CN103288085A - Dry ice generator using cold energy produced in vaporization of cryogenic liquid - Google Patents
Dry ice generator using cold energy produced in vaporization of cryogenic liquid Download PDFInfo
- Publication number
- CN103288085A CN103288085A CN201310132052XA CN201310132052A CN103288085A CN 103288085 A CN103288085 A CN 103288085A CN 201310132052X A CN201310132052X A CN 201310132052XA CN 201310132052 A CN201310132052 A CN 201310132052A CN 103288085 A CN103288085 A CN 103288085A
- Authority
- CN
- China
- Prior art keywords
- dry ice
- cold energy
- pipeline
- inner bag
- cryogenic liquid
- 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.)
- Granted
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 59
- 235000011089 carbon dioxide Nutrition 0.000 title claims abstract description 48
- 239000007788 liquid Substances 0.000 title claims abstract description 26
- 238000009834 vaporization Methods 0.000 title claims abstract description 12
- 239000006200 vaporizer Substances 0.000 claims abstract description 12
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 10
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 10
- 238000003860 storage Methods 0.000 claims abstract description 7
- 238000007789 sealing Methods 0.000 claims description 10
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- 239000010949 copper Substances 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 3
- 238000002309 gasification Methods 0.000 abstract description 2
- 238000005345 coagulation Methods 0.000 abstract 1
- 230000015271 coagulation Effects 0.000 abstract 1
- 238000007711 solidification Methods 0.000 abstract 1
- 238000005057 refrigeration Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000001105 regulatory Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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 relates to a dry ice generator using cold energy produced in vaporization of a cryogenic liquid. According to the invention, one end of a liquid pump is hermetically communicated with a cryogenic storage tank, and the other end of the liquid pump is hermetically communicated with one end of a vaporizer through a pipeline and a valve; the other end of the vaporizer is hermetically communicated with a collision system through a pipeline; two ends of the valve are parallely jointed with a heat exchanger of the dry ice generator through pipelines and another valve; and a carbon dioxide gas inlet of the dry ice generator is hermetically communicated with a carbon dioxide gas cylinder. The dry ice generator provided by the invention uses cryogenic cold energy generated in the processes of filling and gasification of a variety of cryogenic liquids for coagulation and solidification of carbon dioxide without consumption of electric energy, and theoretically, the generation rate of dry ice can 100%; so the dry ice generator is a novel energy-saving environment-friendly technology for production of dry ice.
Description
Technical field
The present invention relates to a kind of dry ice producer, particularly utilize the device of cryogenic liquid vaporization cold energy dry ice processed.
Background technology
What the general employing of dry ice was made in industry is to obtain dry ice with the liquid carbon dioxide throttling expansion, and this technology dry ice production rate generally has only about 40%, and difficult recovery of the carbon dioxide that do not condense mostly caused very big waste; And if adopt freon refrigeration or ammonia refrigeration processing method to obtain that though the low temperature cold can improve the dry ice production rate but need bigger refrigeration compressor, consume more electric energy.
Usefulness low temperature storage tanks such as increasing various cryogenic liquid such as liquid oxygen, liquid argon, liquid nitrogen store, and then with the cryogenic liquid pump pressurization, take to charge into the gas cylinder sale after the empty bath formula vaporizer heat exchange vaporization.When filling operation, because the high pressure low temperature liquid behind the cryogenic liquid pump leans on the air heat exchange carburation by evaporation in vaporizer and the atmosphere, a large amount of cryogenic cold energy is lost in the atmosphere goes.For example, 1 cubic metre of liquid oxygen in the common storage tank from-160C through being gasificated into the cold energy that the normal temperature and pressure gaseous state can produce about 100,000 kilocalories, if consider variation and the influence of charge pressure, also can produce the cold energy of about 80,000 kilocalories, so big cryogenic cold energy recovery is produced dry ice and can be produced huge economy and environmental benefit.
Summary of the invention
In order to overcome the shortcoming of prior art, the invention provides a kind of cryogenic liquid vaporization cold energy dry ice producer that utilizes, it is that all kinds of cryogenic liquids are filled the cryogenic cold energy of gasification for the condensation cure of carbonic acid gas, need not to increase power consumption, the dry ice production rate can reach 100% in theory, is an energy-conserving and environment-protective new technology of producing dry ice.
The present invention solves the technical scheme that its technical problem takes: liquor pump one end communicates with the low temperature storage tank sealing by pipeline, the other end communicates with the end sealing of vaporizer by pipeline, valve, the other end of vaporizer communicates to seal with the collision system sealing by pipeline and communicates, the two ends of described valve by pipeline, valve and dry ice producer interchanger and connect, the carbon dioxide import of dry ice producer communicates with the dioxide bottle sealing.
1), can utilize the cold energy that produces of vaporizing in the liquid filling process to realize the energy-conservation dry ice processed of no consumption the present invention has following advantage:.Greatly reduce than original dry ice function consumption processed; 2), can not destroy the normal operation of former charging system, and can reduce the heat exchange load of original vaporizer; 3), the cold energy of dry ice processed can regulate by variable valve, and temperature can realize automatic control; 4), present technique is applicable to continuously or a bottle production process is filled in the cryogenic liquid that fills continuously in for some time vaporization, does not also influence original charging system work even do not produce dry ice, for enterprise of liquid fueling station increases a coproduction dry ice project.
Description of drawings
The present invention is further described below in conjunction with drawings and Examples.
Fig. 1 is synoptic diagram of the present invention.
Embodiment
As shown in Figure 1, liquor pump 2 one ends communicate with low temperature storage tank 1 sealing by pipeline, the other end communicates with the end sealing of vaporizer 5 by pipeline, valve 4, the other end of vaporizer 5 seals the sealing that communicates by pipeline with collision system 12 and communicates, the two ends of described valve 4 by pipeline, valve 3 and dry ice producer interchanger and connect, the carbon dioxide import of dry ice producer communicates with dioxide bottle 11 sealings, and dioxide bottle 11 also can be the carbonic acid gas storage tank.
Described dry ice producer comprises insulating shell 9, interchanger 7, inner bag 8, piston 6 and dry ice shape switchboard 10, piston 6 is in stainless inner bag 8, be slidingly matched with inner bag 8, one end of inner bag 8 is dry ice shape switchboard 10 fixedly, twine the interchanger 7 of copper pipe formula on the cylindrical surface of inner bag 8, interchanger 7 external parcel insulating shells 9 prevent cold draining; On the described inner bag 8 the carbon dioxide import is arranged.
A plurality of dry ice hole is arranged on the end face of described dry ice shape switchboard 10, and dry ice hole cross section is circle or sheet shape, or other shapes, to satisfy the needs of different user.
During use, according to the aperture of how much coming regulated valve 4 of institute's chilling requirement.Cryogenic liquid with the heat exchange of dry ice producer after return original high-pressure carburetor piping system again, do not influence the vaporization of original high pressure charging system and fill, can also reduce the working load of former vaporizer.
Claims (4)
1. one kind is utilized cryogenic liquid vaporization cold energy dry ice producer, liquor pump (2) one ends communicate with low temperature storage tank (1) sealing by pipeline, the other end communicates with the end sealing of vaporizer (5) by pipeline, valve (4), the other end of vaporizer (5) seals the sealing that communicates by pipeline with collision system (12) and communicates, it is characterized in that: the two ends of described valve (4) by pipeline, valve (3) and dry ice producer interchanger and connect, the carbon dioxide import of dry ice producer seals with dioxide bottle (11) and communicates.
2. the cryogenic liquid vaporization cold energy dry ice producer that utilizes according to claim 1, it is characterized in that: described dry ice producer comprises insulating shell (9), interchanger (7), inner bag (8), piston (6) and dry ice shape switchboard (10), piston (6) is in stainless inner bag (8), be slidingly matched with inner bag (8), one end of inner bag (8) is dry ice shape switchboard (10) fixedly, twine the interchanger (7) of copper pipe formula on the cylindrical surface of inner bag (8), interchanger (7) external parcel insulating shell (9) prevents cold draining; Described inner bag has the carbon dioxide import on (8).
3. the cryogenic liquid vaporization cold energy dry ice producer that utilizes according to claim 2 is characterized in that: a plurality of dry ice hole is arranged on the end face of described dry ice shape switchboard (10).
4. the cryogenic liquid vaporization cold energy dry ice producer that utilizes according to claim 3, it is characterized in that: the cross section in described dry ice hole is circle or sheet shape.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310132052.XA CN103288085B (en) | 2013-04-16 | 2013-04-16 | Utilize cryogenic liquid vaporizer cold energy dry ice generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310132052.XA CN103288085B (en) | 2013-04-16 | 2013-04-16 | Utilize cryogenic liquid vaporizer cold energy dry ice generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103288085A true CN103288085A (en) | 2013-09-11 |
| CN103288085B CN103288085B (en) | 2016-01-06 |
Family
ID=49089700
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310132052.XA Active CN103288085B (en) | 2013-04-16 | 2013-04-16 | Utilize cryogenic liquid vaporizer cold energy dry ice generator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103288085B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104986766A (en) * | 2015-07-28 | 2015-10-21 | 宋开泉 | Equipment for preparing solid carbon dioxide and metal calcium from calcite |
| CN106082218A (en) * | 2016-08-05 | 2016-11-09 | 廊坊市尚奇燃气技术有限责任公司 | Prepare the device of dry ice |
| CN106744957A (en) * | 2017-03-15 | 2017-05-31 | 长沙紫宸科技开发有限公司 | A kind of pump pressure type dry-ice machine |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB932559A (en) * | 1958-10-15 | 1963-07-31 | Laszlo Vahl | Method for the production of carbon dioxide ice |
| CN201628446U (en) * | 2010-04-13 | 2010-11-10 | 济南鲍德气体有限公司 | Recovery system for cold energy released in vaporization of cryogenic liquid |
| CN101913604A (en) * | 2010-07-20 | 2010-12-15 | 浙江大学 | Device and method for manufacturing dry ice by using liquefied natural gas cold energy |
| CN103017402A (en) * | 2011-09-21 | 2013-04-03 | 周健 | Device for recovering liquid gas gasification cold |
-
2013
- 2013-04-16 CN CN201310132052.XA patent/CN103288085B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB932559A (en) * | 1958-10-15 | 1963-07-31 | Laszlo Vahl | Method for the production of carbon dioxide ice |
| CN201628446U (en) * | 2010-04-13 | 2010-11-10 | 济南鲍德气体有限公司 | Recovery system for cold energy released in vaporization of cryogenic liquid |
| CN101913604A (en) * | 2010-07-20 | 2010-12-15 | 浙江大学 | Device and method for manufacturing dry ice by using liquefied natural gas cold energy |
| CN103017402A (en) * | 2011-09-21 | 2013-04-03 | 周健 | Device for recovering liquid gas gasification cold |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104986766A (en) * | 2015-07-28 | 2015-10-21 | 宋开泉 | Equipment for preparing solid carbon dioxide and metal calcium from calcite |
| CN104986766B (en) * | 2015-07-28 | 2017-06-13 | 宋开泉 | The equipment that calcite prepares drikold and calcium metal |
| CN106082218A (en) * | 2016-08-05 | 2016-11-09 | 廊坊市尚奇燃气技术有限责任公司 | Prepare the device of dry ice |
| CN106744957A (en) * | 2017-03-15 | 2017-05-31 | 长沙紫宸科技开发有限公司 | A kind of pump pressure type dry-ice machine |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103288085B (en) | 2016-01-06 |
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| C06 | Publication | ||
| PB01 | Publication | ||
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| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160914 Address after: Room 21, 2301, century street, 056000 high street, Handan, Hebei Patentee after: Handan cryogenic gas separation equipment Co., Ltd. Address before: Handan City, Hebei province 057350 Hanshan Handan Luo two living area 8-5-1 Patentee before: Yang Zhongwei |