CN205938517U - Cold energy utilization device - Google Patents

Cold energy utilization device Download PDF

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Publication number
CN205938517U
CN205938517U CN201620740708.5U CN201620740708U CN205938517U CN 205938517 U CN205938517 U CN 205938517U CN 201620740708 U CN201620740708 U CN 201620740708U CN 205938517 U CN205938517 U CN 205938517U
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CN
China
Prior art keywords
carbon dioxide
cold energy
cold
natural gas
freezer
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
CN201620740708.5U
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Chinese (zh)
Inventor
杨俊�
金春强
张庆军
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.)
Yixing Kunlun Energy Technology Co Ltd
Original Assignee
Yixing Kunlun Energy Technology Co Ltd
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 Yixing Kunlun Energy Technology Co Ltd filed Critical Yixing Kunlun Energy Technology Co Ltd
Priority to CN201620740708.5U priority Critical patent/CN205938517U/en
Application granted granted Critical
Publication of CN205938517U publication Critical patent/CN205938517U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a cold energy utilization device, a cold energy utilization device, including the LNG basic station, safety -valve, the carbon dioxide system that liquefies, the freezer utilizes the cold energy system, carbon dioxide liquefaction system includes the carbon dioxide trap, the liquefied natural gas of LNG basic station passes through the pipeline and by the bottom inlet side upper end output of carbon dioxide liquefier side, incorporates the natural gas pipe net after the natural gas process TRK i gasification of output into, the freezer utilizes the cold energy system to include, the cold -storage groove, and the alarm, the flowmeter, liquefied natural gas process shell and tube heat exchanger carries out the heat transfer, incorporates the natural gas pipe net after the heat transfer after the gasification of TRK ii into, this cold energy utilization device utilize liquefied natural gas cold energy liquefaction carbon dioxide and for the freezer refrigeration, the waste of cold energy has been avoided to ice machine system ice, has improved resource utilization rate.

Description

A kind of cold energy utilization device
Technical field
This utility model LNG Technology field, specially a kind of cold energy utilization device.
Background technology
Liquefied natural gas abbreviation LNG, is a kind of clean energy resource, and liquefied natural gas contains abundant cold energy if it is possible to fill Divide and use, can economize on resources, environmental protection, but current liquefied natural gas cannot after air-heating type gasifier gasification Cold energy is utilized, causes great energy waste.
Utility model content
For problem above, this utility model provides a kind of cold energy utilization device, effective by way of cold energy use Utilization cold energy, as far as possible reduce the energy waste, so can be with the problem in effectively solving background technology.
For achieving the above object, this utility model provides following technical scheme:A kind of cold energy utilization device, including LNG base Stand, safety-valve, carbon dioxide liquefaction system, freezer utilizes cold energy system, and described carbon dioxide liquefaction system includes titanium dioxide Carbon catcher, the liquefied natural gas of described LNG base station passes through pipeline and is exported by co 2 liquefaction device side bottom input side upper end, The natural gas of output is incorporated to gas distributing system after air-heating type gasifier gasification, and the two of described Collecting carbonic anhydride device trapping Carbonoxide is inputted by the top of co 2 liquefaction device, and the carbon dioxide after liquefaction is exported by lower end and is stored in liquefaction titanium dioxide Carbon storage tank, described freezer is included using cold energy system, cold-storage groove, alarm, effusion meter, and liquefied natural gas changes through shell and tube Hot device carries out heat exchange, is incorporated to gas distributing system after heat exchange after air-heating type gasifier gasification, described tubular heat exchanger Cold liquid is transported in cold-storage groove and is transported to freezer refrigerating by liquid pump again, through freezer using after cold liquid be transported to ice making mechanism Ice, subsequently cold liquid be circulated back to tubular heat exchanger.
As a kind of preferred technical scheme of this utility model, described Collecting carbonic anhydride device uses application end group alkene Base alkyl imidazole ion liquid polymer traps to carbon dioxide.
As a kind of preferred technical scheme of this utility model, the coolant in described tubular heat exchanger uses second two Alcohol-water solution and coolant can be changed according to actual needs.
As a kind of preferred technical scheme of this utility model, described alarm uses ethylene glycol leakage alarm.
Compared with prior art, the beneficial effects of the utility model are:This cold energy utilization device, by collecting carbonic anhydride Device trapping carbon dioxide and then liquefaction, carbon dioxide is greenhouse gases and the important raw material of industry, using cold energy liquefaction two Carbonoxide had not only decreased greenhouse gases but also had created the raw material of industry;This cold energy utilization device is using sharp by cold energy after heat exchanger heat exchange Use freezer refrigerating and ice making, save substantial amounts of power consumption.
Brief description
Fig. 1 is this utility model structural representation.
In figure:1- Collecting carbonic anhydride device;2-LNG base station;3- safety-valve;4- tubular heat exchanger;5- ice machine;6- Alarm;7- cold-storage groove;8- liquid pump;9- effusion meter;10- air-heating type gasifier;11- freezer;12- co 2 liquefaction device; 13- air-heating type gasifier;14- liquefied carbon dioxide storage tank.
Specific embodiment
To explain this utility model below in conjunction with embodiment further.
Embodiment:
Refer to Fig. 1, this utility model provides a kind of technical scheme:A kind of cold energy utilization device, including LNG base station 2, pacifies Full valve door 3, carbon dioxide liquefaction system, freezer utilize cold energy system it is characterised in that:Described carbon dioxide liquefaction system bag Include Collecting carbonic anhydride device 1, the liquefied natural gas of described LNG base station 2 is defeated by co 2 liquefaction device 12 side bottom by pipeline Enter the output of side upper end, the natural gas of output is incorporated to gas distributing system after air-heating type gasifier 13 gasification, described carbon dioxide The carbon dioxide of catcher 1 trapping is inputted by the top of co 2 liquefaction device 12, and the carbon dioxide after liquefaction is exported by lower end And it is stored in liquefied carbon dioxide storage tank 14, described freezer is included using cold energy system, cold-storage groove 7, alarm 6, effusion meter 9, liquefied natural gas carries out heat exchange through tubular heat exchanger 4, is incorporated to sky after heat exchange after air-heating type gasifier 10 gasification So gas pipe network, the cold liquid of described tubular heat exchanger 4 is transported in cold-storage groove 7 and is transported to freezer 11 by liquid pump 8 again and freezes, warp Cold liquid after supercool Cooley is transported to ice machine 5 ice making, and subsequently cold liquid is circulated back to tubular heat exchanger 4.
Operation principle of the present utility model:Open the safety-valve door 3, and the liquefied natural gas of LNG base station 2 arrives through pipeline Co 2 liquefaction device 12, carries out low-temperature liquefaction to the carbon dioxide of Collecting carbonic anhydride device 1 trapping, through the titanium dioxide of liquefaction Carbon is stored in liquefied carbon dioxide storage tank 14, is gasified by air-heating type gasifier 13 through the liquefied natural gas of heat exchange, subsequently It is incorporated to gas distributing system;The liquefied natural gas of LNG base station 2 is transported to tubular heat exchanger 4 by an other passage and is changed Heat, the liquefied natural gas after heat exchange is then incorporated into gas distributing system through air-heating type gasifier 10 gasification;In shell and tube heat exchange Cold liquid in device 4, is stored temporarily in cold-storage groove 7, by liquid pump 8, cold liquid is transported to freezer 11 and is freezed, there is effusion meter period Detection flows, after freezer refrigerating, cold liquid is transported to ice machine 5 and carries out ice making, is finally circulated back to heat exchanger.

Claims (3)

1. a kind of cold energy utilization device, including LNG base station (2), safety-valve (3), carbon dioxide liquefaction system, freezer utilizes cold Can system it is characterised in that:Described carbon dioxide liquefaction system includes Collecting carbonic anhydride device (1), described LNG base station (2) Liquefied natural gas passes through pipeline and is exported by co 2 liquefaction device (12) side bottom input side upper end, and the natural gas of output is through empty It is incorporated to gas distributing system, the carbon dioxide that described Collecting carbonic anhydride device (1) traps is by dioxy after heating type gasifier (13) gasification Change the top input of carbon liquefier (12), the carbon dioxide after liquefaction is exported by lower end and is stored in liquefied carbon dioxide storage tank (14), described freezer is included using cold energy system, cold-storage groove (7), alarm (6), effusion meter (9), and liquefied natural gas is through row Pipe heat exchanger (4) carries out heat exchange, is incorporated to gas distributing system, described row after heat exchange after air-heating type gasifier (10) gasification The cold liquid of pipe heat exchanger (4) is transported in cold-storage groove (7) and is transported to freezer (11) refrigeration by liquid pump (8) again, through freezer Using after cold liquid be transported to ice machine (5) ice making, subsequently cold liquid is circulated back to tubular heat exchanger (4).
2. a kind of cold energy utilization device according to claim 1 it is characterised in that:In described tubular heat exchanger (4) Coolant uses glycol water.
3. a kind of cold energy utilization device according to claim 1 it is characterised in that:Described alarm (6) uses second Glycol leakage alarm.
CN201620740708.5U 2016-07-14 2016-07-14 Cold energy utilization device Expired - Fee Related CN205938517U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620740708.5U CN205938517U (en) 2016-07-14 2016-07-14 Cold energy utilization device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620740708.5U CN205938517U (en) 2016-07-14 2016-07-14 Cold energy utilization device

Publications (1)

Publication Number Publication Date
CN205938517U true CN205938517U (en) 2017-02-08

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620740708.5U Expired - Fee Related CN205938517U (en) 2016-07-14 2016-07-14 Cold energy utilization device

Country Status (1)

Country Link
CN (1) CN205938517U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111426099A (en) * 2019-11-22 2020-07-17 国电康能科技股份有限公司 Waste heat recovery device of subcritical carbon dioxide working medium
CN113309920A (en) * 2021-05-10 2021-08-27 安徽省环境科学研究院 High contact nature thermal power plant utilizes LNG to carry out carbon collecting system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111426099A (en) * 2019-11-22 2020-07-17 国电康能科技股份有限公司 Waste heat recovery device of subcritical carbon dioxide working medium
CN113309920A (en) * 2021-05-10 2021-08-27 安徽省环境科学研究院 High contact nature thermal power plant utilizes LNG to carry out carbon collecting system

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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: 20170208

Termination date: 20190714

CF01 Termination of patent right due to non-payment of annual fee