CN205549689U - Multistage separator of profit - Google Patents
Multistage separator of profit Download PDFInfo
- Publication number
- CN205549689U CN205549689U CN201620396056.8U CN201620396056U CN205549689U CN 205549689 U CN205549689 U CN 205549689U CN 201620396056 U CN201620396056 U CN 201620396056U CN 205549689 U CN205549689 U CN 205549689U
- Authority
- CN
- China
- Prior art keywords
- knockout drum
- profit
- tank
- oil
- pipe
- 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
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a multistage separator of profit belongs to the oil -water separating equipment field. It includes that two knockout drums are flash trapping stage jar and grade separation jar respectively, and the top of every knockout drum is provided with the feed liquor pipe, and the bottom is provided with the drain pipe, the lateral wall of the knockout drum position that is close to the top be provided with a plurality of rows of oil pipe, a plurality of rows of oil pipe interval distribution in vertical direction, the top of knockout drum be provided with the atmospheric valve, inside is provided with filter and heater, the outside sets up the liquid level pipe. The utility model discloses can realize the continuous separation of profit, adopt the grade separation operation, water oil separating purity is high, can the internal liquid level of in situ observation jar and the water oil separating condition to according to the suitable row oil pipe of the high selection of liquid level, improved water oil separating's nimble nature and efficiency, also effectively avoid the aqueous phase to discharge from arranging oil pipe, still have the heating function, shorten the profit layering time, improve separation efficiency.
Description
Technical field
This utility model belongs to oily water separating equipment field, more particularly, it relates to a kind of profit multi-stage separation device.
Background technology
Usually having some oil water mixtures in productive life, these oil water mixtures can not directly utilize, and needs profit therein
Separate, utilize resource therein, reduce the wasting of resources.The method of oil-water separation is more, has floating point of physical partition method, electricity
From method and gravitational separation process etc..Gravitational separation process is to utilize the physical phenomenons such as profit density contrast and Filtration Adsorption, is not changing oil
By oil-water separation in the case of chemical property.Gravitational separation process as by the difference of its model of action, also can be divided into mechanical separation, quiet
Put separation and centrifugation three kinds.Mechanical phonograph recorder separation: allow oil-polluted water flow through swash plate, corrugated plating tubule and filter etc., be allowed to produce
Give birth to eddy current, transfer and collide, to promote oil or fat particles to be gathered into bigger elaioleucite, then float through the effect of density contrast, thus
Reach the purpose separated.Standing separation method: be stored in tank by oil-polluted water, under simple action of gravity, through precipitation
Fluid is made naturally to float to reach the purpose separated.Centrifugal separation: utilize the centrifugal force that high speed rotary motion produces, make oil,
Water realizes separating under the effect of centrifugal force and density contrast, and its feature is that the oily water time of staying in the separator is the shortest, institute
Less with separator volume.
The oily water separating equipment structure of existing employing standing separation method is complex, and whole equipment is that closed structure is opaque, whole
Individual separation process visuality is poor so that separation process cannot carry out artificial regulatory, thus cause oil-water separation result undesirable
Situation, affect product quality；On the other hand, existing equipment is all that separation purity is the highest by an oil-water separation, returns
Yield is the highest, and affects subsequent treatment.
The equipment of existing multiple oil-water separation in prior art, as Chinese Patent Application No. is: 201310530895.5, the applying date
For: the patent documentation on November 1st, 2013, disclose a kind of novel rapid oil water separator, described drainage screen is positioned at separation
Inside tank, described drainage screen is positioned at below profit import, and described heater is positioned at inside knockout drum, and described heat pipe is positioned at separation
Inside tank, described heat pipe is positioned at outside heater, and described drain pipe is positioned at below knockout drum, and described flowline is positioned at knockout drum
Side, described profit import is positioned at above knockout drum.In the program, knockout drum is enclosed construction, is difficult to observe that inside liquid level is high
Degree, thus cause the liquid discharged from flowline may not reach this height, nothing for oil-water mixture, water, oil, even liquid level
Liquid flows out, and oil-water separation purity is low.
And for example Chinese Patent Application No. is: 201510329208.2, filing date: the patent documentation on June 9th, 2015, public
Open a kind of oily-water seperating equipment, including profit inlet pipe, cooler bin, solid-liquid separating machine, knockout drum, flowline and outlet pipe,
Described profit inlet pipe entrance point is provided with filter screen, and profit inlet pipe is provided with cooler bin, and profit inlet pipe is installed control valve, and profit enters
Pipe is connected with solid-liquid separating machine, and solid-liquid separating machine side is provided with slag-drip opening, and solid-liquid separating machine is connected with knockout drum by conveying pipeline,
Knockout drum top is provided with overflow pipe, and the overflow pipe other end connects with conveying pipeline, be sequentially provided with from top to bottom in knockout drum coarse sands layer,
Fine sand layer, glass fibre coalescing layer and politef stratum reticulare, knockout drum top is provided with flowline, and knockout drum bottom is provided with water outlet
Pipe.Program structure is relatively complicated, and production cost is high, and in Chemical Manufacture, in profit, solid particle polluter is less, uncomfortable
In using this equipment.
Summary of the invention
1, problem to be solved
It is difficult to observe liquid level position, oil-water separation time length, the problem that purity is low, basis for existing oily water separating equipment when using
Utility model provides a kind of profit multi-stage separation device, and the profit of Chemical Manufacture is carried out the second-order separation, and separation purity is high, and
Can understand liquid level at any time, adapt to the oil-water separation of different liquid level, this device has simple in construction, and separation efficiency is fast,
Effective advantage.
2, technical scheme
For solving the problems referred to above, this utility model adopts the following technical scheme that.
A kind of profit multi-stage separation device, including knockout drum, the top of knockout drum is provided with feed tube, and bottom is provided with drain pipe；
The sidewall of described knockout drum is provided with multiple oil exit pipe near the position at top, and multiple oil exit pipe in the vertical directions are spaced apart.
As further improvement of the utility model, described oil exit pipe has three, and the vertical direction along knockout drum is arranged at equal intervals.
As further improvement of the utility model, described drain pipe arranges drain valve, each oil exit pipe arranges one
Draining valve.
As further improvement of the utility model, the top of described knockout drum is provided with atmospheric valve, can make the inner chamber of knockout drum
With air communication, it is ensured that it is smooth and easy that liquid flows.
As further improvement of the utility model, described knockout drum be internally provided with screen plate, the position height of screen plate
Position height higher than the oil exit pipe of the top.
As further improvement of the utility model, the outside of described knockout drum arranges liquid level tube；The upper end of described liquid level tube
Connecting with the top of knockout drum sidewall, lower end connects with the bottom of knockout drum sidewall.
As further improvement of the utility model, the position height of described liquid level tube upper end is between screen plate and the row of the top
Between oil pipe.
As further improvement of the utility model, the material of described liquid level tube is quartz glass.
As further improvement of the utility model, described knockout drum is provided with heater, it is possible to carry out separating pot liquid
Heating.
As further improvement of the utility model, described knockout drum has two, respectively flash trapping stage tank and the second-order separation
Tank, the drain pipe of flash trapping stage tank is connected with the feed tube of the second-order separation tank；The feed tube of described the second-order separation tank is in vertically side
To height less than the feed tube of flash trapping stage tank at the height of vertical direction.
3, beneficial effect
Compared to prior art, the beneficial effects of the utility model are:
(1) this utility model vertical spacing on knockout drum sidewall arranges multiple oil exit pipe, in knockout drum after profit layering, and can root
According to liquid level, and the thickness of oil reservoir selects corresponding oil exit pipe to carry out discharging fluid, and in prior art, only one row
Oil pipe, fluid must reach a certain height and just can carry out oil extraction operation, and this device is broken this limitation, improve oil-water separation
Nimble property, can prevent the water after separating from discharging from oil exit pipe simultaneously, improve oil-water separation purity；
(2) atmospheric valve at the top of this utility model knockout drum, can make inner chamber and the air communication of knockout drum, and tank internal gas pressure is stable,
Ensure the smooth and easy of liquid flowing；
(3) being internally provided with screen plate and can filter a small amount of solid impurity contained in profit of this utility model knockout drum, improves
Fluid degree of purity after separation；
(4) this utility model arranges the liquid level tube being made up of quartz glass in the outside of knockout drum, and the position of liquid level tube upper end is high
Degree, between screen plate and the oil exit pipe of the top, can observe liquid level in tank body, and oil-water separation situation at any time,
Corresponding oil exit pipe is selected to carry out oil extraction operation by the liquid level of display；
(5) this utility model knockout drum is provided with heater, it is possible to heat separating pot liquid, accelerates fluid layering speed
Degree；
(6) this utility model arranges two knockout drums, respectively flash trapping stage tank and the second-order separation tank, separates through flash trapping stage tank
After aqueous phase in still contain a small amount of fluid, be again introduced into the second-order separation tank and carry out secondary separation recovery, oil-water separation degree is high,
Purity is high, and the aqueous phase oil content after two-stage separates is extremely low, and oil recovery rate is high；
(7) this utility model simple in construction, reasonable in design, it is easy to manufacture.
Accompanying drawing explanation
Fig. 1 is structure principle chart of the present utility model.
In figure: 1, knockout drum；2, feed tube；3, drain pipe；4, oil exit pipe；5, atmospheric valve；6, screen plate；7, row
Water valve；8, draining valve；9, heater；10, liquid level tube；
Detailed description of the invention
Below in conjunction with specific embodiments and the drawings, this utility model is further described below.
Embodiment 1
As it is shown in figure 1, a kind of profit multi-stage separation device of the present embodiment, including two knockout drums 1, respectively flash trapping stage
Tank and the second-order separation tank；The top of described each knockout drum 1 is provided with feed tube 2, and bottom is provided with drain pipe 3, and draining
Arranging drain valve 7 on pipe 3, the drain pipe 3 of flash trapping stage tank is connected with the feed tube 2 of the second-order separation tank, and the second-order separation
The feed tube 2 of tank at the height of vertical direction less than the feed tube 2 of flash trapping stage tank at the height of vertical direction, it is ensured that a fraction
Water after separating in tank can flow into the second-order separation tank under self gravitation effect.
The sidewall of described each knockout drum 1 is provided with multiple oil exit pipe 4 near the position at top, has three in the present embodiment,
Three oil exit pipes are arranged at equal intervals along the vertical direction of knockout drum 1, and arrange a draining valve 8 on each oil exit pipe 4.Row
This kind of structure design of oil pipe 4, can be according to liquid level in knockout drum 1, and the thickness of oil reservoir selects corresponding oil exit pipe 4
Carry out discharging fluid, and in prior art, only one oil exit pipe 4, fluid must reach a certain height and just can carry out oil extraction behaviour
Making, this structure breaks this limitation, improves the nimble property of oil-water separation, and the water after separating can be prevented from oil exit pipe 4 row simultaneously
Go out, improve oil-water separation purity.
In the present embodiment, the top of described knockout drum 1 is provided with atmospheric valve 5, can make inner chamber and the air communication of knockout drum 1,
Tank internal gas pressure is stable, it is ensured that it is smooth and easy that liquid flows.Described knockout drum 1 be internally provided with screen plate 6, screen plate 6
Position height, higher than the position height of the oil exit pipe 4 of the top, can filter a small amount of solid impurity contained in profit, improves and divides
From rear fluid degree of purity.Described knockout drum 1 is provided with heater 9, it is possible to heat liquid in knockout drum 1, accelerates
Oil-water separation speed.
Additionally, in the present embodiment, it is worth mentioning at this point that, the outside of described knockout drum 1 arranges liquid level tube 10, liquid level tube 10
Employing silica glass material is made, and the upper end of liquid level tube 10 connects with the top of knockout drum 1 sidewall, lower end and knockout drum 1 sidewall
Bottom connection；And the position height of liquid level tube 10 upper end is between the oil exit pipe 4 of screen plate 6 and the top, Ke Yisui
Time observe liquid level in knockout drum 1, and oil-water separation situation, select corresponding oil exit pipe 4 to carry out by the liquid level of display
Oil extraction operates.
Time specifically used, oil-water mixture is entered in tank body by the feed tube 2 of flash trapping stage tank, and is filtered off solid by screen plate 6
Body impurity, stand a period of time profit be gradually layered, oil phase upper, aqueous phase under, in the process, heater can be passed through
9 heat, and accelerate layered velocity；Open the drain valve 7 of flash trapping stage tank, the aqueous phase of bottom from drain pipe 3 through the second-order separation
The feed tube 2 of tank enters in tank body, again carries out second order hierarchical；After layering terminates, by liquid level in observation liquid level tube 10
Select suitable oil exit pipe 4 to discharge fluid, such as, in flash trapping stage tank profit interface be in centre oil exit pipe 4 and under
Between the oil exit pipe 4 of side, now can open the draining valve 8 on the oil exit pipe 4 in the middle of flash trapping stage tank, carry out oil extraction operation；
Aqueous phase after two-stage separates is discharged from the drain pipe 3 of the second-order separation tank；So the most repeatedly, it is achieved profit be continuously separated recovery.
Profit multi-stage separation device of the present utility model, can realize being continuously separated of profit, uses the second-order separation operation, and profit divides
High from purity；Liquid level and oil-water separation situation in energy Real Time Observation tank body, and select suitable oil exit pipe according to liquid level,
Improve nimble property and the efficiency of oil-water separation, be also prevented effectively from aqueous phase and discharge from oil exit pipe；Also there is heating function, shorten oil
The water stratification time, improve separation efficiency.
Schematically being described this utility model and embodiment thereof above, this description does not has restricted, shown in accompanying drawing
Be also one of embodiment of the present utility model, actual structure is not limited thereto.So, if this area is common
Technical staff is enlightened by it, in the case of creating objective without departing from this utility model, designs and this technology without creative
Frame mode that scheme is similar and embodiment, all should belong to protection domain of the present utility model.
Claims (10)
1. a profit multi-stage separation device, including knockout drum (1), the top of knockout drum (1) is provided with feed tube (2),
Bottom is provided with drain pipe (3), it is characterised in that: the sidewall of described knockout drum (1) is provided with many near the position at top
Individual oil exit pipe (4), multiple oil exit pipe in the vertical directions are spaced apart.
A kind of profit multi-stage separation device the most according to claim 1, it is characterised in that: described oil exit pipe (4) has
Three, the vertical direction along knockout drum (1) is arranged at equal intervals.
A kind of profit multi-stage separation device the most according to claim 2, it is characterised in that: on described drain pipe (3)
Drain valve (7) is set, each oil exit pipe (4) arranges a draining valve (8).
4. according to a kind of profit multi-stage separation device described in any one in claim 1-3, it is characterised in that: described divides
The top of tank (1) is provided with atmospheric valve (5), inner chamber and the air communication of knockout drum (1) can be made, it is ensured that liquid flowing
Smooth and easy.
5. according to a kind of profit multi-stage separation device described in any one in claim 1-3, it is characterised in that: described divides
Being internally provided with screen plate (6) from tank (1), the position height of screen plate (6) is higher than the oil exit pipe (4) of the top
Position height.
A kind of profit multi-stage separation device the most according to claim 5, it is characterised in that: described knockout drum (1)
Outside arranges liquid level tube (10)；The upper end of described liquid level tube (10) connects with the top of knockout drum (1) sidewall, lower end with
The bottom connection of knockout drum (1) sidewall.
A kind of profit multi-stage separation device the most according to claim 6, it is characterised in that: on described liquid level tube (10)
The position height of end is between the oil exit pipe (4) of screen plate (6) and the top.
A kind of profit multi-stage separation device the most according to claim 6, it is characterised in that: described liquid level tube (10)
Material is quartz glass.
A kind of profit multi-stage separation device the most according to claim 1, it is characterised in that: described knockout drum (1) sets
It is equipped with heater (9), it is possible to knockout drum (1) interior liquid is heated.
10. according to a kind of profit multi-stage separation device described in any one in claim 6-9, it is characterised in that: described divides
From tank (1), there are two, respectively flash trapping stage tank and the second-order separation tank, the drain pipe (3) of flash trapping stage tank and two fraction
Feed tube (2) from tank connects；The feed tube (2) of described the second-order separation tank is less than flash trapping stage at the height of vertical direction
The feed tube (2) of tank is at the height of vertical direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620396056.8U CN205549689U (en) | 2016-04-29 | 2016-04-29 | Multistage separator of profit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620396056.8U CN205549689U (en) | 2016-04-29 | 2016-04-29 | Multistage separator of profit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205549689U true CN205549689U (en) | 2016-09-07 |
Family
ID=56804808
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620396056.8U Active CN205549689U (en) | 2016-04-29 | 2016-04-29 | Multistage separator of profit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205549689U (en) |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106495084A (en) * | 2016-12-30 | 2017-03-15 | 郑佳丹 | A kind of self-adjustable sewage transport equipment of power and its mode of movement |
| CN106517402A (en) * | 2016-11-29 | 2017-03-22 | 森松（江苏）重工有限公司 | Tubular oil and water separation device |
| CN106587410A (en) * | 2016-12-14 | 2017-04-26 | 武汉海德新能源投资有限公司 | Oil-water separating device |
| CN107281779A (en) * | 2017-08-07 | 2017-10-24 | 山东钢铁股份有限公司 | A kind of solvent separation unit |
| CN107626117A (en) * | 2017-11-10 | 2018-01-26 | 大丰鑫源达化工有限公司 | A kind of organic solvent recovery device |
| CN108031147A (en) * | 2018-01-29 | 2018-05-15 | 世本（天津）环境技术有限公司 | A kind of Kitchen waste filtrate oil removing pot and its oil removing system |
| CN109607919A (en) * | 2018-12-27 | 2019-04-12 | 天津海普尔膜科技有限公司 | A kind of waste emulsified mixture high temperature breaking method |
| CN109748348A (en) * | 2019-03-06 | 2019-05-14 | 高桥金属制品（苏州）有限公司 | Liquid volume reduction makeup is set and energy-saving emission-reduction type machining water treatment system |
| CN109761429A (en) * | 2019-03-06 | 2019-05-17 | 高桥金属制品（苏州）有限公司 | Energy-saving emission-reduction type machining coolant liquid, cleaning solution utilization system and its application method |
| CN110642326A (en) * | 2019-10-12 | 2020-01-03 | 广州市绿森环保设备有限公司 | Oil-water separator in medicine extraction of pharmaceutical enterprises |
| CN111675363A (en) * | 2020-06-20 | 2020-09-18 | 张家港市欧微自动化研发有限公司 | Oil-water separation device and use method thereof |
| CN113082775A (en) * | 2021-03-31 | 2021-07-09 | 张田田 | Chemical solution separating tank |
| CN113184948A (en) * | 2021-04-19 | 2021-07-30 | 广东新宏泽包装股份有限公司 | Screw air compressor waste liquid recycling and environment-friendly treatment device and using method thereof |
| CN114768487A (en) * | 2022-05-07 | 2022-07-22 | 江苏凯美酷碳科技有限公司 | Circulating system for recycling solvent, performing gas-liquid separation and recycling wastewater and operating method thereof |
| CN116022979A (en) * | 2023-03-29 | 2023-04-28 | 深圳骏信环境科技有限公司 | Industrial wastewater treatment device |
-
2016
- 2016-04-29 CN CN201620396056.8U patent/CN205549689U/en active Active
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106517402A (en) * | 2016-11-29 | 2017-03-22 | 森松（江苏）重工有限公司 | Tubular oil and water separation device |
| CN106517402B (en) * | 2016-11-29 | 2023-04-28 | 森松（江苏）重工有限公司 | Tubular oil-water separator |
| CN106587410A (en) * | 2016-12-14 | 2017-04-26 | 武汉海德新能源投资有限公司 | Oil-water separating device |
| CN106495084B (en) * | 2016-12-30 | 2019-09-06 | 泰州程顺制冷设备有限公司 | A kind of self-adjustable sewage transport equipment of power and its mode of movement |
| CN106495084A (en) * | 2016-12-30 | 2017-03-15 | 郑佳丹 | A kind of self-adjustable sewage transport equipment of power and its mode of movement |
| CN107281779A (en) * | 2017-08-07 | 2017-10-24 | 山东钢铁股份有限公司 | A kind of solvent separation unit |
| CN107626117A (en) * | 2017-11-10 | 2018-01-26 | 大丰鑫源达化工有限公司 | A kind of organic solvent recovery device |
| CN108031147A (en) * | 2018-01-29 | 2018-05-15 | 世本（天津）环境技术有限公司 | A kind of Kitchen waste filtrate oil removing pot and its oil removing system |
| CN109607919A (en) * | 2018-12-27 | 2019-04-12 | 天津海普尔膜科技有限公司 | A kind of waste emulsified mixture high temperature breaking method |
| CN109761429A (en) * | 2019-03-06 | 2019-05-17 | 高桥金属制品（苏州）有限公司 | Energy-saving emission-reduction type machining coolant liquid, cleaning solution utilization system and its application method |
| CN109748348A (en) * | 2019-03-06 | 2019-05-14 | 高桥金属制品（苏州）有限公司 | Liquid volume reduction makeup is set and energy-saving emission-reduction type machining water treatment system |
| CN110642326A (en) * | 2019-10-12 | 2020-01-03 | 广州市绿森环保设备有限公司 | Oil-water separator in medicine extraction of pharmaceutical enterprises |
| CN111675363A (en) * | 2020-06-20 | 2020-09-18 | 张家港市欧微自动化研发有限公司 | Oil-water separation device and use method thereof |
| CN113082775A (en) * | 2021-03-31 | 2021-07-09 | 张田田 | Chemical solution separating tank |
| CN113184948A (en) * | 2021-04-19 | 2021-07-30 | 广东新宏泽包装股份有限公司 | Screw air compressor waste liquid recycling and environment-friendly treatment device and using method thereof |
| CN114768487A (en) * | 2022-05-07 | 2022-07-22 | 江苏凯美酷碳科技有限公司 | Circulating system for recycling solvent, performing gas-liquid separation and recycling wastewater and operating method thereof |
| CN114768487B (en) * | 2022-05-07 | 2023-11-21 | 江苏凯美酷碳科技有限公司 | Circulating system for solvent recovery gas-liquid separation and wastewater reuse and operation method thereof |
| CN116022979A (en) * | 2023-03-29 | 2023-04-28 | 深圳骏信环境科技有限公司 | Industrial wastewater treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205549689U (en) | Multistage separator of profit | |
| CN105268213B (en) | A kind of water-oil separating method and oil-water separator | |
| CN205627211U (en) | Automatic whirl coalescence water oil separating collection device | |
| CN101584945A (en) | A kind of gas-oil-water three-phase separating device | |
| CN112354262B (en) | Single-layer cavity full-gravity-balance oil-gas-water treatment integrated device | |
| CN201454168U (en) | Gas-oil-water three-phase separation device | |
| CN205917081U (en) | Mechanism is separated to unpowered profit | |
| CN103111098B (en) | Free drive moves on-line continuous dynamic oil air/water separator | |
| CN104341051B (en) | A kind of oil, water, mud are separated urn | |
| CN205699611U (en) | Ocean platform gravity type oil-gas-water separator | |
| CN201775987U (en) | Industrial oil-water separating system | |
| CN201747344U (en) | Oilfield injection water sedimentation filter | |
| CN105413238B (en) | A kind of oil water separator | |
| CN207468366U (en) | A kind of oily wastewater grease removal treatment device | |
| CN203264432U (en) | Environment-friendly unpowered oil-water separator | |
| CN201912795U (en) | Movable oil-water separation device for oil tank cleaning system | |
| CN2559790Y (en) | Horizontal-upward flow energy-saving oil-gas water sand separator | |
| CN205701819U (en) | Kitchen garbage grease pretreatment unit | |
| CN204294066U (en) | A kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation | |
| CN106369898A (en) | Guide barrel type oil adsorber and oil separating method thereof | |
| CN205055541U (en) | Separation chamber is collected to medicine waste residue | |
| CN204563686U (en) | Meal slag liquid gravity divides oily dyeing pot | |
| CN208275052U (en) | A kind of oil water separator | |
| CN102500136A (en) | Combined cylindrical oil-water cyclone separating device | |
| CN203235294U (en) | Drive-free online continuous dynamic oil-gas-water separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |