CN1228587C - Mixed liquid CO2 cold wind generator - Google Patents
Mixed liquid CO2 cold wind generator Download PDFInfo
- Publication number
- CN1228587C CN1228587C CN 01133718 CN01133718A CN1228587C CN 1228587 C CN1228587 C CN 1228587C CN 01133718 CN01133718 CN 01133718 CN 01133718 A CN01133718 A CN 01133718A CN 1228587 C CN1228587 C CN 1228587C
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- China
- Prior art keywords
- liquid
- mixed
- cold wind
- dehumidifier
- nozzle
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- 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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Abstract
The present invention relates to a mixed liquid CO2 cold gas generator. A vortex dehumidifier is arranged on the device, and is composed of a dehumidification casing and a mixed gas dry wind exhaust funnel which is arranged in the casing. A circulation current channel is formed between the dehumidification casing and the mixed gas dry wind exhaust funnel, room temperature mixed gas speeds up at a gas supply nozzle of the dehumidifier of the annular channel and flows inside tangentially, and in addition, an atomization spray nozzle of liquid CO2 is arranged on the position of 180 degrees on the opposite of the channel. The liquid CO2 which is throttled and decompressed can be atomized by high-speed mixed gas flow at a CO2 jetting guide opening of the terminal of a gas supply nozzle of a cold gas pot.
Description
Technical field:
The title of patent of the present invention is: mixed liquid CO
2Cold wind generator belongs to refrigeration and cryogenic technique field.
Background technology:
In the metal cutting process technology, use low-temperature cold wind to replace the technical profession of cutting agent processing to jump up at present, this technology adopts about-30 ℃ low-temperature cold wind to remove to cool off cutting point, has played good effect.In this technology, a kind of method is to use low boiling working fluid to reduce air themperature as low-temperature receiver, at present, mainly is to use liquid nitrogen.Because liquid nitrogen temperature under normal pressure is-196 ℃, air and liquid nitrogen carry out heat exchange in recuperative heat exchanger, and structure is very complicated, and the cost of liquid nitrogen is also higher, produce-30 ℃ air, are inappropriate economically with-196 ℃ liquid nitrogen.
Summary of the invention:
The present invention provides a kind of mixed liquid CO in order to remedy above-mentioned metal cutting processing with the technical deficiency of cold wind generator
2Cold wind generator is by liquid CO
2Storage tank, cyclone dehumidifier, cold wind jar, dehumidifier nozzle of air supply, cold wind canister incoming gas nozzle, flow control valve, choke valve and corresponding liquid CO
2Connecting tube, gas connecting tube are formed, and it is characterized in that: compressed air cooling cooling is by liquid CO
2After the choke valve throttling, be vaporific spraying into and form mist in the air-flow, fog-like liquid CO
2Constantly gasification absorbs heat in mist.The cyclone dehumidifier that uses is by dehumidifier shell and concentric with it and place the cyclone dehumidifier dry wind aiutage in the shell to form, form annular channel between the two, mixed at room temperature gas quickens the tangential inflow in back from the dehumidifier nozzle of air supply of circular passage, and liquid CO is housed in passage
2Atomizer, CO
2The emission direction of liquid mist is identical with the mixed airflow rotation direction.Isolated water droplet accumulates in the dehumidifier bottom.The characteristics of cold wind canister incoming gas nozzle are: the end of negative throat noz(zle) has a liquid CO
2Ejecting port is through the liquid CO of choke valve expenditure and pressure
2Drain by the high-speed mixing aerodynamic atomization and from the end outlet of this nozzle immediately after entering ejecting port.
Description of drawings:
Fig. 1 is mixed liquid CO
2System construction drawing.
Fig. 2 is the cyclone dehumidifier cutaway view.
Fig. 3 is liquid CO
2The injector structure chart.
Wherein: the liquid CO of 1-
2Storage tank; The 2-heat-insulation layer; The liquid CO of 3-
2Feed pipe; The 4-flow control valve; The 5-throttle expansion valve; The 6-drainpipe; 7-cold wind jar; 8-cold wind air supply pipe; 9-low-temperature mixed tracheae; 10-cyclone dehumidifier dry wind aiutage; 11-mixed at room temperature flue; 12-cold wind canister incoming gas nozzle; 13-dehumidifier nozzle of air supply; The 14-cyclone dehumidifier; 15-negative throat noz(zle) interface; The liquid CO of 16-
2Mist pipe; 17-CO
2Balance pipe; 18-CO
2The storage safety valve; The 19-gully.
The specific embodiment:
Fig. 1 represents that also a per minute is for 2M
3Temperature is-30 ℃ mixed liquid CO
2The cold wind generator structure chart.At liquid CO
2The liquid CO of storage in the storage tank 1
2Absorb the heat rear section gasification of passing heat-insulation layer 2 and be CO
2Gas and from the top CO of storage tank 1
2After the compressed air of balance pipe 17 and air compression station supply mixes in the mixed flue 11 of room temperature, the dehumidifier nozzle of air supply 13 of flowing through quickens, and tangentially flows in the cyclone dehumidifier 14 at a high speed, on cyclone dehumidifier 14, also has a branch pipe(tube), through throttle expansion valve 5 and flow control valve 4 and liquid CO
2Feed pipe is connected, the liquid CO of cryogenic high pressure
2Spray into the body clearance of cyclone dehumidifier 14, liquid CO through this branch pipe(tube) at a high speed in vaporific mode
2Gasification descends the mixed airflow temperature rapidly, steam in the mixed airflow just condenses into drop, around cyclone dehumidifier dry wind blast pipe 10 rotation at a high speed, the water droplet in the air-flow is separated and conrotatory wind dehumidifier 14 inwalls flow down, and accumulates in the gully 19 of bottom with air-flow.Dry wind is discharged in cyclone dehumidifier dry wind aiutage 10, is guided to cold wind canister incoming gas nozzle 12 by low-temperature mixed tracheae 9, in the bottom of cold wind canister incoming gas nozzle 12 a liquid CO is arranged
2Atomizing 16, liquid CO
2From liquid CO
2Feed pipe 3 is behind flow control valve 4, throttle expansion valve 5, mix with dry air in the cold wind canister incoming gas nozzle 12 and temperature is further reduced, enter in the cold wind jar 7 and store, its outside has heat-insulation layer 2 to prevent that cold scatters and disappears, and is provided with cold wind air supply pipe 8 and drainpipe 6 above cold wind jar 7.
Shown in the figure, at the liquid CO of the steel of φ 400 high 800mm
2The outside of storage tank 1 is wrapped in the thick polyamine fat vacuole foam heat-insulation layer 2 of 50mm, can preserve liquid CO
2150kg, CO
2Storage safety valve 18 controls jar interior CO
2State is: temperature-20 ℃, and pressure is 2.0MPa, top also has a CO
2Balance pipe 17 imports jar internal cause heat into and the CO that gasifies
2Being discharged into pressure is 0.5MPa, temperature is in 30 ℃ the compressed air hose, two strands of gases mix the back temperature and can descend to some extent, mist by mixed at room temperature flue 11 in dehumidifier nozzle of air supply 13 tangentially sprays into slit between cyclone dehumidifier 14 urceolus and the cyclone dehumidifier dry wind aiutage 10 at a high speed, at the opposite side of slit, liquid CO
2Through liquid CO
2Be vaporific high speed behind feed pipe 3, flow control valve 4, the throttle expansion valve 5 and spray into, low temperature CO
2Liquid mist and mixed at room temperature air-flow further mix, gas flow temperature is dropped to about 2 ℃, the oversaturated steam water droplet that just congeals into, be separated, converge in along cyclone dehumidifier 14 inwalls in the gully 19 of its underpart, 2 ℃ mist is discharged to the low-temperature mixed tracheae 9 from blast pipe, and quickens through cold wind canister incoming gas nozzle 12.Simultaneously, from liquid CO
2One CO of injection in the pipe
2Liquid mixes at cold wind canister incoming gas nozzle 12 and low-temperature mixed gas once more with vaporific behind flow control valve, and gas flow temperature further drops to about-30 ℃, is stored in then in the cold wind jar 7.Cold wind jar diameter is 1000mm, and high 1500mm can preserve 0.25MPa ,-30 ℃ mist 3.7m
3
Claims (3)
1, a kind of mixed liquid CO
2Cold wind generator is by liquid CO
2Storage tank, cyclone dehumidifier, cold wind jar, dehumidifier nozzle of air supply, cold wind canister incoming gas nozzle, flow control valve, choke valve and corresponding liquid CO
2Connecting tube, gas connecting tube are formed, and it is characterized in that: liquid CO
2After throttling, be vaporific spraying in the compressed air stream and form low-temperature mixed gas.
2, mixed liquid CO as claimed in claim 1
2Cold wind generator, it is characterized in that: cyclone dehumidifier by the dehumidifier shell and with it with one heart and place the gaseous mixture dry wind aiutage in the shell to form, form annular channel between the two, mixed at room temperature gas tangentially flows into from the dehumidifier nozzle of air supply of annular channel, and liquid CO is housed on annular channel
2Atomizer, CO
2The emission direction of liquid mist is identical with the rotation direction of mixed at room temperature air-flow, and isolated water droplet accumulates in the bottom of dehumidifier.
3, mixed liquid CO as claimed in claim 1
2Cold wind generator is characterized in that: on the low-temperature mixed feed channel before the cold wind canister incoming gas nozzle liquid CO is housed
2Ejecting port is through the liquid CO of expenditure and pressure
2Enter behind the ejecting port immediately by from the swiftly flowing low-temperature mixed aerosolization of low-temperature mixed tracheae, and enter the cold wind jar from this nozzle end outlet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 01133718 CN1228587C (en) | 2001-12-19 | 2001-12-19 | Mixed liquid CO2 cold wind generator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 01133718 CN1228587C (en) | 2001-12-19 | 2001-12-19 | Mixed liquid CO2 cold wind generator |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1370958A CN1370958A (en) | 2002-09-25 |
CN1228587C true CN1228587C (en) | 2005-11-23 |
Family
ID=4672050
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 01133718 Expired - Fee Related CN1228587C (en) | 2001-12-19 | 2001-12-19 | Mixed liquid CO2 cold wind generator |
Country Status (1)
Country | Link |
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CN (1) | CN1228587C (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101275188B (en) * | 2003-02-28 | 2010-12-01 | 大阳日酸株式会社 | Molten metal treating agent, method for treating molten metal, and apparatus and method for feeding cover gas to molten metal |
CN102155832B (en) * | 2011-02-28 | 2012-10-31 | 华南理工大学 | Chemical and phase-transition compound cooling device and method |
CN102268368A (en) * | 2011-06-15 | 2011-12-07 | 童师颖 | System for charging CO2 through alga culture pond microporous pipe and monitoring charging amount |
CN104275625A (en) * | 2014-09-11 | 2015-01-14 | 东莞市欧立纬机械科技有限公司 | Ultra-low-temperature drying air cooler |
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 |
-
2001
- 2001-12-19 CN CN 01133718 patent/CN1228587C/en not_active Expired - Fee Related
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Publication number | Publication date |
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CN1370958A (en) | 2002-09-25 |
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