CN101871717A - Complete equipment for CO2 recycling with CO2 vaporization and cool recycling device - Google Patents
Complete equipment for CO2 recycling with CO2 vaporization and cool recycling device Download PDFInfo
- Publication number
- CN101871717A CN101871717A CN201010215022A CN201010215022A CN101871717A CN 101871717 A CN101871717 A CN 101871717A CN 201010215022 A CN201010215022 A CN 201010215022A CN 201010215022 A CN201010215022 A CN 201010215022A CN 101871717 A CN101871717 A CN 101871717A
- Authority
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- China
- Prior art keywords
- heat exchanger
- liquid
- accumulation
- fluid reservoir
- reboiler
- 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.)
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Links
- 238000004064 recycling Methods 0.000 title abstract description 5
- 238000009834 vaporization Methods 0.000 title abstract description 3
- 230000008016 vaporization Effects 0.000 title abstract description 3
- 239000007788 liquid Substances 0.000 claims abstract description 46
- 238000005057 refrigeration Methods 0.000 claims abstract description 19
- 239000012535 impurity Substances 0.000 claims abstract description 8
- 238000009825 accumulation Methods 0.000 claims description 29
- 239000012530 fluid Substances 0.000 claims description 26
- 239000006200 vaporizer Substances 0.000 claims description 17
- 238000001035 drying Methods 0.000 abstract description 4
- 238000004146 energy storage Methods 0.000 abstract 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 84
- 229910002092 carbon dioxide Inorganic materials 0.000 description 42
- 239000001569 carbon dioxide Substances 0.000 description 42
- 239000003507 refrigerant Substances 0.000 description 8
- 238000011084 recovery Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 235000013405 beer Nutrition 0.000 description 4
- 238000002309 gasification Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 230000006837 decompression Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 206010013786 Dry skin Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000013124 brewing process Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Abstract
The invention discloses complete equipment for CO2 recycling with a CO2 vaporization and cool recycling device, comprising a CO2 compressor (1), a CO2 drying device (2), a re-boiler (17), a refrigeration compressor (16), a liquefying heat exchanger (4), a liquid storage tank (5) and a carburetor (9). The complete equipment is characterized in that an energy storage tank (10) is installed between the liquid storage tank (5) and the carburetor (9); the pressure of the liquid CO2 in the liquid storage tank (5) is higher than that of the liquid CO2 in the energy storage tank (10); the energy storage tank (10) is connected with the heat exchanger (8); the refrigerating medium in the energy storage tank (10) is circulated between the energy storage tank (10) and the heat exchanger (8) by a circulating pump (11) and a connecting pipeline; the CO2 gas inlet of the heat exchanger (8) is directly communicated with the gas outlet of the re-boiler (17); the gas outlet of the heat exchanger (8) is directly communicated with the liquid CO2 inlet of the liquefying heat exchanger (4); and the liquid CO2 directly flows from the liquefying heat exchanger (4) to the re-boiler (17) and is pumped into the liquid storage tank (5) after impurities are removed. The invention realizes the energy recycle by additionally arranging the energy storage tank and the heat exchanger and remarkably saves the energy.
Description
Technical field
The present invention relates to a kind of carbon dioxide recovery use device, thereby especially a kind ofly utilize a large amount of cold energy that produce in the liquefied carbon dioxide gasification refrigeration compressor to be quit work to reach energy-conservation carbon dioxide recovery use device, the very significant CO that has of specifically a kind of energy-saving effect as the energy of the gaseous carbon dioxide liquefaction that makes recovery
2The CO of cold retracting device vaporizes
2Recycle complete set of equipments.
Background technology
Many institutes hit and know, in beer preparation process, need in beer liquid, to add carbon dioxide injection, make and guarantee its mouthfeel, carbon dioxide can directly be bought food-grade liquid carbon dioxide heating back and annotate to beer from market, it is very high to do cost like this, on the other hand, in the beer brewing process, can produce a large amount of carbon dioxide, directly discharging not only causes waste, and pollutes the environment, so the method that existing brewery generally adopts is recycled the carbon dioxide that produces in the brew process.The roughly process of recycling is, at first utilize gas collector that carbon dioxide is sent in the carbon-dioxide gas compressor 1 and be compressed to 1.8-2.0MPa, after dewatering, dry device 2 dryings of carbon dioxide send in the reboiler 17, high-pressure carbon dioxide enters in the liquefaction heat exchanger 4 through reboiler 17, again through with the refrigeration compressor that links to each other of the liquefaction heat exchanger 4 16 liquefy carbon dioxide that freeze, liquid carbon dioxide flows out back into reboiler 17 from liquefaction heat exchanger 4 removes impurity after pump pumps in the fluid reservoir 5 standby, during use, must earlier pressurized liquid carbon dioxide be introduced in the vaporizer, feed high-temperature steam and make its endothermic gasification, after decompression, send in the follow-up gas equipment again, therefore utilize in the process in whole recovery, need to use the co 2 liquefaction of refrigeration compressor on the one hand with gaseous state, this need consume a large amount of energy, use steam to make the liquid carbon dioxide endothermic gasification on the other hand in the use again, need to consume a large amount of steams equally, cause the waste of the energy again, therefore, though existing carbon dioxide has been realized the purpose of environmental protection, need consume a large amount of energy simultaneously.To this, still there is not good solution at present.
Summary of the invention
The objective of the invention is to utilize system energy consumption and the big problem of waste, invent the very significant CO of having of a kind of energy-saving effect at existing carbon dioxide recovery
2The CO of cold retracting device vaporizes
2Recycle complete set of equipments.
Technical scheme of the present invention is:
A kind of CO that has
2The CO of cold retracting device vaporizes
2Recycle complete set of equipments, it comprises CO
2Compressor 1, CO
2Drier 2, reboiler 17, refrigeration compressor 16, liquefaction heat exchanger 4, fluid reservoir 5 and vaporizer 9, CO
2The input of compressor 1 and CO
2Source of the gas links to each other, CO
2The output of compressor 1 and CO
2The input of drier 2 links to each other, CO
2The output of drier 2 links to each other with the input of reboiler 17, and the gas output end of reboiler 17 links to each other by the gas input of pneumatic ball valve 3 with liquefaction heat exchanger 4, enters the CO in the liquefaction heat exchanger 4
2Gas is cooled to liquid CO through refrigeration compressor 16
2, liquid CO
2Pump in the fluid reservoir 5 after removing impurity in the reboiler 17, it is characterized in that:
Between fluid reservoir 5 and vaporizer 9, accumulation of energy groove 10 is installed, the liquid CO in the fluid reservoir 5
2Pressure greater than the liquid CO in the accumulation of energy groove 10
2Pressure;
Accumulation of energy groove 10 is connected with heat exchanger 8, and the refrigerating medium in the accumulation of energy groove 10 circulates the CO of heat exchanger 8 by circulating pump 11 and connecting pipe between accumulation of energy groove 10 and heat exchanger 8
2Gas feed directly is connected with the gas vent of reboiler 17, the gas vent of heat exchanger 8 directly with the liquid CO of liquefaction heat exchanger 4
2Inlet is connected, liquid CO
2Directly flow into the reboiler 17 and pump into fluid reservoir 5 behind the removal impurity from liquefaction heat exchanger 4.
Accumulation of energy groove 10 wherein and heat exchanger 8 have promptly constituted the liquid carbon dioxide of the present invention cold retracting device that gasifies.
On the pipeline that connects between fluid reservoir 5 and the accumulation of energy groove 10, pressure-reducing valve 6 is installed.
On the tube connector that connects between accumulation of energy groove 10 and the vaporizer 9, shutoff valve 15 is installed; Between described fluid reservoir 5 and vaporizer 9, also be connected with the direct-furnish pipe, on described direct-furnish pipe, direct-furnish valve 14 be installed.
Carrying on the cold system output pipe of described accumulation of energy groove 10 is equipped with temperature sensor 12.
Beneficial effect of the present invention:
The present invention has made full use of the characteristic of carbon dioxide, and realization can purpose.This be because, when liquid carbon dioxide pressure descends, its temperature also descends synchronously, if its temperature is elevated to certain value, just can make refrigerating medium drop to certain temperature, utilize carrying carbon dioxide that cold machine cools off gaseous state again, to make its liquefaction be alternative refrigeration compressor, refrigeration compressor is quit work, realize purpose of energy saving, therefore, the present invention's certain amplitude (dropping to 1.0-1.2MPa) that at first high pressure in the fluid reservoir (1.8-2.0MPa) liquid carbon dioxide at first descended utilizes the pressure cold energy that produces that descends to come gaseous carbon dioxide is freezed, and can reduce the working time and the load of refrigeration compressor, realization can, owing to the temperature that enters the liquid carbon dioxide in the vaporizer is higher, therefore, can reduce the steam use amount again simultaneously.
The present invention has realized energy-conservation purpose by increasing accumulation of energy groove and heat exchanger, and the mature technology that all can adopt of accumulation of energy groove and heat exchanger is realized, manufacturing cost is lower, the input-output ratio height.With the 500kg/h gas production is example, and 45kW per hour can economize on electricity.
The present invention can realize a tractor serves several purposes, by reasonable disposition valve and control system, both can make whole system be in the power save mode operation, also can be in work under the state identical with existing systems.
Description of drawings
Fig. 1 is that system of the present invention forms structural representation.
The specific embodiment
The present invention is further illustrated below in conjunction with drawings and Examples.
As shown in Figure 1.
A kind of CO that has
2The CO of cold retracting device vaporizes
2Recycle complete set of equipments, it comprises and the identical CO of prior art
2Compressor 1, CO
2Drier 2, reboiler 17, refrigeration compressor 16, liquefaction heat exchanger 4, fluid reservoir 5 and vaporizer 9, CO
2The input of compressor 1 and CO
2Source of the gas links to each other, CO
2The output of compressor 1 and CO
2The input of drier 2 links to each other, CO
2The output of drier 2 links to each other with the input of reboiler 17, and the gas output end of reboiler 17 links to each other by the gas input of pneumatic ball valve 3 with liquefaction heat exchanger 4, enters the CO in the liquefaction heat exchanger 4
2Gas is cooled to liquid CO through refrigeration compressor 16
2, liquid CO
2Pump in the fluid reservoir 5 after removing impurity in the reboiler 17, reclaim in order to realize energy, the characteristic that temperature descends when utilizing pressure carbon dioxide to descend, the present invention has installed accumulation of energy groove 10 between fluid reservoir 5 and vaporizer 9, the liquid CO in the fluid reservoir 5
2Pressure greater than the liquid CO in the accumulation of energy groove 10
2Pressure; Pressure 1.8-2.0MPa in the fluid reservoir 5 is high-pressure liquid CO
2After connecting pressure-reducing valve 6 on the pipeline between the two and being decompressed to 1.0-1.2MPa, the temperature of carbon dioxide sharply descends, utilize the temperature of decline that the refrigerant temperature that flows through is descended, again refrigerating medium is pumped into the refrigeration liquefying of realizing in the heat exchanger 8 gaseous carbon dioxide in the heat exchanger 8 of flowing through by circulating pump 11, and the CO of heat exchanger 8
2Gas feed directly is connected with the gas vent of reboiler 17, the gas vent of heat exchanger 8 directly with the liquid CO of liquefaction heat exchanger 4
2Inlet is connected, liquid CO
2Directly flow into the reboiler 17 from liquefaction heat exchanger 4 and pump into fluid reservoir 5 behind the removal impurity, so circulation just can make refrigeration compressor 16 quit work, and realizes purpose of energy saving.Therefore accumulation of energy groove 10 and heat exchanger 8 have promptly constituted the liquid carbon dioxide of the present invention cold retracting device that gasifies.
During concrete enforcement, still can operate as normal when not needing to carry out carbon dioxide recovery in order to make the present invention, can tube connector be set connecting between accumulation of energy groove 10 and the vaporizer 9, and shutoff valve 15 is installed thereon; Also can between described fluid reservoir 5 and vaporizer 9, directly connect a direct-furnish pipe, and on described direct-furnish pipe, direct-furnish valve 14 is installed.In addition, in order to realize the automatic work of circulating pump 11, can be at the mounting temperature sensor 12 on the cold system output pipe that carries of accumulation of energy groove 10.
CO of the present invention
2The method of attachment and the prior art of compressor, drier, reboiler are identical, and the prior aries that maybe can adopt all same as the prior art such as the steam supply air line of vaporizer, the supply of recirculated water and utilization are realized.
