CN2799056Y - Highly efficient solid-liquid separator - Google Patents
Highly efficient solid-liquid separator Download PDFInfo
- Publication number
- CN2799056Y CN2799056Y CN 200520108970 CN200520108970U CN2799056Y CN 2799056 Y CN2799056 Y CN 2799056Y CN 200520108970 CN200520108970 CN 200520108970 CN 200520108970 U CN200520108970 U CN 200520108970U CN 2799056 Y CN2799056 Y CN 2799056Y
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- Prior art keywords
- filter core
- liquid
- shell body
- upper shell
- gas
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Abstract
The utility model relates to a high-efficiency gas and liquid separator which comprises a shell body, a gas and liquid coalescer, a centrifugal separator and a liquid level gauge, wherein the shell body is provided with a separating medium inlet and a separating medium outlet, the bottom of the shell body is provided with a liquid exhaust opening and the liquid level meter is positioned on the lower part of the side part of the shell body. The shell body is divided into an upper shell body and a lower shell body. A connection opening of the lower shell body and the upper shell body is provided with a seal plate. The middle part of the upper surface of the seal plate is fixedly connected with a column-shaped chamber. The top surface of the column-shaped chamber is provided with an upper hole plate which is uniformly distributed with a plurality of fixed holes, and the bottom surface of the column-shaped chamber is a lower hole plate which is uniformly distributed with a plurality of fixed holes. An air outlet pipe opening of the centrifugal separator faces upwards, and an air inlet pipe opening faces downwards. The air inlet pipe opening is arranged in the lower shell body, and the air outlet pipe opening extends to the seal plate. The lower hole plate is covered in the seal plate. Simultaneously, the interior of the air outlet pipe opening is provided with a sintered filter core which is hung and fixed on the fixed holes of the lower hole plate. The gas and liquid coalescer is arranged in the upper shell body, and is provided with a coalescence filter core which is arranged outside the column-shaped chamber. The bottom end of the coalescence filter core is fixed in the fixed holes of the upper hole plate. The utility model has the advantages of high efficiency and high separation precision.
Description
Technical field
The utility model belongs to the operation technique field, further relate to valuable chemical industry intermediate products and chemical products in the industrial processes such as oil, chemical industry, chemical fertilizer, as: the efficient cyclone of gas-liquid two-phase product in various synthesis gas, refinery gas, the cracking gases such as methyl alcohol, synthetic ammonia, acetic acid, propylene, dimethyl ether, hydrogen.
Background technology
Domestic traditional isolation technics has mechanical separation methods such as Gravity Separation, centrifugation, flaggy (filler) separation or foam removal silk screen at present.Its separative efficiency is low, and separation accuracy is generally greater than 5 μ m, and the liquid form product that the production technology by complexity is obtained can not effectively separate, and runs off and slatterns up to the product of 10-20%, causes productivity effect to reduce.
The utility model content
For overcoming the defective of prior art, the utility model provides a kind of efficient height, gas-liquid separator that separation accuracy is high.
For achieving the above object, the utility model is achieved by the following technical solution.
A kind of high efficiency air liquid separation device comprises housing, gas-liquid coalescer and whizzer, liquid level gauge; Described housing is provided with separating medium import, separating medium outlet, and is provided with leakage fluid dram at housing bottom, and described liquid level gauge is positioned at the case side bottom; Described housing is divided into upper shell and lower house two parts, the connector place of described lower house and upper shell is provided with sealing plate, and be connected with cylindrical chamber in sealing plate upper surface middle part, this cylindrical chamber end face is the up-hole plate in uniform plurality of fixed hole, and the bottom surface of cylindrical chamber is the orifice plate that is evenly equipped with the plurality of fixed hole;
Described whizzer is given vent to anger the mouth of pipe up, the air inlet pipe mouth down is arranged in the lower house, and the mouth of pipe of giving vent to anger extends to sealing plate, and orifice plate is covered in wherein, simultaneously be provided with sintered filter core in the mouth of pipe of giving vent to anger, described sintered filter core hangs and is fixed on the fixing hole of orifice plate;
Described gas-liquid coalescer is arranged in the upper shell, comprises coalescent filter core, and this coalescent filter core is located at outside the cylindrical chamber, and the bottom is fixed in the fixing hole of up-hole plate.
The side of upper shell is located in described separating medium outlet, and in the separating medium import radial distribution setting of being located at the lower house side.
Described sintered filter core is the metallic fiber sintered felt filter core.
The bottom of described upper shell is provided with liquid level gauge and leakage fluid dram.
The bottom of described lower house also is provided with capacitance level gauge.
Described upper and lower casing connects by the flange split.
The top of described upper shell is provided with safety valve.
Design by said structure, the utility model provides a kind of new and effective gas-liquid separator, its technical characterstic is with novel efficient condensation technique and traditional organic combining together of mechanical separation technology, have the high separation accuracy of condensation technique, separative efficiency and traditional macrocyclic service life of mechanical separation technology concurrently, its separation accuracy 0.01 μ m, separative efficiency 99.99%.And unique split-type design, the maintenance of very convenient resolution element and replacing are that oil, chemical industry, fertilizer industry improve device and separate quality, the efficient apparatus of energy-conservation, consumption reduction.
Because the utility model when the side lower part of lower house is provided with liquid level gauge, has been set up capacitance level gauge again in the bottom of lower house, be convenient to play the effect of dual fail-safe according to measuring.
Separating medium outlet has been located at the side of upper shell, and with the separating medium import radial distribution that is located at the lower house side, be convenient to the dismounting and the craft piping of upper shell.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
The accompanying drawing sign
1, upper shell 2, lower house 3, sealing plate 4, cylindrical chamber
5, leakage fluid dram 6, sewage draining exit 7, liquid level gauge 8, coalescent filter core
9, up-hole plate 10, orifice plate 11, sintered filter core 12, cyclone
13, liquid header 14, the air inlet mouth of pipe 15, the give vent to anger mouth of pipe 16, safety valve
17, separating medium import 18, separating medium outlet
The specific embodiment
Below in conjunction with the drawings and specific embodiments the utility model is described in detail.
A kind of high efficiency air liquid separation device comprises housing, gas-liquid coalescer and whizzer, liquid level gauge; Described housing is provided with separating medium import, separating medium outlet, and is provided with leakage fluid dram at housing bottom, and described liquid level gauge is positioned at the case side bottom; Described housing is divided into upper shell and lower house two parts, the connector place of described lower house and upper shell is provided with sealing plate, when upper and lower casing lumps together, upper shell and lower house are divided into two airtight cavitys, promptly go up disengagement chamber and following disengagement chamber, so that carry out twice continuous separation, obtain higher separation accuracy.Be connected with cylindrical chamber in sealing plate upper surface middle part, so that hold by the separating medium after the cyclone separation; This cylindrical chamber end face is the up-hole plate in uniform plurality of fixed hole, and the bottom surface of cylindrical chamber is the orifice plate that is evenly equipped with the plurality of fixed hole; Described whizzer is given vent to anger the mouth of pipe up, the air inlet pipe mouth down is arranged in the lower house, and the mouth of pipe of giving vent to anger extends to sealing plate, and orifice plate is covered in wherein, simultaneously be provided with sintered filter core in the mouth of pipe of giving vent to anger, described sintered filter core hangs and is fixed on the fixing hole of orifice plate; Described gas-liquid coalescer is arranged in the upper shell, comprises coalescent filter core, and this coalescent filter core is located at outside the cylindrical chamber, and the bottom is fixed in the fixing hole of up-hole plate.The side of upper shell is located in described separating medium outlet, and in the separating medium import radial distribution setting of being located at the lower house side.Described sintered filter core is the metallic fiber sintered felt filter core.The bottom of described upper shell is provided with liquid level gauge and leakage fluid dram.The bottom of described lower house also is provided with capacitance level gauge.Described upper and lower casing connects by the flange split.The top of described upper shell is provided with safety valve.
Pass through said structure, separating medium enters down disengagement chamber by the separating medium import, the air inlet mouth of pipe by cyclone enters, through separating, the bottom that isolated liquid is collected down disengagement chamber by liquid header, by the magnetic turnover panel liquid level gauge of observing the lower house side and the capacitance level gauge of being located at the lower house bottom, by according to watch down separate intracavity liquid how much, acquire a certain degree into, liquid is discharged by the leakage fluid dram of lower house bottom.Separating medium after cyclone separates is via the fixing hole on sintered filter core and the orifice plate, enter cylindrical chamber, pass through the fixing hole on the up-hole plate then, and the coalescent filter core through being fixed thereon further separates, reached higher separation accuracy at last, separating medium is drawn by the separating medium outlet, in order to using; And through the liquid that coarse separation goes out, amass the bottom at upper cavity, and can watch by the capacitance level gauge of being located at the upper shell bottom surface, when acquiring a certain degree, discharge by the leakage fluid dram of being located at the upper shell bottom.
As shown in Figure 1, for an embodiment of the present utility model, comprise housing, gas-liquid coalescer and whizzer, liquid level gauge; Housing is provided with separating medium import 17, separating medium outlet 18, and the side of upper shell 1 is located in separating medium outlet 18, and in the separating medium import 17 radial distribution settings of being located at lower house 2 sides.Be provided with leakage fluid dram 5 at housing bottom, liquid level gauge 7 is positioned at the case side bottom, and this liquid level is counted magnetic turnover panel liquid level gauge; Housing is divided into upper shell 1 and lower house 2 two parts, and upper and lower casing connects by the flange split; The bottom of upper shell 1 is provided with liquid level gauge 7 and leakage fluid dram 5, and this liquid level gauge 7 is selected capacitance level gauge for use, and the top of upper shell 1 is provided with safety valve 16.Lower house 2 is provided with sealing plate 3 with the connector place of upper shell, and sealing plate 3 is divided into airtight last disengagement chamber and following disengagement chamber with housing when upper and lower casing lumps together; And be connected with cylindrical chamber 4 in sealing plate upper surface middle part, and these cylindrical chamber 4 end faces are the up-hole plate 9 in uniform plurality of fixed hole, the bottom surface of cylindrical chamber is the orifice plate 10 that is evenly equipped with the plurality of fixed hole.
Whizzer 12 give vent to anger the mouth of pipe 15 up, the air inlet mouth of pipe 14 is arranged in the lower house 2 down, the mouth of pipe 15 of giving vent to anger extends to sealing plate 3, and orifice plate 10 covered in wherein, simultaneously be provided with sintered filter core 11 in the mouth of pipe 15 of giving vent to anger, this sintered filter core 11 hangs by screw rod and is fixed on the fixing hole of orifice plate 10; Sintered filter core can be selected the metallic fiber sintered felt filter core for use.Owing in following disengagement chamber, be provided with the optimum organization of whizzer 12 and metallic fiber sintered felt filter core, born the separation task of 85-90%, created the condition of efficient separation for high-precision coalescent filter core 8.The separated liquid of following disengagement chamber is collected in the bottom of lower house 2 through the liquid header 13 of bottom, by the magnetic turnover panel liquid level gauge of observing the lower house side and the capacitance level gauge of being located at the lower house bottom, regularly discharges through the leakage fluid dram 7 of lower house bottom.
The gas-liquid coalescer is arranged in the upper shell 1, comprises coalescent filter core 8, and this coalescent filter core 8 is located at outside the cylindrical chamber 4, and the bottom is fixed in the fixing hole of up-hole plate 1 by screw rod.
Need gas separated by the whizzer 12 in the disengagement chamber under separating medium import 17 warps, sintered filter core 11, cylindrical chamber 4, coalescent filter core 8, being separated at last almost is pure dielectric gas, enters lower procedure by separating medium outlet 18.
Claims (7)
1, a kind of high efficiency air liquid separation device comprises housing, gas-liquid coalescer and whizzer, liquid level gauge; Described housing is provided with separating medium import, separating medium outlet, and is provided with leakage fluid dram at housing bottom, and described liquid level gauge is positioned at the case side bottom; It is characterized in that,
Described housing is divided into upper shell and lower house two parts, the connector place of described lower house and upper shell is provided with sealing plate, and be connected with cylindrical chamber in sealing plate upper surface middle part, this cylindrical chamber end face is the up-hole plate in uniform plurality of fixed hole, and the bottom surface of cylindrical chamber is the orifice plate that is evenly equipped with the plurality of fixed hole;
Described whizzer is given vent to anger the mouth of pipe up, the air inlet pipe mouth down is arranged in the lower house, and the mouth of pipe of giving vent to anger extends to sealing plate, and orifice plate is covered in wherein, simultaneously be provided with sintered filter core in the mouth of pipe of giving vent to anger, described sintered filter core hangs and is fixed on the fixing hole of orifice plate;
Described gas-liquid coalescer is arranged in the upper shell, comprises coalescent filter core, and this coalescent filter core is located at outside the cylindrical chamber, and the bottom is fixed in the fixing hole of up-hole plate.
2, high efficient gas and liquid separator according to claim 1 is characterized in that, the side of upper shell is located in described separating medium outlet, and in the separating medium import radial distribution setting of being located at the lower house side.
3, high efficient gas and liquid separator according to claim 1 is characterized in that, described sintered filter core is the metallic fiber sintered felt filter core.
4, high efficient gas and liquid separator according to claim 1 is characterized in that, the bottom of described upper shell is provided with liquid level gauge and leakage fluid dram.
5, high efficient gas and liquid separator according to claim 1 is characterized in that, the bottom of described lower house also is provided with capacitance level gauge.
6, high efficient gas and liquid separator according to claim 1 is characterized in that, described upper and lower casing connects by the flange split.
7, high efficient gas and liquid separator according to claim 1 is characterized in that, the top of described upper shell is provided with safety valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520108970 CN2799056Y (en) | 2005-06-10 | 2005-06-10 | Highly efficient solid-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520108970 CN2799056Y (en) | 2005-06-10 | 2005-06-10 | Highly efficient solid-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2799056Y true CN2799056Y (en) | 2006-07-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520108970 Expired - Fee Related CN2799056Y (en) | 2005-06-10 | 2005-06-10 | Highly efficient solid-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2799056Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111396022A (en) * | 2020-04-03 | 2020-07-10 | 长江大学 | Oil-water in-situ separation device and method based on power rotating spiral flow technology |
-
2005
- 2005-06-10 CN CN 200520108970 patent/CN2799056Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111396022A (en) * | 2020-04-03 | 2020-07-10 | 长江大学 | Oil-water in-situ separation device and method based on power rotating spiral flow technology |
| CN111396022B (en) * | 2020-04-03 | 2022-10-04 | 长江大学 | Oil-water in-situ separation device and method based on power rotating spiral flow technology |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |