CN205275264U - Forced -ventilated formula automatic slag removal spiral is from towards wash oil water separator - Google Patents
Forced -ventilated formula automatic slag removal spiral is from towards wash oil water separator Download PDFInfo
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- CN205275264U CN205275264U CN201520996836.1U CN201520996836U CN205275264U CN 205275264 U CN205275264 U CN 205275264U CN 201520996836 U CN201520996836 U CN 201520996836U CN 205275264 U CN205275264 U CN 205275264U
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- cabin
- forced
- connecting tube
- water separation
- oil
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Abstract
The utility model discloses a forced -ventilated formula automatic slag removal spiral is from towards wash oil water separator, including the forced -ventilated cabin, forced -ventilated cabin lower part is equipped with wash -out valve and check valve, and forced -ventilated cabin upper portion is passed through the connecting tube and is connected the oily control valve of collection, collects oily control valve and passes through connecting tube connection water oil separating cabin, and forced -ventilated cabin lower part is equipped with the wash -out valve, and second tee bend check valve passes through the connecting tube to be connected the gate valve respectively and assist the pump, assists pump cabin upper portion through excessive water piping connection second grade slagging -off cabin. Compared with the prior art, the utility model discloses can realize an album automatic forced -ventilated, slagging -off, collection oil and receive oily function as an organic whole, the function that still has anti -overflow water, prevent the secondary water simultaneously to structural design is simple, and long service life can carry out efficient handling to the recovery wastes material of catering trade, and resources are saved has very high social and economic benefits.
Description
Technical field
The utility model relates to a kind of oily-water seperating equipment, is specifically related to a kind of forced-ventilated self-skimming spiral from purge oil water separation device.
Background technology
At present, original treatment process is mostly adopted in the water treatment that catering industry is all.
The first method: be provided with a retention basin nearby from draining, is installed sump pump, then all waste water is all discharged in retention basin, is discharged by sump pump in retention basin.
2nd kind of method: establishing one with the Unpowered oil-water separator box of filter frame, after filtering, profit enters oily water separation cabin, and the waste water after separation enters into ready retention basin, and waste water is discharged by sump pump.
The third method: be provided with stainless steel filter screen frame, the profit after net frame filters enters stainless steel oily water separation cabin, and profit waste water wherein after separation enters stainless steel and arranges by force cabin, and waste water is discharged by sump pump.
Above three kinds for the treatment of processs sensation is all very reasonable, all very feasible in theory, but there will be foreign material residue in actual use can not draw clearly in time, the sediment entering oily water separation cabin cannot be discharged in time, foreign material directly contact the serious problems such as sump pump, can cause sump pump frequent breakage, metal run out, drainage often occurs, difficult maintenance, maintenance cost is excessively high. Sewage this kind for the treatment of facility, a large amount of germ reproduction, causes harm to human body for a long time, surrounding environment is polluted.
Practical novel content
The purpose of this utility model is to provide one can realize integrating automatic forced, slagging-off, oil-collecting and receiving functional oil, also there is the function of anti-overflow, anti-extraneous water simultaneously, and structure design is simple, long service life, the recovery refuse of catering trade effectively can be processed, economizing on resources, the forced-ventilated self-skimming spiral with very high Social benefit and economic benefit is from purge oil water separation device.
For achieving the above object, the utility model provides following technical scheme:
A kind of forced-ventilated self-skimming spiral is from purge oil water separation device, comprise and arrange by force cabin, strong row bottom, cabin is provided with water escape valve and vacuum breaker, strong row top, cabin connects oil-collecting control valve by connecting tube, oil-collecting control valve connects oily water separation cabin by connecting tube, strong row bottom, cabin connects main pump by connecting tube, main pump connects the first threeway vacuum breaker by connecting tube, strong row bilge portion is connected in the two grades of slagging-off cabins being located at top, oily water separation cabin by the first connecting tube, first connecting tube is respectively equipped with three grades of slagging-off control valves and two grades of slagging-off control valves, bottom, oily water separation cabin is provided with water escape valve, top, oily water separation cabin is provided with vapor pipe, side, oily water separation cabin is provided with oil trap, oil trap side is electric heater unit, oil trap top is provided with oil drain valve, two grades of slagging-off control valves connect water inlet buffering cabin by water inlet anti-overflow pipe, water inlet buffering bottom, cabin connects spiral from rinsing foreign material tripping device by pipeline, water inlet buffering side, cabin is provided with water-in, water inlet buffering cabin and spiral are provided with check ball from the pipeline rinsed between foreign material tripping device, spiral connects the first threeway vacuum breaker in foreign material tripping device one end from rinsing, first threeway vacuum breaker connects two grades of slagging-off cabins by connecting tube, from rinsing, the foreign material tripping device the other end connects the 2nd threeway vacuum breaker by pipeline to spiral, 2nd threeway vacuum breaker connects gate valve and auxiliary pump respectively by connecting tube, auxiliary pump room top connects two grades of slagging-off cabins by overflow pipe.
As the further improvement of above-mentioned technology, top, described strong row cabin is respectively equipped with main liquid level sensor and secondary liquid level sensor.
As the further improvement of above-mentioned technology, between described two grades of slagging-off cabins and oily water separation cabin, it is provided with seal diaphragm.
As the further improvement of above-mentioned technology, described auxiliary pump is fixed in auxiliary pump room, and auxiliary pump room top is provided with auxiliary liquid level sensor.
As the further improvement of above-mentioned technology, between the connecting tube of described main pump and the first threeway vacuum breaker, it is provided with vacuum breaker, between the connecting tube of auxiliary pump and the 2nd threeway vacuum breaker, it is provided with vacuum breaker.
As the further improvement of above-mentioned technology, described oil trap is long V-groove.
As the further improvement of above-mentioned technology, described strong row cabin, oily water separation cabin and auxiliary pump room are fixed by support.
Compared with prior art, the beneficial effects of the utility model are: by arranging spiral from rinsing foreign material tripping device, from rinsing, foreign material tripping device connects two grades of slagging-off cabins to spiral, two grades of slagging-off cabins are located at oily water separation cabin and the structure in connection strong row cabin, oily water separation cabin, collection automatic forced can be realized, slagging-off, oil-collecting and receipts functional oil are integrated, also there is anti-overflow simultaneously, the function of anti-extraneous water, and structure design is simple, long service life, the recovery refuse of catering trade effectively can be processed, economize on resources, there is very high Social benefit and economic benefit.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: the main liquid level sensor of 1-, the secondary liquid level sensor of 2-, 3-arranges by force cabin, 4-first water escape valve, 5-first vacuum breaker, 6-support, 7-main pump, 8-tri-grades removes the gred control valve, 9-the 2nd water escape valve, 10-seal diaphragm, 11-overflow pipe, the auxiliary pump room of 12-, the auxiliary pump of 13-, 14-vertical supports, 15-oil-collecting control valve, 16-electric heater unit, 17-oil drain valve, 18-oily water separation cabin, 19-bis-grades removes the gred control valve, 20-vapor pipe, 21-bis-grades removes the gred cabin, 22-is intake anti-overflow pipe, 23-water inlet buffering cabin, 24-check ball, 25-gate valve, 26-the 2nd threeway vacuum breaker, 27-spiral is from rinsing foreign material tripping device, 28-the 2nd vacuum breaker.
Embodiment
Below in conjunction with embodiment, the technical scheme of this patent is described in more detail.
A kind of forced-ventilated self-skimming spiral is from purge oil water separation device, comprise strong row cabin 3, strong row top, cabin 3 is respectively equipped with main liquid level sensor 1 and secondary liquid level sensor 2, strong row bottom, cabin 3 is provided with the first water escape valve 4 and the first vacuum breaker 5, strong row top, cabin 3 connects oil-collecting control valve 15 by connecting tube, oil-collecting control valve 15 connects oily water separation cabin 18 by connecting tube, strong row bottom, cabin 3 connects main pump 7 by connecting tube, main pump 7 connects the first threeway vacuum breaker by connecting tube, it is connected in the two grades of slagging-off cabins 21 being located at top, oily water separation cabin 18 bottom strong row cabin 3 by the first connecting tube, it is provided with seal diaphragm 10 between two grades of slagging-off cabins 21 and oily water separation cabin 18, first connecting tube is respectively equipped with three grades of slagging-off control valves 8 and two grades of slagging-off control valves 19, bottom, oily water separation cabin 18 is provided with the 2nd water escape valve 9, top, oily water separation cabin 18 is provided with vapor pipe, side, oily water separation cabin 18 is provided with oil trap, oil trap is long V-groove, oil trap side is electric heater unit 16, oil trap top is provided with oil drain valve 17, two grades of slagging-off control valves 19 connect water inlet buffering cabin 23 by water inlet anti-overflow pipe 22, water inlet buffering bottom, cabin 23 connects spiral from rinsing foreign material tripping device 27 by pipeline, water inlet buffering side, cabin 23 is provided with water-in, water inlet buffering cabin 23 and spiral are provided with check ball 24 from the pipeline rinsed between foreign material tripping device 27, spiral connects the first threeway vacuum breaker in foreign material tripping device 27 one end from rinsing, first threeway vacuum breaker connects two grades of slagging-off cabins 21 by connecting tube, from rinsing, foreign material tripping device 27 the other end connects the 2nd threeway vacuum breaker 26 by pipeline to spiral, 2nd threeway vacuum breaker 26 connects gate valve 25 and auxiliary pump 13 respectively by connecting tube, auxiliary pump 13 is fixed in auxiliary pump room 12, auxiliary pump room 12 top is provided with auxiliary liquid level sensor, auxiliary pump room 12 top connects two grades of slagging-off cabins 21 by overflow pipe 11, it is provided with vacuum breaker between main pump 7 and the connecting tube of the first threeway vacuum breaker, it is provided with vacuum breaker between the connecting tube of auxiliary pump 13 and the 2nd threeway vacuum breaker 26, strong row cabin 3, oily water separation cabin 18 and auxiliary pump room 12 are fixed by support 6, support 6 one end connects vertical supports 14.
When the utility model works, spiral connects water inlet buffering cabin 23 in foreign material tripping device 27 top from rinsing, water inlet buffering side, cabin 23 is provided with water-in for water inlet, water inlet buffering cabin 23 connects two grades of slagging-off cabins 21 by water inlet anti-overflow pipe 22, two grades of slagging-off cabins 21 connect strong row cabin 3 by the first connecting tube, strong row top, cabin 3 is respectively equipped with main liquid level sensor 1 and secondary liquid level sensor 2, main liquid level sensor 1 and secondary liquid level sensor 2 are for detecting liquid level, strong row bottom, cabin 3 is provided with the first water escape valve 4 and the first vacuum breaker 5, first water escape valve 4 is for discharging water, from rinsing, foreign material tripping device 27 connects two grades of slagging-off cabins 21 by the first threeway vacuum breaker to spiral, first one of them valve port of threeway vacuum breaker connects main pump 7 by connecting tube, main pump 7 connects strong row cabin 3, two grades of slagging-off cabins 21 are located in oily water separation cabin 18, oily water separation cabin 18 connects strong row cabin 3 by oil-collecting control valve 15, it is provided with seal diaphragm 10 in the middle of two grades of slagging-off cabins 21 and oily water separation cabin 18, seal diaphragm 10 plays the effect of sealing, side, oily water separation cabin 18 is provided with oil trap, oil trap is long V-groove, when needs oil-collecting, close two oil drain valves 17, then the water surface rises, oil flows in oil trap automatically, enter in corresponding container through oil drain valve 17, oily water separation cabin 18 connects strong row cabin 3 by oil-collecting control valve 15, strong row cabin 3 is provided with vacuum breaker, when running into extraneous water, water can enter strong row cabin 3 by vacuum breaker, strong row cabin 3 connects main pump 7, then enter the water in strong row cabin 3 by outside main pump 7 discharge chamber, when needs carry out oily water separation, oil-water mixture is entered by water-in and cushions cabin 23 into water, and enter spiral from rinsing in foreign material tripping device 27 by water inlet buffering cabin 23 through check ball, spiral connects the first threeway vacuum breaker in foreign material tripping device 27 one end from rinsing, the other end connects the 2nd threeway vacuum breaker 26, 2nd threeway vacuum breaker 26 connects gate valve 25, the foreign material that then in oil-water mixture, volume is bigger are by outside the 2nd threeway vacuum breaker 26 and gate valve 25 discharge chamber, support is provided with auxiliary pump 13, auxiliary pump 13 is connected with outlet pipeline by vacuum breaker, auxiliary pump 13 is fixed in auxiliary pump room 12, auxiliary pump room 12 is connected with two grades of slagging-off cabins 21 by overflow pipe 11, when main pump 7 lost efficacy, sewage enters auxiliary pump room 12 through overflow pipe 11, by auxiliary pump 13, sewage is discharged to outdoor, leakage accident can not be there is in guarantee, the utility model can collect automatic forced, slagging-off, oil-collecting and receipts functional oil are integrated, also there is anti-overflow simultaneously, the function of anti-extraneous water, and structure design is simple, long service life, the recovery refuse of catering trade effectively can be processed, economize on resources, there is very high Social benefit and economic benefit.
The foregoing is only the utility model preferred embodiment; not thereby enforcement mode of the present utility model and protection domain is limited; to those skilled in the art; the equivalent replacement that all utilization the utility model specification sheetss and diagramatic content are made and the scheme that apparent change obtains should be recognized, all should be included in protection domain of the present utility model.
Claims (7)
1. a forced-ventilated self-skimming spiral is from purge oil water separation device, comprise and arrange by force cabin, it is characterized in that, strong row bottom, cabin is provided with water escape valve and vacuum breaker, strong row top, cabin connects oil-collecting control valve by connecting tube, oil-collecting control valve connects oily water separation cabin by connecting tube, strong row bottom, cabin connects main pump by connecting tube, main pump connects the first threeway vacuum breaker by connecting tube, strong row bilge portion is connected in the two grades of slagging-off cabins being located at top, oily water separation cabin by the first connecting tube, first connecting tube is respectively equipped with three grades of slagging-off control valves and two grades of slagging-off control valves, bottom, oily water separation cabin is provided with water escape valve, top, oily water separation cabin is provided with vapor pipe, side, oily water separation cabin is provided with oil trap, oil trap side is electric heater unit, oil trap top is provided with oil drain valve, two grades of slagging-off control valves connect water inlet buffering cabin by water inlet anti-overflow pipe, water inlet buffering bottom, cabin connects spiral from rinsing foreign material tripping device by pipeline, water inlet buffering side, cabin is provided with water-in, water inlet buffering cabin and spiral are provided with check ball from the pipeline rinsed between foreign material tripping device, spiral connects the first threeway vacuum breaker in foreign material tripping device one end from rinsing, first threeway vacuum breaker connects two grades of slagging-off cabins by connecting tube, from rinsing, the foreign material tripping device the other end connects the 2nd threeway vacuum breaker by pipeline to spiral, 2nd threeway vacuum breaker connects gate valve and auxiliary pump respectively by connecting tube, auxiliary pump room top connects two grades of slagging-off cabins by overflow pipe.
2. forced-ventilated self-skimming spiral according to claim 1 is from purge oil water separation device, it is characterised in that, top, described strong row cabin is respectively equipped with main liquid level sensor and secondary liquid level sensor.
3. forced-ventilated self-skimming spiral according to claim 1 is from purge oil water separation device, it is characterised in that, it is provided with seal diaphragm between described two grades of slagging-off cabins and oily water separation cabin.
4. forced-ventilated self-skimming spiral according to claim 1 is from purge oil water separation device, it is characterised in that, described auxiliary pump is fixed in auxiliary pump room, and auxiliary pump room top is provided with auxiliary liquid level sensor.
5. forced-ventilated self-skimming spiral according to claim 1 is from purge oil water separation device, it is characterized in that, it is provided with vacuum breaker between the connecting tube of described main pump and the first threeway vacuum breaker, between the connecting tube of auxiliary pump and the 2nd threeway vacuum breaker, it is provided with vacuum breaker.
6. forced-ventilated self-skimming spiral according to claim 1 is from purge oil water separation device, it is characterised in that, described oil trap is long V-groove.
7. forced-ventilated self-skimming spiral according to claim 1 is from purge oil water separation device, it is characterised in that, described strong row cabin, oily water separation cabin and auxiliary pump room are fixed by support.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520996836.1U CN205275264U (en) | 2015-12-07 | 2015-12-07 | Forced -ventilated formula automatic slag removal spiral is from towards wash oil water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520996836.1U CN205275264U (en) | 2015-12-07 | 2015-12-07 | Forced -ventilated formula automatic slag removal spiral is from towards wash oil water separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205275264U true CN205275264U (en) | 2016-06-01 |
Family
ID=56059858
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520996836.1U Expired - Fee Related CN205275264U (en) | 2015-12-07 | 2015-12-07 | Forced -ventilated formula automatic slag removal spiral is from towards wash oil water separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205275264U (en) |
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2015
- 2015-12-07 CN CN201520996836.1U patent/CN205275264U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| DD01 | Delivery of document by public notice |
Addressee: SHENYANG JIN SHI DA ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. Document name: Notification to Pay the Fees |
|
| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: SHENYANG JIN SHI DA ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. Document name: Notification of Termination of Patent Right |
|
| 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: 20160601 Termination date: 20161207 |