Operation principle of the present invention is:
Pressure is that the liquid CO 2 of 1.8～2.0MPa earlier is decompressed to 1.0～1.2MPa by pressure-reducing valve 6 in the fluid reservoir 5, the carbon dioxide liquid temperature is reduced to-40～-35 ℃, enter accumulation of energy groove 10, refrigerating medium in the accumulation of energy groove 10 is cooled to-35～-30 ℃, utilize circulating pump 11 that refrigerating medium is pumped in the heat exchanger 8, will directly carry the co 2 liquefaction (condensing temperature of carbon dioxide under 1.8-2.0MPa pressure is-20～-25 ℃) of kettle from reboiler 17.Refrigerating medium after the intensification returns in the accumulation of energy groove 10 and recycles.Post-decompression liquid CO 2 can be vaporizated into atmospheric carbon dioxide in the cooling refrigerating medium, enter original vaporizer and further be warmed up to-20～-30 ℃, guarantees the normal use of carbon dioxide, can save a large amount of steam because temperature raises simultaneously; Refrigerating medium enters heat exchanger 8 with co 2 liquefaction, and original refrigeration compressor 16 can be stopped using, and saves a large amount of electric energy.
The course of work of the present invention is:
When system's operate as normal certain hour, when storing liquid carbon dioxide in the fluid reservoir 5, can open valve 13,15, valve-off 14, circulating pump 11 is started working simultaneously.Liquid CO 2 enters pressure-reducing valve 6 from fluid reservoir 5, and carbon dioxide liquid pressure after pressure-reducing valve 6 decompressions are dammed drops to 1.0～1.2MPa; Temperature drops to-40～-35 ℃, and the refrigerant temperature in the accumulation of energy groove 10 is cooled to-35～-30 ℃.Refrigerating medium pumps into heat exchanger 8 by circulating pump 11 works done with refrigerating medium.When temperature sensor 12 detected refrigerant temperature and is lower than-30 ℃, pneumatic ball valve 3 was closed, and the carbon dioxide after drying dewaters enters heat exchanger 8.Through refrigerating medium cooling becoming liquid, flow into liquefaction heat exchanger 4.Provide the refrigeration compressor 16 of low-temperature refrigerant can quit work for liquefaction heat exchanger 4 this moment.
During carbon dioxide after not having drying to dewater, refrigerant temperature can be lower than-40 ℃, and this moment, valve- off 13,15 was opened valve 14, uses vaporizer 9 vaporization carbon dioxide liquid, guarantees rear end gas just commonly used.Be lower than-40 ℃ for a long time as refrigerant temperature, circulating pump 11 can quit work.
When follow-up gas equipment during without gas, no liquid carbon dioxide flows in the accumulation of energy groove, refrigerant temperature constantly raises, no low-temperature receiver, when refrigerant temperature is higher than-25 ℃, for liquefaction heat exchanger 4 provides the refrigeration compressor 16 of cryogenic refrigeration to restart work, normally liquefy to guarantee the carbon dioxide gas physical efficiency that reclaims.
The part that the present invention does not relate to prior art that maybe can adopt all same as the prior art is realized.
Claims (4)
1. one kind has CO
2The CO of cold retracting device vaporizes
2Recycle complete set of equipments, it comprises CO
2Compressor (1), CO
2Drier (2), reboiler (17), refrigeration compressor (16), liquefaction heat exchanger
(4), fluid reservoir (5) and vaporizer (9), CO
2The input and the CO of compressor (1)
2Source of the gas links to each other, CO
2The output and the CO of compressor (1)
2The input of drier (2) links to each other, CO
2The output of drier (2) links to each other with the input of reboiler (17), and the gas output end of reboiler (17) links to each other by the gas input of pneumatic ball valve (3) with liquefaction heat exchanger (4), enters the CO in the liquefaction heat exchanger (4)
2Gas is cooled to liquid CO through refrigeration compressor (16)
2, liquid CO
2Behind the middle removal of reboiler (17) impurity, pump in the fluid reservoir (5), it is characterized in that:
Between fluid reservoir (5) and vaporizer (9), accumulation of energy groove (10) is installed, the liquid CO in the fluid reservoir (5)
2Pressure greater than the liquid CO in the accumulation of energy groove (10)
2Pressure;
Accumulation of energy groove (10) is connected with heat exchanger (8), and the refrigerating medium in the accumulation of energy groove (10) circulates the CO of heat exchanger (8) by circulating pump (11) and connecting pipe between accumulation of energy groove (10) and heat exchanger (8)
2Gas feed directly is connected with the gas vent of reboiler (17), the gas vent of heat exchanger (8) directly with the liquid CO of liquefaction heat exchanger (4)
2Inlet is connected, liquid CO
2Directly flow into the reboiler (17) and pump into fluid reservoir (5) behind the removal impurity from liquefaction heat exchanger (4).
2. the CO that has according to claim 1
2The CO of cold retracting device vaporizes
2Recycle complete set of equipments, it is characterized in that on the pipeline that connects between fluid reservoir (5) and the accumulation of energy groove (10), pressure-reducing valve (6) being installed.
3. the CO that has according to claim 1
2The CO of cold retracting device vaporizes
2Recycle complete set of equipments, it is characterized in that on the tube connector that connects between accumulation of energy groove (10) and the vaporizer (9), shutoff valve (15) being installed; Between described fluid reservoir (5) and vaporizer (9), also be connected with the direct-furnish pipe, direct-furnish valve (14) is installed on described direct-furnish pipe.
4. the CO that has according to claim 1
2The CO of cold retracting device vaporizes
2Recycle complete set of equipments, it is characterized in that carrying on the cold system output pipe of described accumulation of energy groove (10) is equipped with temperature sensor (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102150221A CN101871717B (en) | 2010-07-01 | 2010-07-01 | Complete equipment for CO2 recycling with CO2 vaporization and cool recycling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102150221A CN101871717B (en) | 2010-07-01 | 2010-07-01 | Complete equipment for CO2 recycling with CO2 vaporization and cool recycling device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101871717A true CN101871717A (en) | 2010-10-27 |
| CN101871717B CN101871717B (en) | 2011-11-09 |
Family
ID=42996725
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010102150221A Active CN101871717B (en) | 2010-07-01 | 2010-07-01 | Complete equipment for CO2 recycling with CO2 vaporization and cool recycling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101871717B (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108654905A (en) * | 2018-06-27 | 2018-10-16 | 东莞理工学院 | A kind of energy-saving closed anhydrous coating processes system |
| CN109028629A (en) * | 2018-06-12 | 2018-12-18 | 山东神舟制冷设备有限公司 | A kind of carbon dioxide refrigerating medium refrigeration system and its refrigerating method |
| CN111802912A (en) * | 2020-05-26 | 2020-10-23 | 浙江大学 | Energy-saving kettle |
| CN111895680A (en) * | 2020-07-15 | 2020-11-06 | 广州市华达石化有限公司 | Production control method adopting liquid carbon dioxide for refrigeration |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08311438A (en) * | 1995-05-18 | 1996-11-26 | Osaka Gas Co Ltd | Refrigerant for production of liquefied carbon dioxide and method for operating liquefied carbon dioxide production equipment |
| CN1289720A (en) * | 2000-10-17 | 2001-04-04 | 重庆理想科技有限公司 | Process for preparing food-class high-purity liquid CO2 |
| CN1393398A (en) * | 2001-06-22 | 2003-01-29 | 中国华陆工程公司 | Process for preparing food-class liquid CO2 |
| CN2606739Y (en) * | 2003-03-14 | 2004-03-17 | 大连理工大学 | CO2 purifying device by adsorptive fine disstillation |
| EP1776553A1 (en) * | 2004-07-16 | 2007-04-25 | Statoil ASA | Process and apparatus for the liquefaction of carbon dioxide |
| US20090255273A1 (en) * | 2008-04-09 | 2009-10-15 | Siemens Aktiengesellschaft | Method and device for condensing CO2 |
| JP2009242160A (en) * | 2008-03-31 | 2009-10-22 | Chugoku Electric Power Co Inc:The | Test device and test method for carbon dioxide recovery system |
| CN101607708A (en) * | 2009-07-27 | 2009-12-23 | 申屠晶 | The co-production of technical grade and food-class liquid CO 2 and device |
-
2010
- 2010-07-01 CN CN2010102150221A patent/CN101871717B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08311438A (en) * | 1995-05-18 | 1996-11-26 | Osaka Gas Co Ltd | Refrigerant for production of liquefied carbon dioxide and method for operating liquefied carbon dioxide production equipment |
| CN1289720A (en) * | 2000-10-17 | 2001-04-04 | 重庆理想科技有限公司 | Process for preparing food-class high-purity liquid CO2 |
| CN1393398A (en) * | 2001-06-22 | 2003-01-29 | 中国华陆工程公司 | Process for preparing food-class liquid CO2 |
| CN2606739Y (en) * | 2003-03-14 | 2004-03-17 | 大连理工大学 | CO2 purifying device by adsorptive fine disstillation |
| EP1776553A1 (en) * | 2004-07-16 | 2007-04-25 | Statoil ASA | Process and apparatus for the liquefaction of carbon dioxide |
| JP2009242160A (en) * | 2008-03-31 | 2009-10-22 | Chugoku Electric Power Co Inc:The | Test device and test method for carbon dioxide recovery system |
| US20090255273A1 (en) * | 2008-04-09 | 2009-10-15 | Siemens Aktiengesellschaft | Method and device for condensing CO2 |
| CN101607708A (en) * | 2009-07-27 | 2009-12-23 | 申屠晶 | The co-production of technical grade and food-class liquid CO 2 and device |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109028629A (en) * | 2018-06-12 | 2018-12-18 | 山东神舟制冷设备有限公司 | A kind of carbon dioxide refrigerating medium refrigeration system and its refrigerating method |
| CN109028629B (en) * | 2018-06-12 | 2023-08-01 | 山东神舟制冷设备有限公司 | Carbon dioxide secondary refrigerant refrigerating system and refrigerating method thereof |
| CN108654905A (en) * | 2018-06-27 | 2018-10-16 | 东莞理工学院 | A kind of energy-saving closed anhydrous coating processes system |
| CN111802912A (en) * | 2020-05-26 | 2020-10-23 | 浙江大学 | Energy-saving kettle |
| CN111895680A (en) * | 2020-07-15 | 2020-11-06 | 广州市华达石化有限公司 | Production control method adopting liquid carbon dioxide for refrigeration |
| CN111895680B (en) * | 2020-07-15 | 2021-09-03 | 广州市华达石化有限公司 | Production control method adopting liquid carbon dioxide for refrigeration |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101871717B (en) | 2011-11-09 |
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Free format text: FORMER OWNER: LI CHANGQING ZHAO XIN QIU GUANGLI Effective date: 20130819 Owner name: NANJING YITAN TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: DAI JIANGANG Effective date: 20130819 |
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Effective date of registration: 20130819 Address after: 210022, No. 1 factory building, Weng Jia Ying River Bend Industrial Zone, Qinhuai District, Jiangsu, Nanjing Patentee after: Nanjing Yitan Science and Technology Co., Ltd. Address before: 211100, Xiangshan Town, Jiangning District, Jiangsu, Nanjing 1-305 Patentee before: Dai Jiangang Patentee before: Li Changqing Patentee before: Zhao Xin Patentee before: Qiu Guangli |
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Denomination of invention: Complete set of CO2 recycling equipment with CO2 vaporization cold recovery device Effective date of registration: 20191216 Granted publication date: 20111109 Pledgee: Bank of China Limited by Share Ltd Nanjing City South Branch Pledgor: Nanjing Yitan Science and Technology Co., Ltd. Registration number: Y2019320000364 |
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Date of cancellation: 20210108 Granted publication date: 20111109 Pledgee: Bank of China Limited by Share Ltd. Nanjing City South Branch Pledgor: NANJING YITAN SCIENCE AND TECHNOLOGY Co.,Ltd. Registration number: Y2019320000364 |
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Denomination of invention: CO2 recycling equipment with CO2 vaporization cold recovery device Effective date of registration: 20210112 Granted publication date: 20111109 Pledgee: Bank of China Limited by Share Ltd. Nanjing City South Branch Pledgor: NANJING YITAN SCIENCE AND TECHNOLOGY Co.,Ltd. Registration number: Y2021980000283 |
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