CN205216403U - Swash plate deoiling device - Google Patents
Swash plate deoiling device Download PDFInfo
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- CN205216403U CN205216403U CN201521103301.3U CN201521103301U CN205216403U CN 205216403 U CN205216403 U CN 205216403U CN 201521103301 U CN201521103301 U CN 201521103301U CN 205216403 U CN205216403 U CN 205216403U
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Abstract
The utility model discloses a swash plate deoiling device, including the sedimentation tank, arrange the mud sump and remove the oil tank, sedimentation tank upper portion sets up the disengagement zone, the middle part sets up the swash plate district, the bottom sets up the mud district, disengagement zone one side sets up water inlet manifold, the opposite side sets up the outfall sewer, swash plate district one side sets up the coarse grain and handles the pipe, the union coupling is handled to the coarse grain has the coarse grain treater, mud district bottom sets up the spiral and stirs the cage, mud pipe one end is stirred the cage with the spiral and is connected, the other end is connected with row's mud sump, drinking -water pipe one end is connected with row's mud sump, the other end through a control flap respectively with the coarse grain treater with advance oil pipe one end and be connected, it is connected with the tank deck portion that degreases to advance the oil pipe other end, it sets up out oil pipe to remove tank base portion, it is connected with row oil pipe and drain pipe one end respectively through the 2nd control flap to go out oil pipe, the drain pipe other end with arrange the mud sump and connect, arrange the mud sump and set up useless mud discharge pipe. The utility model discloses simple structure, deoiling with low costs is efficient, and the quality of water that goes out water is good.
Description
Technical field
The utility model belongs to field of mechanical technique, especially relates to a kind of sloping panel deoiling unit.
Background technology
Oily substance is entered in water by different approaches and forms oily waste water.Because it has a large capacity and a wide range, and the feature being difficult to process becomes and a kind ofly endangers serious waste water.Its source mainly contains: the oil exploitation in petroleum industry and the processing of oil product, refinement, storage and transport; Carwash in transport industry, the oily waste water of the discharge such as the oil-washing tank of railway locomotive depot; The steel rolling water produced in machine-building process, the waste water based on oil emulsion such as lubricating oil; Also a large amount of oily substances is contained in addition in catering trade, textile industry, food processing industry and other manufacturing waste water.
Inevitably with impurity such as greases in industrial circulating water, because the equipment at the places such as lubrication station is revealed, the oil skimming pipe that current oil interceptor collection oil slick adopts and steel band Oil scraper all exist installation site need be fixed, general is all utilize the oil absorption of special substance to adsorb oil slick, the oil slick of a neighbouring fritter can only be collected, adsorption efficiency is too low, water-oil separating is inadequate, the oil slick water content of collecting is higher, add the difficulty of after-treatment, oil content in water is often made to remain high, recirculated water oil-containing not only corrosion pipeline, and the adhesive ability increasing impurity.Oil skimming pipe and steel band Oil scraper are all the oleophilic drainage performance absorption oil slick relying on special substance, water-oil separating is not opened, and receives oily effect and take effect slowly, Long-Time Service to play effect, once change appears in recirculated water oil content, oil skimming pipe and steel band Oil scraper will lose efficacy.Oil skimming pipe and steel band Oil scraper complex structure, fault rate is high.
Notification number CN201770516U discloses a kind of swash plate coalescent deoiling oil removal pressure sedimentation device, primary structure comprises shell, coalescent pack, separating filler, hybrid reaction cylinder, dividing plate, deflection plate, sewage inlet and entrance liquid distributor, crude oil reservoir and oil export, intermediate waste collector and outlet, intermediate waste entrance, sewage collector and blowoff valve, sewage inlet is positioned at housing rear head bottom, be connected with the liquid distributor of rear lower in housing, coalescent pack and separating filler is established before liquid distributor, hybrid reaction cylinder is established at casing center position, on hybrid reaction cylinder, rear side upper end is provided with dividing plate to housing top, hybrid reaction cylinder bottom is wastewater inlet, dividing plate rear lower establishes sewage collector, water out is established in sewage collector bottom, hybrid reaction cylinder procapsid establishes baffling behind top to middle and lower part, separating filler is established between deflection plate to front head, housing front head place establishes sewage collector and outlet of sewer, the dirty device of storage and sewage draining exit is established in the bottom of separating filler, oil conservator and oil-out are established in housing top before dividing plate back and deflection plate, this device adopts coalescent pack, separating filler and vertical vortex hybrid reaction cylinder, adopt the oil extraction of crude oil reservoir, store up dirty device blowdown oil removing, the basis utilizing swash plate is improved and with the addition of a large amount of waste-oil scavenger, add overall cost, also make operation more complicated loaded down with trivial details.
Utility model content
In view of this, the purpose of this utility model is for the deficiencies in the prior art, and provide a kind of structure simple, cost is low, and sedimentation effect is good, and can realize the removal of sump oil and solid suspension in sewage, oil removal efficiency is high, and the water quality of water outlet is good.
For achieving the above object, the utility model by the following technical solutions:
A kind of sloping panel deoiling unit, comprise sedimentation basin, spoil disposal pond and oil removing pot, also comprise water inlet manifold, outfall sewer, coarse granule process pipe, discharge pipeline, drinking-water pipe, oil inlet pipe and flowline, described sedimentation basin top arranges Disengagement zone, swash plate district is set in the middle part of described sedimentation basin, mud district is set bottom described sedimentation basin, the top of side, described Disengagement zone sidewall has the water inlet communicated with water inlet manifold, the top of described Disengagement zone opposite side sidewall offers the delivery port communicated with outfall sewer, side, described swash plate district arranges coarse granule process pipe, described coarse granule process pipe is connected with coarse granule processor, bottom described mud district, spiral stirring cage is set, described discharge pipeline one end is connected with described spiral stirring cage, the other end is connected with described spoil disposal pond, described drinking-water pipe one end is connected with spoil disposal pond, the other end is connected with described coarse granule processor and described oil inlet pipe one end respectively by the first by-pass valve control, the described oil inlet pipe other end is connected with described oil removing pot top, oil pipe is set out bottom described oil removing pot, described flowline is connected with oil exit pipe and drainpipe one end respectively by the second by-pass valve control, the described drainpipe other end is connected with described spoil disposal pond, described spoil disposal pond arranges useless mud discharge pipe, the sidewall in described swash plate district and the angle of central axis are all set to 20 degree, the sidewall in described mud district and the angle of central axis are all set to 30 degree.
Preferably, described water inlet manifold and outfall sewer are provided with the 3rd by-pass valve control.
Preferably, between described coarse granule process pipe and swash plate district, screen pack is set.
Preferably, described discharge pipeline arranges mud valve.
Preferably, described water inlet and delivery port are all set to circle.
The beneficial effects of the utility model are:
1. whole oil removing system is divided into two parts that are mutually related by the utility model, the first by-pass valve control is added in the device of desilt and oil removing that dewaters, second by-pass valve control and mud valve, the effect of oil removing is issued in the condition not increasing operating cost, the cooperation control of the first by-pass valve control and the second by-pass valve control is passed through when swash plate oil removing, utilize the light principle of oil ratio anharmonic ratio water, gradually swash plate bottom water is drained, last oil removing, also protect sedimentation basin swash plate to damage because of deposition simultaneously, oil removal efficiency is high, the water quality of water outlet is good, coarse granule process pipe and coarse granule processor are set in swash plate district, what can realize sump oil and solid suspension in sewage is separated removal, decrease the workload that manual cleaning is separated oil removing, improve stability and the high efficiency of settling system and oil removing system.
2. the sidewall in the utility model swash plate district and the angle of central axis are all set to 20 degree, make water (flow) direction and sludge settling direction angled, ensure that deposition efficiency does not affect by water flow velocity, under current stall, heavier muddy water continues to move downward, and lighter oil loses speed along outside and floats; Again make oil slick float after downward current collision point water swash plate, oil slick is separated by coarse granule processor and delivers to oil removing pot by the first by-pass valve control be separated through going out coarse granule process pipe; The profit that may adulterate in spoil disposal pond by drinking-water pipe again suction oil inlet pipe carry out secondary separation, deoiling effect is remarkable, and water-oil separating is thorough, receives oily efficiency high.
3. the sidewall in the utility model mud district and the angle of central axis are all set to 30 degree, mud sinks through mud district, drop down onto gathering in heaps bottom the body of pond after precipitation and be thoroughly separated with oil with current, can not deposit in pond body bottom corner, be beneficial to and discharge from discharge pipeline, by the mud valve of spiral stirring cage by discharge pipeline, mud is discharged, mud valve can control speed and the sludge volume of spoil disposal, more sound removing mud, thus can not secondary pollution water body, obtain the water of better water quality after ensureing oil removing.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment 1;
Fig. 2 is the structural representation of the utility model embodiment 2;
Wherein, 1-Disengagement zone, 2-swash plate district, 3-mud district, 4-water inlet manifold, 5-outfall sewer, 6-delivery port, 7-coarse granule process pipe, 8-coarse granule processor, 9-spiral stirring cage, 10-discharge pipeline, 11-spoil disposal pond, 12-drinking-water pipe, 13-oil inlet pipe, 14-oil removing pot, 15-flowline, 16-oil exit pipe, 17-second by-pass valve control, 18-drainpipe, 19-gives up mud discharge pipe, 20-first control valve, 21-the 3rd by-pass valve control, 22-mud valve.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is further described.
Embodiment 1
As shown in Figure 1, a kind of sloping panel deoiling unit, comprise sedimentation basin, spoil disposal pond 11 and oil removing pot 14, also comprise water inlet manifold 4, outfall sewer 5, coarse granule process pipe 7, discharge pipeline 10, drinking-water pipe 12, oil inlet pipe 13 and flowline 15, the inner wall surface of water inlet manifold 4, outfall sewer 5, coarse granule process pipe 7, discharge pipeline 10, drinking-water pipe 12, oil inlet pipe 13 and flowline 15 is all through hydrophobic treatment, to guarantee the speed that current keep certain, reduce the friction to current and obstruction.
Sedimentation basin top arranges Disengagement zone 1, swash plate district 2 is set in the middle part of sedimentation basin, mud district 3 is set bottom sedimentation basin, the top of side, Disengagement zone 1 sidewall has the circular water inlet communicated with water inlet manifold 5, the top of Disengagement zone 1 opposite side sidewall offers the circular outlets 6 communicated with outfall sewer 5, water inlet manifold 4 and outfall sewer 5 are provided with the 3rd by-pass valve control 21, effectively to control water velocity, side, swash plate district 2 arranges coarse granule process pipe 7, coarse granule process pipe 7 is connected with coarse granule processor 8, the sidewall in swash plate district 2 and the angle of central axis are all set to 20 degree, make water (flow) direction and sludge settling direction angled, ensure that deposition efficiency does not affect by water flow velocity, under current stall, heavier muddy water continues to move downward, and lighter oil loses speed along outside and floats, oil slick is again made to float after downward current collision point water swash plate, oil slick is separated by coarse granule processor 8 and delivers to oil removing pot 14 by the first by-pass valve control 20 be separated through going out coarse granule process pipe 7, what screen pack, coarse granule process pipe 7 and coarse granule processor 8 can realize sump oil and solid suspension in sewage is separated removal, decreases the workload that manual cleaning is separated oil removing.
Drinking-water pipe 12 one end is connected with spoil disposal pond 11, the other end is connected with coarse granule processor 8 and oil inlet pipe 13 one end respectively by the first by-pass valve control 20, drinking-water pipe 12 is again extracted out and is again entered oil removing pot 14 by being separated halfway profit in spoil disposal pond 11 and carry out separation oil removing, the profit that first by-pass valve control 20 controls under coordination drinking-water pipe 12 and coarse granule processor 8 process in this process carries out the oil removing that reasonably circulates, oil inlet pipe 13 other end is connected with oil removing pot 14 top, oil pipe 15 is set out bottom oil removing pot 14, flowline 15 is connected with oil exit pipe 16 and drainpipe 18 one end respectively by the second by-pass valve control 17, by the cooperation control of the first by-pass valve control 20 and the second by-pass valve control 21, utilize the light principle of oil ratio anharmonic ratio water, gradually swash plate bottom water is drained, remaining moisture is also discharged in spoil disposal pond 11 by drainpipe 18 by last oil removing, to be drawn water to circulate repeatedly oil removing by drinking-water pipe 12 again.
The sidewall in mud district 3 and the angle of central axis are all set to 30 degree, spiral stirring cage 9 is set bottom mud district 3, discharge pipeline 10 one end is connected with spiral stirring cage 9, the other end is connected with spoil disposal pond 11, spoil disposal pond 11 also arranges useless mud discharge pipe 19, and mud sinks through mud district 3, drops down onto gathering in heaps bottom the body of pond and be thoroughly separated with oil with current after precipitation, can not deposit in pond body bottom corner, be beneficial to and discharge from useless mud discharge pipe 19.
Embodiment 2
Embodiment 2 is roughly the same with the structure of embodiment 1, unlike: as shown in Figure 2, discharge pipeline 10 arranges mud valve 22, by the mud valve 22 of spiral stirring cage 9 by discharge pipeline 10, mud is discharged, mud valve 22 can control speed and the sludge volume of spoil disposal, more sound removing mud, thus can not secondary pollution water body, obtain the water of better water quality after ensureing oil removing.
In a word, the utility model structure is simple, and cost is low, and sedimentation effect is good, and can realize the removal of sump oil and solid suspension in sewage, oil removal efficiency is high, and the water quality of water outlet is good.
What finally illustrate is, above embodiment is only in order to illustrate the technical solution of the utility model and unrestricted, other amendments that those of ordinary skill in the art make the technical solution of the utility model or equivalently to replace, only otherwise depart from the spirit and scope of technical solutions of the utility model, all should be encompassed in the middle of right of the present utility model.
Claims (5)
1. a sloping panel deoiling unit, comprise sedimentation basin, spoil disposal pond and oil removing pot, it is characterized in that: also comprise water inlet manifold, outfall sewer, coarse granule process pipe, discharge pipeline, drinking-water pipe, oil inlet pipe and flowline, described sedimentation basin top arranges Disengagement zone, swash plate district is set in the middle part of described sedimentation basin, mud district is set bottom described sedimentation basin, the top of side, described Disengagement zone sidewall has the water inlet communicated with water inlet manifold, the top of described Disengagement zone opposite side sidewall offers the delivery port communicated with outfall sewer, side, described swash plate district arranges coarse granule process pipe, described coarse granule process pipe is connected with coarse granule processor, bottom described mud district, spiral stirring cage is set, described discharge pipeline one end is connected with described spiral stirring cage, the other end is connected with described spoil disposal pond, described drinking-water pipe one end is connected with spoil disposal pond, the other end is connected with described coarse granule processor and described oil inlet pipe one end respectively by the first by-pass valve control, the described oil inlet pipe other end is connected with described oil removing pot top, oil pipe is set out bottom described oil removing pot, described flowline is connected with oil exit pipe and drainpipe one end respectively by the second by-pass valve control, the described drainpipe other end is connected with described spoil disposal pond, described spoil disposal pond arranges useless mud discharge pipe, the sidewall in described swash plate district and the angle of central axis are all set to 20 degree, the sidewall in described mud district and the angle of central axis are all set to 30 degree.
2. a kind of sloping panel deoiling unit as claimed in claim 1, is characterized in that: described water inlet manifold and outfall sewer are provided with the 3rd by-pass valve control.
3. a kind of sloping panel deoiling unit as claimed in claim 1, is characterized in that: arrange screen pack between described coarse granule process pipe and swash plate district.
4. a kind of sloping panel deoiling unit as claimed in claim 1, is characterized in that: described discharge pipeline arranges mud valve.
5. a kind of sloping panel deoiling unit as claimed in claim 1, is characterized in that: described water inlet and delivery port are all set to circle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521103301.3U CN205216403U (en) | 2015-12-28 | 2015-12-28 | Swash plate deoiling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521103301.3U CN205216403U (en) | 2015-12-28 | 2015-12-28 | Swash plate deoiling device |
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| Publication Number | Publication Date |
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| CN205216403U true CN205216403U (en) | 2016-05-11 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201521103301.3U Active CN205216403U (en) | 2015-12-28 | 2015-12-28 | Swash plate deoiling device |
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| CN (1) | CN205216403U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111991914A (en) * | 2020-07-28 | 2020-11-27 | 四川中创石油设备有限公司 | Full-automatic flow distribution box and flow distribution method |
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2015
- 2015-12-28 CN CN201521103301.3U patent/CN205216403U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111991914A (en) * | 2020-07-28 | 2020-11-27 | 四川中创石油设备有限公司 | Full-automatic flow distribution box and flow distribution method |
| CN111991914B (en) * | 2020-07-28 | 2022-09-13 | 四川中创石油设备有限公司 | Full-automatic flow distribution box and flow distribution method |
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