CN105107274A - Cyclone air-liquid separator matched with freezing dryer during use - Google Patents
Cyclone air-liquid separator matched with freezing dryer during use Download PDFInfo
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- CN105107274A CN105107274A CN201510595984.7A CN201510595984A CN105107274A CN 105107274 A CN105107274 A CN 105107274A CN 201510595984 A CN201510595984 A CN 201510595984A CN 105107274 A CN105107274 A CN 105107274A
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- liquid separator
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- type drier
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Abstract
The invention discloses a cyclone air-liquid separator matched with a freezing dryer during use. The cyclone air-liquid separator comprises a column, an upper shell cover and a lower shell cover. The separator is vertically installed during use. The separator is characterized by further comprising an air outlet pipe, an air-liquid inflow pipe, a water outlet pipe, an air guide pipe, a cyclone blade and an annular closure plate. The air-liquid inflow pipe is arranged at the upper portion of the annular side wall of the column. The air outlet pipe is inserted in the top of the upper shell cover. The annular closure plate is horizontally arranged on the top of the column. The upper end of the air guide pipe is connected with the annular closure plate, and the lower end of the air guide pipe is located inside the column. The cyclone blade is in a flake shape, is spirally wound and is fixed to the periphery of the air guide pipe. The water outlet pipe penetrates through the lower shell cover, and the lower end of the water outlet pipe is located below the lower shell cover. The cyclone air-liquid separator is small in size, can be well compatible with the freezing dryer and has a better air-liquid separation effect, thereby guaranteeing the quality of compressed air of the freezing dryer.
Description
Technical field
The present invention relates to a kind of gas-liquid separator, be specifically related to a kind of gas-liquid separator for freezing type drier.
Background technology
Compressed air in freezing type drier needs just to enter Cemented filling through refrigerated separation and uses, but because of just cooling compressed air with need long-distance transportation through pipeline, in this process, it is inevitable that generation machinery carries condensed water.And equipment is when using compressed air, need dry compressed air.Therefore, need to use gas-liquid separator gas and fluid separation applications to be come.
In gas-liquid separator, gas-liquid gravity separator is the most common, and its principle is the difference utilizing liquid sedimentation speed and the gas rate of climb, and liquid discharge outlet sedimentation is from below flowed out, and gas is discharged from the exhaust outlet of top, realizes gas-liquid separation.This separate mode simple and fast, but the effect of gas-liquid separation is not ideal, still containing large quantity of moisture in isolated gas.In addition, it is comparatively large that common gas-liquid separator takies volume, cannot be compatible well with freezing type drier.Therefore, need to improve existing gas-liquid separator, make it to be installed on freezing type drier, the effect of gas-liquid separation can be strengthened again.
Summary of the invention
The object of the invention is the problems referred to above existed to solve prior art, providing a kind of freezing type drier supporting vortex gas-liquid separator, being intended to make gas-liquid separator be applicable to freezing type drier, and strengthening the effect of gas-liquid separation.
Technical solution of the present invention is: the supporting vortex gas-liquid separator of freezing type drier, comprise cylinder, upper cover and low head, in use procedure, separator is vertically installed, upper cover and low head are installed on the two ends up and down of cylinder respectively, separately also comprise escape pipe, gas-liquid flow inlet pipe, outlet pipe, gas channeling pipe, cyclone blade and ring sealing plate, described gas-liquid flow inlet pipe is located at the top of cylinder annular sidewall, described escape pipe assigns into the top of upper cover, described cylinder top level is to being provided with ring sealing plate, this ring sealing plate center has circular hole, ring sealing plate is made to be enclosed within the periphery of described gas channeling pipe upper end and to be fixedly connected with gas channeling pipe via this circular hole, the lower end of gas channeling pipe is positioned at column body, and and between low head, leave an intersegmental gap, described cyclone blade in the form of sheets, spiral around and be fixed on described gas channeling pipe periphery, described outlet pipe runs through low head, and its lower end is in outside low head, and upper one end is fixedly connected with low head.
Further, the supporting vortex gas-liquid separator of above-mentioned freezing type drier, wherein: described low head and cylinder connecting portion level are to being provided with a baffle plate, and this baffle plate is fixed on the inwall of low head, is provided with delivery port above baffle plate.
Further, the supporting vortex gas-liquid separator of above-mentioned freezing type drier, wherein: described baffle plate is dull and stereotyped, or the cambered plate that middle part raises up.
Further, the supporting vortex gas-liquid separator of above-mentioned freezing type drier, wherein: the peak of described baffle plate and the distance of gas channeling pipe lower end account for 1/10 ~ 1/2 of height of column.
A more step ground, the supporting vortex gas-liquid separator of above-mentioned freezing type drier, wherein: the delivery port above described baffle plate, is arranged on outside the upright projection scope of gas channeling pipe on baffle plate.
Further, the supporting vortex gas-liquid separator of above-mentioned freezing type drier, wherein: the delivery port above described baffle plate has 2 ~ 10, is evenly arranged on baffle plate periphery, delivery port semicircular in shape or class semicircle.
Further, the supporting vortex gas-liquid separator of above-mentioned freezing type drier, wherein: described cyclone blade is coiled into 1 ~ 6 circle in the periphery of gas channeling pipe.
Again further, the supporting vortex gas-liquid separator of above-mentioned freezing type drier, wherein: described gas-liquid flow inlet pipe is arranged on the top one be coiled in gas channeling pipe periphery with cyclone blade and encloses corresponding position
Technique effect of the present invention is embodied in: the supporting vortex gas-liquid separator of freezing type drier of the present invention, its gas channeling pipe periphery is wound with cyclone blade, because cyclone blade liquid towards water droplet has good immersional wetting, the water droplet of different-grain diameter with cyclone blade collision rift, understand in the very thin one deck water meeting of cyclone blade Surface Creation and flow down along cyclone blade, the water droplet of larger particle is agglomerated into afterwards at cyclone blade edge, make water droplet under Action of Gravity Field own and air separation, the effect of gas-liquid separation is more outstanding, and the present invention takies small volume, can be compatible well with freezing type drier, thus ensure that the compressed-air actuated quality of freezing type drier, operation for freezing type drier is highly profitable.
Accompanying drawing explanation
Fig. 1 is the overall schematic of the supporting vortex gas-liquid separator of freezing type drier;
Fig. 2 is the schematic internal view of the supporting vortex gas-liquid separator of freezing type drier.
In figure, the implication of each Reference numeral is: 1-cylinder, 2-escape pipe, 3-gas-liquid flow inlet pipe, 4-outlet pipe, 5-cyclone blade, 6-baffle plate, 61-delivery port, 7-upper cover, 8-low head, 9-gas channeling pipe, 10-ring sealing plate.
Detailed description of the invention
Below in conjunction with accompanying drawing, the specific embodiment of the present invention is described in further detail, is easier to make technical solution of the present invention understand and grasp.
As shown in Figures 1 and 2, the supporting vortex gas-liquid separator of freezing type drier of the present invention, comprise cylinder 1, escape pipe 2, upper cover 7, gas-liquid flow inlet pipe 3, gas channeling pipe 9, outlet pipe 4, low head 8 and cyclone blade 5, described upper cover 7 and low head 8 are installed on the two ends up and down of cylinder 1 respectively, described gas-liquid flow inlet pipe 3 is installed on the side face of cylinder 1, described escape pipe 2 runs through upper cover 7, described cylinder 1 top level is to being provided with ring sealing plate 10, this ring sealing plate 10 center has circular hole, ring sealing plate 10 is made to be enclosed within the periphery of described gas channeling pipe 9 upper end and to be fixedly connected with gas channeling pipe 9 via this circular hole, the lower end of gas channeling pipe 9 is positioned at cylinder 1 inside, and and between low head 8, leave an intersegmental gap, described cyclone blade 5 in the form of sheets, spiral around and be fixed on described gas channeling pipe 9 periphery, described outlet pipe 4 runs through low head 8, and its lower end is in outside low head 8, and upper end is fixedly connected with low head 8.
As shown in Figure 2, described low head 8 is with cylinder 1 connecting portion level to being provided with a baffle plate 6, and this baffle plate 6 is fixed on the inwall of low head 8, and baffle plate 6 is provided with delivery port 61 above; Described baffle plate 6 is dull and stereotyped, or the cambered plate that middle part raises up, and is convenient to liquid and discharges.The peak of described baffle plate 6 and the distance of gas channeling pipe 9 lower end account for 1/10 ~ 1/2 of height of column, if the distance of the peak of baffle plate 6 and gas channeling pipe 9 lower end is excessive, then illustrate that gas channeling pipe 9 is too short, more cyclone blade 5 then cannot be installed, gas-liquid separation may be caused abundant not, if and the delivery port 61 above described baffle plate 6, is arranged on outside the upright projection scope of gas channeling pipe 9 on baffle plate 6; The distance going out the peak of baffle plate 6 and gas channeling pipe 9 lower end is too small, then liquid may be caused to flow into gas channeling pipe 9.Delivery port 61 has 2 ~ 10, is evenly arranged on baffle plate 6 periphery, delivery port 61 semicircular in shape or class semicircle.After gas-liquid mixture passes into from gas-liquid flow inlet pipe 3, there is gas-liquid separation, liquid flow on baffle plate 6 through the outer wall of gas diversion tube 9 and cyclone blade 5, because baffle plate 6 middle part raises up, be convenient to guide liquid stream to put the delivery port 61 of baffle plate 6 periphery, and delivery port 61 is arranged on outside the upright projection scope of gas channeling pipe 9 on baffle plate 6, prevents liquid from entering mozzle 9.
Here it should be noted that, although cyclone blade 5 is only provided with two circles in Fig. 2, be only a kind of preferred version; As required, described cyclone blade 5 can be arranged to 1 ~ 6 circle, and described gas-liquid flow inlet pipe is arranged on the top one be coiled in gas channeling pipe periphery with cyclone blade and encloses corresponding position.
The course of work of the present invention is as follows: the gas-liquid of mixing flows to in cylinder 1 from gas-liquid flow inlet pipe 3, the gas-liquid contact of mixing is to gas channeling pipe 9 and cyclone blade 5, because cyclone blade 5 liquid towards water droplet has good immersional wetting, the water droplet of different-grain diameter with cyclone blade 5 collision rift, can flow down along cyclone blade 5 at the very thin one deck water of cyclone blade 5 Surface Creation, and the water droplet of larger particle is agglomerated at cyclone blade 5 edge, water droplet is under Action of Gravity Field own and air separation.Final liquid water stream on the baffle plate 6 of low head 8, and flows to the delivery port 61 of baffle plate 6 periphery, finally flows out from outlet pipe 4; Gas then flows to from the bottom of gas channeling pipe 9, finally flow out from the top of escape pipe 2, in the process, still having part water droplet along with the bottom of gas from gas channeling pipe 9 flows to, because gas channeling pipe 9 is longer, in the process, water droplet can condense in the inside of gas channeling pipe 9, finally drip under gravity and flow to low head 8 inside, finally flowing out from outlet pipe 4.
By describing above and can finding out, the supporting vortex gas-liquid separator of freezing type drier, its gas channeling pipe 9 periphery is wound with cyclone blade 5, because cyclone blade 5 liquid towards water droplet has good immersional wetting, the water droplet of different-grain diameter with cyclone blade 5 collision rift, very thin one deck water can be generated on cyclone blade 5 surface and flow down along cyclone blade 5, the water droplet of larger particle is agglomerated into afterwards at cyclone blade 5 edge, make water droplet under Action of Gravity Field own and air separation, thus the effect of gas-liquid separation is more outstanding, and the present invention takies small volume, can be compatible well with freezing type drier, thus ensure that the compressed-air actuated quality of freezing type drier, operation for freezing type drier is highly profitable.
Certainly, be more than representative instance of the present invention, in addition, the present invention can also have other multiple detailed description of the invention, and all employings are equal to the technical scheme of replacement or equivalent transformation formation, all drop within the scope of protection of present invention.
Claims (8)
1. the supporting vortex gas-liquid separator of freezing type drier, comprise cylinder, upper cover and low head, in use procedure, separator is vertically installed, upper cover and low head are installed on the two ends up and down of cylinder respectively, it is characterized in that: also comprise escape pipe, gas-liquid flow inlet pipe, outlet pipe, gas channeling pipe, cyclone blade and ring sealing plate, described gas-liquid flow inlet pipe is located at the top of cylinder annular sidewall, described escape pipe assigns into the top of upper cover, described cylinder top level is to being provided with ring sealing plate, this ring sealing plate center has circular hole, ring sealing plate is made to be enclosed within the periphery of described gas channeling pipe upper end and to be fixedly connected with gas channeling pipe via this circular hole, the lower end of gas channeling pipe is positioned at column body, and and between low head, leave an intersegmental gap, described cyclone blade in the form of sheets, spiral around and be fixed on described gas channeling pipe periphery, described outlet pipe runs through low head, and its lower end is in outside low head, and upper one end is fixedly connected with low head.
2. the supporting vortex gas-liquid separator of freezing type drier according to claim 1, is characterized in that: described low head and cylinder connecting portion level are to being provided with a baffle plate, and this baffle plate is fixed on the inwall of low head, is provided with delivery port above baffle plate.
3. the supporting vortex gas-liquid separator of freezing type drier according to claim 1, is characterized in that: described baffle plate is for dull and stereotyped, or the cambered plate that middle part raises up.
4. the supporting vortex gas-liquid separator of the freezing type drier according to Claims 2 or 3, is characterized in that: the peak of described baffle plate and the distance of gas channeling pipe lower end account for 1/10 ~ 1/2 of height of column.
5. the supporting vortex gas-liquid separator of the freezing type drier according to Claims 2 or 3, is characterized in that: the delivery port above described baffle plate, is arranged on outside the upright projection scope of gas channeling pipe on baffle plate.
6. the supporting vortex gas-liquid separator of the freezing type drier according to Claims 2 or 3, is characterized in that: the delivery port above described baffle plate has 2 ~ 10, is evenly arranged on baffle plate periphery, delivery port semicircular in shape or class semicircle.
7. the supporting vortex gas-liquid separator of freezing type drier according to claim 1, is characterized in that: described cyclone blade is coiled into 1 ~ 6 circle in the periphery of gas channeling pipe.
8. the supporting vortex gas-liquid separator of freezing type drier according to claim 7, is characterized in that: described gas-liquid flow inlet pipe is arranged on the top one be coiled in gas channeling pipe periphery with cyclone blade and encloses corresponding position.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510595984.7A CN105107274A (en) | 2015-09-17 | 2015-09-17 | Cyclone air-liquid separator matched with freezing dryer during use |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510595984.7A CN105107274A (en) | 2015-09-17 | 2015-09-17 | Cyclone air-liquid separator matched with freezing dryer during use |
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| CN105107274A true CN105107274A (en) | 2015-12-02 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510595984.7A Pending CN105107274A (en) | 2015-09-17 | 2015-09-17 | Cyclone air-liquid separator matched with freezing dryer during use |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107469472A (en) * | 2017-09-13 | 2017-12-15 | 江苏新凯晟机械设备有限公司 | Gas-liquid separator |
| CN107970645A (en) * | 2017-11-30 | 2018-05-01 | 陈炳坤（天津）生物技术有限公司 | A kind of high efficient gas and liquid separator |
| CN111265939A (en) * | 2020-01-21 | 2020-06-12 | 张洋洋 | High-efficient vapour and liquid separator of desulfurization system |
| CN116943345A (en) * | 2023-07-21 | 2023-10-27 | 华东理工大学 | Gas-liquid separation inner member for strengthening condensation heat exchange |
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| CN201711048U (en) * | 2010-05-11 | 2011-01-19 | 南京航空航天大学 | Centrifugal gas and liquid separator |
| CN202962136U (en) * | 2012-12-24 | 2013-06-05 | 成都兰华电子工程有限公司 | Special centrifugal type oil stain separator for compressed natural gas |
| US20130247764A1 (en) * | 2010-10-08 | 2013-09-26 | Cameron Systems As | Inlet Device For Gravity Separator |
| CN203904298U (en) * | 2014-06-13 | 2014-10-29 | 广东宾士动力科技有限公司 | Biogas dehydrating and dust-removing device |
-
2015
- 2015-09-17 CN CN201510595984.7A patent/CN105107274A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201711048U (en) * | 2010-05-11 | 2011-01-19 | 南京航空航天大学 | Centrifugal gas and liquid separator |
| US20130247764A1 (en) * | 2010-10-08 | 2013-09-26 | Cameron Systems As | Inlet Device For Gravity Separator |
| CN202962136U (en) * | 2012-12-24 | 2013-06-05 | 成都兰华电子工程有限公司 | Special centrifugal type oil stain separator for compressed natural gas |
| CN203904298U (en) * | 2014-06-13 | 2014-10-29 | 广东宾士动力科技有限公司 | Biogas dehydrating and dust-removing device |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107469472A (en) * | 2017-09-13 | 2017-12-15 | 江苏新凯晟机械设备有限公司 | Gas-liquid separator |
| CN107970645A (en) * | 2017-11-30 | 2018-05-01 | 陈炳坤（天津）生物技术有限公司 | A kind of high efficient gas and liquid separator |
| CN111265939A (en) * | 2020-01-21 | 2020-06-12 | 张洋洋 | High-efficient vapour and liquid separator of desulfurization system |
| CN116943345A (en) * | 2023-07-21 | 2023-10-27 | 华东理工大学 | Gas-liquid separation inner member for strengthening condensation heat exchange |
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Application publication date: 20151202 |