CN201371007Y - High-efficiency baffle-plate oil/ mist eliminator - Google Patents
High-efficiency baffle-plate oil/ mist eliminator Download PDFInfo
- Publication number
- CN201371007Y CN201371007Y CN200920083656U CN200920083656U CN201371007Y CN 201371007 Y CN201371007 Y CN 201371007Y CN 200920083656 U CN200920083656 U CN 200920083656U CN 200920083656 U CN200920083656 U CN 200920083656U CN 201371007 Y CN201371007 Y CN 201371007Y
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- Prior art keywords
- baffle plate
- separator
- flap
- flap separator
- oil removing
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Abstract
The utility model relates to a high-efficiency baffle-plate oil/ mist eliminator, which consists of a baffle plate separator, a downcomer, an isolating plate and a shell body. The baffle plate separator consists of a baffle plate and a collecting tank; the shell body is provided with an air inlet and an air outlet; the bottom part of the shell body is provided with a liquid or solid particle vent; the isolating plate is connected with the shell body and the baffle plate separator by welding or bolts; the air inlet and the air outlet are respectively positioned at both sides of the isolating plate; the upper end of the downcomer is connected with the bottom parts of the baffle plate separator and the collecting tank by welding or bolts and the lower part is fixed at the suitable position of the shell body by a pipe clamp; and the baffle plate has a S-shaped blade with 1 or more than two barbs and a two-channel trapezoidal blade or three-channel trapezoidal blade. The oil/ mist eliminator has the advantages of high separation efficiency, lower resistance, simple equipment structure, wide application range, elastic operation, long service life, low operation cost and the like.
Description
Technical field
The utility model relates to profit, gas-liquid (mist) separator, relates to industry vertical and cylindrical profit, gas-liquid (mist) separators such as being used in chemical industry, petrochemical industry, medicine, light industry, environmental protection particularly.
Background technology
In the process of Chemical Manufacture, oil, water and mist separate production process, product quality and economic benefit influence very big, and normally used equipment has cyclone separator, eddy flow plate separator, combined type separator, silk screen separator, material filling type separator etc.When these separators carry out separating treatment, there are deficiencies such as isolation resistance height, equipment is huge, separation equipment easily stops up, separative efficiency is low, operating flexibility is little, particularly under the fast too high condition of gas, it is outstanding that separator reentrainment problem shows especially, has a strong impact on the normal operation of chemical system.
Summary of the invention
The utility model is in order to overcome problem and the shortcoming that above-mentioned prior art exists, a kind of efficient baffle plate type oil removing or demister are provided, characteristics such as big, the difficult obstruction of the air velocity that this device has compact conformation, separative efficiency height, resistance is little, operating flexibility is big, allow, the utility model are widely used in solution-air in the chemical process (mist) and separate, reclaim the gas-liquid separation of valuables in the chemical-process, compressor or circulator outlet, water-oil separating etc.
Technical solutions of the utility model are:
A kind of efficient baffle plate type oil removing or demister, by the flap separator, down-comer, dividing plate and housing are formed, the flap separator is made up of baffle plate and feeder, housing is provided with gas feed, the bottom is provided with liquid or solid particulate emissions mouth, dividing plate and housing, the flap separator adopts welding or bolt to connect, gas inlet and outlet is respectively in dividing plate one side, the down-comer upper end adopts welding or bolt to be connected with flap separator feeder bottom, the bottom is fixed on the housing appropriate location with pipe clamp, it is characterized in that: baffle plate has the S type blade of 1 barb or 2 above barbs, two passage trapezoid blades or triple channel trapezoid blade.
The mounting means of described flap separator in device is: the mounting means of the mounting means of bottom horizontal flow sheet, the mounting means of perpendicular flow or oblique flow.
Described 1-4 kind baffle plate is combined into the flap separator to be installed in the device.
The mode of 1-4 flap separator with combination is installed in the device.
The import of flap separator adds the cohesion silk screen according to the liquid particle diameter in the device below 5--15 μ m.
Can add Washing spray nozzle or steam blowing mouth according to the situation of medium in the import of flap separator.
The material of flap separator is corrosion resistant materials such as stainless steel, plastics or fiberglass.
Characteristics such as the utlity model has the separative efficiency height, resistance drop is little, device structure is simple, applied widely, operating flexibility big, long service life, operating cost are low.
The utlity model has following advantage:
1, device structure is simple: for example: compare with activated carbon oil expeller behind the former compressor, and the diameter of equipment of the present utility model and highly have only half of activated carbon oil expeller equipment, weight has only 1/3 of activated carbon oil expeller.
2, optimum range is wide: gas-solid can both separate mutually, has overcome the shortcoming that wire mesh demister can only separate clean and the less gas-liquid mixture of viscosity.
3, operating flexibility is big: the air velocity of passing through is big, the optimum operation flow velocity of wire mesh demister is the 1.8--2.5 meter per second, and optimum operation flow velocity of the present utility model is at the 3--6 meter per second.
4, operating cost is low: the utility model separates for band liquid airflow collision, do not need internals such as activated carbon or filler, be furnished with the steam blowing mouth and washer jet can clean greasy dirt and the attachment that bonds on the flap separator assembly surface at oil expeller equipment entrance face, need not to carry out the labor cleaning.
5, long service life: separator assembly of the present utility model is made up of plate and framework, and plate and framework all adopt corrosion resistant materials such as stainless steel, north material, fiberglass to make, and enough intensity and resistance to corrosion are arranged, and service life is more than 10 years.
6, separative efficiency height, resistance are little: the droplet more than the 15 μ m is adopted double-deck combination trap assembly, its separative efficiency reaches more than 99%, add the cohesion silk screen for the droplet below the 5-10 μ m in the separator assembly porch, make less than the droplet below the 5-10 μ m collide mutually during silk screen by cohesion be condensed into bigger particle after, enter the flap separator assembly again and separate, its separative efficiency reaches more than 99%.The resistance of individual layer flap separator assembly is below 10--15mmH2O.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is the structural representation of the mobile mounting means of flap separator level of band cohesion silk screen.
Fig. 3 is a flap separator oblique flow mounting means structural representation.
Fig. 4 a is single hook S type flap form and fundamental diagram.
Fig. 4 b is many hooks S type flap form and fundamental diagram.
Fig. 4 c is two passage ladder type flap form and fundamental diagrams.
Fig. 4 d is triple channel ladder type flap form and fundamental diagram.
Fig. 5 is for being flap separator perpendicular flow mounting means structural representation.
The specific embodiment
The utility model will be further described in conjunction with the accompanying drawings.
As can be seen from Figure 1, the utility model is made up of flap separator 4, down-comer 8, dividing plate 5 and housing 6, flap separator 4 is made up of baffle plate and feeder, housing 6 is provided with gas feed 1, be provided with baffle plate 9 in gas feed place, the 9 main effects of gas feed baffle plate are anti-airflow scouring housings of carrying drop or solids secretly, and separate the drop or the solids of large-size at this; The bottom is provided with liquid or solid particulate emissions mouth 3, and dividing plate 5 adopts and is welded to connect with housing 6, flap separator 4, and the main effect of dividing plate 5 is the gas of isolating before and after separating; Gas feed 1 and gas vent 2 are respectively in dividing plate 5 both sides, down-comer 8 upper ends and flap separator 4 feeders bottom are adopted and are welded to connect, the bottom is fixed on housing 6 appropriate locations with pipe clamp 7, the effect of pipe clamp 7 is fixing down-comers, baffle plate has the S type blade of 1 barb, can also select S type blade, two passage trapezoid blades and the triple channel trapezoid blade of 2 above barbs, 10 are the cohesion silk screen.
Flap separator 4 is the utility model core, the flap separator is made up of baffle plate and feeder, baffle plate is the S type blade that has 1 barb, shown in Fig. 4 a, and the flap separator level type of flow is installed in this device, as shown in Figure 1, each parts is by being welded to connect in device.The flap separator separates according to the physics principle of inertia, when flap that the air-flow of entrained drip or solids is shaped by particular design with certain speed, turning or barb place at flap, drop or solids are under effect of inertia, change by collision movement direction and gas motion direction, make liquid foam drop or solids produce and separate with gas.In the utility model, the working condition of droplets entrained or solids in the divided gas flow: the air-flow of entrained drip or solids enters this device case from gas feed, behind baffle plate, enter the flap separator and separate drop or solids, air-flow goes out the flap separator, enter the dividing plate opposite side, go out this device through gas vent; Drop that separates or solids under the gravity effect through deflection plate separator bottom feeder and down-comer to housing bottom, discharge this device through floss hole again.
Baffle plate of the present utility model can also select to have the S type blade of 3 barbs, shown in Fig. 4 b, can also select to have two passage ladder type blades, shown in Fig. 4 c.Can also select to have triple channel ladder type blade, shown in Fig. 4 d.The import of flap separator adds the cohesion silk screen according to the liquid particle diameter, and the flap separator level type of flow is installed in this device, as shown in Figure 2.Flap separator oblique flow mode is installed in this device, as shown in Figure 3.Flap separator perpendicular flow mode is installed in this device, as shown in Figure 5.
Claims (7)
1, a kind of efficient baffle plate type oil removing or demister, by the flap separator, down-comer, dividing plate and housing are formed, the flap separator is made up of baffle plate and feeder, housing is provided with gas feed, outlet, the bottom is provided with liquid or solid particulate emissions mouth, dividing plate and housing, the flap separator adopts welding or bolt to connect, gas feed and outlet are respectively in the dividing plate both sides, the down-comer upper end adopts welding or bolt to be connected with flap separator feeder bottom, the bottom is fixed on the housing appropriate location with pipe clamp, it is characterized in that: baffle plate has the S type blade of 1 barb or 2 above barbs, two passage trapezoid blades or triple channel trapezoid blade.
2, efficient baffle plate type oil removing according to claim 1 or demister is characterized in that: the mounting means of described flap separator in device is: the mounting means of the mounting means of bottom horizontal flow sheet, the mounting means of perpendicular flow or oblique flow.
3, efficient baffle plate type oil removing according to claim 1 or demister is characterized in that: described 1-4 kind baffle plate is combined into the flap separator is installed in the device.
4, efficient baffle plate type oil removing according to claim 1 or demister is characterized in that: the mode of 1-4 flap separator with combination is installed in the device.
5, according to claim 1,2 or 3 described efficient baffle plate type oil removing or demisters, it is characterized in that: the import of flap separator adds the cohesion silk screen according to the liquid particle diameter in the device.
6, according to claim 1,2 or 3 described efficient baffle plate type oil removing or demisters, it is characterized in that: can add Washing spray nozzle or steam flush mouth according to the situation of medium in the import of flap separator.
7, according to claim 1,2 or 3 described efficient baffle plate type oil removing or demisters, it is characterized in that: the material of flap separator is corrosion resistant materials such as stainless steel, plastics or fiberglass.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920083656U CN201371007Y (en) | 2009-02-12 | 2009-02-12 | High-efficiency baffle-plate oil/ mist eliminator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920083656U CN201371007Y (en) | 2009-02-12 | 2009-02-12 | High-efficiency baffle-plate oil/ mist eliminator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201371007Y true CN201371007Y (en) | 2009-12-30 |
Family
ID=41497086
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200920083656U Expired - Fee Related CN201371007Y (en) | 2009-02-12 | 2009-02-12 | High-efficiency baffle-plate oil/ mist eliminator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201371007Y (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102883790A (en) * | 2010-04-09 | 2013-01-16 | Run技术系统有限公司 | Apparatus for water separation in the vacuum system of a paper machine and method for utilizing the same |
| CN102961925A (en) * | 2012-11-20 | 2013-03-13 | 江苏华强电力设备有限公司 | Baffle plate of separator |
| CN103861385A (en) * | 2012-12-10 | 2014-06-18 | 河南宇天化工有限公司 | Vacuum tail gas treatment system for benzene hydrogenation device |
| CN108458522A (en) * | 2018-02-26 | 2018-08-28 | 冰轮环境技术股份有限公司 | high-efficiency oil separator |
| CN111408194A (en) * | 2020-04-20 | 2020-07-14 | 合肥中亚环保科技有限公司 | Chimney liquid drop removing system after wet desulphurization of cement kiln |
| CN111921320A (en) * | 2020-08-04 | 2020-11-13 | 广东韶钢松山股份有限公司 | Gas-liquid separator and acid gas mist catcher |
| CN112945823A (en) * | 2021-02-22 | 2021-06-11 | 浙江浙能嘉华发电有限公司 | Particle enrichment device and method for flow field |
| CN114307501A (en) * | 2022-01-04 | 2022-04-12 | 中煤科工集团重庆研究院有限公司 | Antiseized patching machine dust collector |
-
2009
- 2009-02-12 CN CN200920083656U patent/CN201371007Y/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102883790A (en) * | 2010-04-09 | 2013-01-16 | Run技术系统有限公司 | Apparatus for water separation in the vacuum system of a paper machine and method for utilizing the same |
| CN102883790B (en) * | 2010-04-09 | 2016-10-12 | Run技术系统有限公司 | For realizing the equipment that water separates and the method using described equipment in the vacuum system of paper machine |
| CN102961925A (en) * | 2012-11-20 | 2013-03-13 | 江苏华强电力设备有限公司 | Baffle plate of separator |
| CN103861385A (en) * | 2012-12-10 | 2014-06-18 | 河南宇天化工有限公司 | Vacuum tail gas treatment system for benzene hydrogenation device |
| CN103861385B (en) * | 2012-12-10 | 2017-04-05 | 河南宇天化工有限公司 | A kind of vacuum tail gas processing system for benzol hydro refining unit |
| CN108458522A (en) * | 2018-02-26 | 2018-08-28 | 冰轮环境技术股份有限公司 | high-efficiency oil separator |
| CN111408194A (en) * | 2020-04-20 | 2020-07-14 | 合肥中亚环保科技有限公司 | Chimney liquid drop removing system after wet desulphurization of cement kiln |
| CN111921320A (en) * | 2020-08-04 | 2020-11-13 | 广东韶钢松山股份有限公司 | Gas-liquid separator and acid gas mist catcher |
| CN111921320B (en) * | 2020-08-04 | 2022-04-12 | 广东韶钢松山股份有限公司 | Gas-liquid separator and acid gas mist catcher |
| CN112945823A (en) * | 2021-02-22 | 2021-06-11 | 浙江浙能嘉华发电有限公司 | Particle enrichment device and method for flow field |
| CN114307501A (en) * | 2022-01-04 | 2022-04-12 | 中煤科工集团重庆研究院有限公司 | Antiseized patching machine dust collector |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20091230 Termination date: 20170212 |