CN109425197A - A kind of argon gas recover device - Google Patents
A kind of argon gas recover device Download PDFInfo
- Publication number
- CN109425197A CN109425197A CN201710745409.XA CN201710745409A CN109425197A CN 109425197 A CN109425197 A CN 109425197A CN 201710745409 A CN201710745409 A CN 201710745409A CN 109425197 A CN109425197 A CN 109425197A
- Authority
- CN
- China
- Prior art keywords
- argon gas
- board
- cylinder
- liquid nitrogen
- partition
- 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.)
- Pending
Links
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 title claims abstract description 81
- 229910052786 argon Inorganic materials 0.000 title claims abstract description 41
- 239000007789 gas Substances 0.000 title claims abstract description 36
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 13
- 238000005192 partition Methods 0.000 claims abstract description 10
- 238000009834 vaporization Methods 0.000 claims abstract description 10
- 230000008016 vaporization Effects 0.000 claims abstract description 10
- 229910000838 Al alloy Inorganic materials 0.000 claims abstract description 4
- 239000000956 alloy Substances 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims abstract description 4
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 238000001704 evaporation Methods 0.000 claims description 2
- 230000008020 evaporation Effects 0.000 claims description 2
- 238000003860 storage Methods 0.000 abstract description 7
- 238000009833 condensation Methods 0.000 abstract description 4
- 230000005494 condensation Effects 0.000 abstract description 4
- 208000002925 dental caries Diseases 0.000 abstract description 3
- 238000011084 recovery Methods 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J5/00—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
- F25J5/002—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger
- F25J5/005—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger in a reboiler-condenser, e.g. within a column
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04012—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling
- F25J3/04042—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling of argon or argon enriched stream
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/42—Nitrogen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/58—Argon
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/90—Boil-off gas from storage
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
- F25J2270/904—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration by liquid or gaseous cryogen in an open loop
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The present invention provides a kind of argon gas recover devices, including cylinder, partition, top end socket, bottom head, board-like unit, baffle to constitute.The top end socket and cylinder, board-like channel and bottom head and cylinder form a working space cavity, the cavity of board-like outer wall, upper lower clapboard and middle cylinder composition liquid nitrogen vaporization, shell is divided into two closed cavitys by partition, for board-like unit as argon gas liquefaction, the carrier of liquid nitrogen vaporization, the material used is aluminum alloy material.Argon gas recover device provided by the invention is for that can carry out condensation liquefaction using the liquid nitrogen of device itself for the argon gas of the vaporization from storage tank, liquid argon can return storage tank, and recovery efficiency is high in air separation unit system.
Description
Technical field
The present invention relates to a kind of argon gas recovers, in air separation unit system.
Background technique
Argon gas is industrially to apply very wide rare gas at present, and property is very inactive, can neither burn, also not help
Combustion.In aircraft manufacturing, shipbuilding, atomic energy industry and mechanical industry department, when being welded to particulate metal, often made with argon gas
Gas is protected for welding, prevents weldment oxidation by air or nitridation.
Argon gas can be extracted from air and synthetic ammonia tailgas.Currently, by-product argon gas has become life from air separation unit
Produce the main method of argon gas.But with the enlargement of ammonia synthesizing industry, mention argon using synthetic ammonia tailgas and also increasing year by year, skill
Art economic indicator is also constantly improving.Argon gas has preferable valence regardless of international sale is used by oneself or be used as production simultaneously
Lattice advantage, this makes gas generation producer increasingly pay attention to the potentiality of excavating equipment, improves Argon recovery rate to the maximum extent, recycling
And then the argon for this part vaporization of liquefying realizes its application value, economical and feasibility again.
In this background, the present invention is to realize that argon gas recycles function, and proposition designs a kind of liquid nitrogen using device itself
Condensation liquefaction is carried out, storage tank is then returned, realizes the device that argon gas effectively recycles.
Summary of the invention
In order to solve prior art problem, the present invention provides a kind of argon gas recover devices, mainly use following technology
Scheme:
A kind of argon gas recover device, including cylinder, partition, top end socket, bottom head, board-like unit, baffle are constituted,
The top end socket and cylinder, board-like channel and bottom head and cylinder form a working space cavity, board-like outer wall, up and down
The cavity of partition and middle cylinder composition liquid nitrogen vaporization.
Further, shell is divided into two closed cavitys by the partition.
Further, for the board-like unit as argon gas liquefaction, the carrier of liquid nitrogen vaporization, the material used is aluminium alloy material
Matter.
Compared with prior art, the present invention has the following advantages:
The present invention provides a kind of argon gas recover devices, can be by the argon gas of the vaporization from storage tank using device itself
Liquid nitrogen carries out condensation liquefaction, and liquid argon can return storage tank, and recovery efficiency is high.
Detailed description of the invention
Fig. 1 is structure chart of the invention.
Wherein, 1-partition；2-aluminium-made plate type units；3-liquid nitrogen outlets；4-argon gas inlet tubes；5-end sockets；6—
Liquid nitrogen inlet tube；
7-baffles；8-cylinders；9-liquid argon outlets.
Specific embodiment
Below with reference to embodiment, the present invention is further illustrated.
The present invention provides a kind of argon gas recover devices, including cylinder, partition, top end socket, bottom head, board-like list
Member, baffle are constituted, and the top end socket and cylinder, board-like channel and bottom head and cylinder form a working space cavity,
The cavity of board-like outer wall, upper lower clapboard and middle cylinder composition liquid nitrogen vaporization.
Shell is divided into two closed cavitys by partition, and board-like unit makes as argon gas liquefaction, the carrier of liquid nitrogen vaporization
Material is aluminum alloy material.
The working principle of argon gas recover device: argon gas comes from liquid argon storage tank, the argon little in saturated mode or the degree of superheat
Gas enters case top, is full of board-like ar gas passage side, since liquid argon side temperature is lower, the temperature difference of evaporation side and condensation side compared with
Greatly, so that argon gas starts to condense in board-like argon gas side, drop gradually collects in bottom, becomes liquid argon, returns to storage tank, and then realize
Recycling.
The foregoing is only a preferred embodiment of the present invention, is not intended to restrict the invention.Based in the present invention
Embodiment, every other embodiment obtained by those of ordinary skill in the art without making creative efforts, institute
Any modification, equivalent substitution, improvement and etc. of work, should all be included in the protection scope of the present invention.
Claims (3)
1. a kind of argon gas recover device, including cylinder, partition, top end socket, bottom head, board-like unit, baffle are constituted, institute
State top end socket and cylinder, board-like channel and bottom head and cylinder and form a working space cavity, board-like outer wall, up and down every
The cavity of plate and middle cylinder composition liquid nitrogen vaporization.
2. argon gas recover device as described in claim 1, it is characterised in that: the partition by shell be divided into two it is closed
Cavity.
3. argon gas recover device as described in claim 1, it is characterised in that: the board-like unit is as argon gas liquefaction, liquid
The carrier of nitrogen evaporation, the material used are aluminum alloy material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710745409.XA CN109425197A (en) | 2017-08-26 | 2017-08-26 | A kind of argon gas recover device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710745409.XA CN109425197A (en) | 2017-08-26 | 2017-08-26 | A kind of argon gas recover device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109425197A true CN109425197A (en) | 2019-03-05 |
Family
ID=65500212
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710745409.XA Pending CN109425197A (en) | 2017-08-26 | 2017-08-26 | A kind of argon gas recover device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109425197A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1120651A (en) * | 1994-02-24 | 1996-04-17 | 林德股份公司 | Method and apparatus for pure argon recovery |
| CN203572142U (en) * | 2013-12-02 | 2014-04-30 | 中空能源设备有限公司 | Argon recycling device |
| CN104142044A (en) * | 2014-08-06 | 2014-11-12 | 杭州杭氧股份有限公司 | Modular argon recovery liquefier and argon recovery method |
| CN204085056U (en) * | 2014-08-06 | 2015-01-07 | 杭州杭氧股份有限公司 | A kind of modularization argon reclaims liquefier |
| US20150316318A1 (en) * | 2014-05-01 | 2015-11-05 | Karl K. Kibler | System and method for production of argon by cryogenic rectification of air |
-
2017
- 2017-08-26 CN CN201710745409.XA patent/CN109425197A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1120651A (en) * | 1994-02-24 | 1996-04-17 | 林德股份公司 | Method and apparatus for pure argon recovery |
| CN203572142U (en) * | 2013-12-02 | 2014-04-30 | 中空能源设备有限公司 | Argon recycling device |
| US20150316318A1 (en) * | 2014-05-01 | 2015-11-05 | Karl K. Kibler | System and method for production of argon by cryogenic rectification of air |
| CN104142044A (en) * | 2014-08-06 | 2014-11-12 | 杭州杭氧股份有限公司 | Modular argon recovery liquefier and argon recovery method |
| CN204085056U (en) * | 2014-08-06 | 2015-01-07 | 杭州杭氧股份有限公司 | A kind of modularization argon reclaims liquefier |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20190305 |