CN108981287A - A kind of anti-icing stifled multistage drain formula liquefier - Google Patents
A kind of anti-icing stifled multistage drain formula liquefier Download PDFInfo
- Publication number
- CN108981287A CN108981287A CN201811047465.7A CN201811047465A CN108981287A CN 108981287 A CN108981287 A CN 108981287A CN 201811047465 A CN201811047465 A CN 201811047465A CN 108981287 A CN108981287 A CN 108981287A
- Authority
- CN
- China
- Prior art keywords
- fluid reservoir
- liquefier
- heat exchanger
- small
- liquefaction
- 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
- 239000012530 fluid Substances 0.000 claims abstract description 32
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 241000521257 Hydrops Species 0.000 claims abstract description 4
- 206010030113 Oedema Diseases 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- 230000008901 benefit Effects 0.000 abstract description 4
- 238000009835 boiling Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 230000008439 repair process Effects 0.000 abstract description 2
- 230000006872 improvement Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 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
-
- 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
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/42—Nitrogen or special cases, e.g. multiple or low purity N2
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The present invention relates to Thermal Equipment field, more particularly to a kind of anti-icing stifled multistage drain formula liquefier, including heat exchanger and fluid reservoir, the settings of several stages of the heat exchanger point；It is equipped with small-sized fluid reservoir between two two heat exchangers and is used as hydrops；The bottom of the small-sized fluid reservoir is additionally provided with liquid trap and leads to main fluid reservoir.It takes out the advantage of the invention is that can in time separate condensed fluid and retain gas and continue to liquefy, the stifled phenomenon of ice often occurs in when gas liquefaction that boiling point and fusing point can be effectively prevent to be closer to, substantially increases liquefaction efficiency.The present invention has the advantages that structure is simple, liquefaction efficiency is high, manufacture is easy to repair, economic cost is low, plays a significant role in low-temperature liquefaction and field of heat exchange.
Description
Technical field
The present invention relates to Thermal Equipment fields, more particularly to a kind of anti-icing stifled multistage drain formula liquefier.
Background technique
Cold header heat exchanger is the key equipment for low-temperature gas liquefaction, and increasing heat exchange area is the routine for improving liquefied fraction
Means.But for the gas such as nitrogen that fusing point and boiling point are closer to, increase heat exchange area makes it possible to gas and is too cold
Solid blocking heat exchanger channel is formed below to freezing point, to cause the sharply decline of heat exchange efficiency.If but not increasing
Heat exchange area, liquefied fraction are then difficult to improve again.
Summary of the invention
The purpose of the present invention is overcoming the shortcomings of prior art process, a kind of anti-icing stifled multistage drain formula liquefaction is provided
Device.
To achieve the above object, technical solution provided by the invention is as follows:
A kind of anti-icing stifled multistage drain formula liquefier, including heat exchanger and fluid reservoir, several ranks of the heat exchanger point
Section setting；It is equipped with small-sized fluid reservoir between two two heat exchangers and is used as hydrops；The bottom of the small-sized fluid reservoir is additionally provided with liquid trap
Lead to main fluid reservoir.
As a further improvement of the present invention, the main fluid reservoir is one, and each liquid trap is accessed in parallel way
Same main fluid reservoir.
As a further improvement of the present invention, the solenoid valve of control liquid outflow is respectively equipped on each liquid trap.
As a further improvement of the present invention, the small-sized fluid reservoir is hermetically sealed can, and gas in tank can be pushed back to described change
Hot device.
Further improvement of the present invention, the liquefier are suitable for liquefaction of nitrogen.
Compared with prior art, it takes out the advantage of the invention is that can in time separate condensed fluid and retains gas and continue liquid
Change, the stifled phenomenon of ice often occurs in when gas liquefaction that boiling point and fusing point can be effectively prevent to be closer to, substantially increases liquefaction
Efficiency.The present invention has the advantages that structure is simple, liquefaction efficiency is high, manufacture is easy to repair, economic cost is low, in low-temperature liquefaction and
It plays a significant role in field of heat exchange.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
In figure, 1 heat exchanger, 2 small-sized fluid reservoirs, 3 main fluid reservoirs, 4 solenoid valves, 5 liquid traps.
Specific embodiment
As shown in Figure 1, anti-icing stifled multistage drain formula liquefier of the invention, including multiple-stage heat exchanger 1, multiple small-sized storages
Flow container 2, main fluid reservoir 3, solenoid valve 4 and liquid trap 5.The heat exchanger 1 in each stage and multiple small-sized fluid reservoirs 2 are replaced by pipeline
It is sequentially connected, and outlet is arranged at the bottom of multiple small-sized fluid reservoirs 2, is linked into the same main storage by 5 pipeline of liquid trap in parallel
Flow container 3 makees last hydrops storage.Solenoid valve 4 is respectively arranged on being exported between the import of main fluid reservoir 3 of small-sized fluid reservoir 2
On liquid trap 5, the process of main fluid reservoir 3 is flowed into for controlling liquid from multiple small-sized fluid reservoirs 2；Small-sized fluid reservoir 2 is sealing
Structure can push back gas in tank to next heat exchanger 1.
Work implementation process of the invention is as follows:
Extraneous refrigeration machine is opened, gas (usually nitrogen) enters multiple-stage heat exchanger, gas to be liquefied from left end entrance
It is cooled to gas-liquid two-phase state after into first segment heat exchanger, is then pressed into the small-sized fluid reservoir bottom for having certain liq
Portion, liquid phase stay in tank body, and gas phase is picked out from tank body top, enter back into second segment heat exchanger and second small-sized holding vessel.Such as
This is repeatedly.After multiple small-sized fluid reservoirs run up to certain amount of liquid, the solenoid valve of bottom is opened, liquid flow is become owner of into liquid storage
In tank.
Finally, it is also noted that listed above is only a specific embodiment of the invention.Obviously, the present invention is gone back
Directly it can export or associate from present disclosure there are many deformation, those skilled in the art and is all
Deformation, is considered as protection scope of the present invention.
Claims (5)
1. a kind of anti-icing stifled multistage drain formula liquefier, including heat exchanger and fluid reservoir, which is characterized in that the heat exchanger
(1) several stages is divided to be arranged；It is equipped with small-sized fluid reservoir (2) between two two heat exchangers and is used as hydrops；The small-sized fluid reservoir (2)
Bottom be additionally provided with liquid trap (5) and lead to main fluid reservoir (3).
2. anti-icing stifled multistage drain formula liquefier according to claim 1, which is characterized in that the main fluid reservoir (3)
It is one, each liquid trap (5) accesses same main fluid reservoir (3) in parallel way.
3. anti-icing stifled multistage drain formula liquefier according to claim 3, which is characterized in that each liquid trap (5)
On be respectively equipped with control liquid outflow solenoid valve (4).
4. anti-icing stifled multistage drain formula liquefier according to claim 1, which is characterized in that the small-sized fluid reservoir
(2) it is hermetically sealed can, gas in tank can be pushed back the heat exchanger (1).
5. anti-icing stifled multistage drain formula liquefier according to claim 1, which is characterized in that the liquefier is suitable for
Liquefaction of nitrogen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811047465.7A CN108981287A (en) | 2018-09-09 | 2018-09-09 | A kind of anti-icing stifled multistage drain formula liquefier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811047465.7A CN108981287A (en) | 2018-09-09 | 2018-09-09 | A kind of anti-icing stifled multistage drain formula liquefier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108981287A true CN108981287A (en) | 2018-12-11 |
Family
ID=64544682
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811047465.7A Pending CN108981287A (en) | 2018-09-09 | 2018-09-09 | A kind of anti-icing stifled multistage drain formula liquefier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108981287A (en) |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5584194A (en) * | 1995-10-31 | 1996-12-17 | Gardner; Thomas W. | Method and apparatus for producing liquid nitrogen |
| FR2805034A1 (en) * | 2000-02-11 | 2001-08-17 | Air Liquide | Nitrogen liquefaction process involves compressing nitrogen to supercritical pressure, cooling by heat exchange with flow of liquefied natural gas in primary exchanger, expanded to specific pressure and liquefying |
| CN102564066A (en) * | 2012-02-10 | 2012-07-11 | 南京柯德超低温技术有限公司 | Low-temperature device for separating and purifying gas based on small-sized low-temperature refrigerating machine |
| EP2669613A1 (en) * | 2012-05-31 | 2013-12-04 | Linde Aktiengesellschaft | Method and device for liquefying nitrogen |
| CN103787286A (en) * | 2014-03-03 | 2014-05-14 | 天津凯德实业有限公司 | Nitrogen separation and liquefaction system |
| CN104457138A (en) * | 2014-10-23 | 2015-03-25 | 江西恒兴源化工有限公司 | Method for recovering carbon sulfide and hydrogen in separation mode |
| CN205084440U (en) * | 2015-10-14 | 2016-03-16 | 浙江邦成化工有限公司 | Solvent distilling Recycle condensing system |
| CN106938170A (en) * | 2017-03-31 | 2017-07-11 | 武汉金中石化工程有限公司 | A kind of processing unit and processing method of cobalt-based fixed bed F- T synthesis off-gas |
| CN108266966A (en) * | 2018-01-16 | 2018-07-10 | 中科睿凌江苏低温设备有限公司 | The Cryo Equipment for detaching and purifying for gas based on small-sized Cryo Refrigerator |
| CN209085178U (en) * | 2018-09-09 | 2019-07-09 | 杭州紫明冷链科技有限责任公司 | A kind of anti-icing stifled multistage drain formula liquefier |
-
2018
- 2018-09-09 CN CN201811047465.7A patent/CN108981287A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5584194A (en) * | 1995-10-31 | 1996-12-17 | Gardner; Thomas W. | Method and apparatus for producing liquid nitrogen |
| FR2805034A1 (en) * | 2000-02-11 | 2001-08-17 | Air Liquide | Nitrogen liquefaction process involves compressing nitrogen to supercritical pressure, cooling by heat exchange with flow of liquefied natural gas in primary exchanger, expanded to specific pressure and liquefying |
| CN102564066A (en) * | 2012-02-10 | 2012-07-11 | 南京柯德超低温技术有限公司 | Low-temperature device for separating and purifying gas based on small-sized low-temperature refrigerating machine |
| EP2669613A1 (en) * | 2012-05-31 | 2013-12-04 | Linde Aktiengesellschaft | Method and device for liquefying nitrogen |
| CN103787286A (en) * | 2014-03-03 | 2014-05-14 | 天津凯德实业有限公司 | Nitrogen separation and liquefaction system |
| CN104457138A (en) * | 2014-10-23 | 2015-03-25 | 江西恒兴源化工有限公司 | Method for recovering carbon sulfide and hydrogen in separation mode |
| CN205084440U (en) * | 2015-10-14 | 2016-03-16 | 浙江邦成化工有限公司 | Solvent distilling Recycle condensing system |
| CN106938170A (en) * | 2017-03-31 | 2017-07-11 | 武汉金中石化工程有限公司 | A kind of processing unit and processing method of cobalt-based fixed bed F- T synthesis off-gas |
| CN108266966A (en) * | 2018-01-16 | 2018-07-10 | 中科睿凌江苏低温设备有限公司 | The Cryo Equipment for detaching and purifying for gas based on small-sized Cryo Refrigerator |
| CN209085178U (en) * | 2018-09-09 | 2019-07-09 | 杭州紫明冷链科技有限责任公司 | A kind of anti-icing stifled multistage drain formula liquefier |
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