CN204550234U - Clustered aggregates is reclaimed in a kind of oil removal - Google Patents
Clustered aggregates is reclaimed in a kind of oil removal Download PDFInfo
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- CN204550234U CN204550234U CN201520117772.3U CN201520117772U CN204550234U CN 204550234 U CN204550234 U CN 204550234U CN 201520117772 U CN201520117772 U CN 201520117772U CN 204550234 U CN204550234 U CN 204550234U
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- oil
- room
- oil removal
- reclaimed
- pipe
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Abstract
The utility model patent relates to a kind of sewage disposal device, refers in particular to a kind of oil removal simultaneously can reclaiming heavy oil and light oil and reclaims clustered aggregates.One-level oil removal is reclaimed heavy fuel equipment, cluster tool such as connection such as system in combination bunchiness such as secondary oil removal recovery light oil equipment and oil-collecting equipment etc., between each equipment, carry out separately isolation by dividing plate.The utility model can reclaim heavy oil in sewage and oil slick, part dispersion oils light oil material simultaneously, is conducive to green circulation economy.
Description
Technical field
The utility model patent relates to a kind of sewage disposal device, refers in particular to a kind of oil removal simultaneously can reclaiming heavy oil and light oil and reclaims clustered aggregates.
Background technology
At present, in industry oily(waste)water, some organic pollutants is often present in sewage with oil phase, these oily substances exist with the form of heavy oil and oil slick, dispersion oils light oil to a great extent, if this oily substance treatment effect is bad, often very easily affect postorder sewage treatment process.
Gravity separation heavy oil and oil slick, dispersion oils light oil are most widely used general, the most practical a kind of oil-containing sewage treatment techniques, and this method can be used for the oil slick, part dispersion oils light oil and the heavy oil that reclaim in sewage.
Conventional gravity formula is separated oil removal facility and is generally single separation oil removal facility, and the overwhelming majority is parallel flow intercepter or single tilted plate intercepter, is separated oil slick, dispersion oils light oil material to process; Reclaim for the oil removal of heavy oil kind material, often usually adopt and set up individual curing facility and carry out otherwise processed, the oil slick on Gravity separate oil removal facility upper strata often needs artificial clearly to wash in a pan simultaneously, and operation of equipment intensity is comparatively large, and oil removal efficiency is low; Simultaneously traditional oil removal facility process light oil type material adopts flocculation reaction deposition usually, oil removal oil removing mode processes, and is unfavorable for green circulation economy.
Tradition oil removal facility and bunkerage unit often independent split type facility, arrange dispersion, and total floor space is comparatively large, land utilization ratio is not high.
Summary of the invention
The utility model patent is exactly for the problems referred to above, provides a kind of oil removal simultaneously can reclaiming heavy oil and light oil to reclaim clustered aggregates.
The technical scheme of the utility model patent: in order to solve the problem,
One-level oil removal is reclaimed heavy fuel equipment, cluster tool such as connection such as system in combination bunchiness such as secondary oil removal recovery light oil equipment and oil-collecting equipment etc., between each equipment, carry out separately isolation by dividing plate.
Described oil removal is reclaimed clustered aggregates and is comprised one-level oil removal recovery room, secondary oil removal recovery room, collecting chamber and gathering room.
One-level oil removal is reclaimed indoor middle part and is provided with water inlet pipe, cyclonic separation room, and bottom is provided with and arranges the bunker A oil recovery room that the first swash plate forms inverted cone-shaped structure; Bottom arranges recovery first oil pipe, and top is provided with the first flow deflector; Separated by the first dividing plate between gathering room with one-level oil removal room, one-level oil removal recovery room is reclaimed between room with secondary oil removal and is separated by second partition.
Secondary oil removal is reclaimed top, room and is provided with row's light oil overflow weir and row's light oil mouth of pipe, and bottom is provided with two bunker A oils arranging the second swash plate formation inverted cone-shaped structure and reclaims room; Two bunker A oils reclaim bottom room and arrange the second recovery oil pipe, and two bunker A oils reclaim side, room and are provided with the second flow deflector and the 3rd flow deflector that are communicated with collecting chamber.
Secondary oil removal is reclaimed between room with collecting chamber and is separated by the 3rd dividing plate, the second flow deflector and the 3rd flow deflector; Oil removal filler is provided with between second flow deflector and the 3rd flow deflector.
Collecting chamber top is provided with effluent overflow weir water, effluent pipe mouth; Bottom is provided with collecting chamber end-of-the-pipe.
Gathering room top arranges to arrange into the light oil mouth of pipe and bottom reclaims the light oil mouth of pipe, and the light oil mouth of pipe that enters on top reclaims the low 500mm of row's light oil mouth of pipe of room than secondary oil removal.
Described oil removal is reclaimed clustered aggregates top and is sealed, and arranges inspection manhole.
Sewage containing heavy oil and light oil tangentially enters by water inlet pipe the cyclonic separation room that room is reclaimed in one-level oil removal, in the indoor formation tangential swirl motion of cyclonic separation, carries out one-level oily water separation; Heavy oil eddy flow after one-level oily water separation sinks down into a bunker A oil and reclaims indoor; Waste water with light oil eddy flow after one-level oily water separation rise through the first flow deflector water conservancy diversion enter secondary oil removal reclaim room carry out secondary oily water separation.
The sewage that room is reclaimed in secondary oil removal carries out oily water separation again by the oil removal filler between the second flow deflector and the 3rd flow deflector, and the sewage after separation enters collecting chamber, rises through draining overflow weir and discharges through drain pipe port.
Reclaim indoor in secondary oil removal, in sewage, a small amount of unsegregated heavy oil continues to sink down into two bunker A oils recovery indoor; The light oil of secondary oil removal recovery room rises through row's light oil overflow weir and certainly flow to gathering room through row's light oil mouth of pipe and the outer pipeline of oil extraction through entering the light oil mouth of pipe; Gathering room arranges tank level control system, regularly the light oil of gathering room is pumped out recycled through being reclaimed the light oil mouth of pipe with pump by Liquid level.
The heavy oil of one-level oil removal recovery room and secondary oil removal recovery room is pumped out by the first recovery oil pipe and the second recovery oil pipe pump respectively and is recycled.
Described water inlet pipe arranges and tangentially enters cyclonic separation room; Cyclonic separation room central structure arranges cylindrical tube structure, and upper and lower part is arranged to turbination and conical tube body structure respectively; Cyclonic separation room arranges cyclonic separation room strut member and is fixed in the middle part of the casing of a bunker A oil recovery room; The opening angle of turbination and divergent-cone wall is 75 °.
Described effluent overflow weir water 35 ~ 50mm lower than row's light oil height of weir plate, and effluent overflow weir water weir plate arranges adjustable.
Described second reclaims oil pipe is provided with some oil supply holes, aperture φ 32 ~ 50mm.
The first described flow deflector is bending-type structure, and top differs 350mm with effluent overflow weir water height.
The second described flow deflector and the 3rd flow deflector angle of inclination arrange 45 °.
The first described swash plate and the second swash plate angle of inclination arrange 55 °.
Described oil removal filler employing aperture is the inclined tube filler of φ 40mm.
Compared with processed conventionally traditional oil removal facility:
This oil removal is reclaimed clustered aggregates and is adopted oily(waste)water tangentially to enter one-level oil removal to reclaim the cyclonic separation room of indoor cylindrical tube structure and opening angle and be in the turbination of 75 ° and divergent-cone wall and carry out the tangential rotary motion of current, carry out one-level oily water separation containing the heavy oil in waste water and light oil and water, the heavy oil recycling efficiency in sewage is up to more than 98.5%.
Oily(waste)water after preliminary heavy oil oily water separation enters secondary oil removal recovery indoor by the first flow deflector of bending-type structure and carries out secondary oily water separation, and secondary oil removal is reclaimed room and adopted inclined tube-type oil-water separating structure.Employing aperture is that the inclined tube filler of φ 40mm can make the separating area of per unit volume increase, and oil-water separation is good; Oil slick in sewage, part dispersion oils light oil material recycling efficiency are up to more than 98.5%; Carry out the heavy oil secondary recovery in waste water further, the heavy oil secondary recovery processing efficiency in sewage is up to more than 98.5% simultaneously.
Often only conventional processing is separated oil slick to tradition oil removal facility, dispersion oils is main light oil material; It is serial module structure unitized construction that clustered aggregates is reclaimed in this oil removal, is connected between each room by dividing plate, overflow passage structure; The heavy oil in sewage and oil slick, part dispersion oils light oil material can be reclaimed simultaneously, be conducive to green circulation economy.
This oil removal recovery clustered aggregates is simple and compact for structure, and floor space is little, can save floor space more than 30%, less investment, and operation operational management is simple, and oily water separation processing efficiency is high, for further subsequent treatment process creates good condition of water quality.
Accompanying drawing explanation
Fig. 1 is oil removal clustered aggregates vertical view.
Fig. 2 is oil removal clustered aggregates A-A vertical planning drawing.
Fig. 3 oil removal clustered aggregates B-B vertical planning drawing.
Fig. 4 oil removal clustered aggregates C is to vertical planning drawing.
Fig. 5 oil removal clustered aggregates D is to vertical planning drawing.
Fig. 6 oil removal clustered aggregates E-E vertical planning drawing.
Fig. 7 oil removal clustered aggregates F-F vertical planning drawing.
Fig. 8 oil removal clustered aggregates G-G vertical planning drawing.
Wherein: 1, oil separation equipment casing; 2, effluent pipe mouth; 3, collecting chamber end-of-the-pipe; 4, manhole; 5, second oil pipe is reclaimed; 6, first oil pipe is reclaimed; 7, water inlet pipe; 8, the light oil mouth of pipe is reclaimed; 9, the light oil mouth of pipe is entered; 10, the outer pipeline of oil extraction; 11, the light oil mouth of pipe is arranged; 12, the first dividing plate; 13, the first swash plate; 14, second partition; 15, the second swash plate; 16, the second flow deflector; 17, the 3rd dividing plate; 18, the 3rd flow deflector; 19, packing support part; 20, cyclonic separation room; 21, cyclonic separation room strut member; 22, the first flow deflector; 23, light oil overflow weir is arranged; 24, effluent overflow weir water; 25, oil removal filler; 26, gathering room; 27, room is reclaimed in one-level oil removal; 28, room is reclaimed in secondary oil removal; 29, collecting chamber; 30, a bunker A oil reclaims room; 31, two bunker A oils reclaim room.
Embodiment
As shown in Fig. 1 ~ 7, the technical scheme for the utility model patent provides a kind of novel oil removal clustered aggregates schematic diagram.
Containing a large amount of heavy oil and oil slick, part dispersion oils light oil material in certain enterprise's production waste, if oily substance is unprocessed directly enter the surface that subsequent biochemical treatment system can be attached to active sludge, suppress the normal growth of microorganism in biochemical treatment unit, directly will affect biochemical system to run, the sludge activity of Sludge System can be destroyed time serious, affect Biochemical Treatment, oil removal pre-treatment need be carried out to this oily(waste)water.
Described equipment comprises one-level oil removal and reclaims room 27, secondary oil removal recovery room 28 and gathering room 26 and collecting chamber 29 4 unit integral parts, and structure formation is serial module structure clustered aggregates.
One-level oil removal is reclaimed middle part in room 27 and is provided with water inlet pipe 7, cyclonic separation room 20; Bottom is provided with and arranges the bunker A oil recovery room 30 that the first swash plate 13 forms pyramidal structure; Bottom is arranged reclaims oil pipe 1; Top is provided with the first flow deflector 22; Separated by the first dividing plate 12 between gathering room 26 with one-level oil removal room 27, one-level oil removal recovery room 27 is reclaimed between room 28 with secondary oil removal and is separated by second partition 14.
Secondary oil removal is reclaimed top, room 28 and is provided with row's light oil overflow weir 23 and row's light oil mouth of pipe 11, and bottom is provided with the two bunker A oils recovery rooms 31 that the second swash plate 15 forms pyramidal structure; Bottom arranges recovery second oil pipe 5 and the second flow deflector 16.
Secondary oil removal is reclaimed between room 28 with collecting chamber 29 and is separated by the 3rd dividing plate 17, second flow deflector 16 and the 3rd flow deflector 18; Oil removal filler 25 is provided with between second flow deflector 16 and the 3rd flow deflector 18.
Collecting chamber 29 top is provided with effluent overflow weir water 24, effluent pipe mouth 2; Bottom is provided with collecting chamber end-of-the-pipe 3.
Gathering room 26 arranges into the light oil mouth of pipe 9 and reclaims the light oil mouth of pipe 8.
Oil separation equipment top seals, and arranges inspection manhole 4.
Sewage containing heavy oil and light oil tangentially enters by water inlet pipe 7 the cyclonic separation room 20 that room 27 is reclaimed in one-level oil removal, forms tangential swirl motion, carry out one-level oily water separation in cyclonic separation room 20; Heavy oil eddy flow after one-level oily water separation sinks down into a bunker A oil and reclaims in room 30; Waste water with light oil eddy flow after one-level oily water separation rise through flow deflector 1 water conservancy diversion enter secondary oil removal reclaim room 28 carry out secondary oily water separation.
The sewage that room 28 is reclaimed in secondary oil removal carries out oily water separation again by the oil removal filler 25 between flow deflector 2 16 and flow deflector 3 18, and the sewage after separation enters collecting chamber 29, rises through draining overflow weir 24 and discharges through drain pipe port 2.
Reclaim in room 28 in secondary oil removal, in sewage, a small amount of unsegregated heavy oil continues to sink down in two bunker A oils recovery rooms 31; The light oil of secondary oil removal recovery room rises through row's light oil overflow weir 23 and certainly flow to gathering room 26 through row's light oil mouth of pipe 11 and the outer pipeline 10 of oil extraction through entering the light oil mouth of pipe 9.Gathering room 26 arranges tank level control system, regularly the light oil of gathering room is pumped out recycled through being reclaimed the light oil mouth of pipe 8 with pump by Liquid level.
One-level oil removal is reclaimed heavy oil that room 27 and secondary oil removal reclaim room 28 and is reclaimed oil pipe 5 by recovery first oil pipe 6 and second respectively and to pump out with pump and recycle.
Described water inlet pipe 7 arranges and tangentially enters cyclonic separation room 20; Cyclonic separation room 20 central structure arranges cylindrical tube structure, and upper and lower part arranges conical tube body structure; Cyclonic separation room arranges cyclonic separation room strut member 21 and is fixed in the middle part of the casing of a bunker A oil recovery room.
Described effluent overflow weir water 24 is than the highly low 35 ~ 50mm of row's light oil overflow weir 23, and effluent overflow weir water weir plate arranges adjustable.
Described recovery second oil pipe 5 is provided with some oil supply holes, aperture φ 32 ~ 50mm.
The first described flow deflector 22 is bending-type structure, and top highly differs 350mm with effluent overflow weir water 24.
The second described flow deflector 16 and the 3rd flow deflector 18 angle of inclination arrange 45 °.
The first described swash plate 13 and the second swash plate 15 angle of inclination arrange 55 °.
Described oil removal filler 25 adopts aperture to be the inclined tube filler of φ 40mm.
This oil removal is reclaimed clustered aggregates and is adopted oily(waste)water tangentially to enter one-level oil removal to reclaim the cyclonic separation room of indoor cylindrical tube structure and opening angle and be in the turbination of 75 ° and divergent-cone wall and carry out the tangential rotary motion of current, carry out one-level oily water separation containing the heavy oil in waste water and light oil and water, the heavy oil recycling efficiency in sewage is up to more than 98.5%.
Oily(waste)water after preliminary heavy oil oily water separation enters secondary oil removal recovery indoor by the first flow deflector of bending-type structure and carries out secondary oily water separation, and secondary oil removal is reclaimed room and adopted inclined tube-type oil-water separating structure; Employing aperture is that the inclined tube filler of φ 40mm can make the separating area of per unit volume increase, and oil-water separation is good; Oil slick in sewage, part dispersion oils light oil material recycling efficiency are up to more than 98.5%.Carry out the heavy oil secondary recovery in waste water further, the heavy oil secondary recovery processing efficiency in sewage is up to more than 98.5% simultaneously.
Often only conventional processing is separated oil slick to tradition oil removal facility, dispersion oils is main light oil material.It is serial module structure unitized construction that clustered aggregates is reclaimed in this oil removal, is connected between each room by dividing plate, overflow passage structure.The heavy oil in sewage and oil slick, part dispersion oils light oil material can be reclaimed simultaneously, be conducive to green circulation economy.
This oil removal recovery clustered aggregates is simple and compact for structure, and floor space is little, can save floor space more than 30%, less investment, and operation operational management is simple, and oily water separation processing efficiency is high, for further subsequent treatment process creates good condition of water quality.
Claims (8)
1. a clustered aggregates is reclaimed in oil removal, it is characterized in that: described equipment comprises one-level oil removal and reclaims room, secondary oil removal recovery room, collecting chamber and gathering room;
One-level oil removal is reclaimed indoor middle part and is provided with water inlet pipe, cyclonic separation room, and bottom is provided with and arranges the bunker A oil recovery room that the first swash plate forms inverted cone-shaped structure; Bottom arranges recovery first oil pipe, and top is provided with the first flow deflector; Separated by the first dividing plate between gathering room with one-level oil removal room, one-level oil removal recovery room is reclaimed between room with secondary oil removal and is separated by second partition;
Secondary oil removal is reclaimed top, room and is provided with row's light oil overflow weir and row's light oil mouth of pipe, and bottom is provided with two bunker A oils arranging the second swash plate formation inverted cone-shaped structure and reclaims room; Two bunker A oils reclaim bottom room and arrange the second recovery oil pipe, and two bunker A oils reclaim side, room and are provided with the second flow deflector and the 3rd flow deflector that are communicated with collecting chamber;
Secondary oil removal is reclaimed between room with collecting chamber and is separated by the 3rd dividing plate, the second flow deflector and the 3rd flow deflector; Oil removal filler is provided with between second flow deflector and the 3rd flow deflector;
Collecting chamber top is provided with effluent overflow weir water, effluent pipe mouth; Bottom is provided with collecting chamber end-of-the-pipe;
Gathering room top arranges and arranges the recovery light oil mouth of pipe into the light oil mouth of pipe and bottom;
Sewage containing heavy oil and light oil tangentially enters by water inlet pipe the cyclonic separation room that room is reclaimed in one-level oil removal, in the indoor formation tangential swirl motion of cyclonic separation, carries out one-level oily water separation; Heavy oil eddy flow after one-level oily water separation sinks down into a bunker A oil and reclaims indoor; Waste water with light oil eddy flow after one-level oily water separation rise through the first flow deflector water conservancy diversion enter secondary oil removal reclaim room carry out secondary oily water separation;
The sewage that room is reclaimed in secondary oil removal carries out oily water separation again by the oil removal filler between the second flow deflector and the 3rd flow deflector, and the sewage after separation enters collecting chamber, rises through draining overflow weir and discharges through drain pipe port;
Reclaim indoor in secondary oil removal, in sewage, a small amount of unsegregated heavy oil continues to sink down into two bunker A oils recovery indoor; The light oil of secondary oil removal recovery room rises through row's light oil overflow weir and certainly flow to gathering room through row's light oil mouth of pipe and the outer pipeline of oil extraction through entering the light oil mouth of pipe; Gathering room arranges tank level control system, regularly the light oil of gathering room is pumped out recycled through being reclaimed the light oil mouth of pipe with pump by Liquid level;
The heavy oil of one-level oil removal recovery room and secondary oil removal recovery room is pumped out by the first recovery oil pipe and the second recovery oil pipe pump respectively and is recycled.
2. clustered aggregates is reclaimed in a kind of oil removal as claimed in claim 1, it is characterized in that: the light oil mouth of pipe that enters on gathering room top reclaims the low 500mm of row's light oil mouth of pipe of room than secondary oil removal.
3. clustered aggregates is reclaimed in a kind of oil removal as claimed in claim 1, it is characterized in that: described oil removal is reclaimed clustered aggregates top and sealed, and arranges inspection manhole.
4. clustered aggregates is reclaimed in a kind of oil removal as claimed in claim 1, it is characterized in that: described water inlet pipe arranges and tangentially enters cyclonic separation room; Cyclonic separation room central structure arranges cylindrical tube structure, and upper and lower part is arranged to turbination and conical tube body structure respectively; Cyclonic separation room arranges cyclonic separation room strut member and is fixed in the middle part of the casing of a bunker A oil recovery room; The opening angle of turbination and divergent-cone wall is 75 °.
5. clustered aggregates is reclaimed in a kind of oil removal as claimed in claim 1, it is characterized in that: described effluent overflow weir water 35 ~ 50mm lower than row's light oil height of weir plate, and effluent overflow weir water weir plate arranges adjustable.
6. clustered aggregates is reclaimed in a kind of oil removal as claimed in claim 1, it is characterized in that: described second reclaims oil pipe is provided with some oil supply holes, aperture φ 32 ~ 50mm.
7. clustered aggregates is reclaimed in a kind of oil removal as claimed in claim 1, it is characterized in that: the first described flow deflector is bending-type structure, and top differs 350mm with effluent overflow weir water height; The second described flow deflector and the 3rd flow deflector angle of inclination arrange 45 °; The first described swash plate and the second swash plate angle of inclination arrange 55 °.
8. clustered aggregates is reclaimed in a kind of oil removal as claimed in claim 1, it is characterized in that: described oil removal filler employing aperture is the inclined tube filler of φ 40mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520117772.3U CN204550234U (en) | 2015-02-27 | 2015-02-27 | Clustered aggregates is reclaimed in a kind of oil removal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520117772.3U CN204550234U (en) | 2015-02-27 | 2015-02-27 | Clustered aggregates is reclaimed in a kind of oil removal |
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| Publication Number | Publication Date |
|---|---|
| CN204550234U true CN204550234U (en) | 2015-08-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520117772.3U Expired - Fee Related CN204550234U (en) | 2015-02-27 | 2015-02-27 | Clustered aggregates is reclaimed in a kind of oil removal |
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| Country | Link |
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| CN (1) | CN204550234U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104649453A (en) * | 2015-02-27 | 2015-05-27 | 江苏江大环境工程有限责任公司 | Oil-separation recovery combination apparatus |
-
2015
- 2015-02-27 CN CN201520117772.3U patent/CN204550234U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104649453A (en) * | 2015-02-27 | 2015-05-27 | 江苏江大环境工程有限责任公司 | Oil-separation recovery combination apparatus |
| CN104649453B (en) * | 2015-02-27 | 2016-11-30 | 江苏江大环境工程有限责任公司 | Unit equipment is reclaimed in a kind of oil removal |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150812 Termination date: 20170227 |