CN110496420A - A kind of continous way oily water separating equipment - Google Patents
A kind of continous way oily water separating equipment Download PDFInfo
- Publication number
- CN110496420A CN110496420A CN201910760555.9A CN201910760555A CN110496420A CN 110496420 A CN110496420 A CN 110496420A CN 201910760555 A CN201910760555 A CN 201910760555A CN 110496420 A CN110496420 A CN 110496420A
- Authority
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- China
- Prior art keywords
- water
- oil
- main cylinder
- taper
- oil separating
- 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.)
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 61
- 239000004519 grease Substances 0.000 claims abstract description 14
- 238000003780 insertion Methods 0.000 claims abstract description 7
- 230000037431 insertion Effects 0.000 claims abstract description 7
- 238000005192 partition Methods 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims description 14
- 239000010865 sewage Substances 0.000 claims description 7
- 238000000926 separation method Methods 0.000 abstract description 13
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 12
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 235000019198 oils Nutrition 0.000 description 40
- 235000019476 oil-water mixture Nutrition 0.000 description 19
- 230000000694 effects Effects 0.000 description 7
- 239000002351 wastewater Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 239000000446 fuel Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000002955 isolation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0217—Separation of non-miscible liquids by centrifugal force
Landscapes
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Centrifugal Separators (AREA)
Abstract
The invention discloses a kind of continous way oily water separating equipments, including main cylinder；Upper cover is equipped at the top of the main cylinder, bottom is equipped with lower head；The center of the upper cover is equipped with the feed pipe inside insertion main cylinder, and the upper cover is equipped with anti-tracheae；The main cylinder bottom is equipped with taper water-oil separating bucket；In the middle part of the feed pipe insertion taper water-oil separating bucket, charging bottom of the tube is equipped with centrifugal distributor；It is equipped with grease partition between the taper water-oil separating bucket outer wall and main cylinder, the region between main cylinder and taper water-oil separating bucket is separated into water collecting region and oil collection area；The taper water-oil separating bucket bottom is equipped with the low opening for leading to water collecting region, and the high opening for leading to oil collection area is equipped at the top of taper water-oil separating bucket.The present invention reduces energy consumption using the pressure of methanol liquefaction system as the power of oily water separating equipment, and the design of centrifugal distributor keeps water-oil separating more efficient, and the design of taper water-oil separating bucket keeps oil-water separation more preferable.
Description
Technical field
The present invention relates to oily water separation technique field more particularly to a kind of continous way oily water separating equipments.
Background technique
In methanol liquefaction system in existing oily water separating equipment, according to oil does not dissolve in water, and density is less than water, utilizes
Its is not soluble in water, and density is less than the property of water, and the existing many applications of water-oil separating are carried out by the way of settle and separate, however
Separating effect and separative efficiency still need to improve.It is general using the method for forcing centrifugation in order to accelerate water-oil separating, i.e., it is logical
Crossing increase external impetus makes oil water mixture generate centrifugal action, this undoubtedly increases energy consumption；Or use this dynamic of rotor
Component easily breaks down.
A kind of gas and water that China Patent No. is 201620123836.5, oil separating device, including gas-liquid separation zone, grease
Disengagement zone, oil product collecting tank and waste water collection tank, it is characterised in that: the inlet porting on the separator is condensed from gas-liquid
The gas-liquid phase mixture of device enters the gas-liquid separation zone of the separator by pipeline and entrance, in gas-liquid separation zone and grease point
From isolation board is arranged between area, isolation board is inclined-plane, and one end close to inlet is slightly higher, and there are skies in the side tilted down
Gap, water-oil separating area upper layer are reserve, and lower layer is storage area, and reserve and storage area automatically form oil water surface；Every
There is no the lower end setting oil product collecting tank of gap side and waste water collection tank from plate, oil product collecting tank is by overflow weir, bottom plate, grease
Semi enclosed area is collectively formed in baffle, and in addition grease baffle top is fixed with ramp separates plate, and pipe is arranged in the bottom of oil product collecting tank
Road is connect with storage tank；Waste water outflow weir or waste water outflow pipe, bottom end setting outlet is arranged in waste water collection tank import.By using more
The mode of a subregion and balance pressure, based on the principle of standing come oil-water separation mixture, although certain effect can be obtained,
But the efficiency of its separation is difficult to be guaranteed.
China Patent No. be 201310010162.9 a kind of oil water separator, including inhalant region, Disengagement zone, oil collecting zone and
Exhalant region；Water inlet distribution pipe is equipped in the inhalant region；The inhalant region and Disengagement zone are isolated by baffle and overflow weir；The gear
The upper half of tank body ontology is connected at the top of the arc of plate, the top center of baffle is equipped with semi-circular through hole；The overflow weir
Curved bottom be connected to the lower half of tank body ontology, the bottom centre position of overflow weir is equipped with semi-circular through hole；The separation
Area is equipped with nitrogen gas stirring pipe；The Disengagement zone is isolated with the oil collecting zone by fuel-displaced weir；The oil collecting zone passes through with exhalant region
Oil baffle and effluent weir separate；The upper half of tank body ontology is connected at the top of the arc of the oil baffle；The arcuate bottom of the effluent weir
Portion connects the lower half of tank body ontology, and the bottom centre position of effluent weir is equipped with semi-circular through hole；The end of the water inlet distribution pipe
End is equipped with the first transverse tube；Dispensing orifice is uniformly arranged in the bottom of first transverse tube；The fuel-displaced weir and the oil baffle are constituted
The oil collecting zone；The fuel-displaced weir is L-shaped.Oily wastewater flows into inhalant region by water inlet distribution pipe, passes through baffle and overflow weir flow
Enter Disengagement zone, oil droplet floats to assemble in Disengagement zone forms certain thickness light oil layer, collects light oil by oil collecting zone, water phase is then led to
Oil baffle is crossed, enters exhalant region through effluent weir jacking, the final separation for realizing water and light oil.The invention is equally to use to stand
Principle, Lai Shixian water-oil separating, efficiency cannot ensure.
China Patent No. is a kind of 201210002763.0 centrifugal oil-water separators, including pallet, stem, outer cylinder, cover
Shell and the rotor that can be rotated in outer cylinder relative to stem, pallet, stem and outer cylinder are an entirety, and rotor is placed on stem,
It is placed between stem and outer cylinder；Housing covers in the outside of outer cylinder, and is bolted on pallet, is allowed to constitute an envelope
Close inner cavity；Rotor is constituted by cylinder and from the pillar filter of cylinder body bottom protrusion, and the cylinder body bottom periphery of rotor is equipped with
The inner cavity of nozzle, pillar filter is communicated by nozzle with the inner cavity of outer cylinder；Stem is equipped with import, and pallet is equipped with water outlet
Mouthful, housing is equipped with oil outlet；Entrance is equipped with heater, is respectively equipped with filter screen on the middle part of stem and outer cylinder.It has used
Complete mechanical mode is effectively separated grease, and without adding any chemical agent, structure is simple, easy to operate, the row of reduction
It puts；High pressure oil water mixture, which impinges upon, generates reaction force on outer cylinder, make rotor high speed rotation, thus by the small liquid of oil water mixture
Drop is sufficiently broken, and oil water mixture is made to become suspension by emulsifying, then under the effect of gravity, grease voluntarily precipitation and separation,
Whole device is inputted without any power, energy-saving and emission-reduction.The pressure of high pressure oil water mixture itself is utilized as dynamic in the program
Power has energy-efficient effect, when high pressure oil water mixture enters in rotor, drives rotor to rotate and passes through after pillar filter again
It is projected by nozzle, on the pressure rotary power that a part is consumed in rotor in transmission of high pressure oil water mixture, one
Dividing is consumed by pillar filter, and in the case where no external power supply, the pressure of high pressure oil water mixture is multiple
Consumption and waste, so that oil-water separation is bad, are unable to reach good separating effect, while oil water mixture is not special
Flow through channel, be directly entered in rotor region make it is various it is invalid shock can equally consume many energy, to affect oil
The effect of water separation.
Summary of the invention
There is provided that a kind of structure is simple, cost it is an object of the invention to overcome the deficiencies in the prior art described above place
A kind of low, energy-efficient continous way oily water separating equipment.
The present invention realizes in the following way:
A kind of continous way oily water separating equipment, including main cylinder；Upper cover is equipped at the top of the main cylinder, bottom is equipped with down
End socket；The center of the upper cover is equipped with the feed pipe inside insertion main cylinder, it is characterised in that: the upper cover is equipped with anti-
Tracheae；The main cylinder bottom is equipped with taper water-oil separating bucket；In the middle part of the feed pipe insertion taper water-oil separating bucket, feed pipe
Bottom is equipped with centrifugal distributor；Grease partition is equipped between the taper water-oil separating bucket outer wall and main cylinder by main cylinder
Region between taper water-oil separating bucket is separated into water collecting region and oil collection area；The taper water-oil separating bucket bottom is equipped with
Lead to the low opening of water collecting region, the high opening for leading to oil collection area is equipped at the top of taper water-oil separating bucket.
Further, the taper water-oil separating bucket is arranged in up-small and down-big form in main cylinder bottom.
Further, water collecting region bottom is equipped with outlet pipe, is provided with outlet valve on outlet pipe；The water collecting region
Inside it is provided with water level sensor.
Further, the bottom of the taper water-oil separating bucket is equipped with sewage pipe, is provided with blowdown valve on sewage pipe.
Further, the oil collection area bottom is equipped with flowline, and flowline has delivery valve；The oil collection area
Inside it is provided with fuel level sensor.
Further, the centrifugal distributor includes flange plate and flow guiding disc；The flange plate is sealed in water conservancy diversion
Above disk；The center of the flange plate is equipped with deflector hole；The central bus slot of the inside of the flow guiding disc from center is outside
Extend a plurality of material guiding groove in divergent shape；In the outermost end and flow guiding disc circumference of the material guiding groove tangentially
The outlet of direction setting communicates, and the outlet is round nozzle；The deflector hole is connected with central bus slot.
Further, the flange plate be circumferentially with it is multiple for the flange holes fixed with flow guiding disc.
Further, the width of the material guiding groove becomes larger outward along central bus slot.
Further, the material guiding groove is eight, and corresponding outlet is eight.
The beneficial effects of the present invention are: the present invention using the pressure of methanol liquefaction system as the power of oily water separating equipment,
Reduce energy consumption；The design of centrifugal distributor keeps water-oil separating more efficient；The design of taper water-oil separating bucket makes grease point
It is more preferable from effect.
Detailed description of the invention
Fig. 1 main view sectional view of the present invention；
Fig. 2 left view sectional view of the present invention；
The centrifugal distributor stereoscopic schematic diagram of Fig. 3 present invention；
The centrifugal distributor top view of Fig. 4 present invention；
Fig. 5 flow guiding disc main view of the present invention；
Fig. 6 flow guiding disc top view of the present invention；
Specific embodiment
To keep the purposes, technical schemes and advantages of embodiment of the present invention clearer, implement below in conjunction with the present invention
The technical solution in embodiment of the present invention is clearly and completely described in attached drawing in mode, it is clear that described reality
The mode of applying is some embodiments of the invention, rather than whole embodiments.Based on the embodiment in the present invention, ability
Domain those of ordinary skill every other embodiment obtained without creative efforts, belongs to the present invention
The range of protection.Therefore, the detailed description of the embodiments of the present invention provided in the accompanying drawings is not intended to limit below and is wanted
The scope of the present invention of protection is sought, but is merely representative of selected embodiment of the invention.Based on the embodiment in the present invention,
Every other embodiment obtained by those of ordinary skill in the art without making creative efforts belongs to this
Invent the range of protection.
In the description of the present invention, it should be noted that term " on ", "lower", "inner", "outside" " front end ", " rear end ",
The orientation or positional relationship of the instructions such as " both ends ", " one end ", " other end " is to be based on the orientation or positional relationship shown in the drawings, only
It is that for the convenience of describing the present invention and simplifying the description, rather than the device or element of indication or suggestion meaning must have specifically
Orientation is constructed and operated in a specific orientation, therefore is not considered as limiting the invention.In addition, term " first ", " the
Two " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " installation " " is set
Have ", " connection " etc., shall be understood in a broad sense, such as " connection ", may be a fixed connection, may be a detachable connection, or one
Ground connection；It can be mechanical connection, be also possible to be electrically connected；It can be directly connected, the indirect phase of intermediary can also be passed through
Even, it can be the connection inside two elements.For the ordinary skill in the art, can be understood with concrete condition above-mentioned
The concrete meaning of term in the present invention.
Embodiment:
As shown in figures 1 to 6, a kind of continous way oily water separating equipment, including main cylinder 20；It is equipped at the top of the main cylinder 20
Upper cover 18, bottom are equipped with lower head 19；20 upper and lower ends of main cylinder are welded with upper cover 18 and lower head 19 respectively.On described
The center of end socket 18 is equipped with the feed pipe 1 inside insertion main cylinder 20, it is characterised in that: the upper cover 18 is equipped with anti-tracheae
9；20 bottom of main cylinder is equipped with taper water-oil separating bucket 3；The feed pipe 1 is inserted into 3 middle part of taper water-oil separating bucket, charging
1 bottom of pipe is equipped with centrifugal distributor 2；Grease partition 8 is equipped between 3 outer wall of taper water-oil separating bucket and main cylinder 20
Region between main cylinder 20 and taper water-oil separating bucket 3 is separated into water collecting region 6 and oil collection area 7；The taper grease
3 bottom of separating barrel is equipped with the low opening 5 for leading to water collecting region 6, is equipped at the top of taper water-oil separating bucket 3 and leads to oil collection area 7
High opening 4.
Further, the taper water-oil separating bucket 3 is arranged in up-small and down-big form in 20 bottom of main cylinder.
Further, 6 bottom of water collecting region is equipped with outlet pipe 11, is provided with outlet valve 10 on outlet pipe 11；It is described
Water level sensor 16 is provided in water collecting region 6.
Further, the bottom of the taper water-oil separating bucket 3 is equipped with sewage pipe 15, is provided with blowdown valve on sewage pipe 15
14。
Further, 7 bottom of oil collection area is equipped with flowline 13, and flowline 13 has delivery valve 12；It is described
Fuel level sensor 17 is provided in oil collection area 7.
Further, the centrifugal distributor 2 includes flange plate 21 and flow guiding disc 22；The flange plate 21 seals
Above flow guiding disc 22；The center of the flange plate 21 is equipped with deflector hole 23；The inside of the flow guiding disc 22 is from center
Central bus slot 24 extends a plurality of material guiding groove 25 in divergent shape outward；The outermost end of the material guiding groove 25
It is communicated with the outlet 26 being arranged along a tangential direction on 22 circumference of flow guiding disc, the outlet 26 is round nozzle；The deflector hole 23
It is connected with central bus slot 24.
Further, the flange plate 21 be circumferentially with it is multiple for the flange holes 27 fixed with flow guiding disc 22.
Further, the width of the material guiding groove 25 becomes larger outward along central bus slot 24.
Further, the material guiding groove 25 is eight, and corresponding outlet 26 is eight.
Working principle: oil water mixture enters centrifugal distributor under the pressure of methanol liquefaction system, through feed pipe 1
2, centrifugal distributor 2 is located at the medium position of taper water-oil separating bucket 3, after oil water mixture comes out from centrifugal distributor 2
Into taper water-oil separating bucket 3, since oil does not dissolve in water, and oil density is lower than the density of water, therefore oil is concentrated and is enriched in taper
3 top of water-oil separating bucket, 3 top side of taper water-oil separating bucket set high opening 4, and oil overflows to oil collection area 7 from high opening 4；
The 3 lower part other side of taper water-oil separating bucket sets low opening 5, and water enters water collecting region 6 from low opening 5.Water level sensor 16 is used
It is switched in control outlet valve 10, guarantees peak level not higher than 3 top of taper water-oil separating bucket, lowest water level is not less than low opening
5 upper positions.Fuel level sensor 17 is not higher than 4 lower positions of high opening for controlling the switch of delivery valve 12, guarantee highest oil level,
Minimum oil level is not less than minimum oil level as defined in oil collection area 7.Outlet pipe 11, flowline 13 and sewage pipe 15 both pass through lower head
19 draw.
Oil water mixture enters inside flow guiding disc from the deflector hole 23 at 21 center of flange plate, deflector hole 23 and central bus
Slot 24 is connected, and oil water mixture disperses after reaching central bus slot 24 into eight material guiding grooves 25, and material guiding is recessed
The width of slot 25 becomes larger outward along central bus slot 24, can reduce the flow velocity of oil water mixture, reduces and hits generation
Energy loss sprays using the minor caliber circular nozzle of outlet 26, generates the oil water mixture fluid of high-voltage high-speed, due to going out
Mouth 26 is arranged along the tangent line of flow guiding disc 22, and the high-voltage high-speed oil water mixture ejected reaches taper water-oil separating bucket 3 after spraying
Inner wall, due to the blocking of 3 inner wall of taper water-oil separating bucket, oil water mixture forms rotation, generates centrifugal action, keeps grease quick
Separation.Water-oil separating is inputted without any power, energy-saving and emission-reduction.Reasonable in design, the pressure of oil water mixture is by abundant benefit
With not being wasted in the energy loss hit in the rotation or operation of flow guiding disc, the channel design that flows through of oil water mixture is closed
It manages and less energy can be lost to the greatest extent, improve water-oil separating efficiency.
The foregoing is merely the preferred embodiment of the present invention, are not intended to restrict the invention, for this field
For technical staff, the invention may be variously modified and varied.All within the spirits and principles of the present invention, made any
Modification, equivalent replacement, improvement etc., should all be included in the protection scope of the present invention.
Claims (9)
1. a kind of continous way oily water separating equipment, including main cylinder (20)；Upper cover (18) are equipped at the top of the main cylinder (20),
Bottom is equipped with lower head (19)；The center of the upper cover (18) is equipped with the internal feed pipe (1) of insertion main cylinder (20), special
Sign is: the upper cover (18) is equipped with anti-tracheae (9)；Main cylinder (20) bottom is equipped with taper water-oil separating bucket (3)；
In the middle part of feed pipe (1) insertion taper water-oil separating bucket (3), feed pipe (1) bottom is equipped with centrifugal distributor (2)；Institute
It states and is equipped with grease partition (8) between taper water-oil separating bucket (3) outer wall and main cylinder (20) for main cylinder (20) and taper grease
Region between separating barrel (3) is separated into water collecting region (6) and oil collection area (7)；Taper water-oil separating bucket (3) bottom is set
There is the low opening (5) for leading to water collecting region (6), the high opening for leading to oil collection area (7) is equipped at the top of taper water-oil separating bucket (3)
(4)。
2. a kind of continous way oily water separating equipment according to claim 1, it is characterised in that: the taper water-oil separating bucket
(3) it is arranged in up-small and down-big form in main cylinder (20) bottom.
3. a kind of continous way oily water separating equipment according to claim 1, it is characterised in that: water collecting region (6) bottom
Portion is equipped with outlet pipe (11), is provided with outlet valve (10) on outlet pipe (11)；Level sensor is provided in the water collecting region (6)
Device (16).
4. a kind of continous way oily water separating equipment according to claim 1, it is characterised in that: the taper water-oil separating bucket
(3) bottom is equipped with sewage pipe (15), is provided with blowdown valve (14) on sewage pipe (15).
5. a kind of continous way oily water separating equipment according to claim 1, it is characterised in that: oil collection area (7) bottom
Portion is equipped with flowline (13), and flowline (13) has delivery valve (12)；Oil level sensing is provided in the oil collection area (7)
Device (17).
6. a kind of continous way oily water separating equipment according to claim 1, it is characterised in that: the centrifugal distributor
It (2) include flange plate (21) and flow guiding disc (22)；The flange plate (21) is sealed in above flow guiding disc (22)；The flange
The center of cover board (21) is equipped with deflector hole (23)；The central bus slot (24) of the inside of the flow guiding disc (22) from center is outside
Extend a plurality of material guiding groove (25) in divergent shape；The outermost end of material guiding groove (25) and flow guiding disc (22)
The outlet (26) being arranged along a tangential direction on circumference communicates, and the outlet (26) is round nozzle；The deflector hole (23) is in
Heart collecting tray (24) is connected.
7. a kind of continous way oily water separating equipment according to claim 5, it is characterised in that: the flange plate (21)
It is circumferentially with multiple for the flange hole (27) fixed with flow guiding disc (22).
8. a kind of continous way oily water separating equipment according to claim 1, it is characterised in that: the material is oriented to groove
(25) width becomes larger outward along central bus slot (24).
9. a kind of continous way oily water separating equipment according to claim 1, it is characterised in that: the material is oriented to groove
It (25) is eight, corresponding outlet (26) is eight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910760555.9A CN110496420B (en) | 2019-08-16 | 2019-08-16 | Continuous oil-water separation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910760555.9A CN110496420B (en) | 2019-08-16 | 2019-08-16 | Continuous oil-water separation equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110496420A true CN110496420A (en) | 2019-11-26 |
| CN110496420B CN110496420B (en) | 2024-05-28 |
Family
ID=68588155
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910760555.9A Active CN110496420B (en) | 2019-08-16 | 2019-08-16 | Continuous oil-water separation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110496420B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114292694A (en) * | 2021-11-18 | 2022-04-08 | 重庆智青阳油脂有限公司 | Oil-water separator for Chinese prickly ash |
| CN115282744A (en) * | 2022-08-04 | 2022-11-04 | 合肥科安设备安装有限公司 | Natural gas recovery device |
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| WO2007054651A1 (en) * | 2005-11-09 | 2007-05-18 | Saipem S.A. | Multiphase liquid separating method and device |
| CN102225381A (en) * | 2011-04-11 | 2011-10-26 | 东北石油大学 | Co-rotating outflow internal-hole type high performance swirling separator |
| CN103566627A (en) * | 2013-10-30 | 2014-02-12 | 森松(江苏)海油工程装备有限公司 | Oil-water separating device |
| CN103922497A (en) * | 2014-04-14 | 2014-07-16 | 中国石油大学(华东) | Three-stage pressure-reducing V-shaped hydraulic cyclone air floatation device |
| CN210751403U (en) * | 2019-08-16 | 2020-06-16 | 新榕能源(福建)有限公司 | Continuous oil-water separation equipment |
-
2019
- 2019-08-16 CN CN201910760555.9A patent/CN110496420B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007054651A1 (en) * | 2005-11-09 | 2007-05-18 | Saipem S.A. | Multiphase liquid separating method and device |
| CN102225381A (en) * | 2011-04-11 | 2011-10-26 | 东北石油大学 | Co-rotating outflow internal-hole type high performance swirling separator |
| CN103566627A (en) * | 2013-10-30 | 2014-02-12 | 森松(江苏)海油工程装备有限公司 | Oil-water separating device |
| CN103922497A (en) * | 2014-04-14 | 2014-07-16 | 中国石油大学(华东) | Three-stage pressure-reducing V-shaped hydraulic cyclone air floatation device |
| CN210751403U (en) * | 2019-08-16 | 2020-06-16 | 新榕能源(福建)有限公司 | Continuous oil-water separation equipment |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114292694A (en) * | 2021-11-18 | 2022-04-08 | 重庆智青阳油脂有限公司 | Oil-water separator for Chinese prickly ash |
| CN114292694B (en) * | 2021-11-18 | 2024-02-20 | 重庆智青阳油脂有限公司 | Oil-water separator for pricklyash peel |
| CN115282744A (en) * | 2022-08-04 | 2022-11-04 | 合肥科安设备安装有限公司 | Natural gas recovery device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110496420B (en) | 2024-05-28 |
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