CN207227071U - A kind of oily water separating equipment - Google Patents

A kind of oily water separating equipment Download PDF

Info

Publication number
CN207227071U
CN207227071U CN201720752193.5U CN201720752193U CN207227071U CN 207227071 U CN207227071 U CN 207227071U CN 201720752193 U CN201720752193 U CN 201720752193U CN 207227071 U CN207227071 U CN 207227071U
Authority
CN
China
Prior art keywords
plate
coalescing
babinet
double
oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201720752193.5U
Other languages
Chinese (zh)
Inventor
王越
徐娟
任万龙
刘进
刘波
郝宗睿
袁健
华志励
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong Ocean Instrument Technology Center Co.,Ltd.
Original Assignee
Shandong Province Oceanographic Instrumentation Technology Center
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shandong Province Oceanographic Instrumentation Technology Center filed Critical Shandong Province Oceanographic Instrumentation Technology Center
Priority to CN201720752193.5U priority Critical patent/CN207227071U/en
Application granted granted Critical
Publication of CN207227071U publication Critical patent/CN207227071U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Removal Of Floating Material (AREA)

Abstract

The utility model discloses a kind of oily water separating equipment, including babinet, the babinet top is equipped with inlet tube and oil exit pipe, and lower part is equipped with discharge outlet, and middle part is equipped with the secondary drainage mouth that can be periodically turned on;The flow-stopping plate tilted upward is equipped with the babinet below inlet tube, the secondary drainage mouth is located at the secondary separation room lower part being made of babinet and secondary oil dividing plate, and the secondary oil dividing plate is equipped with overflow pipe;The double M types coalescing-plate groups fixed in the babinet equipped with spacing, cabinet wall is fixed on by fixed press strip above double M types coalescing-plate groups, the fixed press strip is equipped with handle, bottom plate is equipped with below double M types coalescing-plate groups, string column is equipped between the fixed press strip and bottom plate, the string column passes through double M types coalescing-plate groups, Gravity Separation is combined by equipment disclosed in the utility model with coalescence technology, farthest improve oil removal efficiency, good separating effect, residence time is short, and disposal ability is big.

Description

A kind of oily water separating equipment
Technical field
It the utility model is related to a kind of oily water separating equipment.
Background technology
Oily wastewater of the Produced Liquid in oil field after three phase separator separates by settling tank, it is necessary to further settle Separation, at present mainly there is oils existing forms in oily wastewater:(1) floating oil:Particle diameter >=100 micron, slightly take standing or half The method of standing, you can float on the water surface and be easy to remove;(2) dispersed oil:Particle diameter is at 10 100 microns, if enough quiet Put the time, oil droplet can also shift to the water surface, need to generally stand 12 it is small when more than, oily removal rate is more than 80%;(3) oil emulsion: About 0.1 to 10 micron of particle diameter, has certain stability, is merely that can not separate itself and water by gravitational settling, it is necessary to through broken It could be separated after breast or flocculation, seriously affect production.
If separating treatment is carried out, it is necessary to add flocculant, flocculation aid to the oil emulsion in oily wastewater by traditional method And reverse demulsifier.If the sewage quantity containing oil emulsion of required processing is very big, then certainly will will consume substantial amounts of manpower, financial resources And material resources.Oily waste water treatment technology improves at present, and biochemical treatment oily wastewater technology has been obtained for very well Ground application, but the oil emulsion problem in settling tank does not solve also, and the biochemical treatment to sewage plant brings burden.
Utility model content
In order to solve the above technical problems, the utility model provides a kind of oily water separating equipment, to reach good separating effect, Separative efficiency is high, and the residence time is short, the big purpose of disposal ability.
To reach above-mentioned purpose, the technical solution of the utility model is as follows:
A kind of oily water separating equipment, including babinet, the babinet top are equipped with inlet tube and oil exit pipe, and lower part is equipped with draining Mouthful, middle part is equipped with the secondary drainage mouth that can be periodically turned on;The baffle tilted upward is equipped with the babinet below inlet tube Plate, the secondary drainage mouth is on the secondary separation room lower part being made of babinet and secondary oil dividing plate, the secondary oil dividing plate Equipped with overflow pipe;The double M types coalescing-plate groups fixed in the babinet equipped with spacing, double M types coalescing-plate groups tops pass through solid Level pressure bar is fixed on cabinet wall, and the fixed press strip is equipped with handle, bottom plate is equipped with below double M types coalescing-plate groups, described solid String column is equipped between level pressure bar and bottom plate, the string column passes through double M types coalescing-plate groups.
In such scheme, double M types coalescing-plate groups include the coalescing-plate several stacked on top together, the coalescing-plate Coalescing-plate body including cross section for double M types, the coalescing-plate body is along longitudinal direction in wavy, pair of the coalescing-plate body Oil slick hole is equipped with wavy wave crest along longitudinal direction on M types top, trough is equipped with sedimentation hole one, between wave crest and trough Raised fore-set is equipped with node, double M types bottom centers of the coalescing-plate body distribute sedimentation hole two along the longitudinal, described poly- The lower position that the back side of knot tying body is located at fore-set is equipped with groove, the fore-set front end insertion upper strata coalescing-plate of lower floor's coalescing-plate Groove in.
In such scheme, the inlet tube and oil exit pipe are L-type, and the outlet of the inlet tube is positioned at the upper of flow-stopping plate Side;The oil exit pipe is installed on babinet by the oil discharge outlet of babinet, and the apical position of the mouth of pipe is less than the top of double M type coalescing-plate groups End position.
In such scheme, the secondary oil dividing plate is L-type, and overflow pipe is setting up and down in the bottom of L-type, the mouth of pipe of overflow pipe Apical position is less than the spout tops position of oil exit pipe.
In such scheme, the flow-stopping plate is welded on babinet, and horizontal by 45° angle.
In such scheme, the string column passes through the oil slick hole, and the top of the string column is installed on fixation by locking cap On press strip, the bottom of the string column is fixed on bottom plate.
Through the above technical solutions, oily water separating equipment good separating effect provided by the utility model, separative efficiency is high, stops Stay the time short, disposal ability is big, and floor space is small, meets water-oil separating to efficient, miniaturization trend.Specific manifestation :
(1) Gravity Separation farthest improves oil removal efficiency after coalescence technology is combined.
(2) horizontal stream water intake mode, increases coalescence area, and to force current to be formed special for the tortuous passageway of coalescing-plate Fluidised form so that increase stream pearl between collision probability, promote it is small trip pearl coalescence.
(3) double M types coalescing-plate groups can carry out integral installation and dismounting by handle, fixed press strip and bottom plate, easy to use.
Brief description of the drawings
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment Or attached drawing needed to be used in the description of the prior art is briefly described.
Fig. 1 is a kind of oily water separating equipment dimensional structure diagram disclosed in the utility model embodiment;
Fig. 2 is the oily water separating equipment front view disclosed in the utility model embodiment;
Fig. 3 coalesces plate structure schematic diagram for single M types;
Fig. 4 is the top view of Fig. 3;
Fig. 5 is the left view of Fig. 3;
Fig. 6 is section plan where the fore-set of coalescing-plate;
Fig. 7 is Section A-A schematic diagram in Fig. 3;
Fig. 8 is the structure diagram of fixed press strip, string column and bottom plate.
In figure, 1, coalescing-plate body;2nd, oil slick hole;3rd, fore-set;4th, sedimentation hole one;5th, groove;6th, sedimentation hole two;7th, it is fixed Press strip;8th, bottom plate;9th, string column;10th, double M types coalescing-plate groups;11st, babinet;12nd, secondary drainage mouth;13rd, overflow pipe;14th, secondary point Oiled-plate method;15th, oil exit pipe;16th, inlet tube;17th, flow-stopping plate;18th, discharge outlet;19th, handle;20th, locking cap;21st, tabletting.
Embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out Clearly and completely describe.
The utility model provides a kind of oily water separating equipment, structure as depicted in figs. 1 and 2, the equipment gravitational method with Coalescence technology is combined, and improves hydraulics, enhances the state of the water-oil separating of oil emulsion.
Oily-water seperating equipment as depicted in figs. 1 and 2, including babinet 11,11 top of babinet are equipped with inlet tube 16 and oil extraction Pipe 15, lower part are equipped with discharge outlet 18, and middle part is equipped with the secondary drainage mouth 12 that can be periodically turned on;It is located on babinet 11 under inlet tube 16 Side is welded with the flow-stopping plate 17 set horizontal by 45° angle, and secondary drainage mouth 12 is located at by babinet 11 and secondary oil dividing plate 14 The secondary separation room lower part of composition, secondary oil dividing plate 14 are L-type, are welded on the upper left of babinet 11, second for grease Secondary separation;Overflow pipe 13 is setting up and down in the bottom of L-type, and the spout tops position of overflow pipe 13 is less than the mouth of pipe top of oil exit pipe 15 End position.
Inlet tube 16 and oil exit pipe 15 are L-type, and the outlet of inlet tube 16 is positioned at the top of flow-stopping plate 17;Oil exit pipe 15 is logical The oil discharge outlet for crossing babinet 11 is installed on babinet 11, and the apical position of the mouth of pipe is less than the apical position of double M type coalescing-plates groups 10.
The double M types coalescing-plate groups 10 fixed in babinet 11 equipped with spacing, double tops of M types coalescing-plate group 10 pass through fixed press strip 7 are fixed on cabinet wall, and cabinet wall is fixed in side by tabletting 21.As shown in figure 8, fixed press strip 7 is equipped with handle, it is double The lower section of M type coalescing-plates group 10 is equipped with bottom plate, and string column 9 is equipped between fixed press strip 7 and bottom plate 8, and string column 9 passes through double M type coalescing-plates Group 10.String column 9 passes through oil slick hole 2, and the top of string column 9 is installed on fixed press strip 7 by locking cap 20, and the bottom of string column 9 is consolidated Due on bottom plate 8.
As shown in Fig. 3 to Fig. 7, coalescing-plate includes the coalescing-plate body 1 that cross section is double M types, and coalescing-plate body 1 is along longitudinal direction In wavy, oil slick hole 2 is equipped with wavy wave crest along longitudinal direction on double M types tops of coalescing-plate body 1, trough is equipped with Sedimentation hole 1, raised fore-set 3 is equipped with the node between wave crest and trough.Double M types bottom center edges of coalescing-plate body 1 Genesis analysis has a sedimentation hole 26, and the lower position that the back side of coalescing-plate body 1 is located at fore-set 3 is equipped with groove 5, lower floor's coalescence In the groove 5 of 3 front end of the fore-set insertion upper strata coalescing-plate of plate.
As shown in figure 4, oil slick hole 2 is uniformly arranged on the wave crest of coalescing-plate body 1, sedimentation hole 1 is uniformly arranged on poly- On the trough of knot tying body 1, fore-set 3 is uniformly arranged at the node between wave crest and trough, and sedimentation hole 26 is uniformly arranged on poly- On double M types bottom center lines of knot tying body 1.
The board selection polypropylene of coalescing-plate, adds bone meal, to polypropylene board in polypropylene board manufacturing process Tow sides are modified processing.Modified mechanism is hydroxyl in the positive and negative grafting of basic unit, makes it have strong oleophilic drainage Characteristic, so as to realize emulsified oil droplet be demulsified after grease rapid coalescence.
Specific separation process is as follows:
Oil emulsion is inputted in babinet 11 with suitable flow by inlet tube 16;Into babinet 11 oil emulsion to flow down In dynamic process, flow-stopping plate 17 is encountered, and under the action of flow-stopping plate 17, is flowed along 17 direction of flow-stopping plate to upper left side, So as to avoid oil emulsion from directly flowing to 11 bottom of babinet.
Oil emulsion lateral flow enters double M type coalescing-plates groups 10, and the surface of coalescing-plate is waveform, its complications provided is led to Road and very big coalescence surface, generate the current similar to sine wave, make coalescing during tiny oil droplets bottom horizontal flow sheet The surface collision of plate, coalescence, when droplet diameter is coalesced to certain particle diameter, oil droplet passes through the floating of double 10 tops of M types coalescing-plate group Oilhole starts to float, the sedimentation hole 1 and sedimentation hole 26 that the relatively low mixed liquor of oil content passes through double 10 bottoms of M types coalescing-plate group Start to sink.Oil droplet gradually floats up to the top of babinet 11 by coalescing-plate layer by layer, and the relatively low mixed liquor of oil content by gathering layer by layer Knot tying sinks down into 11 bottom of babinet, is discharged from discharge outlet 18, floats up to the oil droplet at the top of babinet 11 and can be exported by oil exit pipe Outside babinet 11, the first time recycling of oil droplet is carried out.
The relatively low mixed liquor of 11 bottom oil content of babinet is secondary into being formed by secondary oil dividing plate 14 via overflow pipe 13 Separation chamber, under the effect of gravity, mixed liquor form layering, and the of a relatively high mixed liquor of oil content is located at top, and oil content phase Lower part is located to lower mixed liquor, periodically opens secondary drainage mouth 12, the low water of oil content is discharged into outdoor, forms grease Second of separation.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or new using this practicality Type.A variety of modifications to these embodiments will be apparent for those skilled in the art, determine herein The General Principle of justice can be realized in other embodiments without departing from the spirit or scope of the present utility model.Cause This, the utility model is not intended to be limited to the embodiments shown herein, and is to fit to and principles disclosed herein The most wide scope consistent with features of novelty.

Claims (6)

  1. A kind of 1. oily water separating equipment, it is characterised in that including babinet, the babinet top is equipped with inlet tube and oil exit pipe, under Portion is equipped with discharge outlet, and middle part is equipped with the secondary drainage mouth that can be periodically turned on;It is equipped with and tilts below inlet tube on the babinet Upward flow-stopping plate, the secondary drainage mouth are located at the secondary separation room lower part that is made of babinet and secondary oil dividing plate, and described two Secondary oil dividing plate is equipped with overflow pipe;The double M types coalescing-plate groups fixed in the babinet equipped with spacing, double M types coalescing-plate groups Cabinet wall is fixed in top by fixed press strip, and the fixed press strip is equipped with handle, bottom is equipped with below double M types coalescing-plate groups Plate, is equipped with string column between the fixed press strip and bottom plate, the string column passes through double M types coalescing-plate groups.
  2. 2. a kind of oily water separating equipment according to claim 1, it is characterised in that double M types coalescing-plate groups include number The coalescing-plate of a stacked on top together, the coalescing-plate include the coalescing-plate body that cross section is double M types, the coalescing-plate sheet Body is in wavy along longitudinal direction, and oil slick hole is equipped with wavy wave crest along longitudinal direction on double M types tops of the coalescing-plate body, Trough is equipped with sedimentation hole one, and raised fore-set, double M types of the coalescing-plate body are equipped with the node between wave crest and trough Bottom center distributes sedimentation hole two along the longitudinal, and the back side of the coalescing-plate body is located at the lower position of fore-set equipped with recessed Groove, the fore-set front end of lower floor's coalescing-plate are inserted into the groove of upper strata coalescing-plate.
  3. 3. a kind of oily water separating equipment according to claim 1, it is characterised in that the inlet tube and oil exit pipe are L Type, the outlet of the inlet tube is positioned at the top of flow-stopping plate;The oil exit pipe is installed on babinet by the oil discharge outlet of babinet, pipe The apical position of mouth is less than the apical position of double M type coalescing-plate groups.
  4. 4. a kind of oily water separating equipment according to claim 3, it is characterised in that the secondary oil dividing plate is L-type, overflow Manage setting up and down in the bottom of L-type, the spout tops position of overflow pipe is less than the spout tops position of oil exit pipe.
  5. A kind of 5. oily water separating equipment according to claim 1, it is characterised in that the flow-stopping plate is welded on babinet, And horizontal by 45° angle.
  6. A kind of 6. oily water separating equipment according to claim 2, it is characterised in that the string column passes through the oil slick hole, The top of the string column is installed on fixed press strip by locking cap, and the bottom of the string column is fixed on bottom plate.
CN201720752193.5U 2017-06-27 2017-06-27 A kind of oily water separating equipment Active CN207227071U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720752193.5U CN207227071U (en) 2017-06-27 2017-06-27 A kind of oily water separating equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720752193.5U CN207227071U (en) 2017-06-27 2017-06-27 A kind of oily water separating equipment

Publications (1)

Publication Number Publication Date
CN207227071U true CN207227071U (en) 2018-04-13

Family

ID=61852020

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720752193.5U Active CN207227071U (en) 2017-06-27 2017-06-27 A kind of oily water separating equipment

Country Status (1)

Country Link
CN (1) CN207227071U (en)

Similar Documents

Publication Publication Date Title
CN106007209B (en) A kind of oil refinery's sewage oil removing pretreating process
CN2648068Y (en) High efficiency three phase separating device
CN200964362Y (en) High efficiency non-powered oil-water separating device
CN108298741A (en) A kind of oily wastewater electric flocculation high-level cleaner
CN105000704B (en) Pipe type oil moisture trap and separation method
CN202400880U (en) Device for treating oil-containing sewage through secondary conglomeration
CN207259251U (en) A kind of equipment for water-oil separating
CN207227067U (en) A kind of new oily-water seperating equipment
CN103043747A (en) Oil-water separator
CN2500366Y (en) Oil gas separator for thickened oil and special thickened oil
CN201301258Y (en) Oily sewage silt treatment equipment
CN207227069U (en) A kind of oily-water seperating equipment
CN207227068U (en) Equipment for water-oil separating
CN207227070U (en) Device for water-oil separating
CN106045088B (en) A kind of joint multi-grade oil laden water separation process
CN207227071U (en) A kind of oily water separating equipment
CN207227072U (en) A kind of new oily water separating equipment
CN207227140U (en) A kind of device for water-oil separating
CN202968270U (en) Water treatment device of oil water separator
CN101961567B (en) Oil-removing three-phase separator
CN206886743U (en) Adjustable height water-oil separating coalescing-plate group
CN206881207U (en) Water-oil separating coalescing-plate group
CN201880406U (en) Deoiling three-phase separator
CN2442987Y (en) Pot for removing oil and sand from sewage
CN206886741U (en) A kind of water-oil separating coalescing-plate group

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CP03 Change of name, title or address

Address after: No.28, Zhejiang Road, Shinan District, Qingdao City, Shandong Province

Patentee after: Shandong Ocean Instrument Technology Center Co.,Ltd.

Address before: No. 28, Zhejiang Road, Southern District, Shandong, Qingdao, Shandong

Patentee before: SHANDONG PROVINCE OCEANOGRAPHIC INSTRUMENTATION TECHNOLOGY CENTER

CP03 Change of name, title or address