CN110104818A - Normal temperature and pressure coagulation type egg Shape Plate Separator - Google Patents
Normal temperature and pressure coagulation type egg Shape Plate Separator Download PDFInfo
- Publication number
- CN110104818A CN110104818A CN201910477766.1A CN201910477766A CN110104818A CN 110104818 A CN110104818 A CN 110104818A CN 201910477766 A CN201910477766 A CN 201910477766A CN 110104818 A CN110104818 A CN 110104818A
- Authority
- CN
- China
- Prior art keywords
- warehouse
- normal temperature
- conduit
- egg shape
- shape plate
- 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.)
- Pending
Links
- 238000005345 coagulation Methods 0.000 title claims abstract description 17
- 230000015271 coagulation Effects 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 239000006071 cream Substances 0.000 claims abstract description 19
- 239000003463 adsorbent Substances 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims description 10
- 239000002699 waste material Substances 0.000 claims description 8
- 238000004891 communication Methods 0.000 claims description 5
- 238000012423 maintenance Methods 0.000 claims description 5
- 238000010521 absorption reaction Methods 0.000 claims description 3
- 238000000926 separation method Methods 0.000 abstract description 4
- 239000003921 oil Substances 0.000 description 37
- 239000010865 sewage Substances 0.000 description 22
- 239000002351 wastewater Substances 0.000 description 4
- 239000012528 membrane Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000013019 agitation Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/42—Liquid level
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The invention discloses normal temperature and pressure coagulation type egg Shape Plate Separators, comprising: outer housing, water inlet pipe, outlet pipe, shoe cream room and the first warehouse being fixed in side by side inside outer housing, the second warehouse, third warehouse, the 4th warehouse, the 5th warehouse；First cyclone is set in the first warehouse；First warehouse is connected with the second warehouse by the first conduit；Second cyclone is set in the second warehouse；Be obliquely installed multiple parallel-plates on the side wall of third warehouse, multiple parallel-plates are parallel and adjacent parallel-plate between there are gaps；The adsorbent equipment of the internal filling cohesion medium of setting in 4th warehouse；Shoe cream room be placed in outer housing and the first warehouse, the second warehouse, third warehouse, the 4th warehouse, between the 5th warehouse.Oily-water seperating equipment treatment effeciency height, oil-water separation in the present invention is good, at low cost.
Description
Technical field
The present invention relates to technical field of sewage treatment equipment, more particularly to normal temperature and pressure coagulation type high efficiency oil-water
Separator.
Background technique
Contain greasy dirt in waste water caused by oil field and oil refining enterprise, is needed before waste discharge to the waste water with greasy dirt
Carry out water-oil separating processing.
The physics mode of common water-oil separating mainly takes the technologies such as high pressure, quick-fried oxygen, UF membrane at present.High pressure, quick-fried oxygen side
The higher cost of method, and high pressure is higher to the requirement standard of pressurized equipment and pressure vessel, and regular maintenance cost is higher, uses
Service life is shorter.Membrane separating method is because for oil droplet in viscous pasty state, easily blocking film is empty, and causes to Membrane cleaning larger in oily wastewater
It hinders, reduces the service efficiency of film, increase use cost.
Therefore, developing the oily-water seperating equipment that a kind for the treatment of effeciency is high, oil-water separation is good, at low cost is this field
The problem of technical staff's urgent need to resolve.
Summary of the invention
In view of this, the present invention provides a kind of normal temperature and pressure coagulation type high efficient oils that separation is thorough, high-efficient, at low cost
Water separation device.
To achieve the goals above, the present invention adopts the following technical scheme:
Normal temperature and pressure coagulation type egg Shape Plate Separator, comprising: outer housing, water inlet pipe, outlet pipe, shoe cream room and simultaneously
Row is fixed on the first warehouse, the second warehouse, third warehouse, the 4th warehouse, the 5th warehouse inside the outer housing；
The water inlet pipe is placed in the outer housing close to the outside of first warehouse side, and with the first warehouse phase
Connection；
First cyclone is set in first warehouse, and the water inlet of first cyclone is connected with the water inlet pipe
It is logical；First warehouse is connected with second warehouse by the first conduit；
Second cyclone is set in second warehouse, and the water inlet of second cyclone is connected with first conduit
It is logical；
Multiple parallel-plates are obliquely installed on the side wall of the third warehouse, multiple parallel-plates are parallel and adjacent described
There are gaps between parallel-plate；The position that the third warehouse side wall connects the parallel-plate opens up multiple for liquid communication
First through hole；
The adsorbent equipment of the internal filling cohesion medium of setting, the adsorbent equipment fill the cohesion in 4th warehouse
The second through-hole for liquid communication is opened up on the side wall at medium position；Second is connected between 4th warehouse and the 5th warehouse
Conduit；
The outlet pipe is placed in the outer housing close to the outside of the 5th warehouse side, and with the 5th warehouse phase
Connection；
The shoe cream room is placed in the outer housing and first warehouse, the second warehouse, third warehouse, the 4th warehouse, the
Between five warehouses；First warehouse, the second warehouse, third warehouse, the 4th warehouse, the 5th warehouse are close to the side of the shoe cream room
Wall top opens up oil scupper, and is connected by first oil scupper with the shoe cream room.
Beneficial effect by adopting the above technical scheme is, by the first cyclone and the second cyclone to sewage in the present invention
High speed agitation is carried out, the oil droplet of bulky grain is made directly to float up to liquid level under the influence of centrifugal force, then makes sewage by multilayer
Parallel-plate changes the whirlpool of water flow formation, increases the contact area of smaller oil droplet, particulate matter, make 40 microns or more of oil
Drop cohesion is floated, and other impurities sedimentation, sewage passes through parallel-plate and then the absorption Jing Guo cohesion medium, can be by 15 microns
The absorption of the above oil droplet, realization Oil in Sewage Water drop is completely separated, the oil liquid to float in each warehouse can by oil scupper into
Enter into shoe cream room and the oil liquid isolated is recycled.
Preferably, switch valve is set at the water inlet pipe.The amount that the first warehouse can be passed through to sewage controls.
Preferably, water level sensor is arranged in the top of first warehouse and the 5th warehouse.Master control platform to separator into
Row control, and switch valve, water level sensor are connect with master control platform, and water level sensor is in the first warehouse and the second warehouse
Water level is detected, and the signal that will test is transferred to master control platform, and master control platform is according to the water level information detected, tune appropriate
Whole switch valve stablizes the flow velocity of sewage.
Preferably, first warehouse, the second warehouse, third warehouse, the 4th warehouse, be respectively provided with dimension at the top of the 5th warehouse
Repair window.Maintenance window can be top closed by each warehouse, prevents the entrance of dust and sundries.
Preferably, first warehouse, the second warehouse, third warehouse, the 4th warehouse, the 5th warehouse bottom it is tapered and
Offer the waste port for draining waste material.
Preferably, the adsorbent equipment includes: shell, the fixed frame for containing cohesion medium；The fixed frame is placed in
Handle is arranged in the top of the inside of the shell, the fixed frame.The setting of handle facilitates extracts fixed frame out from shell, right
Cohesion medium is replaced.
Preferably, third conduit is set in the 5th warehouse, and second conduit and third conduit are L-shaped, institute
The outlet end of the second conduit is stated towards the top of the 5th warehouse；One end of the third conduit is connected with the outlet pipe
Logical, the other end is towards the bottom of the 5th warehouse.The setting of second conduit outlet end and third conduit feed liquor end opening direction,
It can guarantee that sewage stops 8-10 minutes in separator, guarantee the steady of effluent flow rate, separate sewage more thorough.
Preferably, inclined upward of the parallel-plate towards the 4th warehouse, the inclined direction of the parallel-plate and court
It is in 30 ° of angles to the horizontal line of the 4th warehouse.Parallel-plate inclination, the interstitial velocity that sewage is passed through between parallel-plate can slow down,
The contact area that oil droplet can be increased makes oil droplet preferably build up floating.
Preferably, the bottom of the shoe cream room opens up oil discharge outlet.
Preferably, hanging ring is arranged in the four corners at the top of the outer housing.The setting of hanging ring conveniently pass through lifting equipment to point
It is lifted from device.
It can be seen via above technical scheme that compared with prior art, it is solidifying that the present disclosure provides a kind of normal temperature and pressures
Poly- formula egg Shape Plate Separator, it has the advantage that:
It (1) can be with to sewage, multilayer parallel plate and cohesion medium by the first cyclone, the second cyclone in the present invention
15 microns or more oil droplets are separated, are adsorbed, impurity sedimentation can remove in oily wastewater 96% or more oil droplet and miscellaneous
Matter has reached the standard of national water injection；
(2) the first warehouse, the second warehouse, third warehouse, the 4th warehouse, the oil droplet warp built up in the 5th warehouse in the present invention
It crosses oil scupper to enter in shoe cream room, the oil in sewage is recycled；
(3) separator in the present invention uses under room temperature, normal pressure, to device without excessive wear, in processing engineering
It does not need additionally to heat or increase mechanical device progress high speed agitation, treatment effeciency is higher, cost is relatively low.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
The embodiment of invention for those of ordinary skill in the art without creative efforts, can also basis
The attached drawing of offer obtains other attached drawings.
Fig. 1 attached drawing is the main view of separator internal structure provided by the invention；
Fig. 2 attached drawing is the left view of separator provided by the invention；
Fig. 3 attached drawing is the right view of separator provided by the invention；
Fig. 4 attached drawing is the top view of separator provided by the invention.
Wherein, in figure,
1- outer housing；2- water inlet pipe；3- outlet pipe；
4- shoe cream room；
41- oil scupper；42- oil discharge outlet；
The first warehouse of 5-；
The first cyclone of 51-；The first conduit of 52-；
The second warehouse of 6-；
The second cyclone of 61-；
7- third warehouse；
71- parallel-plate；
The 4th warehouse of 8-；
81- adsorbent equipment；
811- shell；812- fixed frame；813- cohesion medium；814- handle；
The 5th warehouse of 9-；
The second conduit of 91-；92- third conduit；
10- switch valve；11- water level sensor；12- maintenance window；13- waste port；14- hanging ring.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
The embodiment of the invention discloses normal temperature and pressure coagulation type egg Shape Plate Separators, comprising: outer housing 1, water inlet pipe
2, outlet pipe 3, shoe cream room 4 and the first warehouse 5 being fixed in side by side inside outer housing 1, the second warehouse 6, third warehouse 7,
Four warehouses 8, the 5th warehouse 9；Water inlet pipe 2 is placed in outer housing 1 close to the outside of 5 side of the first warehouse, and is connected with the first warehouse 5
It is logical；First cyclone 51 is set in first warehouse 5, the water inlet of the first cyclone 51 is connected with water inlet pipe 2；First warehouse 5
It is connected with the second warehouse 6 by the first conduit 52；Second cyclone 61 is set in second warehouse 6, the second cyclone 61 into
The mouth of a river is connected with the first conduit 52；Multiple parallel-plates 71 are obliquely installed on the side wall of third warehouse 7, multiple parallel-plates 71 are equal
There are gaps between capable and adjacent parallel-plate 71；The position of 7 side wall of third warehouse connection parallel-plate 71 opens up multiple for liquid
The first through hole of circulation；The adsorbent equipment 81 of interior internal filling cohesion Jie 813 of setting of 4th warehouse 8, the filling of adsorbent equipment 81 are solidifying
The second through-hole for liquid communication is opened up on the side wall at poly- 813 position of medium；It is connected between 4th warehouse 8 and the 5th warehouse 9
Second conduit 91；Outlet pipe 3 is placed in outer housing 1 close to the outside of 9 side of the 5th warehouse, and is connected with the 5th warehouse 9；Oil storage
Chamber 4 be placed in outer housing 1 and the first warehouse 5, the second warehouse 6, third warehouse 7, the 4th warehouse 8, between the 5th warehouse 9；First storehouse
Room 5, the second warehouse 6, third warehouse 7, the 4th warehouse 8, the 5th warehouse 9 open up oil scupper close to the side wall upper part of shoe cream room 4
41, and be connected by oil scupper 41 with shoe cream room 4.
In order to further optimize the above technical scheme, switch valve 10 is set at water inlet pipe 2, and switch valve 10 selects motor switch
Valve.
In order to further optimize the above technical scheme, water level sensor is arranged in the top of the first warehouse 5 and the 5th warehouse 9
11, water level sensor 11 also can be set in the 4th warehouse 8 in the second warehouse 6, third warehouse 7, makes the water level detecting of each warehouse more
What is added is accurate.
In order to further optimize the above technical scheme, the first warehouse 5, the second warehouse 6, third warehouse 7, the 4th warehouse 8,
The top of five warehouses 9 is respectively provided with maintenance window 12.
In order to further optimize the above technical scheme, the first warehouse 5, the second warehouse 6, third warehouse 7, the 4th warehouse 8,
The bottom of five warehouses 9 is tapered and offers waste port 13 for draining waste material.
In order to further optimize the above technical scheme, adsorbent equipment 81 includes: shell 811, for containing cohesion medium 813
Fixed frame 812；Fixed frame 812 is placed in the inside of shell 811, and handle 814 is arranged in the top of fixed frame 812.
In order to further optimize the above technical scheme, as shown in Figure 1, third conduit 92 is arranged in the 5th warehouse 9, second leads
Pipe 91 and third conduit 92 are L-shaped, the top of outlet end the 5th warehouse 9 of direction of the second conduit 91；Third conduit 92
One end is connected with outlet pipe 3, the bottom of the other end the 5th warehouse 9 of direction.
In order to further optimize the above technical scheme, as shown in Figure 1, parallel-plate 71 towards the 4th warehouse 8 inclined upward,
The horizontal line of the 4th warehouse 8 of inclined direction and direction of parallel-plate 71 is in 30 ° of angles.
In order to further optimize the above technical scheme, the bottom of shoe cream room 4 opens up oil discharge outlet 42.
In order to further optimize the above technical scheme, hanging ring 14 is arranged in the four corners at 1 top of outer housing.
The course of work: sewage is entered in the first cyclone 51 by water inlet pipe 2, and sewage carries out in the first cyclone 51
High speed rotation builds up biggish oil droplet and floats, and then the sewage in the first warehouse 5 is flowed into the second rotation by the first conduit 52
In stream device 61 sewage is subjected to high-speed stirred again, makes to build up compared with larger oil droplet and float, passed through by the sewage of the second cyclone 61
First through hole enters between multilayer parallel plate 71, and movement speed of the sewage between parallel-plate 71 is slow, keeps oil droplet more abundant
Accumulation float, entered in the 4th warehouse 8 by the sewage of parallel-plate 71, sewage is entered cohesion and is situated between by the second through-hole
In matter 813, cohesion medium 813 adsorbs the oil droplet greater than 15 microns, and the sewage by cohesion medium 813 is led by second
Pipe 91 enters in the 5th warehouse 9, and the sewage in the 5th warehouse 9 is discharged by third conduit 92 from outlet pipe 3.First warehouse
5, the second warehouse 6, third warehouse 7, the 4th warehouse 8, the oil droplet in the 5th warehouse 9 float on the water surface, by oil scupper 41 into
Enter into oil-discharging cavity 4, the oil liquid isolated is collected.
Each embodiment in this specification is described in a progressive manner, the highlights of each of the examples are with other
The difference of embodiment, the same or similar parts in each embodiment may refer to each other.
The foregoing description of the disclosed embodiments enables those skilled in the art to implement or use the present invention.
Various modifications to these embodiments will be readily apparent to those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, of the invention
It is not intended to be limited to the embodiments shown herein, and is to fit to and the principles and novel features disclosed herein phase one
The widest scope of cause.
Claims (10)
1. normal temperature and pressure coagulation type egg Shape Plate Separator characterized by comprising outer housing (1), water inlet pipe (2), water outlet
It manages (3), shoe cream room (4) and is fixed in internal the first warehouse (5) of the outer housing (1), the second warehouse (6), third side by side
Warehouse (7), the 4th warehouse (8), the 5th warehouse (9)；
The water inlet pipe (2) is placed in the outside of the outer housing (1) close to the first warehouse (5) side, and with described first
Warehouse (5) is connected；
The first cyclone (51) are set in first warehouse (5), the water inlet of first cyclone (51) and the water inlet
Pipe (2) is connected；First warehouse (5) is connected with second warehouse (6) by the first conduit (52)；
The second cyclone (61) are set in second warehouse (6), the water inlet and described first of second cyclone (61)
Conduit (52) is connected；
Be obliquely installed multiple parallel-plates (71) on the side wall of the third warehouse (7), multiple parallel-plates (71) it is parallel and
There are gaps between the adjacent parallel-plate (71)；It opens the position that third warehouse (7) side wall connects the parallel-plate (71)
If multiple first through hole for liquid communication；
The adsorbent equipment (81) of internal filling cohesion medium (813) of setting, the adsorbent equipment (81) in 4th warehouse (8)
Fill the second through-hole opened up on the side wall at the cohesion medium (813) position for liquid communication；4th warehouse (8) with
The second conduit (91) are connected between 5th warehouse (9)；
The outlet pipe (3) is placed in the outside of the outer housing (1) close to the 5th warehouse (9) side, and with the described 5th
Warehouse (9) is connected；
The shoe cream room (4) be placed in the outer housing (1) and first warehouse (5), the second warehouse (6), third warehouse (7),
Between 4th warehouse (8), the 5th warehouse (9)；First warehouse (5), the second warehouse (6), third warehouse (7), the 4th warehouse
(8), side wall upper part of the 5th warehouse (9) close to the shoe cream room (4) opens up oil scupper (41), and passes through the oil scupper
(41) it is connected with the shoe cream room (4).
2. normal temperature and pressure coagulation type egg Shape Plate Separator according to claim 1, which is characterized in that the water inlet pipe
(2) switch valve (10) are set at.
3. normal temperature and pressure coagulation type egg Shape Plate Separator according to claim 1 or 2, which is characterized in that described
Water level sensor (11) are arranged in the top of one warehouse (5) and the 5th warehouse (9).
4. normal temperature and pressure coagulation type egg Shape Plate Separator according to claim 3, which is characterized in that first storehouse
Room (5), third warehouse (7), the 4th warehouse (8), is respectively provided with maintenance window (12) at the top of the 5th warehouse (9) at the second warehouse (6).
5. normal temperature and pressure coagulation type egg Shape Plate Separator according to claim 4, which is characterized in that first storehouse
Room (5), the second warehouse (6), third warehouse (7), the 4th warehouse (8), the bottom of the 5th warehouse (9) are tapered and offer and be used for
Drain the waste port (13) of waste material.
6. normal temperature and pressure coagulation type egg Shape Plate Separator according to claim 1, which is characterized in that the absorption dress
Setting (81) includes: shell (811), the fixed frame (812) for containing cohesion medium (813)；The fixed frame (812) is placed in institute
The inside of shell (811) is stated, handle (814) are arranged in the top of the fixed frame (812).
7. -2, the described in any item normal temperature and pressure coagulation type egg Shape Plate Separators of 4-6, feature exist according to claim 1
In, third conduit (92) are set in the 5th warehouse (9), second conduit (91) and third conduit (92) are L-shaped,
The outlet end of second conduit (91) is towards the top of the 5th warehouse (9)；One end of the third conduit (92) and institute
It states outlet pipe (3) to be connected, the other end is towards the bottom of the 5th warehouse (9).
8. -2, the described in any item normal temperature and pressure coagulation type egg Shape Plate Separators of 4-6, feature exist according to claim 1
In, inclined upward of the parallel-plate (71) towards the 4th warehouse (8), the inclined direction and direction of the parallel-plate (71)
The horizontal line of 4th warehouse (8) is in 30 ° of angles.
9. normal temperature and pressure coagulation type egg Shape Plate Separator according to claim 8, which is characterized in that the shoe cream room
(4) bottom opens up oil discharge outlet (42).
10. normal temperature and pressure coagulation type egg Shape Plate Separator according to claim 9, which is characterized in that the shell
Hanging ring (14) are arranged in four corners at the top of body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910477766.1A CN110104818A (en) | 2019-06-03 | 2019-06-03 | Normal temperature and pressure coagulation type egg Shape Plate Separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910477766.1A CN110104818A (en) | 2019-06-03 | 2019-06-03 | Normal temperature and pressure coagulation type egg Shape Plate Separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110104818A true CN110104818A (en) | 2019-08-09 |
Family
ID=67493602
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910477766.1A Pending CN110104818A (en) | 2019-06-03 | 2019-06-03 | Normal temperature and pressure coagulation type egg Shape Plate Separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110104818A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2533953A1 (en) * | 2006-01-25 | 2007-07-25 | 958698 Alberta Ltd. | Fluid treatment process and apparatus |
| CN104671487A (en) * | 2013-11-27 | 2015-06-03 | 中国石油化工股份有限公司 | Water diversion purification plant and purification method thereof |
| CN105152265A (en) * | 2015-07-29 | 2015-12-16 | 杭州科瑞特环境技术有限公司 | Composite coalescence type oil-water separation device and method |
| CN107540049A (en) * | 2017-09-22 | 2018-01-05 | 刘超 | A kind of oil-polluted water separator |
| CN207468255U (en) * | 2017-11-14 | 2018-06-08 | 青岛百利达环保科技有限公司 | A kind of Horizontal oil-water separator |
| CN210559689U (en) * | 2019-06-03 | 2020-05-19 | 张�杰 | Normal temperature and pressure condensation type high-efficiency oil-water separation device |
-
2019
- 2019-06-03 CN CN201910477766.1A patent/CN110104818A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2533953A1 (en) * | 2006-01-25 | 2007-07-25 | 958698 Alberta Ltd. | Fluid treatment process and apparatus |
| CN104671487A (en) * | 2013-11-27 | 2015-06-03 | 中国石油化工股份有限公司 | Water diversion purification plant and purification method thereof |
| CN105152265A (en) * | 2015-07-29 | 2015-12-16 | 杭州科瑞特环境技术有限公司 | Composite coalescence type oil-water separation device and method |
| CN107540049A (en) * | 2017-09-22 | 2018-01-05 | 刘超 | A kind of oil-polluted water separator |
| CN207468255U (en) * | 2017-11-14 | 2018-06-08 | 青岛百利达环保科技有限公司 | A kind of Horizontal oil-water separator |
| CN210559689U (en) * | 2019-06-03 | 2020-05-19 | 张�杰 | Normal temperature and pressure condensation type high-efficiency oil-water separation device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA1174180A (en) | Coolant recovery system | |
| AU621143B2 (en) | Centrifuge processor and liquid level control system | |
| US4483774A (en) | Oil concentrating method and apparatus | |
| US2710071A (en) | Horizontal separator for mixed fluids | |
| US4233154A (en) | Method for treating petroleum well pumping power fluid | |
| CN107162239A (en) | Eddy flow agglomerated air floatation removes oil column | |
| JP4406521B2 (en) | A device that collects substances floating in certain water areas | |
| US20090039003A1 (en) | Single-Cell Mechanical Flotation System | |
| NO761656L (en) | ||
| CN207012610U (en) | A kind of oil water separator in garlic flavor oil manufacturing process | |
| CN110104818A (en) | Normal temperature and pressure coagulation type egg Shape Plate Separator | |
| CN107721016A (en) | A kind of oil-polluted water grease removal treatment device and processing method | |
| CN208436470U (en) | A kind of filter separator being centrifuged dirt collection | |
| CN210559689U (en) | Normal temperature and pressure condensation type high-efficiency oil-water separation device | |
| CN106006840A (en) | Industrial circulating water online oil monitoring and oil removal device | |
| CN207259250U (en) | Eddy flow agglomerated air floatation removes oil column | |
| CN205856055U (en) | A kind of industrial circulating water is at the monitoring of tape oil, degreasing unit | |
| CN2550026Y (en) | Combined oil and water separator of cyclone hydraulic jet flow coarse graining | |
| CN108946865A (en) | A kind of chemical machinery oil-liquid separator | |
| CN212347807U (en) | Oil-water separation device with flow adjusting function | |
| CN109011711B (en) | Kitchen wastewater oil-water separation tank | |
| CN209618943U (en) | Oil-water separation system | |
| CN106745502A (en) | A kind of sump oil water separation device | |
| SE428429B (en) | GRAVITATION SEPARATOR FOR NON-MIXABLE WETS, EXTING OIL AND WATER | |
| CN206621830U (en) | A kind of cutting lubricant water separation device |
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 |