CN2638830Y - High-efficient gas-liquid separator with cooling - Google Patents
High-efficient gas-liquid separator with cooling Download PDFInfo
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- CN2638830Y CN2638830Y CN 03258455 CN03258455U CN2638830Y CN 2638830 Y CN2638830 Y CN 2638830Y CN 03258455 CN03258455 CN 03258455 CN 03258455 U CN03258455 U CN 03258455U CN 2638830 Y CN2638830 Y CN 2638830Y
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Abstract
The utility model belongs to a highly efficient gas-liquid separation device used for the gas-liquid separation in the cooling system. The separation device consists of five parts:(1) an impact and condensation chamber which also functions as a middle cooling chamber close to the air inlet;(2) a cyclone separating device, the most part of which is positioned in the lower cooling chamber;(3) an upper cooling chamber;(4) a core tube separation chamber close to the air outlet;(5) a casing, a bracket and a liquid discharge pipe. The device has the advantages of high separation efficiency, more than 99 percent gas-liquid separation efficiency and energy conservation, applicable to the bioengineering units such as the pharmaceutical factory, gourmet powder factory and enzyme product factory or other factories needing to cool the compressed air and separate the gas and liquid such as the chemical plant.
Description
Technical field
The utility model belongs to a kind of gas-liquid separation equipment, is specifically related to a kind of high efficiency air liquid separation device with cooling.
Background technology
Often use a large amount of compressed air in bioengineering unit such as pharmaceutical factory, Gourmet Powder Factory, enzyme preparation factory, Citric Acid Plant and chemical plant etc., through the gases at high pressure temperature behind the air compressor machine usually more than 150 ℃, need to be transported to the workshop again after the cooling, profit in the gases at high pressure of cooling back condenses, and is vaporific more and is carried secretly by air-flow.The processing of will anhydrating through deoiling of such compressed air.Need degerming to handle bioengineering unit toward contact.To entering the used compressed air in biofermentation workshop, cooling is gone forward side by side and is heated up after promoting the circulation of qi liquid separates again, and anhydrous to guarantee the compressed air that enters in the efficient gas sterilizing filter, the droplet that oil condenses reappears.Obviously, carry out these processing and usually spend great amount of manpower, material resources.The ratio that huge operating cost accounts for production cost is very big, therefore improves compressed-air actuated processing method, and it is necessary reducing processing cost.Though up to the present develop some efficient than higher equipment, handle compressed-air actuated cost and also descend to some extent, its cooling of the structure of existing equipment and cyclonic separation be separate, temperature is balance, so efficient is not high enough.Also exist as area of dissipation greatly inadequately in addition, the liquid problems such as design is not good enough that reflux are so it still restricts one of factor of production cost.
Summary of the invention
The object of the present invention is to provide a kind ofly in cooled compressed air, near cooling surface, carry out the device of the saving energy of gas-liquid separation, promptly be provided at the energy-efficient equipment that carries out gas-liquid separation in the cooling system.
Technical scheme of the present invention is as follows: the gas-liquid separation device of band cooling, form by five parts: and the collision condensation gravity separator of (1) contiguous air inlet pipe, it also is middle cooling chamber simultaneously; (2) sub-parallel connection of a plurality of whirlwind or single tube cyclone separator, wherein the middle part cylinder is in following cooling chamber, and the outside of bottom cone is an atmosphere, and the major part of tangential rectangular air inlet and core pipe is in the middle cooling chamber; (3) go up cooling chamber; (4) be close to the core pipe separation chamber of air inlet pipe; (5) housing, fluid drainage pipe and support etc.
Cooling system is by last cooling chamber, and middle cooling chamber and following cooling chamber are formed.Last cooling chamber is less, and the sub-core pipe of whirlwind is only arranged, and helps the gas-liquid separation in the core pipe separation chamber of contiguous escape pipe by the cooling to the core pipe.With following cooling chamber, middle cooling chamber is compared, and the cooling water water temperature in the last cooling chamber is the highest, and the cooling water after the heat exchange is discharged from cooling water outlet pipe.In install in the cooling chamber many vertical, interior cold cooling tube, sub-gas tangential entry of whirlwind and core pipe major part all are within this cooling chamber, also in this chamber, it also is a collision condensation gravity separator to the device air inlet pipe.At following cooling chamber, the sub-top of whirlwind cylindrical shell is a water cooling, and the sub-lower taper pipe of whirlwind is cooled off by naturally.Compare with last cooling chamber, middle cooling chamber, the cooling water temperature in descending cooling chamber is minimum, and cooling water is to enter cooler from the cooling water inlet pipe that descends the cooling chamber bottom.
Gas-liquid separation chamber also has three: collision condensation gravity separator, sub-separation chamber of whirlwind and core pipe separation chamber.Collision condensation gravity separator also is middle cooling chamber simultaneously, and the pipeline of compressed air collision is exactly the cooling tube in the middle cooling chamber.Under the gravity effect, collision forms the bottom that bigger drop sinks to middle cooling chamber, by excretory duct the liquid of separating is drained.The core pipe has been installed slanting baffle and has been stoped cooling water to enter the tangential rectangular air inlet of whirlwind, and the sub-separation chamber of whirlwind is formed in parallel by a plurality of whirlwind, and its number depends on compressed air metered flow and the sub ability of handling air quantity of each whirlwind that device need be handled.The tubular plate washer of one mouth down is installed on the core pipe in the sub-stage casing of whirlwind, and compressed air can only pass through from the space between stage casing round tube inner wall and the plate washer.Core pipe upper end is core pipe separation chamber, and upper end, core pipe separation chamber is an orifice plate, and the upper end of the sub-core pipe of whirlwind and the upper end of cooling tube are separately fixed on the upper perforated plate, and the lower end of cooling tube is fixed on the lower perforated plate, and the hole on the orifice plate is corresponding with the core pipe, and on same axis.Bore dia on the orifice plate is slightly smaller than the diameter of core pipe.
The shell of device is a cooler casing, also is separator shell.The compressed air that Purge gas is compiled in the chamber separates through three times.The height that compiles the chamber is greater than three times of core pipe diameter, so that gas flow smooth.The liquid that whirlwind is separated is pooled in the liquid collection chamber, is drained by excretory duct.Keep certain liquid level in the liquid collection chamber, avoid the interference that whirlwind is separated.Support is born the weight of whole device, and for keeping its stability, support should have certain gradient, for example with horizontal plane angle about 80 °.
When not needing to cool off, can be only with a sub-separator tube of whirlwind.Cyclone tube divides two parts up and down, and is upper coarse and lower fine.The device air inlet pipe also is to go up the cyclonic separation air inlet pipe, and tangent with the tornadotron cylinder, and the liquid of being separated by centrifugal force sinks to the extra heavy pipe bottom, is discharged to the device outside from excretory duct.After a gas-liquid separation, air-flow enters guide vane, has strengthened rotation, flows to the bottom.Flow downward through the crack between tubular baffle plate and the cylinder, the liquid of being thrown to cylinder inner wall by centrifugal force moves downward under the gravity effect, be discharged to the device outside by excretory duct, and the turning of the air-flow after separating rotates up along the core pipe mobile.Escape pipe and core pipe have common central axis, and the escape pipe external diameter is slightly littler than core bore.Distance is less between escape pipe lower end and core pipe upper end.Excretory duct is discharged the liquid of dishing out outside the gap, the compressed air that flows out from escape pipe has passed through three gas-liquid separations like this.
Description of drawings
Fig. 1 band cooling high efficiency air liquid separation device structural representation;
Fig. 2 cools off or sprays the high efficiency air liquid separation device structural representation of cooling water naturally;
Fig. 3 cools off the high efficiency air liquid separation device structural representation of single tube cyclone separator series connection naturally.
Wherein:
The sub-core pipe of 1 escape pipe, 2 shells, 3 whirlwind
Cooling chamber (contiguous air inlet pipe separation chamber) in the cooling chamber 5 on 4
6 cooling water outlet pipes, 7 air inlet pipe, 8 slanting baffles
11 times cooling chambers of 9 air inlets, 10 cooling tubes
15 liquid collection chambers, 16 fluid drainage pipes, 17 cooling water inlet pipes
18 fluid drainage pipes, 19 core pipe separation chambers (going up the separation chamber)
20 fluid drainage pipes, 21 orifice plates, 22 gases compile the chamber
23 lower shoes, 24 guide vanes, 25 supports
26 upper perforated plates, 27 lower perforated plates
The specific embodiment
As shown in Figure 1, this device is by three cooling chambers in upper, middle and lower 4,5,11 and 5 (middle separation chambers), contiguous air inlet pipe separation chamber, and sub-separation chamber 11 of whirlwind (following separation chamber) and core pipe separation chamber 19 three separation chambers such as (going up the separation chamber) constitute.The sub-separation chamber of whirlwind (following separation chamber) is formed in parallel by a plurality of whirlwind.Whirlwind subnumber order is by device and the sub-metered flow decision of whirlwind.Recommend the sub-size of whirlwind as follows: whirlwind middle part cylinder 12 diameter D=200mm, core pipe 3 diameter d=100mm, tangential rectangular air inlet area is 50 * 100 (mm
2), cylindrical shell height (not comprising the core pipe) is 1200mm, about 10 meters of the sub-metered flow of such whirlwind (under standard state)
3/ minute.Require to determine used this whirlwind subnumber order according to the gas-liquid separation device metered flow.
The device the top is an escape pipe 1, and it is received on the crust of the device 2, and shell around the escape pipe 1 and last separation chamber orifice plate 21 are formed discharge gas and compiled chamber 22, is core pipe separation chamber (going up the separation chamber) 19 between orifice plate 21 and the last cooling chamber 4.The upper end of the sub-core pipe 3 of each whirlwind is all in last separation chamber 19, the upper end of the sub-core pipe 3 of whirlwind and the upper end of cooling tube 10 are separately fixed on the upper perforated plate 26, the lower end of cooling tube (10) is fixed on the lower perforated plate 27, hole on the orifice plate 21 and core pipe 3 correspondences, and they are on same axis.Bore dia on the orifice plate 21 is slightly less than the external diameter of core pipe 3.The gas-liquid separation of last separation chamber 19 just occurs among the gap of hole on the orifice plate 21 and core pipe 3 upper ends, and under centrifugal action, the liquid that is separated is discharged to the device outside by last separation chamber 19 bottom excretory ducts 20.Be to go up cooling chamber 4 below the last separation chamber 19, fully carried out the cooling water of heat exchange and discharged from the upper end drainpipe 6 of last cooling chamber 4.
Being middle cooling chamber 5 below the last cooling chamber 4, also is middle separation chamber simultaneously, at middle cooling chamber the cooling tube 10 of many vertical placements is installed, and it is interior cooling.Middle cooling chamber 5 links to each other with device air inlet pipe 7, and the separation of middle cooling chamber 5 mainly occurs in the outside of cooling tube 10, also occurs in the outer surface of core pipe 3 simultaneously.Because steam collision cold surface in the air-flow, steam condenses into droplet.Collision between droplet also can form big drop, and under the gravity effect, drop drops on the bottom surface of middle separation chamber 5.The liquid of separating the therefrom excretory duct 18 of 5 belows, separation chamber is discharged to outside the device.In the middle cooling chamber 5 the sub-cylinder 12 of whirlwind is housed also, tangential rectangular air inlet 9 is housed on the top of the sub-cylinder 12 of whirlwind.Among falling into the tangential rectangular air inlet 9 of whirlwind for fear of the drop of collision condensation, near the excircle of the core pipe 3 above the air inlet 9, a sloping baffle 8 is installed.
In the cooling chamber 5, in the cooling chamber 11, the bottom of the sub-cylinder 12 of whirlwind was that conical pipe 13 is nature coolings under the sub-cylinder 12 of whirlwind was in during whirlwind of series connection, top air inlet were in, and cooling water inlet pipe 17 is arranged at following cooling chamber 11 bottoms, supplies with cooling water to cooler.
Make thin and grow in order to increase area of dissipation whirlwind.If the diameter of whirlwind middle part cylinder 12 is D, core pipe diameter d ≈ D/2, the length that core pipe 3 is inserted in the cylindrical shell is (1.25-1.5) D, and whirlwind middle part cylinder 12 length are not less than 1.25D (beginning to calculate from tangential rectangular air inlet bottom), and the height of lower cone 13 is (2.9-3.3) D.The sectional area of the sectional area ratio core pipe 3 of the tangential rectangular air inlet 9 of whirlwind is smaller slightly, length-width ratio 2: 1.The sub-air inlet rotating part of whirlwind is a scroll casing shape, and its equivalent diameter is bigger than D, be approximately D (1.3-1.5) doubly.
In order to increase the collision probability of steam in the Compressed Gas or water droplet and whirlwind middle part cylinder 12 inwalls, device one tubular plate washer 14 below tangential rectangular air inlet 9, it and core pipe are coaxial, and are connected on the core pipe.Have voltage supply to contract between tubular plate washer 14 and cylinder 12 inwalls gap that gas passes through.The sectional area of interval area smaller and tangential rectangular air inlet 9 than the sectional area of core pipe 3 is close.Tubular plate washer 14 smooth surfaces are to reduce air drag.
The whirlwind sub-component has common liquid collection chamber 15, is excretory duct 16 below the collecting chamber 15, and the liquid that it separates whirlwind is discharged to the device outside.Liquid collection chamber 15 should have bigger volume, and is close to guarantee the flow regime between whirlwind, and the mixed flow phenomenon does not take place.Appliance stand 25 will be outward-dipping and about 80 ° of horizontal plane angle, with the stability of assurance device.
As shown in Figure 2, this device is simpler than embodiment 1 device, has cancelled last cooling chamber 4 and following cooling chamber 11, and cooling chamber 5 in the reservation.Device if natural cooling heat dissipation amount is not enough, can strengthen heat dissipation capacity mainly to the atmosphere heat radiation from top sprinkling cooling water.Spray line does not draw in the drawings.In order to adapt to the needs that spray cooling water, below whirlwind, add the lower shoe 23 of a short cylinder shape, appliance stand 25 is arranged below it, bear the effect of supportive device weight.Short cylinder above the lower shoe 23 is in order to collect the cooling water of sprinkling.The cooling water of collecting can be discharged by an aperture (not drawing among the figure) of lower shoe 23.Same reason, orifice plate 21 outer rims have also been installed the short cylinder that makes progress.
Because this device mainly is the nature cooling, not only the claimed apparatus area of dissipation is big, and claimed apparatus external ventilation condition is good.
As shown in Figure 3, if cooler has been installed, and reached the cooling requirement before separator, at this moment needn't consider to increase the film-cooled heat problem especially, the mode of connecting with two single tube cyclone separators also can reach the high efficient gas and liquid separation requirement.
Remove outside the single tube, two main distinctions of this separator and front are not have cooling tube 10 in middle separation chamber 5, do not utilize the collision condensation separation, and utilize cyclonic separation.Compressed air after the first separation enters second level cyclonic separation again.The first order and the second level are in series.Cyclone tube is upper coarse and lower fine.Device air inlet pipe 7 also is to go up the cyclonic separation air inlet pipe, and tangent with the top of the sub-cylinder 12 of whirlwind, and the liquid of being separated by centrifugal force sinks to the extra heavy pipe bottom, discharges from excretory duct 18.Second level cyclonic separation inlet is equipped with guide vane 24, flow to the edge with middle cylindrical section 12 and core pipe 3 coaxial tubular baffle plate 14 forced draft, the liquid pearl is dirty along the inwall of cylinder 12, and air-flow turns to 180 ° to move upward by core pipe 3 rotation, has finished secondary separation.Last separation chamber 19 (being core pipe separation chamber) is made up of escape pipe 1, shell 2 and core pipe 3 upper ends.Escape pipe 1 and core pipe 3 have common central axis, and escape pipe 1 external diameter is slightly littler than core pipe 3 internal diameters.Escape pipe 1 lower end and core pipe 3 upper end spacings are less.Excretory duct 20 can be discharged the liquid of throwing outside the gap, the compressed air that flows out from escape pipe 1 has passed through three gas-liquid separations like this.Wherein the inclination angle of guide vane is 25-30 °.
The lower shoe 23 of short cylinder shape has been installed in single tube cyclone separator bottom, appliance stand 25 is arranged below it, and the short cylinders above the lower shoe 23 are in order to collect the cooling water of sprinkling.About 80 ° of the outward-dipping and horizontal plane angle of appliance stand 25.
This device has stronger adaptability, even when flow has bigger variation, the flow field is still stable, and the fluid that can not take place between the separation chamber disturbs.When environment temperature is too high, also can spray cooling water, be beneficial to condensing of steam, reduce the content of steam.
The course of work of this gas-liquid separation device is as follows:
As shown in Figure 1, during the work of band cooling high efficiency air liquid separation device, contain liquid compression air cooling chamber 5 from air inlet pipe 7 enters, when cooling tube 10 outer walls in steam in the air-flow and the middle cooling chamber 5 or the sub-outer wall of whirlwind (outer wall that comprises core pipe 3) collision, because the temperature low (near cooling water temperature) of cooling tube 10 outer walls, steam condenses into the globule, and collision forms large water drop between the droplet, 5 bottoms, separation chamber are discharged to outside the device through excretory duct 18 in the gravity effect sinks to.Slanting baffle 8 on the core pipe 3 stops the globule that sinks to fall into the tangential rectangular air inlet 9 of whirlwind.Through the compressed air after the dehydration for the first time, enter whirlwind from the tangential rectangular air inlet 9 of each whirlwind, rotation moves downward, centrifugal force is thrown to sub-cylinder 12 inwalls of whirlwind the globule in the air-flow outward, coaxial therewith tubular baffle plate 14 forced draft of installing at the sub-core pipe 3 of whirlwind flow to cylinder 12 inwalls, the collision probability of particulate and cylinder 12 inwalls in the increase gas, because cylinder 12 is cooling tubes of following cooling chamber 11, temperature is low on cylinder 12 walls, and the steam in the compressed air is condensed.Still rotate downwards by the inwall of cylinder 12 and the compressed air in the space between the tubular baffle plate 14, compressed air turns to 180 °, flows to along core pipe 3 and goes up separation chamber 19.And sink in the sub-liquid collection chamber 15 of whirlwind in the gravity effect at the moisture that cylinder inner wall condenses, by excretory duct 16 with liquid discharge device.Move upward along 3 rotations of core pipe through the compressed air after the twice dehydration, cooling chamber 5 in the process, last cooling chamber 4 coolings, remaining steam of compressed air or mist, condensation mist formation pearl on the inwall of core pipe 3 is compressed air and is entrained in the separation chamber (core pipe separation chamber) 19.Abacuses 21 above the last separation chamber 19, the hole on the orifice plate 21 are corresponding with the sub-core pipe of whirlwind 3 respectively.And coaxial, fine pitch is arranged between the two.Because through slightly littler than the internal diameter of core pipe 3, the globule is thrown outside the hole, sinks under the gravity effect outside the hole on the orifice plate 21, liquid is discharged to outside the device through excretory duct 21.Finished and separated the back air-flows for three times and collect gas and compile chamber 22, flowed to the place that needs by escape pipe 1.With after three times are separated, 99% liquid mist in the compressed air is separated through three condensations.Because gas is cooled in flow process, separated, separate occurring in the temperature lower, gas temperature does not reach balance and front and passes through the compressed air of triple dewatering and converge in gas collection chamber 22 in device.Temperature reaches balance substantially, and the temperature after the balance is higher than temperature on the cooling surface.Liquid must be higher than saturated vapor pressure on the low cooling surface of temperature at the saturated vapor pressure after the balance.If the compressed air delivery after the flow separation to filter, as long as filter outlet temperature and gas-flow separation unit outlet air temperature are more or less the same, needn't add heat riser between filter and gas-flow separation unit, condenses can not take place yet in filter.
If cooling medium is not water two but atmosphere, the device that equipment therefor such as embodiment 2 are introduced, cooler has been simplified.The course of work and the embodiment 1 of device do not have much difference.Cooling surface temperature height only, cooling effect is weaker.Winter environment temperature low, naturally the cooling also can reach requirement.If the environment temperature height does not reach requirement, can spray cooling water, reduce the cooling surface temperature, it is quite beneficial that steam in the compressed air is condensed.
Finish as cooling off before the gas-liquid separation device, used gas-liquid separation device as shown in Figure 3, the mode of gas-liquid compressed air separation chamber from air inlet pipe 7 enters is a tangential admission, and air-flow enters cyclone separator through square tangential admission mouth 7, and rotation moves downward.The globule in the air-flow is thrown outside under centrifugal action, and the liquid that excretory duct 18 will be thrown sinking outward is discharged to outside the device.Compressed air through last cyclone separator first separation enters down cyclone separator by guide vane 24, the air-flow rotation downwards, under the effect of tubular baffle plate 14, air flow direction cylinder 12 inwalls, thrown the drop and the inwall collision of outside by centrifugal force, change from small to big, sink to lower cone 13, the liquid of separating is discharged by excretory duct 16.Rotatablely move to flow to along core pipe 3 through the air-flow of twice dehydration and go up separation chamber 19.Device escape pipe 1 is also in last separation chamber 19, and escape pipe 1 and core pipe 3 are coaxial and an intersegmental crack is arranged, and escape pipe 1 diameter is slightly less than core pipe 3 internal diameters.A part of liquid pearl of still carrying secretly after the secondary separation or fog are thrown to core pipe 3 and escape pipe 1 outside in this gap, so compressed air separates for the third time, be compressed air through three grades of dehydrations from escape pipe 1 effluent air.
This device separative efficiency height, gas-liquid separation efficient reaches more than 99%, saves energy, can be used on pharmaceutical factory, Gourmet Powder Factory, enzyme preparation factory, bioengineering units such as Citric Acid Plant, also can be used on chemical plant etc. need cool off factory with gas-liquid separation to compressed air.
Claims (10)
1, a kind of high efficiency air liquid separation device with cooling, comprise shell (2) and be installed in the escape pipe (1) at shell (2) top, be installed in the air inlet pipe (7) of shell (2) upper side and be installed in the support (25) of shell (2) bottom, it is characterized in that: the sub-core pipes of a plurality of whirlwind (3) and a plurality of cooling tube (10) are installed in the inside of shell (2), the upper end of the upper end of the sub-core pipe of whirlwind (3) and cooling tube (10) is separately fixed on the upper perforated plate (26), the lower end of cooling tube (10) is fixed on the lower perforated plate (27), the lower device of the sub-core pipe of whirlwind (3) has and prevents that condensed water from falling into the slanting baffle (8) and the tubular baffle plate (14) of the sub-cylinder of whirlwind (12), pack into the inside, upper end of the sub-cylinder of whirlwind (12), the lower end of the sub-core pipe of whirlwind (3); The orifice plate (21) of porous is installed in the bottom that gas compiles chamber (22), the top of the installation site of air inlet pipe (7) and shell (2) is tangent, a side device has fluid drainage pipe (20) in the bottom of core pipe separation chamber (19), fluid drainage pipe (18) is arranged, at the bottom one side device that descends cooling chamber (11) cooling water inlet pipe (17) is arranged at the bottom of middle cooling chamber (a 5) side device.
2, a kind of high efficiency air liquid separation device with cooling according to claim 1 is characterized in that: the bottom of the sub-cylinder of whirlwind (12) is conical pipe (13), is provided with liquid header (15) in the bottom of conical pipe (13).
3, a kind of high efficiency air liquid separation device with cooling according to claim 1, it is characterized in that: the diameter in the hole on the orifice plate (21) is less than the diameter of the sub-core pipe of whirlwind (3).
4, a kind of high efficiency air liquid separation device with cooling according to claim 2 is characterized in that: be provided with fluid drainage pipe (16) in the bottom of liquid header (15).
5, the high efficiency air liquid separation device of a kind of single tube of cooling naturally cyclone separator series connection, comprise shell (2) and be installed in shell (2) top escape pipe (1), be installed in the air inlet pipe (7) of shell (2) top one side, it is characterized in that: a sub-core pipe of whirlwind (3) is installed in the inside at shell (2), device has guide vane (24) in the outside, middle part of the sub-core pipe of whirlwind (3), lower device at the sub-core pipe of whirlwind (3) has tubular baffle plate (14), pack into the inside of the sub-cylinder of whirlwind (12), the lower end of the sub-core pipe of whirlwind (3).
6, the high efficiency air liquid separation device of a kind of single tube of cooling naturally cyclone separator according to claim 5 series connection, it is characterized in that: the diameter of escape pipe (1) is less than the diameter of the sub-core pipe of whirlwind (3).
7, the high efficiency air liquid separation device of a kind of single tube of cooling naturally cyclone separator according to claim 5 series connection, it is characterized in that: the top of the installation site of air inlet pipe (7) and the sub-cylinder of whirlwind (12) is tangent.
8, the high efficiency air liquid separation device of a kind of single tube of cooling naturally cyclone separator according to claim 5 series connection, it is characterized in that: the inclination angle of guide vane (24) is 25-30 °.
9, the high efficiency air liquid separation device of a kind of single tube of cooling naturally cyclone separator according to claim 5 series connection, it is characterized in that: the bottom of the sub-cylinder of whirlwind (12) is conical pipe (13), is provided with columnar lower shoe (23) in the below of conical pipe (13).
10, the high efficiency air liquid separation device of a kind of single tube of cooling naturally cyclone separator according to claim 5 series connection, it is characterized in that: the lower device in core pipe separation chamber (19) has fluid drainage pipe (20), fluid drainage pipe (18) is arranged, at the following end device of lower shoe (23) fluid drainage pipe (16) is arranged at the top of the sub-cylinder of whirlwind (12) bottom surface device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03258455 CN2638830Y (en) | 2003-09-18 | 2003-09-18 | High-efficient gas-liquid separator with cooling |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03258455 CN2638830Y (en) | 2003-09-18 | 2003-09-18 | High-efficient gas-liquid separator with cooling |
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| CN2638830Y true CN2638830Y (en) | 2004-09-08 |
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ID=34295818
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| Application Number | Title | Priority Date | Filing Date |
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| CN 03258455 Expired - Fee Related CN2638830Y (en) | 2003-09-18 | 2003-09-18 | High-efficient gas-liquid separator with cooling |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101298004B (en) * | 2008-01-18 | 2010-06-02 | 杨解定 | Vapor-liquid separator |
| CN101822924A (en) * | 2010-05-11 | 2010-09-08 | 南京航空航天大学 | Centrifugal gas-liquid separator |
| CN112286242A (en) * | 2019-07-25 | 2021-01-29 | 北京康斯特仪表科技股份有限公司 | Gas pressure control device |
-
2003
- 2003-09-18 CN CN 03258455 patent/CN2638830Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101298004B (en) * | 2008-01-18 | 2010-06-02 | 杨解定 | Vapor-liquid separator |
| CN101822924A (en) * | 2010-05-11 | 2010-09-08 | 南京航空航天大学 | Centrifugal gas-liquid separator |
| CN101822924B (en) * | 2010-05-11 | 2012-05-16 | 南京航空航天大学 | Centrifugal gas-liquid separator |
| CN112286242A (en) * | 2019-07-25 | 2021-01-29 | 北京康斯特仪表科技股份有限公司 | Gas pressure control device |
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