CN105858801A - High-salinity oily sewage post-treatment device - Google Patents
High-salinity oily sewage post-treatment device Download PDFInfo
- Publication number
- CN105858801A CN105858801A CN201610058834.7A CN201610058834A CN105858801A CN 105858801 A CN105858801 A CN 105858801A CN 201610058834 A CN201610058834 A CN 201610058834A CN 105858801 A CN105858801 A CN 105858801A
- Authority
- CN
- China
- Prior art keywords
- pipe
- oil
- cone
- collecting
- pump
- 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.)
- Granted
Links
Classifications
-
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/463—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrocoagulation
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Electrochemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- Cyclones (AREA)
- Removal Of Floating Material (AREA)
Abstract
The invention discloses a high-salinity oily sewage post-treatment device including a cyclone separator, an original liquid trough and a liquid collecting trough; the cyclone separator includes a separation cone and a tail tube; an opening of the upper end of the tail tube communicates with an opening of the lower end of the separation cone; an opening of the upper end of the separation cone is sealed by a cone-top circular plate, and the separation cone is provided with a tangential liquid inlet tube; the liquid collecting trough is arranged below the tail tube. The high-salinity oily sewage treatment device also includes an original liquid draw-off pump; the original liquid draw-off pump is provided with an original liquid inlet tube and an original liquid outlet tube; an inlet end of the original liquid inlet tube extends into the original liquid trough; an outlet end of the original liquid outlet tube communicates with the tangential liquid inlet tube; the cyclone separator is internally provided with a core tube; the upper end of the core tube is connected to an oil collecting tank through an oil collecting pipeline, and the core tube is provided with a plurality of oil inlet holes. The high-salinity oily sewage treatment device has the beneficial effects that the highly efficient separation of oil and water can be realized, additional chemical agents are not required, equipment can also be reused, and the overall cost is relatively low; the treatment process is extremely continuous, pausing and work station switching are not required, and the working efficiency is high; and continuous separation and oil automatic collection are achieved, and the treatment effect is good.
Description
Technical field
The invention belongs to oily waste water treatment technical field, particularly relate to a kind of high salinity oil-polluted water after-treatment device.
Background technology
In the fields such as oil exploitation industry, marine ship transport service, often need oil-polluted water, oil-containing seawater etc. are post-processed, it is to avoid greasy residues, pollution environment.At present, both at home and abroad the method administering oil-polluted water is mainly had following three classes: method of chemical treatment, physical treatment process and biochemical treatment process.Wherein physical treatment process is without extra interpolation material, and equipment can be with Reusability, and overall cost is relatively low, is to use more method.And for large batch of oily waste water treatment, also can more use centrifugal separation.But, at present when oil-polluted water is processed, separative efficiency, separation costs, separating effect comprehensive consideration on, the most not enough.
Summary of the invention
The present invention is to overcome deficiency of the prior art, it is provided that a kind of rational in infrastructure, has good disposal ability, can the most quickly process a large amount of oil-polluted waters, oil-containing seawater, and holistic cost is relatively low and the processing means of high treating effect.
To achieve these goals, the present invention is by the following technical solutions:
nullA kind of high salinity oil-polluted water after-treatment device，Including cyclone separator、Stoste groove、Collecting tank，Described cyclone separator includes separating cone、Cone is coaxial to be connected and vertical tail pipe with separating，Separate on cone、The equal opening in lower end，On tail pipe、The equal opening in lower end，Separate cone upper end open more than separating cone lower ending opening，Tail pipe upper end open connects with separating cone lower ending opening，Separate cone upper end open to be sealed by a vertex of a cone plectane，Separate the tangential direction pipe that cone is provided with and separates the internal connection of cone，Collecting tank is in below tail pipe，Also include a stoste draw-off pump，Stoste draw-off pump is provided with into stoste pipe、Go out stoste pipe，The entrance point entering stoste pipe stretches in stoste groove，The port of export going out stoste pipe connects with tangential direction pipe，The core pipe coaxial with tail pipe it is provided with in cyclone separator，Core pipe upper end is through vertex of a cone plectane and stretches out outside cyclone separator，Core pipe upper end is connected to an accumulator tank by oil-collecting pipeline，Core pipe is provided with some pipe fuel feed holes of connecting internal with core pipe,Also include a circulating pump，Circulating pump is provided with into circulation fluid pipe、Go out circulation fluid pipe，The entrance point entering circulation fluid pipe stretches in collecting tank，The port of export going out circulation fluid pipe connects with tangential direction pipe，Go out circulation fluid pipe and be provided with circulation fluid on-off valve，Described enter stoste pipe be provided with horn mouth feed tube，The upper end of horn mouth feed tube connects with the entrance point entering stoste pipe，The lower end of horn mouth feed tube is provided with the miscellaneous filter screen of sieve，In the pipe of horn mouth feed tube, bore is from top to bottom gradually increased.
As preferably, described separate cone in be provided with the equal opening of upper and lower end help rotation cylinder, described in help rotation cylinder with to separate cone coaxial, help and being tightly connected between rotation cylinder upper end and vertex of a cone plectane, help rotation cylinder height more than 2/3rds of separation cone height.
As preferably, described in help the cylinder top side wall of rotation cylinder to be provided with some return ports.
As preferably, described tangential direction pipe axis is tangential parallel with separate cone one.
As preferably, the self-regulated pipe joint that can relatively slide up and down in core pipe it is provided with in described core pipe, on self-regulated pipe joint, the equal opening in lower end, between self-regulated pipe joint lateral wall with core pipe madial wall, slipper seal coordinates, self-regulated pipe joint lower end is stretched out outside core pipe, self-regulated pipe joint lower end is provided with shrouding under the pipe sealing self-regulated pipe joint lower ending opening, the lower shrouding of pipe is provided with buoyancy aid, buoyancy aid is provided with floating foundation seat, tail pipe is provided with the guiding montant being connected with tail pipe, guide montant cross section rectangular, guide montant to be slidably connected with floating foundation seat, self-regulation tube side wall is provided with some pipe oil throughs of connecting internal with self-regulated pipe joint, pipe oil through and pipe fuel feed hole one_to_one corresponding, corresponding pipe oil through with in pipe fuel feed hole: pipe oil through aperture is identical with pipe fuel feed hole aperture, pipe oil through and pipe fuel feed hole dead in line.
As preferably, described guiding montant is connected with tail pipe by support body, and described support body includes that at least horizontal connecting rod, horizontal connecting rod one end are fixed with tail pipe madial wall, guides montant lower end and is connected with horizontal connecting rod.
As preferably, described oil-collecting pipeline includes oil-collecting supervisor, transition connecting pipe, and oil-collecting is responsible for one end and is connected with accumulator tank, and oil-collecting supervisor's other end connects with transition connecting pipe one end, and the transition connecting pipe other end connects with core pipe upper end.
As preferably, described oil-collecting supervisor is provided with collection oil pump, oil-collecting check valve, the drawing liquid direction of collection oil pump is to collecting oil pump by core pipe, the discharge opeing direction of collection oil pump is to accumulator tank by collection oil pump, Tong Guo the direction of oil-collecting check valve is to accumulator tank by collection oil pump, goes out and is provided with feed liquor on-off valve between stoste pipe and tangential direction pipe.
As preferably, also include electricity flocculation post processing structure, post processing pump, electricity flocculation post processing structure includes processing container, post processing feed tube, post processing drain pipe, positive electrode plate, negative electrode plate, post processing feed tube is provided with some liquid inlet head connected with post processing feed tube, post processing drain pipe is provided with some liqiud outlet heads connected with post processing drain pipe, process in container and be provided with row's arc-shaped partition, adjacent two pieces of arc-shaped partitions surround a process single-chamber in processing container, process single-chamber and liquid inlet head one_to_one corresponding, process single-chamber and liqiud outlet head one_to_one corresponding, liquid inlet head, liqiud outlet head is all in the process single-chamber of correspondence, post processing pump is provided with into treatment fluid pipe, go out treatment fluid pipe, the entrance point entering treatment fluid pipe stretches in collecting tank, the port of export going out treatment fluid pipe connects with post processing feed tube.
The invention has the beneficial effects as follows: efficiently separating of profit can be realized, simple to operate, and without by additional chemical agent, equipment also can reuse, overall cost is relatively low；Processing procedure is the most continuous, it is not necessary to suspend and switch station, and operating efficiency is high；It is continuously separated and automatically collects oil, high treating effect.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention
Fig. 2 is the enlarged drawing in Fig. 1 at A；
Fig. 3 is the enlarged drawing in Fig. 1 at B；
Enlarged drawing at C in Fig. 4 Fig. 1.
nullIn figure: stoste groove 1、Stoste draw-off pump 11、Enter stoste pipe 12、Horn mouth feed tube 121、Sieve miscellaneous filter screen 122、Go out stoste pipe 13、Feed liquor on-off valve 131、Collecting tank 2、Separate cone 3、Vertex of a cone plectane 31、Tangential direction pipe 32、Help rotation cylinder 33、Return port 331、Tail pipe 4、Horizontal connecting rod 41、Brake pad 42、Core pipe 5、Accumulator tank 51、Pipe fuel feed hole 52、Self-regulated pipe joint 53、The lower shrouding 531 of pipe、Buoyancy aid 532、Floating foundation seat 533、Guide montant 534、Pipe oil through 535、Oil-collecting supervisor 54、Transition connecting pipe 55、Collection oil pump 56、Oil-collecting check valve 57、Post processing pump 61、Process container 62、Post processing feed tube 63、Liquid inlet head 631、Post processing drain pipe 64、Liqiud outlet head 641、Arc-shaped electrode plate 65、Enter treatment fluid pipe 66、Go out treatment fluid pipe 67、Go out treatment fluid on-off valve 671、Circulating pump 71、Enter circulation fluid pipe 72、Go out circulation fluid pipe 73、Circulation fluid on-off valve 74.
Detailed description of the invention
The present invention will be further described with detailed description of the invention below in conjunction with the accompanying drawings.
nullEmbodiment 1: in embodiment as shown in Figures 1 to 4，A kind of high salinity oil-polluted water after-treatment device，Including cyclone separator、Stoste groove 1、Collecting tank 2，Described cyclone separator includes that profile is round table-like separation cone 3、Cone is coaxial to be connected and vertical tail pipe 4 with separating，Separate on cone、The equal opening in lower end，On tail pipe、The equal opening in lower end，Separate cone upper end open more than separating cone lower ending opening，Tail pipe upper end open connects with separating cone lower ending opening，Separate cone upper end open to be sealed by a vertex of a cone plectane 31，Separate the tangential direction pipe 32 that cone is provided with and separates the internal connection of cone，Collecting tank is in below tail pipe，Also include a stoste draw-off pump 11，Stoste draw-off pump be provided with stoste draw-off pump inlet communication enter stoste pipe 12、With stoste draw-off pump outlet go out stoste pipe 13，The entrance point entering stoste pipe stretches in stoste groove，The port of export going out stoste pipe connects with tangential direction pipe，The core pipe 5 coaxial with tail pipe it is provided with in cyclone separator，Core pipe upper end is through vertex of a cone plectane and stretches out outside cyclone separator，Core pipe upper end is connected to an accumulator tank 51 by oil-collecting pipeline，Core pipe is provided with some pipe fuel feed holes 52 of connecting internal with core pipe,Also include a circulating pump 71，Circulating pump be provided with connect with pump inlet enter circulation fluid pipe 72、Connect with circulating-pump outlet goes out circulation fluid pipe 73，The entrance point entering circulation fluid pipe stretches in collecting tank，The port of export pumping out circulation fluid pipe connects with tangential direction pipe，Go out circulation fluid pipe and be provided with circulation fluid on-off valve 74，Described enter stoste pipe be provided with horn mouth feed tube 121，The upper end of horn mouth feed tube connects with the entrance point entering stoste pipe，The lower end of horn mouth feed tube is provided with the miscellaneous filter screen 122 of sieve，In the pipe of horn mouth feed tube, bore is from top to bottom gradually increased.Circulation fluid on-off valve is for controlling the break-make of circulation fluid pipe.Described tangential direction pipe axis is tangential parallel with separate cone one.Oil-polluted water (seawater) is stored in stoste groove, stoste draw-off pump extracts stoste (oil-polluted water) from stoste groove, oil-polluted water is through entering stoste pipe, stoste draw-off pump, going out stoste pipe and reach tangential direction pipe, and send in separation cone from tangential direction pipe with tangential (or approximation is tangential), up big and down small owing to separating cone, again due to the effect of gravity, oil-polluted water starts helical flow in separating cone, and overall trend is downward spiral flowing.Owing to having density contrast between profit, during oil-polluted water high-speed rotational, water can against separation conical inner surface relatively, and oil droplet (oily) can shift to center (near separating axis of cone line) relatively.And along with the entirety of fluid is downward, spiral moves, cross section constantly reduces, and oil continues move towards center and converges into wick (core pipe is in wick), and wick outer layer is then " water wall " (a large amount of water oil on a small quantity).Fluid then goes through mouth (tail pipe), and fluid can produce back pressure to epimere, make the upwards overflow of low pressure wick, enter into inside core pipe from pipe fuel feed hole, and be collected in entering accumulator tank by oil-collecting pipeline, as for outer layer " water wall ", then it is discharged in collecting tank down through tail pipe lower ending opening, thus efficiently separating of profit can be realized, and without by additional chemical agent, equipment also can reuse, and processing procedure is very continuous, and overall cost is relatively low.In addition, whenever necessary, circulating pump can extraction processed from collecting tank oil-polluted water, make it through entering circulation fluid pipe, circulating pump, going out circulation fluid pipe and reach tangential direction pipe (now circulation fluid on-off valve unblank, stoste draw-off pump can work, can not also work, during stoste extraction air pump inoperative, need to cut off stoste draw-off pump place pipeline, ensure that fluid flows into and separate cone), and again send in separation cone from tangential direction pipe, process such that it is able to realize repeatedly multi-cycle separation, promote treatment effect.Oil-containing seawater is entering before stoste pipe, first pass through the miscellaneous filter screen of sieve and horn mouth feed tube, sieve miscellaneous filter screen and can filter off large volume impurity, promote disposed of in its entirety effect, again owing to when sieving miscellaneous, impurity may temporarily be blocked a part of opening of sieve, affect feed liquor efficiency, so using the initial feed liquor form of up-small and down-big horn mouth feed tube, ensure that initial feed liquor bore is sufficiently large.
Described separate cone in be provided with the equal opening of upper and lower end help rotation cylinder 33, described in help rotation cylinder with separate cone coaxial, help rotation cylinder upper end and vertex of a cone plectane between being tightly connected, help rotation cylinder height more than separation cone height 2/3rds.The described cylinder top side wall helping rotation cylinder is provided with some return ports 331.Help the existence of rotation cylinder, be equivalent to constitute one section of circular passage (help rotation cylinder and separate between cone), contribute to the formation of eddy flow, flow up (as previously mentioned on can also suppressing, owing to the formed wick of back pressure and a part against " the water wall " of wick) to excessive dissipate formed disturb stream in a large number, the stability of processing procedure can be promoted.But, rise and flow to local eddy currents that external diffusion formed and flow-disturbing still exists, and the setting of return port, up-flow can be allowed to rise to top after, a part flows out from return port, feed liquor is formed opposing back pressure, controls the balance of feed liquor on the whole, improve regularity and the stability separating cone interior fluid flowing the most further, can effectively promote the oil-water separation of entirety.
nullThe self-regulated pipe joint 53 that can relatively slide up and down in core pipe it is provided with in described core pipe，On self-regulated pipe joint、The equal opening in lower end，Between self-regulated pipe joint lateral wall with core pipe madial wall, slipper seal coordinates，Self-regulated pipe joint lower end is stretched out outside core pipe，Self-regulated pipe joint lower end is provided with shrouding 531 under the pipe sealing self-regulated pipe joint lower ending opening，The lower shrouding of pipe is provided with buoyancy aid 532，Buoyancy aid is provided with floating foundation seat 533，Tail pipe is provided with the guiding montant 534 being connected with tail pipe，Guide montant cross section rectangular，Guide montant to be slidably connected with floating foundation seat，The slidably direction of floating foundation seat is above-below direction，Self-regulation tube side wall is provided with some pipe oil throughs 535 of connecting internal with self-regulated pipe joint，Pipe oil through and pipe fuel feed hole one_to_one corresponding，Corresponding pipe oil through with in pipe fuel feed hole: pipe oil through aperture is identical with pipe fuel feed hole aperture，Pipe oil through and pipe fuel feed hole dead in line.Described guiding montant is connected with tail pipe by support body, and described support body includes at least horizontal connecting rod 41, and horizontal connecting rod one end is fixed with tail pipe madial wall, guides montant lower end and is connected with horizontal connecting rod.Some brake pads 42 fixing with tail pipe it are provided with in tail pipe, brake pad contact self-regulated pipe joint lateral wall, at the beginning, owing to fluid oil content is bigger, now buoyancy aid part contact water, remaining part contact oil, now the buoyancy suffered by buoyancy aid is also not sufficient to exceed gravity (self-regulated pipe joint, the gravity of whole float structure etc.) and frictional force (the mainly frictional force between brake pad and self-regulated pipe joint, remaining fraction is the frictional force etc. between self-regulated pipe joint and core pipe) sum, so self-regulated pipe joint will not slide up and down, so crossing the total bore (aperture of pipe oil through pipe fuel feed hole in other words of oil, namely oil enters total bore of self-regulated pipe joint) constant, the most fuel-displaced.And when fluid oil content reduces (when original oil content is the highest in other words), wick can become very carefully, wick length also can reduce (wick hypomere part is replaced with water), " water wall " can become the thickest, owing to now water is too close to pipe fuel feed hole, if the oil-feed speed of self-regulated pipe joint, it is easily caused water and enters core pipe (self-regulated pipe joint), the oil-containing ratio of the oil that impact is collected.And in this programme, after fluid oil content is reduced to a certain degree, owing to wick shortens, so the part of buoyancy aid contact water becomes many, the part of contact oil tails off, the buoyancy that buoyancy aid is subject to increases, at a time, buoyancy has exceeded gravity (self-regulated pipe joint, the gravity of whole float structure etc.) and frictional force (the mainly frictional force between brake pad and self-regulated pipe joint, remaining fraction is the frictional force etc. between self-regulated pipe joint and core pipe) sum, buoyancy aid starts to drive shifting on self-regulated pipe joint, thus pipe oil through and pipe fuel feed hole start dislocation, cross the total bore of oil to diminish, thus, the oil-feed speed in self-regulated pipe joint can be reduced, such that it is able to ensure that still only oil enters self-regulated pipe joint, avoid a part of water entrance self-regulated pipe joint now caused because feed liquor speed is too fast.Accordingly, fluid oil content is the lowest, and it is the most that buoyancy aid drives self-regulated pipe joint to rise, and crosses the total bore of oil the least, it is achieved thereby that cross being automatically adjusted of the total bore of oil.And, after fluid oil content is reduced to a certain degree, (surrounded by water completely outside buoyancy aid owing to buoyancy aid drives the rising of self-regulated pipe joint to reach extreme position, the buoyancy that buoyancy aid is subject to is all from water), now pipe oil through and pipe fuel feed hole stagger completely, oil-collecting pipeline stops oil-collecting, has thoroughly blocked when fluid oil content is the lowest, and water enters the possibility of oil-collecting pipeline.
Described oil-collecting pipeline includes oil-collecting supervisor 54, transition connecting pipe 55, and oil-collecting is responsible for one end and is connected with accumulator tank, and oil-collecting supervisor's other end connects with transition connecting pipe one end, and the transition connecting pipe other end connects with core pipe upper end.Described oil-collecting supervisor is provided with collection oil pump 56, oil-collecting check valve 57, the drawing liquid direction of collection oil pump is to collecting oil pump by core pipe, the discharge opeing direction of collection oil pump is to accumulator tank by collection oil pump, Tong Guo the direction of oil-collecting check valve is to accumulator tank by collection oil pump, goes out and is provided with feed liquor on-off valve 131 between stoste pipe and tangential direction pipe.Controllability and the accuracy of processing procedure can be promoted by each pump, valve.
nullAlso include electricity flocculation post processing structure、Post processing pump 61，Electricity flocculation post processing structure includes processing container 62、Post processing feed tube 63、Post processing drain pipe 64，Post processing feed tube is provided with some liquid inlet head 631 connected with post processing feed tube，Post processing drain pipe is provided with some liqiud outlet heads 641 connected with post processing drain pipe，Process in container and be provided with row's arc-shaped electrode plate 65，Adjacent two blocks of arc-shaped electrode plates surround a process single-chamber in processing container，Process single-chamber and liquid inlet head one_to_one corresponding，Process single-chamber and liqiud outlet head one_to_one corresponding，Liquid inlet head、Liqiud outlet head is all in the process single-chamber of correspondence，Post processing pump be provided with post-process that pump inlet connects enter treatment fluid pipe 66、With post processing pump discharge connect go out treatment fluid pipe 67，The entrance point entering treatment fluid pipe stretches in collecting tank，The port of export going out treatment fluid pipe connects with post processing feed tube，Go out treatment fluid pipe and be provided with out treatment fluid on-off valve 671.After aforementioned separating treatment, the treatment fluid oil content of discharge is the lowest, and the most again by if physical method oil removing, effect is the most inconspicuous, so using electricity flocculence, can promote final treatment effect.The alfer plate that battery lead plate can use iron content to be 10%.Because simple aluminum electrode plate produces Al (OH)3Flocculant has preferable removal effect to oil emulsion most in oil-polluted water and suspended oil, poor to dissolved oil (COD) removal effect of oil-polluted water small portion.And alfer battery lead plate can produce and have certain oxidisability Fe3+, therefore the dissolved oil of oxidable small molecule structure.Battery lead plate can use semicircle perpendicular stream warp architecture form, flocculation efficiency is improved relative to the electrode plate structure of advection, and the battery lead plate bent can also increase oil-polluted water flow distance in the reactor, add the oil-polluted water reaction time, therefore can fully remove the oil in oil-polluted water and divide and pollutant.Battery lead plate can exchange a both positive and negative polarity every one end time, it is to avoid near battery lead plate, concentration polarization causes water electrolysis and the electric energy loss that produces.
Claims (9)
1. a high salinity oil-polluted water after-treatment device, is characterized in that, including cyclone separator, stoste groove, collection
Liquid bath, described cyclone separator includes separating cone, boring coaxial being connected and vertical tail pipe with separating, separates
The cone equal opening of upper and lower end, the equal opening of tail pipe upper and lower end, separate cone upper end open more than separating cone lower end
Opening, tail pipe upper end open connects with separating cone lower ending opening, separates cone upper end open by a vertex of a cone plectane
Sealing, separate the tangential direction pipe that cone is provided with and separates the internal connection of cone, collecting tank is in below tail pipe,
Also including a stoste draw-off pump, stoste draw-off pump is provided with into stoste pipe, goes out stoste pipe, enters stoste pipe
Entrance point stretches in stoste groove, and the port of export going out stoste pipe connects with tangential direction pipe, in cyclone separator
Being provided with the core pipe coaxial with tail pipe, core pipe upper end is through vertex of a cone plectane and stretches out outside cyclone separator, core pipe
Upper end is connected to an accumulator tank by oil-collecting pipeline, and core pipe is provided with some pipes of connecting internal with core pipe and enters
Oilhole, also includes a circulating pump, and circulating pump is provided with into circulation fluid pipe, goes out circulation fluid pipe, enters circulation fluid pipe
Entrance point stretch in collecting tank, the port of export going out circulation fluid pipe connects with tangential direction pipe, goes out circulation fluid
Pipe is provided with circulation fluid on-off valve, described in enter stoste pipe and be provided with horn mouth feed tube, horn mouth feed tube
Upper end connect with the entrance point entering stoste pipe, the lower end of horn mouth feed tube be provided with sieve miscellaneous filter screen, loudspeaker
In the pipe of mouth feed tube, bore is from top to bottom gradually increased.
One the most according to claim 1 high salinity oil-polluted water after-treatment device, is characterized in that, described point
Be provided with the equal opening of upper and lower end in cone helps rotation cylinder, described in help rotation cylinder with to separate cone coaxial, help and revolve on cylinder
It is tightly connected between end and vertex of a cone plectane, helps rotation cylinder height more than separating 2/3rds of cone height.
One the most according to claim 1 high salinity oil-polluted water after-treatment device, is characterized in that, described in help
The cylinder top side wall of rotation cylinder is provided with some return ports.
One the most according to claim 1 high salinity oil-polluted water after-treatment device, is characterized in that, described in cut
Tangential parallel with separate cone one to feed tube axis.
5., according to the one high salinity oil-polluted water after-treatment device described in claim 1 or 2 or 3, it is characterized in that,
Being provided with the self-regulated pipe joint that can relatively slide up and down in core pipe in described core pipe, self-regulated pipe joint upper and lower end is all opened
Mouthful, between self-regulated pipe joint lateral wall with core pipe madial wall, slipper seal coordinates, and core is stretched out in self-regulated pipe joint lower end
Outside pipe, self-regulated pipe joint lower end is provided with shrouding under the pipe sealing self-regulated pipe joint lower ending opening, and the lower shrouding of pipe sets
There are buoyancy aid, buoyancy aid to be provided with floating foundation seat, tail pipe is provided with the guiding montant being connected with tail pipe, guide montant
Cross section is rectangular, guide montant be slidably connected with floating foundation seat, self-regulation tube side wall be provided with some with oneself
The pipe oil through of the internal connection of regulation pipe, pipe oil through and pipe fuel feed hole one_to_one corresponding, lead at corresponding pipe
Oilhole with in pipe fuel feed hole: pipe oil through aperture is identical with pipe fuel feed hole aperture, pipe oil through and pipe oil-feed
Axially bored line overlaps.
One the most according to claim 5 high salinity oil-polluted water after-treatment device, is characterized in that, described in lead
Being connected with tail pipe by support body to montant, described support body includes at least horizontal connecting rod, horizontal connecting rod one
End is fixed with tail pipe madial wall, guides montant lower end and is connected with horizontal connecting rod.
7., according to the one high salinity oil-polluted water after-treatment device described in claim 1 or 2 or 3, it is characterized in that,
Described oil-collecting pipeline includes oil-collecting supervisor, transition connecting pipe, and oil-collecting is responsible for one end and is connected with accumulator tank, oil-collecting
Supervisor's other end connects with transition connecting pipe one end, and the transition connecting pipe other end connects with core pipe upper end.
One the most according to claim 7 high salinity oil-polluted water after-treatment device, is characterized in that, described collection
Oil supervisor is provided with collection oil pump, oil-collecting check valve, and the drawing liquid direction of collection oil pump is to collecting oil pump by core pipe,
The discharge opeing direction of collection oil pump be to be by oil-collecting by collecting oil pump to accumulator tank, Tong Guo the direction of oil-collecting check valve
Pump, to accumulator tank, goes out and is provided with feed liquor on-off valve between stoste pipe and tangential direction pipe.
One the most according to claim 1 high salinity oil-polluted water after-treatment device, is characterized in that, also include
Electricity flocculation post processing structure, post processing pump, electricity flocculation post processing structure include process container, post-process into
Liquid pipe, post processing drain pipe, post processing feed tube is provided with some feed liquors connected with post processing feed tube
Head, post processing drain pipe is provided with some liqiud outlet heads connected with post processing drain pipe, processes in container and set
Having row's arc-shaped electrode plate, adjacent two blocks of arc-shaped electrode plates surround a process single-chamber in processing container, place
Reason single-chamber and liquid inlet head one_to_one corresponding, process single-chamber and liqiud outlet head one_to_one corresponding, and liquid inlet head, liqiud outlet head are equal
Being in the process single-chamber of correspondence, post processing pump is provided with into treatment fluid pipe, goes out treatment fluid pipe, enters to process
The entrance point of liquid pipe stretches in collecting tank, and the port of export going out treatment fluid pipe connects with post processing feed tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610058834.7A CN105858801B (en) | 2016-01-27 | 2016-01-27 | High salinity oily sewage aftertreatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610058834.7A CN105858801B (en) | 2016-01-27 | 2016-01-27 | High salinity oily sewage aftertreatment device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105858801A true CN105858801A (en) | 2016-08-17 |
| CN105858801B CN105858801B (en) | 2021-05-18 |
Family
ID=56623964
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610058834.7A Active CN105858801B (en) | 2016-01-27 | 2016-01-27 | High salinity oily sewage aftertreatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105858801B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105797434A (en) * | 2016-03-14 | 2016-07-27 | 浙江理工大学 | Separation and collection device |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201157703Y (en) * | 2007-11-28 | 2008-12-03 | 北京石油化工学院 | Compact type rotary flow air float separating device for oily wastewater treatment |
| CN102225382A (en) * | 2011-04-11 | 2011-10-26 | 东北石油大学 | Pitting oil collecting curved cyclone of overflow pipe |
| CN102417212A (en) * | 2011-10-17 | 2012-04-18 | 中国海洋石油总公司 | Cyclone gas-flotation separation device for treating oily sewage |
| CN203347776U (en) * | 2013-07-24 | 2013-12-18 | 东北石油大学 | Oil-gas-water three-phase flow gas-liquid separation device for yield profile logging |
| CN103894001A (en) * | 2012-12-28 | 2014-07-02 | 赫菲斯热处理系统江苏有限公司 | Floating-type oil absorption device of oil-water separator |
| US20160045841A1 (en) * | 2013-03-15 | 2016-02-18 | Transtar Group, Ltd. | New and improved system for processing various chemicals and materials |
-
2016
- 2016-01-27 CN CN201610058834.7A patent/CN105858801B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201157703Y (en) * | 2007-11-28 | 2008-12-03 | 北京石油化工学院 | Compact type rotary flow air float separating device for oily wastewater treatment |
| CN102225382A (en) * | 2011-04-11 | 2011-10-26 | 东北石油大学 | Pitting oil collecting curved cyclone of overflow pipe |
| CN102417212A (en) * | 2011-10-17 | 2012-04-18 | 中国海洋石油总公司 | Cyclone gas-flotation separation device for treating oily sewage |
| CN103894001A (en) * | 2012-12-28 | 2014-07-02 | 赫菲斯热处理系统江苏有限公司 | Floating-type oil absorption device of oil-water separator |
| US20160045841A1 (en) * | 2013-03-15 | 2016-02-18 | Transtar Group, Ltd. | New and improved system for processing various chemicals and materials |
| CN203347776U (en) * | 2013-07-24 | 2013-12-18 | 东北石油大学 | Oil-gas-water three-phase flow gas-liquid separation device for yield profile logging |
Non-Patent Citations (1)
| Title |
|---|
| 刘德新: "《油田污水处理》", 30 April 2015, 石油大学出版社 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105797434A (en) * | 2016-03-14 | 2016-07-27 | 浙江理工大学 | Separation and collection device |
| CN105797434B (en) * | 2016-03-14 | 2018-04-06 | 浙江理工大学 | The de- collection device of one kind point |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105858801B (en) | 2021-05-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206767690U (en) | A kind of ozone air-float reactor | |
| CN101417184A (en) | Gas floatation separation device | |
| CN107473306A (en) | A kind of adjustable single tank twin-stage cyclone air-flotation device of stabilizing feed well | |
| CN203212356U (en) | Unpowered oil-water separation device | |
| CN105858801A (en) | High-salinity oily sewage post-treatment device | |
| CN202576037U (en) | Unpowered oil-storage type oil water separation system | |
| CN105413238B (en) | A kind of oil water separator | |
| CN105858800A (en) | Oily sewage separation-removal post-treatment device | |
| CN105858929A (en) | Seawater oily sewage treatment device | |
| CN105727597B (en) | A kind of drain oil recovery equipment | |
| CN105776422B (en) | A kind of oily water separating equipment | |
| CN106064843A (en) | A kind of resistant oily-water seperating equipment | |
| CN101139122A (en) | Multifunctional oil-contained waste water treatment device | |
| CN105797434B (en) | The de- collection device of one kind point | |
| CN105858803A (en) | Oily sewage treatment device | |
| CN103466751B (en) | Coarse graining oil separation apparatus for processing oil-containing wastewater | |
| CN105776423B (en) | A kind of circulating purifying device | |
| CN209138055U (en) | A kind of novel pipe oil water separator | |
| CN207891090U (en) | A kind of oily waste water separator | |
| CN113023914A (en) | Oil-water separation treatment system and treatment method for oil field chemical flooding oil displacement produced water | |
| CN206553296U (en) | A kind of municipal sewage oil stain isolation of purified system | |
| CN202265493U (en) | Sludge concentrating device | |
| CN205999181U (en) | Oily waste water integrated treatment unit | |
| CN206089268U (en) | Novel oiliness waste water treatment device | |
| CN115477406B (en) | Micro-nano bubble treatment equipment for sewage |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |