CN207566940U - Oil removing device - Google Patents
Oil removing device Download PDFInfo
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- CN207566940U CN207566940U CN201721134145.6U CN201721134145U CN207566940U CN 207566940 U CN207566940 U CN 207566940U CN 201721134145 U CN201721134145 U CN 201721134145U CN 207566940 U CN207566940 U CN 207566940U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 155
- 239000007788 liquid Substances 0.000 claims abstract description 72
- 238000006243 chemical reaction Methods 0.000 claims abstract description 29
- 238000009826 distribution Methods 0.000 claims description 28
- 238000005238 degreasing Methods 0.000 claims description 15
- 239000010802 sludge Substances 0.000 claims description 12
- 238000004891 communication Methods 0.000 claims description 3
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 238000000605 extraction Methods 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 26
- 239000010779 crude oil Substances 0.000 description 17
- 208000015943 Coeliac disease Diseases 0.000 description 8
- 239000000701 coagulant Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 230000008569 process Effects 0.000 description 6
- 230000001112 coagulating effect Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000012279 drainage procedure Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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- Removal Of Floating Material (AREA)
Abstract
The utility model discloses an oil removing device belongs to oil gas field extraction water treatment field. The device includes: the tank-shaped body, a water inlet pipe, a first oil outlet pipe, a second oil outlet pipe, a water outlet pipe, a pipeline mixer and a second liquid passing pipeline. The tank-shaped body is internally provided with a first deoiling area, a second deoiling area and a reaction area which are independent of each other. The entry end of inlet tube is located outside the tank body, and the exit end sets up in first except that oily district after passing second except that oily district. The outlet end of the first oil outlet pipe is positioned outside the tank-shaped body, and the inlet end of the first oil outlet pipe penetrates through the side wall of the tank-shaped body and then is arranged in a first oil removing area above the outlet end of the water inlet pipe. The outlet end of the second oil outlet pipe is positioned outside the tank-shaped body, and the inlet end of the second oil outlet pipe penetrates through the side wall of the tank-shaped body and then is arranged at the upper part of the second oil removing area. The inlet end of the water outlet pipe is communicated with the lower part of the second oil removing area, and the outlet end of the water outlet pipe is arranged outside the tank-shaped body. The oil removing device provided by the utility model has the advantages of small occupied area and low cost. And the operation flow is short, and the operation efficiency is higher.
Description
Technical field
The utility model is related to oil field gas field produced water treatment field, more particularly to a kind of degreasing unit.
Background technology
In exploitation of oil-gas field operation process, with being continuously increased for activity duration, the moisture content for producing crude oil constantly rises
Height, oil gas field generate a large amount of recovered water, which generally comprises：Water, crude oil and suspended matter.These recovered waters are directly outer to be arranged
Environmental pollution can be caused, it will cause formation contaminants for direct re-injection oil gas field.Therefore, it is necessary to remove the crude oil in recovered water.
The prior art completes the oil removing operation to recovered water by using multiple structures coordinating operations.It specifically, will be certainly
Right settling tank, coagulating setting tank, surge tank are sequentially connected with by pipeline, and recovered water are discharged into natural subsidence tank, make it certainly
Water-oil separating occurs, and precipitate the partial suspended thing of recovered water in right settling tank.Then, by the extraction after water-oil separating
Water is discharged into coagulating setting tank, and coagulant, flocculant are added in into coagulating setting tank, to increase suspended particle size, improves
The subsidence velocity of suspended matter, while strengthen oil-water separation.In the process, suspended matter is in natural subsidence tank and coagulant precipitation
Tank bottom is settled down in tank；The flowline discharge that crude oil is connected from the tank skin with natural subsidence tank and coagulating setting tank.Then, it will adopt
Water outlet is drained into surge tank, ensures the stable operation of follow-up equipment, at this point, completing to before recovered water progress subsequent job
Oil removing operation.
Designer has found that the prior art has at least the following problems：
The prior art needs, using multiple structures coordinating operations, to take up a large area in the crude oil in removing recovered water,
It is of high cost.Moreover, work flow is longer, operating efficiency is low.
Utility model content
In order to solve the above-mentioned technical problem it is, the utility model embodiment provides a kind of degreasing unit.Particular technique
Scheme is as follows：
The utility model embodiment provides a kind of degreasing unit, and described device includes：Can-like ontology, the can-like ontology
Inside it is provided with the first oil-removing area independent of each other, the second oil-removing area and reaction zone；
Water inlet pipe, it is external that arrival end is located at the can-like sheet, the port of export pass through be arranged on behind second oil-removing area it is described
In first oil-removing area；
First flowline, the port of export are located at that the can-like sheet is external, and arrival end is set after passing through the side wall of the can-like ontology
It puts in first oil-removing area above the water inlet pipe port of export；
Second flowline, the port of export are located at that the can-like sheet is external, and arrival end is set after passing through the side wall of the can-like ontology
It puts on the top of second oil-removing area；
Outlet pipe, arrival end are connected with the lower part of second oil-removing area, and it is external that the port of export is arranged on the can-like sheet；
First crosses liquid pipe line, and arrival end is located in first oil-removing area below the water inlet pipe port of export, the port of export
In the reaction zone, described first, which crosses liquid pipe line upper edge, crosses liquid direction and is sequentially arranged that there are two sprue and pipelines to mix
Device；
Second crosses liquid pipe line, and arrival end is connected with the reaction zone, and the port of export connects, and described with second oil-removing area
Second port of export for crossing liquid pipe line is located at the lower section of the second flowline arrival end.
Specifically, preferably, described device further includes：Outer cap body, Open Side Down, lower end and the bottom of the can-like ontology
Wall vertical connection；
First cylinder is sleeved on outside the outer cap body, and lower end is connect with the bottom wall of the can-like ontology；
First annular baffle, inner ring and outer rings connect respectively with the inner wall of the upper end of first cylinder and the can-like ontology
It connects；
The cavity that the can-like ontology, the outer cap body, first cylinder and the first annular baffle surround is formed
First oil-removing area；
The cavity that first cylinder, the first annular baffle and the can-like ontology surround forms second oil removing
Area；
The inner cavity of the outer cap body forms the reaction zone.
Specifically, preferably, described device further includes：Multiple perforated sludge discharge pipes connected in sequence；
Multiple perforated sludge discharge pipes extend transversely through first oil-removing area, second oil-removing area and the reaction zone
Lower part.
Specifically, preferably, being arranged with interior cap body, the lower end of the interior cap body and institute in the middle part of the inner cavity of the outer cap body
The first port of export connection for crossing liquid pipe line is stated, and closing is cooperatively formed in the middle part of the interior cap body and the inner cavity of the outer cap body
Annular space；
The side wall on the interior cap body top, the annular space of the closing bottom wall be in mesh structure；
Liquid pipe line is crossed with being located at below the annular space of the closing in the top of first cylinder by described second
The outer cap body connection；
Described device further includes：Multiple Vortex reactors are arranged in the annular space of the interior cap body and the closing.
Specifically, preferably, described device further includes：First water distribution system, the second water distribution system and collecting system；
First water distribution system is sleeved on the upper end of the outer cap body, and the port of export of arrival end and the water inlet pipe connects
It connects；
Second water distribution system is sleeved on the top of first cylinder, and arrival end crosses going out for liquid pipe line with described second
The connection of mouth end；
The collecting system is sleeved on the middle part of the outer cap body, and the arrival end that the port of export crosses liquid pipe line with described first connects
It connects.
Specifically, preferably, first water distribution system includes：It is sleeved on the first water distribution of the outer cap body upper end
Slot, with the port of export connected in sequence first of first water distributing trough with water conduit tube, the first range pipe and with described first
First horn mouth of two nozzles connection of range pipe, the arrival end of the port of export of the water inlet pipe and first water distributing trough
Connection；
Second water distribution system includes：It is sleeved on second water distributing trough on the first cylinder top, matches with described second
The port of export connected in sequence second of sink is with water conduit tube, the second range pipe and two with second range pipe
Second horn mouth of nozzle connection, the port of export that the arrival end of second water distributing trough crosses liquid pipe line with described second are connect；
The collecting system includes：It is sleeved on catch basin in the middle part of the outer cap body, suitable with the arrival end of the catch basin
Collection water conduit tube, collection branch pipe and the third horn mouth connected with two nozzles of the collection branch pipe of secondary connection, the collection
The arrival end that the port of export of sink crosses liquid pipe line with described first is connect.
Specifically, preferably, described device further includes：Snorkel inside first oil-removing area, across simultaneously
It is fixed on the first annular baffle；
The exhaust pipe being in communication with the outside is passed through and is fixed on the roof of the can-like ontology.
Specifically, preferably, described device further includes：Float apparatus for collecting oil, the arrival end with first flowline
Connection.
Specifically, preferably, described device further includes：First gate valve is arranged on the institute of the pipe-line mixer upstream
First is stated to cross on liquid pipe line；
First gate valve, be arranged on the pipe-line mixer downstream described first are crossed on liquid pipe line.
Specifically, preferably, being set with separator on first cylinder below second water distribution system；
The separator includes：Second cylinder and the second ring baffle；
Second barrel jacket has outside first cylinder between first cylinder and the can-like ontology
Spacing；
The inner ring and outer rings of second ring baffle respectively with the upper end of second cylinder and first cylinder
Outer wall connects.
The advantageous effect brought of technical solution that the utility model embodiment provides is：
The degreasing unit that the utility model embodiment provides, by setting can-like ontology, and sets that in can-like ontology
This first independent oil-removing area, the second oil-removing area, reaction zone and first flowline and the second flowline, and pass through the first mistake
Liquid pipe line connects the first oil-removing area with reaction zone, and crossing liquid pipe line by second connects the second oil-removing area with reaction zone, passes through
First flowline and the second flowline discharge the crude oil in recovered water in can-like ontology, and the oil extraction twice for realizing recovered water is made
Industry.By setting water inlet pipe, and the arrival end of the first flowline is arranged on to the top of the water inlet pipe port of export, both ensure that extraction
The normal discharge of water Crude Oil, and make that there is spacing between the arrival end of the first flowline and the port of export of water inlet pipe, for extraction
Water provides cushion space, it is ensured that stability hydraulic.Two sprues are sequentially arranged by being crossed on liquid pipe line first and pipeline mixes
Clutch, convenient for crossing injection coagulant and flocculant in liquid pipe line to first in operation process, accelerate suspended matter subsidence velocity and
Water-oil separating speed improves operating efficiency.Based on degreasing unit above-mentioned, that the utility model embodiment provides, not only take up an area face
Product is small, at low cost.And work flow is short, and operating efficiency is higher.
Description of the drawings
It is required in being described below to embodiment in order to illustrate more clearly of the technical scheme in the embodiment of the utility model
Attached drawing to be used is briefly described, it should be apparent that, the accompanying drawings in the following description is only some realities of the utility model
Example is applied, it for those of ordinary skill in the art, without creative efforts, can also be according to these attached drawings
Obtain other attached drawings.
Fig. 1 is the structure diagram for the degreasing unit that the utility model embodiment provides.
Reference numeral represents respectively：
1 can-like ontology,
2 first oil-removing areas,
3 second oil-removing areas,
4 reaction zones,
5 water inlet pipes,
6 first flowlines,
7 second flowlines,
8 outlet pipes,
9 first cross liquid pipe line,
10 pipe-line mixers,
11 second cross liquid pipe line,
12 outer cap bodies,
13 first cylinders,
14 first annular baffles,
15 perforated sludge discharge pipes,
Cap body in 16,
17 Vortex reactors,
18 first water distribution systems,
1801 first water distributing troughs,
1802 first match water conduit tube,
1803 first range pipes,
1804 first horn mouths,
19 second water distribution systems,
1901 second water distributing troughs,
1902 second match water conduit tube,
1903 second range pipes,
1904 second horn mouths,
20 collecting systems,
2001 catch basins,
2002 collection water conduit tubes,
2003 collection branch pipes,
2004 third horn mouths,
21 snorkels,
22 exhaust pipes,
23 float apparatus for collecting oil,
24 first gate valves,
25 second gate valves,
26 separators,
2601 second cylinders,
2602 second ring baffles.
Specific embodiment
It is new to this practicality below in conjunction with attached drawing to make the purpose of this utility model, technical solution and advantage clearer
Type embodiment is described in further detail.
It should be noted that recovered water is located in crude oil dehydrating plant, it, will water inlet before oil removing operation is carried out to recovered water
The arrival end of pipe 5 is connect with the water pipeline that comes of crude oil dehydrating plant.Also, suspended particle mentioned below is suspended in recovered water
A part for object.
The utility model embodiment provides a kind of degreasing unit, and as shown in Figure 1, which includes：Can-like ontology 1,
Water inlet pipe 5, the first flowline 6, the second flowline 7, outlet pipe 8, pipe-line mixer 10 and second cross liquid pipe line 11.Wherein, tank
The first oil-removing area 2 independent of each other, the second oil-removing area 3 and reaction zone 4 are provided in shape ontology 1.The arrival end of water inlet pipe 5 is located at
Outside can-like ontology 1, the port of export is arranged on after passing through the second oil-removing area 3 in the first oil-removing area 2.The port of export position of first flowline 6
In outside can-like ontology 1, arrival end passes through the first oil-removing area 2 being arranged on after the side wall of can-like ontology 1 above 5 port of export of water inlet pipe
It is interior.The port of export of second flowline 7 is located at outside can-like ontology 1, and arrival end is arranged on second and removes after passing through the side wall of can-like ontology 1
The top in oily area 3.Outlet pipe 8, arrival end are connected with the lower part of the second oil-removing area 3, and the port of export is arranged on outside can-like ontology 1.The
One arrival end for crossing liquid pipe line 9 is located in the first oil-removing area 2 below 5 port of export of water inlet pipe, and the port of export is located in reaction zone 4,
First, which crosses 9 upper edge of liquid pipe line, crosses liquid direction and is sequentially arranged that there are two sprue and pipe-line mixers 10.Second crosses liquid pipe line 11
Arrival end is connected with reaction zone 4, and the port of export is connected with the second oil-removing area 3, and second port of export for crossing liquid pipe line 11 is located at second
The lower section of 7 arrival end of flowline.
The operation principle for the degreasing unit that the utility model embodiment provides is as described below：
The arrival end of recovered water from water inlet pipe 5 is discharged into can-like ontology 1, its port of export from water inlet pipe 5 is made to drain into
One oil-removing area 2, and natural subsidence occurs in the first oil-removing area 2, i.e., the partial suspended thing in recovered water is due under its own gravity
The bottom of the first oil-removing area 2 is sink to, recovered water carries out first time water-oil separating.At this point, crude oil in recovered water is in the top of water,
Since the arrival end of the first flow line 6 is located at the top of 5 port of export of water inlet pipe, when the liquid level of crude oil in can-like ontology 1
When reaching the incoming-side location of the first flow line 6, part crude oil in recovered water can then enter the first flowline 6, and from the
The port of export of one flowline 6 is drained into outside can-like ontology 1.
Since the first 9 arrival end of liquid pipe line excessively is located in the first oil-removing area 2 below 5 port of export of water inlet pipe, logical
It crosses during water inlet pipe 5 constantly injects recovered water into can-like ontology 1, recovered water also constantly enters first and crosses liquid pipe line 9, and
Enter reaction zone 4 after pipe-line mixer 10 is flowed through.In the process, coagulant and flocculation are added in into two sprues respectively
Agent makes recovered water enter reaction zone 4, and react in reaction zone 4 after being mixed with coagulant and flocculant, makes in recovered water
Suspended particle become larger.
Recovered water enters second in reaction zone 4 and crosses liquid pipe line 11, and cross liquid pipe line 11 from second and flow into second after reaction
Oil-removing area 3.At this point, the suspended matter in the recovered water sinks down into the bottom of the second oil-removing area 3, second of grease point occurs for recovered water
From.The port of export for crossing liquid pipe line 11 due to second is located at the lower section of 7 arrival end of the second flowline, and the crude oil in recovered water is located at
The top of water, therefore, need discharge crude oil when, it is only necessary to open control the second flowline 7 valve, crude oil will automatically from
The port of export of second flowline 7 is drained into outside can-like ontology 1, and water then discharges can-like ontology 1 from outlet pipe 8.
The degreasing unit that the utility model embodiment provides by setting can-like ontology 1, and is set in can-like ontology 1
First oil-removing area 2 independent of each other, the second oil-removing area 3,4 and first flowline 6 of reaction zone and the second flowline 7, and pass through
First, which crosses liquid pipe line 9, connects the first oil-removing area 2 with reaction zone 4, and liquid pipe line 11 is crossed by the second oil-removing area 3 and reaction by second
Area 4 connects, and discharges the crude oil in recovered water in can-like ontology 1 by the first flowline 6 and the second flowline 7, realizes and adopt
The oil extraction operation twice of water outlet.5 port of export of water inlet pipe is arranged on by setting water inlet pipe 5, and by the arrival end of the first flowline 6
Top, not only ensure that the normal discharge of recovered water Crude Oil, but also make the arrival end of the first flowline 6 and the outlet of water inlet pipe 5
Between end there is spacing, provide cushion space for recovered water, it is ensured that stability hydraulic.By being crossed on liquid pipe line 9 sequentially first
Two sprues and pipe-line mixer 10 are set, convenient for crossing injection coagulant and wadding in liquid pipe line 9 to first in operation process
Solidifying agent, accelerates suspended matter subsidence velocity and water-oil separating speed, improves operating efficiency.Based on above-mentioned, the utility model embodiment
The degreasing unit of offer, not only floor space is small, at low cost.And work flow is short, and operating efficiency is higher.
Wherein, " liquid direction is crossed " to refer to：In operation process, recovered water crosses the flow direction in liquid pipe line 9 first.
Pipe-line mixer 10 is common for this field, and those skilled in the art can be obtained by purchased in market, for example,
It can be the pipe-line mixer that the Shanghai electromechanical Co., Ltd of full letter produces and sells.
In the utility model embodiment, as shown in Figure 1, which further includes：Outer cap body 12, the first cylinder
13rd, first annular baffle 14.Wherein, Open Side Down for outer cap body 12, lower end and the bottom wall vertical connection of can-like ontology 1.First
Outside outer cap body 12, lower end is connect 13 sets of body with the bottom wall of can-like ontology 1.The inner ring and outer rings of first annular baffle 14 respectively with
The upper end of first cylinder 13 is connected with the inner wall of can-like ontology 1.Can-like ontology 1, outer cap body 12, the first cylinder 13 and first annular
The cavity that baffle 14 surrounds forms the first oil-removing area 2；The chamber that first cylinder 13, first annular baffle 14 and can-like ontology 1 surround
Body forms the second oil-removing area 3；The inner cavity of outer cap body 12 forms reaction zone 4.
By setting outer cap body 12, the first cylinder 13 and first annular baffle 14, and make lower end and the can-like of outer cap body 12
The bottom wall vertical connection of ontology 1；Outside outer cap body 12, lower end is connect first 13 sets of cylinder with the bottom wall of can-like ontology 1, ensure that
The first oil-removing area 2 independent of each other, the second oil-removing area 3 and reaction zone 4 can be formed in can-like ontology 1, it is subsequent to carry out
Oil removing operation twice.
Wherein, the first cylinder 13 is crossed liquid pipe line 11 by second with outer cap body 12 and is connected.First crosses the port of export of liquid pipe line 9
It is arranged in outer cap body 12 after sequentially passing through the second oil-removing area 3, the first oil-removing area 2, and part first crosses liquid pipe line 9 and is exposed at can-like
Outside ontology 1, two sprues, pipe-line mixer 10, which are sequentially arranged, to be crossed in first be exposed at outside can-like ontology 1 on liquid pipe line 9, with
Just staff adds coagulant and flocculant into two sprues respectively.
First annular baffle 14 tilts down that (the outer shroud position height of i.e. first annular baffle 14 is in the inner after mounting
Position where ring), suspended matter is enable quickly to be snapped down to the bottom of can-like ontology 1 by first annular baffle 14.
In order to which the discharge of the suspended matter of 1 bottom of can-like ontology will be sunk to, avoid blocking in can-like ontology 1, so as to influence
Subsequent construction operation.As shown in Figure 1, which further includes：Multiple perforated sludge discharge pipes connected in sequence 15.It is multiple
Perforated sludge discharge pipe 15 extends transversely through the lower part of the first oil-removing area 2, the second oil-removing area 3 and reaction zone 4.
During operation, the suspended matter of 4 bottom of the first oil-removing area 2, the second oil-removing area 3 and reaction zone is sunk to from perforated sludge discharge pipe 15
On hole enter in perforated sludge discharge pipe 15, and from the end of perforated sludge discharge pipe 15 discharge.
Wherein, it can also be separately provided in the second oil-removing area 3 or the lower part of the first oil-removing area 2 and the second oil-removing area 3 multiple
Perforated sludge discharge pipe 15 connected in sequence, so that the suspended matter in the first oil-removing area 2 or the second oil-removing area 3 is discharged.
In order to improve the velocity of discharge of suspended matter, multiple perforated sludge discharge pipes 15 and multiple non-porous sludge pipes can sequentially be handed over
Mistake connection.
In the utility model embodiment, interior cap body 16 (referring to attached drawing 1), interior cap are arranged in the middle part of the inner cavity of outer cap body 12
The port of export that the lower end of body 16 crosses liquid pipe line 9 with first connects, and is cooperatively formed in the middle part of interior cap body 16 and the inner cavity of outer cap body 12
Have an annular space of closing, the side wall on interior 16 top of cap body, the annular space of the closing bottom wall be in mesh structure；First
The top of body 13 is crossed liquid pipe line 11 by second and is connected with the outer cap body 12 below the annular space of the closing.The oil removing fills
It puts and further includes：Multiple Vortex reactors 17 (referring to attached drawing 1) are arranged in the annular space of interior cap body 16 and the closing.
During operation, after the port of export that the recovered water by first time water-oil separating crosses liquid pipe line 9 from first is discharged, sequentially
Flow through multiple vortex in the annular space between multiple Vortex reactors 17 in interior cap body 16, interior cap body 16 and outer cap body 12
Liquid pipe line 11 is crossed after reactor 17 from second to discharge, into the second oil-removing area 3.
By cap body in setting 16, and set in the annular space between interior cap body 16, interior cap body 16 and outer cap body 12
Multiple Vortex reactors 17, enable recovered water fully to be collided when flowing through multiple Vortex reactors 17, make outstanding in recovered water
Float loss of stability, so as to agglomerate, volume increase finally crosses liquid pipe line 11 through second and is discharged into the second oil-removing area 3, into one
Step improves the using effect of flocculant.By the way that the bottom wall of the annular space of the side wall on interior 16 top of cap body, the closing is set
For mesh structure, it ensure that recovered water can smoothly flow through, while Vortex reactor 17 is avoided to be passed through from the sieve.
Wherein, interior 16 opening upwards of cap body cooperatively form the annular space of closing with outer cap body 12.Vortex reactor 17 with
The mesh structure is adapted, and the mesh diameter of mesh structure is less than the diameter of Vortex reactor 17.
Further, for the ease of in the annular space between inside cap body 16, interior cap body 16 and outer cap body 12 addition or
Vortex reactor 17 is discharged, to meet job requirements.The annular closed between interior cap body 16, interior cap body 16 and outer cap body 12 is empty
Between upper end be separately provided for addition Vortex reactor 17 feed pipe.In interior cap body 16, interior cap body 16 and outer cap body 12
Between the lower end of annular space closed be separately provided for the discharge nozzle of discharge Vortex reactor 17.The feed pipe and discharging
The blank flange for controlling its break-make is both provided on pipe.
Wherein, the arrival end of feed pipe is passed through and is fixed on the roof of can-like ontology 1；The arrival end of discharge nozzle and interior cap
The lower end of annular space closed between body 16, interior cap body 16 and outer cap body 12 connects, and the port of export sequentially pass through outer cap body 12,
First cylinder 13 and can-like ontology 1 are exposed at the outside of can-like ontology 1.
In order to make to enter the first recovered water crossed in liquid pipe line 9, the recovered water that water inlet pipe 5 is discharged, cross liquid pipe line from second
11 discharge containing sewage it is more uniform in acquisition and discharge, to promote operation effectiveness.As shown in Figure 1, the degreasing unit
It further includes：First water distribution system 18, the second water distribution system 19 and collecting system 20.Wherein, the first water distribution system 18 is sleeved on outer
The upper end of cap body 12, arrival end are connect with the port of export of water inlet pipe 5；Second water distribution system 19 is sleeved on the upper of the first cylinder 13
Portion, the port of export that arrival end crosses liquid pipe line 11 with second are connect；Collecting system 20 is sleeved on the middle part of outer cap body 12, the port of export with
First crosses the arrival end connection of liquid pipe line 9.
Further, as shown in Figure 1, the first water distribution system 18 includes：It is sleeved on the first water distribution of outer 12 upper end of cap body
The port of export connected in sequence first of slot 1801 and the first water distributing trough 1801 matches water conduit tube 1802, the first range pipe 1803, with
And the first horn mouth 1804 connected with two nozzles of the first range pipe 1803, the port of export of water inlet pipe 5 and the first water distribution
The arrival end connection of slot 1801.Second water distribution system 19 includes：Be sleeved on 13 top of the first cylinder the second water distributing trough 1901, with
The port of export connected in sequence second of second water distributing trough 1901 is with water conduit tube 1902, the second range pipe 1903 and with second
Second horn mouth 1904 of two nozzles connection of range pipe 1903, the arrival end of the second water distributing trough 1901 and second cross liquid pipe
The port of export connection of line 11.Collecting system 20 includes：Be sleeved on 12 middle part of outer cap body catch basin 2001, with catch basin 2001
It arrival end collection water conduit tube 2002 connected in sequence, collection branch pipe 2003 and connects with two nozzles of collection branch pipe 2003
Third horn mouth 2004, the arrival end that the port of export of catch basin 2001 crosses liquid pipe line 9 with first are connect.
After recovered water is discharged from water inlet pipe 5, the first water distributing trough 1801, first is sequentially flowed through with water conduit tube 1802, first
Range pipe 1803, the first horn mouth 1804, and discharged from the first horn mouth 1804.Liquid pipe line 9 is crossed when recovered water enters first
Before, third horn mouth 2004, collection branch pipe 2003, collection water conduit tube 2002 and catch basin 2001 are sequentially flowed through, and through catch basin
2001, which are discharged into first, crosses liquid pipe line 9.After recovered water crosses liquid pipe line 11 from second to be excluded, sequentially flow through the second water distributing trough 1901,
Second with water conduit tube 1902, the second range pipe 1903, the second horn mouth 1904, and is discharged from the second horn mouth 1904.
By setting the first water distributing trough 1801, the second water distributing trough 1901 and catch basin 2001, so as to carry out subsequent water distribution,
It catchments operation.By setting the first horn mouth 1804, the second horn mouth 1904 and third horn mouth 2004, drainage speed is reduced
Sum aggregate water speed, further improves operating efficiency.
Further, in order to improve the acquisition of recovered water and emission effect, the first horn mouth 1804 and the second horn mouth
1904 could be provided as opening upwards, and third horn mouth 2004 is set as that Open Side Down.
For the ease of the air in the second oil-removing area 3 is discharged, it is avoided to influence being smoothed out for oil removing operation.Such as attached drawing
Shown in 1, which further includes：Snorkel 21 inside the first oil-removing area 2 passes through and is fixed on first annular baffle
On 14；The exhaust pipe 22 being in communication with the outside is passed through and is fixed on the roof of can-like ontology 1.
When in the second oil-removing area 3 there are during air, as recovered water constantly injects the second oil-removing area 3, in the second oil-removing area 3
Air will move up to the first oil-removing area 2 along snorkel 21 automatically, and can-like ontology 1 is discharged from exhaust pipe 22.
In order to which the first flowline 6 is allow to carry out oil extraction operation at any time, it is not necessary to be limited by recovered water liquid level in can-like ontology 1
System.The degreasing unit further includes：Float apparatus for collecting oil 23 (as shown in Figure 1).23 and first flowline 6 of float apparatus for collecting oil
Arrival end connection.
Wherein, float apparatus for collecting oil 23 is common for this field, and those skilled in the art can be obtained by purchased in market, lifts
Can be the float apparatus for collecting oil that Fushun Nuoxin Machinery Manufacturing Co., Ltd. produces and sells for example.
For the ease of installing or removing pipe-line mixer 10.As shown in Figure 1, which further includes：First gate valve
24 and second gate valve 25.Wherein, the first gate valve 24 is arranged on the first of two sprue upstreams and crosses on liquid pipe line 9.Second gate valve
25 are arranged on the first mistake liquid pipe line 9 in 10 downstream of pipe-line mixer.
When needing to install, dismantling pipe-line mixer 10, it is only necessary to simultaneously close off the first gate valve 24 and the second gate valve 25 i.e.
It can.
In order to increase the collision area containing sewage when flowing downward, oil-water separation is improved, while convenient for suspending
Object moves downward.Ring support is set on the first cylinder 13 below the second water distribution system 19, is provided on ring support
Multiple inclined tubes connected up and down.
Wherein, " connection up and down " refers to：It is connected above and below inclined tube by the inclined tube.Also, ring support with
Multiple inclined tubes are adapted, and ring support can be the plate body for being provided with multiple inclined tube mounting holes.
In the utility model embodiment, as shown in Figure 1, it is set on the first cylinder 13 of 19 lower section of the second water distribution system
There is separator 26.The separator 26 includes：Second cylinder 2601 and the second ring baffle 2602.Wherein, 2601 sets of the second cylinder
Outside the first cylinder 13, and there is spacing between the first cylinder 13 and can-like ontology 1；The inner ring of second ring baffle 2602 and
Outer wall of the outer shroud respectively with the upper end of the second cylinder 2601 and the first cylinder 13 is connect.
By setting the second cylinder 2601 and the second ring baffle 2602, and the second cylinder 2601 is made to be sleeved on the first cylinder 13
Outside, and between the first cylinder 13 and can-like ontology 1 there is spacing, while the arrival end of outlet pipe 8 is made sequentially to pass through can-like sheet
The side wall of body 1, the first cylinder 13 side wall after, be arranged on 26 and first cylinder 13 of separator formation annular space in, avoid
In drainage procedure, the suspended matter for sinking down into can-like ontology 1 bottom is smoked under the swabbing action of collecting system 20 and (is separated
Part 26 plays compartmentation), so as to influence being smoothed out for entire operation.
Wherein, the second ring baffle 2602 tilts down (the i.e. inner ring position of second ring baffle 2602 after mounting
Higher than the position where its outer shroud), suspended matter is enable quickly to be snapped down to the bottom of can-like ontology 1 by second ring baffle 2602
Portion.
In conclusion the degreasing unit that the utility model embodiment provides is by buffering, homogeneous, sedimentation, the multi-functional conjunction of oil removing
It is integrated, not only floor space is small, at low cost.And work flow is short, and operating efficiency is higher, and operation effectiveness is preferable.
The above is only the preferred embodiment of the present invention, the protection domain being not intended to limit the utility model,
Within the spirit and principle of the utility model, any modification, equivalent replacement, improvement and so on should be included in this reality
Within novel protection domain.
Claims (10)
1. a kind of degreasing unit, which is characterized in that described device includes：Can-like ontology (1), the can-like ontology (1) is interior to be set
There are the first oil-removing area (2) independent of each other, the second oil-removing area (3) and reaction zone (4)；
Water inlet pipe (5), arrival end are located at the can-like ontology (1) outside, and the port of export is arranged on after passing through second oil-removing area (3)
In first oil-removing area (2)；
First flowline (6), the port of export are located at the can-like ontology (1) outside, and arrival end passes through the side wall of the can-like ontology (1)
It is arranged on afterwards first oil-removing area (2) above the water inlet pipe (5) port of export Nei；
Second flowline (7), the port of export are located at the can-like ontology (1) outside, and arrival end passes through the side wall of the can-like ontology (1)
It is arranged on the top of second oil-removing area (3) afterwards；
Outlet pipe (8), arrival end are connected with the lower part of second oil-removing area (3), and the port of export is arranged on the can-like ontology (1)
Outside；
First crosses liquid pipe line (9), and arrival end is located at first oil-removing area (2) below the water inlet pipe (5) port of export Nei, goes out
Mouthful end is located in the reaction zone (4), described first cross liquid pipe line (9) upper edge cross liquid direction be sequentially arranged there are two sprue with
Pipe-line mixer (10)；
Second crosses liquid pipe line (11), and arrival end is connected with the reaction zone (4), and the port of export is connected with second oil-removing area (3),
And the port of export of the second mistake liquid pipe line (11) is located at the lower section of the second flowline (7) arrival end.
2. the apparatus according to claim 1, which is characterized in that described device further includes：Outer cap body (12), Open Side Down,
Lower end and the bottom wall vertical connection of the can-like ontology (1)；
First cylinder (13) is sleeved on the outer cap body (12) outside, and lower end is connect with the bottom wall of the can-like ontology (1)；
First annular baffle (14), inner ring and outer rings respectively with the upper end of first cylinder (13) and the can-like ontology (1)
Inner wall connection；
The can-like ontology (1), the outer cap body (12), first cylinder (13) and the first annular baffle (14) surround
Cavity form first oil-removing area (2)；
Described in the cavity that first cylinder (13), the first annular baffle (14) and the can-like ontology (1) surround is formed
Second oil-removing area (3)；
The inner cavity of the outer cap body (12) forms the reaction zone (4).
3. the apparatus of claim 2, which is characterized in that described device further includes：Multiple perforation rows connected in sequence
Mud pipe (15)；
Multiple perforated sludge discharge pipes (15) extend transversely through first oil-removing area (2), second oil-removing area (3) and described anti-
Answer the lower part of area (4).
4. device according to claim 3, which is characterized in that be arranged with interior cap body in the middle part of the inner cavity of the outer cap body (12)
(16), the lower end of the interior cap body (16) with described first cross liquid pipe line (9) the port of export connect, and the interior cap body (16) and
The annular space of closing is cooperatively formed in the middle part of the inner cavity of the outer cap body (12)；
The side wall on interior cap body (16) top, the annular space of the closing bottom wall be in mesh structure；
Liquid pipe line (11) is crossed with being located under the annular space of the closing in the top of first cylinder (13) by described second
Outer cap body (12) connection of side；
Described device further includes：Multiple Vortex reactors (17), the annular for being arranged on the interior cap body (16) and the closing are empty
Between in.
5. device according to claim 4, which is characterized in that described device further includes：First water distribution system (18), second
Water distribution system (19) and collecting system (20)；
First water distribution system (18) is sleeved on the upper end of the outer cap body (12), and arrival end goes out with the water inlet pipe (5)
The connection of mouth end；
Second water distribution system (19) is sleeved on the top of first cylinder (13), and arrival end crosses liquid pipe line with described second
(11) port of export connection；
The collecting system (20) is sleeved on the middle part of the outer cap body (12), and the port of export crosses liquid pipe line (9) with described first
Arrival end connects.
6. device according to claim 5, which is characterized in that first water distribution system (18) includes：It is sleeved on described
The first water distributing trough (1801) of outer cap body (12) upper end, the port of export connected in sequence first with first water distributing trough (1801)
It is connected with water conduit tube (1802), the first range pipe (1803) and with two nozzles of first range pipe (1803)
The first horn mouth (1804), the port of export of the water inlet pipe (5) connect with the arrival end of first water distributing trough (1801)；
Second water distribution system (19) includes：Be sleeved on the first cylinder (13) top the second water distributing trough (1901), with
The port of export connected in sequence second of second water distributing trough (1901) matches water conduit tube (1902), the second range pipe (1903),
And the second horn mouth (1904) connected with two nozzles of second range pipe (1903), second water distributing trough
(1901) port of export that arrival end crosses liquid pipe line (11) with described second is connect；
The collecting system (20) includes：Catch basin (2001) and the catch basin being sleeved in the middle part of the outer cap body (12)
(2001) arrival end collection water conduit tube (2002) connected in sequence, collection branch pipe (2003) and with the collection branch pipe
(2003) the third horn mouth (2004) of two nozzles connection, the port of export of the catch basin (2001) cross liquid with described first
The arrival end connection of pipeline (9).
7. device according to claim 6, which is characterized in that described device further includes：Positioned at first oil-removing area (2)
Internal snorkel (21), passes through and is fixed on the first annular baffle (14)；
The exhaust pipe (22) being in communication with the outside is passed through and is fixed on the roof of the can-like ontology (1).
8. device according to claim 7, which is characterized in that described device further includes：Float apparatus for collecting oil (23), with institute
State the arrival end connection of the first flowline (6).
9. device according to claim 8, which is characterized in that described device further includes：First gate valve (24), is arranged on institute
State pipe-line mixer (10) upstream described first is crossed on liquid pipe line (9)；
Second gate valve (25), be arranged on the pipe-line mixer (10) downstream described first are crossed on liquid pipe line (9).
10. device according to claim 9, which is characterized in that described first below second water distribution system (19)
Separator (26) is set on cylinder (13)；
The separator (26) includes：Second cylinder (2601) and the second ring baffle (2602)；
Second cylinder (2601) is sleeved on first cylinder (13) outside, and with first cylinder (13) and the can-like sheet
There is spacing between body (1)；
The inner ring and outer rings of second ring baffle (2602) respectively with the upper end of second cylinder (2601) and described
The outer wall connection of one cylinder (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721134145.6U CN207566940U (en) | 2017-09-06 | 2017-09-06 | Oil removing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721134145.6U CN207566940U (en) | 2017-09-06 | 2017-09-06 | Oil removing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207566940U true CN207566940U (en) | 2018-07-03 |
Family
ID=62697341
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721134145.6U Active CN207566940U (en) | 2017-09-06 | 2017-09-06 | Oil removing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207566940U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108793575A (en) * | 2018-07-13 | 2018-11-13 | 黄秋凤 | A kind of environmental protecting device of use group containing bis ether magnetism environmental friendly material |
| CN114618189A (en) * | 2022-04-24 | 2022-06-14 | 北京石油化工学院 | Vertical tank-shaped oil-water two-stage three-time separation equipment |
-
2017
- 2017-09-06 CN CN201721134145.6U patent/CN207566940U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108793575A (en) * | 2018-07-13 | 2018-11-13 | 黄秋凤 | A kind of environmental protecting device of use group containing bis ether magnetism environmental friendly material |
| CN114618189A (en) * | 2022-04-24 | 2022-06-14 | 北京石油化工学院 | Vertical tank-shaped oil-water two-stage three-time separation equipment |
| CN114618189B (en) * | 2022-04-24 | 2023-04-07 | 北京石油化工学院 | Vertical tank-shaped oil-water two-stage three-stage separation equipment |
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