CN113058365B - Flue gas purification device for processing black betel nuts - Google Patents
Flue gas purification device for processing black betel nuts Download PDFInfo
- Publication number
- CN113058365B CN113058365B CN202110339890.9A CN202110339890A CN113058365B CN 113058365 B CN113058365 B CN 113058365B CN 202110339890 A CN202110339890 A CN 202110339890A CN 113058365 B CN113058365 B CN 113058365B
- Authority
- CN
- China
- Prior art keywords
- flue gas
- spiral pipe
- pipe
- communicated
- smoke
- Prior art date
- 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.)
- Active
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/40—Combinations of devices covered by groups B01D45/00 and B01D47/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/10—Combinations of devices covered by groups B01D45/00, B01D46/00 and B01D47/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
Abstract
The invention discloses a smoke purification device for processing black areca nuts, which comprises an induced draft fan, a smoke purifier and a smoke washing box, wherein a gas outlet of the induced draft fan is communicated with the smoke purifier, the gas outlet of the smoke purifier is communicated with the smoke washing box, the smoke washing box comprises a box body, a spiral pipe and an exhaust pipe, a lipophilic solution is arranged in the box body, the spiral pipe is immersed in the lipophilic solution, a plurality of permeation holes are formed in the side wall of the spiral pipe, the gas outlet of the smoke purifier is communicated with an opening at one end, far away from the center, of the spiral pipe, an opening at one end, close to the center, of the spiral pipe is communicated with a pressure release valve, the pressure release valve extends out of the surface of the lipophilic solution, and the exhaust pipe is communicated with the top of the box body. The invention can lead the oil mist in the smoke to be more uniformly absorbed in the spiral pipe, and the oil mist is taken away by the lipophilic solution, thereby not needing to frequently replace the filter plate and improving the production efficiency.
Description
Technical Field
The invention relates to the technical field of flue gas treatment, in particular to a flue gas purification device for processing black areca nuts.
Background
The betel nuts are classified into ginkgo nuts and black nuts according to different processing modes, the black nuts are prepared by cooking the betel nuts, putting the cooked betel nuts into a smoking furnace for smoking and drying, and the pericarp of the smoked and dried betel nuts is blackened, so the betel nuts are called as the black nuts. The black fruit has better taste, so the black fruit is favored by people. In the black fruit course of working, produce the flue gas and can not directly discharge into the atmosphere, need remove the oil mist to the flue gas, prior art adopts filtration or absorbent mode usually when removing the oil mist, and the filter that lies in the front end among the process of processing has collected a large amount of oil mist very fast, and the oil mist volume of rear end is few, and the oil mist is different at the quantity of the filter of different positions, and the filter that can not be abundant needs frequent change, influences production efficiency.
Disclosure of Invention
In view of the prior art, the invention provides a flue gas purification device for processing black areca nuts, which is characterized in that oil mist in flue gas is more uniformly adsorbed in a spiral pipe, the oil mist is taken away by lipophilic solution, a filter plate does not need to be frequently replaced, and the production efficiency is improved.
The technical scheme of the invention is realized as follows:
the utility model provides a smoke purification device of black sesame oil of processing, includes draught fan, flue gas purifier and washes the cigarette case, the gas outlet of draught fan with flue gas purifier intercommunication, flue gas purifier's gas outlet and washing cigarette case intercommunication, it includes box, spiral pipe and blast pipe to wash the cigarette case, be equipped with lipophilic solution in the box, the submergence of spiral pipe is in the lipophilic solution, the lateral wall of spiral pipe is equipped with a plurality of infiltration hole, flue gas purifier's gas outlet with the opening intercommunication of center one end is kept away from to the spiral pipe, the opening intercommunication that the spiral pipe is close to center one end has the relief valve, the relief valve stretches out lipophilic solution surface, the top intercommunication of box has the blast pipe.
Furthermore, the diameter of the penetration hole is 0.1-1 mm.
Further, flue gas purifier includes the purifying column and a plurality of honeycomb formula oil separating plate of locating in the purifying column, the range upon range of setting of honeycomb formula oil separating plate, the upper portion and the draught fan intercommunication of purifying column, the lower part and the smoke scrubber case intercommunication of purifying column, the bottom and the waste oil collecting pipe intercommunication of purifying column.
Furthermore, the waste oil collecting pipe is communicated with the waste oil collecting box.
Further, the relief valve through vertical pipe with spiral pipe intercommunication, vertical pipe only upper end and lower extreme are equipped with the opening, the relief valve includes disk seat, pouring weight, sealed pad, floating block, sleeve and lever, the disk seat is fixed the upper end of vertical pipe, the pouring weight lid on the disk seat, the pouring weight is equipped with the disk seat contact surface sealed pad, telescopic lower part is soaked in lipophilic solution, be equipped with in the sleeve the floating block, the middle part and the box of lever rotate to be connected, the both ends of lever are connected respectively pouring weight and floating block.
Furthermore, a bottom plate is arranged at the bottom of the sleeve, a pipeline is communicated with the lower portion of the side wall of the sleeve, and the other end of the pipeline is opened at the bottom of the box body.
Further, the floating block is connected with the lever through a connecting rod.
Further, the connecting rod includes upper connecting rod and lower connecting rod, the upper connecting rod bottom is equipped with first spring, the lower connecting rod top is equipped with the second spring, first spring and second spring are connected, the precision coefficient of first spring and second spring is different.
Further, a thickening agent is added into the lipophilic solution.
The invention has the beneficial effects that:
the flue gas gets into from the opening that the center was kept away from to the spiral pipe to when flowing along the spiral pipe, the spiral pipe is close to the opening intercommunication of center one end and has the relief valve, makes the flue gas in the spiral pipe have certain pressure. The lateral wall of spiral pipe is equipped with a plurality of infiltration hole, and in lipophilic solution can follow the infiltration hole and get into the spiral pipe, flue gas in the spiral pipe had certain pressure and makes the flue gas along forming airflow channel in the spiral pipe, and does not get into the spiral pipe by a large amount of lipophilic solution and block up the flow of flue gas. When the smoke flows, because the density of the oil mist is higher than that of the air, the centrifugal force is higher in the flowing process, the oil mist deflects to the outer edge of the inner pipe under the action of the centrifugal force, and finally the oil mist is adsorbed on the side wall of the inner pipe and finally dissolved in the lipophilic solution. The gaseous velocity of flow in the spiral pipe is the same, and the radius of spiral pipe periphery is greater than the radius at center, the flue gas gets into the inner tube from the neighboring edge of spiral pipe, the oil mist of the great granule of in-process along the inner tube motion is separated earlier and is adsorbed, the oil mist of tiny granule moves and adsorbs again behind the position that is close to the inner tube center, thereby avoid the oil mist to concentrate to adsorb at initial position, make the adsorption site of oil mist disperse more, make full use of spiral pipe's different positions adsorb, also be convenient for clear up the adsorbed oil mist of spiral pipe.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings needed to be used in the description of the embodiments will be briefly introduced below, and it is obvious that the drawings in the following description are only preferred embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained according to these drawings without inventive exercise.
Fig. 1 is a schematic structural view of a flue gas purification device for processing black betel nuts according to the present invention;
FIG. 2 is an enlarged view of the structure of area A of FIG. 1;
FIG. 3 is a top view of the scroll of the present invention;
FIG. 4 is a cross-sectional view of the valve seat, weight and seal of the present invention;
FIG. 5 is a top view of the honeycomb oil separation plate of the present invention;
in the figure, 1 draught fan, 2 flue gas purifier, 3 smoke washing box, 4 box body, 5 spiral pipe, 6 exhaust pipe, 7 oleophilic solution, 8 permeation hole, 9 relief valve, 11 purifying tower, 12 honeycomb type oil separating plate, 13 waste oil collecting pipe, 14 waste oil collecting box, 15 vertical pipe, 16 valve seat, 17 weight, 18 sealing gasket, 19 floating block, 20 sleeve, 21 lever, 22 bottom plate, 23 pipeline, 24 connecting rod, 25 upper connecting rod, 26 lower connecting rod, 27 first spring, 28 second spring.
Detailed Description
For a better understanding of the technical content of the present invention, the following detailed description is provided in conjunction with the accompanying drawings for further explanation of the present invention.
Example 1
Referring to fig. 1-5, a processing black sesame oil's gas cleaning device, includes draught fan 1, smoke purifier 2 and washes cigarette case 3, the gas outlet of draught fan 1 with smoke purifier 2 intercommunication, smoke purifier 2's gas outlet and washing cigarette case 3 intercommunication, it includes box 4, spiral pipe 5 and blast pipe 6 to wash cigarette case 3, be equipped with lipophilic solution 7 in the box 4, spiral pipe 5 submergence is in the lipophilic solution 7, the lateral wall of spiral pipe 5 is equipped with a plurality of infiltration hole 8, smoke purifier 2's gas outlet with the opening intercommunication of central one end is kept away from to spiral pipe 5, the opening intercommunication that spiral pipe 5 is close to central one end has relief valve 9, relief valve 9 stretches out lipophilic solution 7 surfaces, the top intercommunication of box 4 has blast pipe 6.
In the flue gas that draught fan 1 during operation will process black sesame oil was taken out to gas cleaning ware 2, gas cleaning ware 2 can get rid of the impurity of large granule, and the flue gas after gas cleaning ware 2 handles enters into next to carry out purification treatment in the smoke box 3 of washing. Be equipped with spiral pipe 5 in washing cigarette case 3, the lateral wall of spiral pipe 5 is equipped with a plurality of infiltration hole 8 to submerge in oleophilic solution 7 of box 4, the gas outlet of gas cleaning ware 2 with the opening intercommunication that center one end was kept away from to spiral pipe 5, the opening that the center was kept away from to the flue gas gets into from spiral pipe 5, and when flowing along spiral pipe 5, the opening intercommunication that spiral pipe 5 was close to center one end has relief valve 9, makes the flue gas in the spiral pipe 5 have certain pressure. The lateral wall of spiral pipe 5 is equipped with a plurality of infiltration hole 8, and in lipophilic solution 7 can follow infiltration hole 8 entering spiral pipe 5, the flue gas in spiral pipe 5 had certain pressure and makes the flue gas along forming airflow channel in spiral pipe 5, and is not blockked up the flow of flue gas in being got into spiral pipe 5 by a large amount of lipophilic solution 7. When the smoke flows, because the density of the oil mist is greater than that of the air, the centrifugal force is large in the flowing process, the oil mist is deviated towards the outer edge of the inner pipe under the action of the centrifugal force, and finally the oil mist is adsorbed on the side wall of the inner pipe and finally dissolved in the lipophilic solution 7. Gaseous velocity of flow in the spiral pipe 5 is the same, and the radius of spiral pipe 5 periphery is greater than the radius at center, the flue gas gets into the inner tube from the neighboring edge of spiral pipe 5, the oil mist of the great granule of in-process along the inner tube motion is separated earlier and is adsorbed, the oil mist of granule is moved and is adsorbed again after the position that is close to the inner tube center, thereby avoid the oil mist to concentrate the absorption at initial position, make the absorption position of oil mist disperse more, make full use of spiral pipe 5's different positions adsorb, also be convenient for clear up the adsorbed oil mist of spiral pipe 5. In the flowing process of the flue gas, part of the lipophilic solution 7 flows in and out of the lipophilic solution 7 of the spiral pipe 5 and finally flows out of the penetration hole 8 at the bottom of the spiral pipe 5, part of the flue gas is discharged from the penetration hole 8 of the spiral pipe 5 and enters the lipophilic solution 7, the flue gas entering the lipophilic solution 7 is small in volume and fully contacts with the lipophilic solution 7, so that the oil mist in the flue gas is adsorbed and dissolved by the lipophilic solution 7, the gas entering the lipophilic solution 7 finally comes out of the liquid level, the gas enters the top of the box body 4 and then is discharged from the exhaust pipe 6, and the gas coming out of the pressure release valve 9 also enters the top of the box body 4 and then is discharged from the exhaust pipe 6. The pressure relief valve 9 can keep the flue gas in the spiral pipe 5 in a relatively stable pressure range.
Optionally, the flue gas purifier 2 is provided with a plurality of, is equipped with between the flue gas purifier 2 wash smoke box 3. The treatment effect of the flue gas is improved through multiple times of treatment and purification.
Specifically, the diameter of the penetration hole 8 is 0.1-1 mm. The lipophilic solution 7 can permeate into the inner wall of the spiral pipe 5 under the gas pressure, and meanwhile, the smoke can be ensured to flow along the spiral pipe 5.
Specifically, flue gas purifier 2 includes purifying column 10 and a plurality of honeycomb formula oil separating plate 12 of locating in purifying column 10, the range upon range of setting of honeycomb formula oil separating plate 12, the upper portion and the draught fan 1 intercommunication of purifying column 10, the lower part and the washing cigarette case 3 intercommunication of purifying column 10, the bottom and the waste oil collecting pipe 13 intercommunication of purifying column 10. When the flue gas enters from the upper part of the purification tower 10, large particle impurities in the flue gas can settle down, oil mist in the flue gas can be adsorbed on the honeycomb type oil separation plate 12, and finally, the oil mist is settled down and flows into the waste oil collection pipe 13. The plurality of honeycomb type oil separation plates 12 can improve the adsorption of the oil mist. The purified flue gas enters the flue gas washing box 3 from the lower part of the purification tower 10 for further purification treatment.
Specifically, the waste oil collecting pipe 13 is communicated with a waste oil collecting box 14. The waste oil collected by the waste oil collecting pipe 13 is collected in the waste oil flowing collecting box.
Optionally, the relief valve 9 through vertical pipe 15 with the spiral pipe 5 intercommunication, vertical pipe 15 only upper end and lower extreme are equipped with the opening, the relief valve 9 includes disk seat 16, pouring weight 17, sealed pad 18, floater 19, sleeve 20 and lever 21, disk seat 16 fixes the upper end of vertical pipe 15, pouring weight 17 lid on the disk seat 16, pouring weight 17 is equipped with disk seat 16 contact surface sealed pad 18, the lower part of sleeve 20 is soaked in lipophilic solution 7, be equipped with in the sleeve 20 floater 19, the middle part and the box 4 of lever 21 are rotated and are connected, the both ends of lever 21 are connected respectively pouring weight 17 and floater 19. The side surface of the vertical pipe 15 is not provided with a through hole, and the flue gas discharged from the spiral pipe 5 flows upwards along the vertical pipe 15 and enters the pressure release valve 9. The spiral pipe 5 is horizontally arranged, and the hydraulic pressure received by each part of the spiral pipe 5 is basically consistent. And the hydraulic pressure of the upper portion of the vertical pipe 15 and the lower portion differs greatly, the air pressure in the vertical pipe 15 is the same, no opening is arranged on the side wall of the vertical pipe 15, the smoke can be prevented from being discharged from the side face of the vertical pipe 15, and the air pressure in the spiral pipe 5 can be controlled conveniently. When the smoke is discharged from the pressure relief valve 9, the smoke needs to be lifted up against the gravity of the weight 17, and after the weight 17 is lifted up, the sealing gasket 18 is separated from the valve seat 16, and the smoke can be discharged from the valve seat 16. When the atmospheric pressure in the spiral pipe 5 is not enough, the flue gas can not open the relief valve 9, only can open the relief valve 9 when the pressure of flue gas reaches the default, because there is the jar in the range that the pouring weight 17 rose and the dynamics of the jack-up that receives, consequently the flue gas pressure in the spiral pipe 5 is big more the angle that the pouring weight 17 opened is big more to make the pressure in the spiral pipe 5 keep invariable relatively. Along with the oil mist in the flue gas is continuous to be dissolved in lipophilic solution 7, the height of lipophilic solution 7 can rise, the hydraulic pressure that the spiral pipe 5 received is also along with rising along with the height of lipophilic solution 7 rises, the buoyancy that floating block 19 received when the liquid level rose increases, floating block 19 applys decurrent pressure to pouring weight 17 through lever 21, make the atmospheric pressure that needs bigger could promote pouring weight 17 and open, thereby make the atmospheric pressure in the spiral pipe 5 also increase, make the atmospheric pressure in the spiral pipe 5 tend to the equilibrium again with the outer hydraulic pressure of spiral rod, avoid a large amount of lipophilic solution 7 to get into in the spiral pipe 5. The floating block 19 is arranged in the sleeve 20, the bottom of the sleeve 20 is communicated with the lipophilic solution 7, the upper part of the sleeve is communicated with the air on the upper part of the lipophilic solution 7, so that the liquid level in the sleeve 20 is level with the liquid level in the box body 4, but when the liquid level in the box body 4 is influenced by smoke and fluctuates up and down, the sleeve 20 can reduce the influence of water waves on the liquid level in the sleeve 20, and the acting force of the floating block 19 on the weight 17 is kept relatively stable.
Specifically, a bottom plate 22 is arranged at the bottom of the sleeve 20, a pipeline 23 is communicated with the lower portion of the side wall of the sleeve 20, and the other end of the pipeline 23 is opened at the bottom of the box body 4. The bottom plate 22 prevents bubbles from moving upward and impacting the liquid level in the sleeve 20, and the sleeve 20 separates the liquid level of the floating block 19 from other liquid levels, so that the liquid level in the sleeve 20 is kept relatively stable, and the acting force of the floating block 19 on the weight 17 is kept relatively stable. The lower portion of the sidewall of the sleeve 20 is communicated with the bottom of the tank 4 through a duct 23, and the sleeve 20 is raised or lowered when the overall liquid level in the tank 4 is raised or lowered.
Specifically, the floating block 19 is connected with the lever 21 through a connecting rod 24. The floating block 19 is connected through the connecting rod 24, so that the installation is convenient, and the lever 21 does not interfere with the sleeve 20 when the floating block 19 fluctuates up and down.
Optionally, the link 24 includes an upper link 25 and a lower link 26, a first spring 27 is disposed at the bottom of the upper link 25, a second spring 28 is disposed at the top of the lower link 26, the first spring 27 and the second spring 28 are connected, and the first spring 27 and the second spring 28 have different precision coefficients. While the liquid level is kept stable, the float 19 applies a stable force to the lever 21 through the link 24. When the liquid level fluctuates slightly, the floating block 19 fluctuates slightly up and down, the first spring 27 and the second spring 28 deform simultaneously to buffer, the overall coefficient of stiffness coefficients of the first spring 27 and the second spring 28 is small, and the influence of fluctuation of the floating block 19 on the lever 21 is reduced. When the liquid level has large fluctuation, the first spring 27 is completely compressed, only the second spring 28 is compressed, the integral coefficient of the stiffness coefficients of the first spring 27 and the second spring 28 is large, and the large-amplitude fluctuation of the floating block 19 is absorbed.
Specifically, the lipophilic solution 7 is added with a thickening agent. The concentration of the lipophilic solution 7 is increased so that the smoke does not easily pass out of the spiral pipe 5.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and should not be taken as limiting the scope of the present invention, which is intended to cover any modifications, equivalents, improvements, etc. within the spirit and scope of the present invention.
Claims (8)
1. The utility model provides a smoke purification device of black sesame oil of processing, its characterized in that, includes draught fan, flue gas purifier and washes the cigarette case, the gas outlet of draught fan with flue gas purifier intercommunication, flue gas purifier's gas outlet with wash the cigarette case intercommunication, it includes box, spiral pipe and blast pipe to wash the cigarette case, be equipped with lipophilic solution in the box, the spiral pipe submergence is in the lipophilic solution, the lateral wall of spiral pipe is equipped with a plurality of permeability hole, flue gas purifier's gas outlet with the opening intercommunication of center one end is kept away from to the spiral pipe, the opening intercommunication that the spiral pipe is close to center one end has the relief valve, the relief valve stretches out lipophilic solution surface, the top intercommunication of box has the blast pipe, lipophilic solution adds has the thickening agent, improves lipophilic solution's concentration for the flue gas is difficult for wearing out the spiral pipe.
2. The flue gas purification device for processing black areca nuts as claimed in claim 1, wherein the diameter of said permeation holes is 0.1-1 mm.
3. The flue gas purification device for processing the black areca nuts as claimed in claim 1, wherein the flue gas purifier comprises a purification tower and a plurality of honeycomb type oil separation plates arranged in the purification tower, the honeycomb type oil separation plates are arranged in a stacked manner, the upper part of the purification tower is communicated with an induced draft fan, the lower part of the purification tower is communicated with a flue gas cleaning box, and the bottom of the purification tower is communicated with a waste oil collecting pipe.
4. The flue gas purification device for processing the black areca nuts as claimed in claim 3, wherein the waste oil collecting pipe is communicated with the waste oil collecting box.
5. The flue gas purification device for processing black areca nuts as claimed in claim 1, wherein said pressure release valve is communicated with said spiral pipe through a vertical pipe, only the upper end and the lower end of said vertical pipe are provided with openings, said pressure release valve comprises a valve seat, a weight, a sealing pad, a floating block, a sleeve and a lever, said valve seat is fixed on the upper end of said vertical pipe, said weight covers said valve seat, the contact surface between said weight and said valve seat is provided with said sealing pad, the lower part of said sleeve is immersed in a lipophilic solution, said floating block is arranged in said sleeve, the middle part of said lever is rotatably connected with the box body, and both ends of said lever are respectively connected with said weight and said floating block.
6. The flue gas purification device for processing black areca nuts, as claimed in claim 5, wherein a bottom plate is disposed at the bottom of the sleeve, a duct is connected to the lower portion of the sidewall of the sleeve, and the other end of the duct is opened at the bottom of the box.
7. The smoke purifying device for processing black areca nuts, as claimed in claim 5, wherein said floating block is connected with said lever through a connecting rod.
8. The flue gas purification device for processing black betel nuts, as claimed in claim 7, wherein said connecting rod comprises an upper connecting rod and a lower connecting rod, a first spring is disposed at the bottom of said upper connecting rod, a second spring is disposed at the top of said lower connecting rod, said first spring is connected to said second spring, and the stiffness coefficients of said first spring and said second spring are different.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110339890.9A CN113058365B (en) | 2021-03-30 | 2021-03-30 | Flue gas purification device for processing black betel nuts |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110339890.9A CN113058365B (en) | 2021-03-30 | 2021-03-30 | Flue gas purification device for processing black betel nuts |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN113058365A CN113058365A (en) | 2021-07-02 |
| CN113058365B true CN113058365B (en) | 2022-11-11 |
Family
ID=76564533
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202110339890.9A Active CN113058365B (en) | 2021-03-30 | 2021-03-30 | Flue gas purification device for processing black betel nuts |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN113058365B (en) |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4293524A (en) * | 1978-09-20 | 1981-10-06 | Teller Environmental Systems, Inc. | Method and apparatus for cooling and neutralizing acid gases |
| CN2224651Y (en) * | 1994-12-27 | 1996-04-17 | 胡存维 | Rotary cylinder fluid desulfuring dust collector |
| AU7436000A (en) * | 1999-09-22 | 2001-04-24 | Mantis Oil Separation Limited | Fluid control systems |
| KR20030067266A (en) * | 2002-02-07 | 2003-08-14 | 주식회사 엘지이아이 | Oil seperator of air conditioner |
| NO329085B1 (en) * | 2008-01-31 | 2010-08-16 | Sorbwater Technology As | Process and apparatus for separating fluid phases, and their applications |
| EP2113266A1 (en) * | 2008-04-30 | 2009-11-04 | Gambro Lundia AB | Degassing device |
| CN101518696A (en) * | 2009-04-02 | 2009-09-02 | 中国海洋石油总公司 | Method and device for separating oil and water |
| CN101943019B (en) * | 2009-07-08 | 2013-01-02 | 吉孟福 | Fireproof and dust removing device used for underground loader |
| CN101837200B (en) * | 2010-06-12 | 2012-05-09 | 中国海洋石油总公司 | Industrial oil water separation method and system thereof |
| CN102166436B (en) * | 2011-01-20 | 2013-10-02 | 上海益道投资管理有限公司 | Method and device for purifying multicomponent contaminated fluids |
| CN105311871A (en) * | 2014-08-01 | 2016-02-10 | 胡桂生 | Novel liquid-solid separation filtering device |
| CN206252888U (en) * | 2016-12-08 | 2017-06-16 | 广州蓝清环保工程有限公司 | One kind centrifugation oily-water seperating equipment |
| CN107281822A (en) * | 2017-07-07 | 2017-10-24 | 郝占宁 | A kind of vortex type demisting dehydrating unit |
| CN210751898U (en) * | 2019-09-21 | 2020-06-16 | 河南海天环境科技有限公司 | High-efficient meal kitchen oil smoke comprehensive treatment equipment |
| CN212493491U (en) * | 2020-09-30 | 2021-02-09 | 哈尔滨恒通排水设备制造股份有限公司 | Spiral type multi-runner assembly and oil-water separator provided with same |
-
2021
- 2021-03-30 CN CN202110339890.9A patent/CN113058365B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN113058365A (en) | 2021-07-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101779935B (en) | Cyclonic water filtration dust collecting device | |
| CN102716634A (en) | Gas-water separator with coarse-fine separation function | |
| CN113058365B (en) | Flue gas purification device for processing black betel nuts | |
| CN112933842B (en) | Wave plate helicla flute dust removal defogging device | |
| CN106966520A (en) | A kind of contaminant filter pre-processed for water quality | |
| CN206985779U (en) | A kind of percussion flow photocatalysis membrana separator | |
| CN110124428A (en) | A kind of industrial waste gas treating column | |
| CN112774445B (en) | Rod floating ball type gas-liquid separation ultrafiltration membrane component | |
| CN202628462U (en) | Gas-water separator with crude separation and fine separation functions | |
| CN201341850Y (en) | Cyclone type dust collecting device with the function of water filtration | |
| CN209934145U (en) | Oil-water separation device | |
| CN2570640Y (en) | Vortex type boiler dust catcher | |
| CN217961978U (en) | Low-concentration gas separation and purification device | |
| CN220360932U (en) | Front-end air inlet separation tank structure | |
| CN208687767U (en) | A kind of new type purification device for incinerator | |
| CN219502391U (en) | Waste gas absorption packed tower | |
| CN213901029U (en) | Device for recycling boiler continuous-discharge and fixed-discharge sewage | |
| CN217367717U (en) | Harmful gas dust removal filter equipment | |
| CN216799035U (en) | Liquid precise filtering device | |
| CN210097261U (en) | Printing exhaust gas purification device | |
| CN207928806U (en) | A kind of bag type filter | |
| CN220142941U (en) | Vertical gas-liquid separator | |
| CN204111361U (en) | A kind of adsorption tower for purifying dirty acid | |
| CN219922485U (en) | Air filter | |
| CN220758540U (en) | Catalyst drying tail gas combination suspension separation purifier |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |