable device |
-
2017
- 2017-10-18 CN CN201721344455.0U patent/CN207280082U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109297261A (en) * | 2018-10-17 | 2019-02-01 | 浙江海天气体有限公司 | A kind of neon helium cryogenic gas cold energy recyclable device |
| CN109297261B (en) * | 2018-10-17 | 2023-06-30 | 浙江海畅气体股份有限公司 | Neon helium low temperature gas cold energy recovery unit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180427 Termination date: 20191018 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |