CN201770584U - Oil-water separation device - Google Patents
Oil-water separation device Download PDFInfo
- Publication number
- CN201770584U CN201770584U CN201020290100XU CN201020290100U CN201770584U CN 201770584 U CN201770584 U CN 201770584U CN 201020290100X U CN201020290100X U CN 201020290100XU CN 201020290100 U CN201020290100 U CN 201020290100U CN 201770584 U CN201770584 U CN 201770584U
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- oily
- swash plate
- water
- oil
- disengaging zone
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Abstract
The utility model discloses an oil-water separation device. The device comprises a water inlet pipe, a water outlet pipe, an anaerobic baffled reactor region and a tilted plate separation region, wherein a water flow passage is connected between the top of the anaerobic baffled reactor region and the top of the tilted plate separation region; the water inlet pipe is connected with the anaerobic baffled reactor region; the water outlet pipe is connected with the tilted plate separation region; a residue collection bucket is arranged below the anaerobic baffled reactor region; a plurality of tilted plates are arranged in the tilted plate separation region; the top of the tilted plate separation region is provided with an oil discharge pipe; a perforated aeration pipe is also arranged in the tilted plate separation region; and the perforated aeration pipe is connected with a negative ion generator. The oil-water separation device of the utility model has self-cleaning function due to the adoption of the negative ion generator and can automatically collect the waste oil.
Description
Technical field
The utility model belongs to a kind of water-and-oil separator that need to be used to the sewage disposal of oily water separation industry, particularly a kind of oily-water seperating equipment of suitable catering trade.
Background technology
Food and drink waste water is mainly derived from hotel, hotel, dining room, dining room etc., and along with the city fast development, the food and drink waste water quantity discharged increases year by year.Vegetable and animals oils in the food and drink waste water is most important pollution factor, the vegetable and animals oils of high density flows into water drain and can cause the duct wall grease to pile up, cause network of drains to stop up and paralysis, and the grease that inner-walls of duct hardens is extremely difficult to be cleaned, the grease of high density can make the chemical oxygen demand (COD) (COD) in the water increase greatly in addition, causes the municipal drainage severe contamination.
At present, traditional gravity oil trap is mainly adopted in the oily water separation of catering trade, and its principle is exactly to utilize profit not dissolve each other and the oily lighter characteristic of density, stop by certain hour, the profit natural layering, from flowing to sewage outfall sewer net, oil reservoir is by manually regularly dragging for clearly by drainage pipeline for water layer.There is following problem in the tradition oil trap: 1. manual operation dependency is strong, neglects management in case drag for oily personnel, just is easy to cause grease excessive.2. to drag for workload clearly big for scum silica frost, needs the artificial barrier bucket that cleans.3. oil trap place environmental aspect is poor, and stench overflows, and mosquitos and flies grows.4. long-time running after-bay body grease hardens seriously, and cleaning is big comprehensively.
How the food and drink oily water separating equipment is accomplished mechanize, automatic control, energy-conservation, researchdevelopment direction that environment well becomes water-and-oil separator of new generation.
The utility model content
The purpose of this utility model provides a kind of oily-water seperating equipment, has overcome the problem that traditional oil trap need manually be dragged for oil and is difficult to clean.
The utility model is solved by the following technical solutions:
A kind of oily-water seperating equipment of the utility model, comprise water inlet pipe and rising pipe, also comprise an anaerobic baffled reactor district and a swash plate disengaging zone, be connected with water stream channel between the top of the top in anaerobic baffled reactor district and swash plate disengaging zone, described water inlet pipe is connected with the anaerobic baffled reactor district, described rising pipe is connected with the swash plate disengaging zone, the below in anaerobic baffled reactor district is provided with slag gathering hopper, the swash plate disengaging zone is provided with a plurality of swash plates, and the top of swash plate disengaging zone is provided with oil exit pipe; Also be provided with boring aeration pipe in the swash plate disengaging zone, described boring aeration pipe is connected with anion generator.
Below, swash plate described in the utility model disengaging zone also is provided with slag gathering hopper.
Be provided with electronic residual cake valve below the slag gathering hopper described in the utility model.
All slag gathering hoppers of the utility model are connected with thickner by electronic residual cake valve respectively, and the thickner output tube connects the collection inder pot.
Thickner described in the utility model is a screw concentrator.
The top of swash plate described in the utility model disengaging zone is provided with oil pooling dipper, and described oil exit pipe is located on the oil pooling dipper.
Be provided with oil level gauge in the oil pooling dipper described in the utility model, described oil exit pipe is provided with motorized valve, and described oil level gauge is connected with electrical control cubicles with motorized valve.
Be connected with the overflow protective tube between the top of oil pooling dipper described in the utility model and the anaerobic baffled reactor district.
Be provided with the dividing plate of vertical installation and the flow deflector that tilts to install in the anaerobic baffled reactor described in the utility model district.
The ingress of water stream channel described in the utility model is provided with grid.
By above technical scheme, oily-water seperating equipment of the present utility model has the following advantages:
(1) anion generator is set and has the self-stip function, assurance equipment is after long-time running, and the device interior grease that can not harden has been avoided comprehensive cleaning of equipment.
(2) adopt advanced negative ion to prohibit the flavor technology, accomplish energy-conserving and environment-protective, inputs such as non-secondary pollution and medicament.
(3) full automatic control, the improper bottom line that drops to of equipment operation that human factor is caused, operator only need reclaim grease and treating refuse gets final product.
(4) main process adopts swash plate to separate, good separating effect, and do not have energy consumption; Off-set facility is all the intermittent operational outfit of less energy-consumption.
Description of drawings
The structure iron of Fig. 1 oily-water seperating equipment of the present utility model
Embodiment
As shown in Figure 1, a kind of oily-water seperating equipment of the utility model, comprise water inlet pipe 1 and rising pipe 2, also comprise anaerobic baffled reactor district 4 and swash plate disengaging zone 5, be connected with water stream channel 23 between the top of the top in anaerobic baffled reactor district 4 and swash plate disengaging zone 5, water inlet pipe 1 is connected with anaerobic baffled reactor district 4, rising pipe 2 is connected with swash plate disengaging zone 5, be provided with the dividing plate 21 of vertical installation and the flow deflector 22 that tilts to install in anaerobic baffled reactor 4 districts, below, anaerobic baffled reactor district is provided with slag gathering hopper 11, swash plate disengaging zone 5 is provided with a plurality of swash plates 6, those swash plate 6 tops are provided with oil exit pipe 9, anaerobic baffled reactor (ABR) major function is for separating floating matter and the large-scale particulate matter of removing in the water, and swash plate disengaging zone major function is oily water separation, removes less suspended particulate simultaneously.Swash plate disengaging zone 5 also is provided with boring aeration pipe 8, links to each other with anion generator 3, and the negative ion that anion generator 3 produces enters swash plate disengaging zone 5 by air carrier, and air carrier is produced by pneumatic pump.Be provided with oil pooling dipper 17 above swash plate disengaging zone 5, oil exit pipe 9 is located on this oil pooling dipper, and is provided with a plurality of slag gathering hoppers 11 below swash plate disengaging zone 5.Oil pooling dipper is installed suspension oil level gauge 7 for 17 li and is measured content of oil and grease in the oil pooling dipper 17 of swash plate disengaging zone above those swash plates 6, after the fat content in the oil pooling dipper 17 acquires a certain degree, top motorized valve 10 is opened the discharge grease automatically, after treating that grease drops to set(ting)value, the oil extraction motorized valve cuts out automatically.Electronic residual cake valve 16 is installed at slag gathering hopper 11 places of anaerobic baffled reactor district and below, swash plate disengaging zone respectively, electronic residual cake valve carries out the automatic control regular cinder-discharge according to the water yield, slag gathering hopper 11 is connected with screw thickner 14 by electronic residual cake valve 16 respectively, the grid slag of being discharged concentrates by the screw thickner and extruding is delivered to collection inder pot 13, and the waste water that produces in the concentration process is incorporated water drain into by drainage pipeline 20.Suspension oil level gauge 7, motorized valve 10 and residual cake valve 16 all link to each other with electrical control cubicles 15, and centralized Control also realizes automatization.
The utility model anaerobic baffled reactor district 4 is higher than swash plate disengaging zone 5; and the ingress of water stream channel 23 is provided with grid 18; above-mentioned anion generator can place top, swash plate disengaging zone; be connected overflow protective tube 19 between 4 tops, anaerobic baffled reactor district and swash plate disengaging zone; this overflow protective tube also is provided with a mouth of pipe that communicates with atmosphere, can guarantee that draining is unaffected when maintenance of equipment.
Food and drink waste water is entered the anaerobic baffled reactor district of the utility model oily-water seperating equipment by water inlet pipe 1, the effect of dividing plate 21 and flow deflector 22 by anaerobic baffled reactor (ABR), make sewage from catering business form the baffling precipitation, large-scale particulate matter precipitation enters slag gathering hopper 11, and grease and sewage carry out next step processing from flowing into the swash plate disengaging zone.Oily(waste)water is under swash plate 6 effects, and grease is dammed in the top of swash plate 6, collects grease by the oil pooling dipper 17 of top, and is disposed to oil-collecting bucket 12 by oil exit pipe 9; Waste water, precipitates simultaneously in the baffling process and removes suspended substance in the water from the effluent oil water separation equipment by behind the swash plate baffling.Below, 5 oil pooling dippers, 17 places, swash plate disengaging zone is provided with annular aeration pipe network 8, the bubble that contains negative ion like this is with the inclined-plane of even branch in swash plate disengaging zone 5 oil pooling dippers 17, and move upward along awl bucket inclined-plane, in the process that negative ion moves upward, make oil, steel bonding interface loss of stability, harden grease by the carrier gas peel-off device, thereby reach the function of equipment self-stip, in addition, because negative ion itself has the de-odorised function, so after carrying out self-stip night, negative ion more than needed can be free on the equipment machine room of water-and-oil separator, even equipment machine room does not dispose ventilation system like this, can guarantee good operating environment.It is some that equipment only disposes anion generator, screw concentrator and motorized valve, and the complete machine installed capacity is 1.5kw, and periodic running, 5 kilowatts of daily power consumption less thaies/time.
The utility model is not limited to above-mentioned best configuration, and other any identical with the utility model or proximate products that anyone draws under enlightenment of the present utility model all drop in the protection domain of the present utility model.
Claims (10)
1. oily-water seperating equipment, comprise water inlet pipe and rising pipe, it is characterized in that, also comprise an anaerobic baffled reactor district and a swash plate disengaging zone, be connected with water stream channel between the top of the top in anaerobic baffled reactor district and swash plate disengaging zone, described water inlet pipe is connected with the anaerobic baffled reactor district, described rising pipe is connected with the swash plate disengaging zone, the below in anaerobic baffled reactor district is provided with slag gathering hopper, the swash plate disengaging zone is provided with a plurality of swash plates, and the top of swash plate disengaging zone is provided with oil exit pipe; Also be provided with boring aeration pipe in the swash plate disengaging zone, described boring aeration pipe is connected with anion generator.
2. oily-water seperating equipment according to claim 1 is characterized in that, below, described swash plate disengaging zone also is provided with slag gathering hopper.
3. oily-water seperating equipment according to claim 1 and 2 is characterized in that, is provided with electronic residual cake valve below the described slag gathering hopper.
4. oily-water seperating equipment according to claim 3 is characterized in that, all slag gathering hoppers are connected with thickner by electronic residual cake valve respectively, and the thickner output tube connects the collection inder pot.
5. oily-water seperating equipment according to claim 4 is characterized in that, described thickner is a screw concentrator.
6. oily-water seperating equipment according to claim 1 is characterized in that, the top of described swash plate disengaging zone is provided with oil pooling dipper, and described oil exit pipe is located on the oil pooling dipper.
7. oily-water seperating equipment according to claim 6 is characterized in that, is provided with oil level gauge in the described oil pooling dipper, and described oil exit pipe is provided with motorized valve, and described oil level gauge is connected with electrical control cubicles with motorized valve.
8. oily-water seperating equipment according to claim 6 is characterized in that, is connected with the overflow protective tube between the top of described oil pooling dipper and the anaerobic baffled reactor district.
9. oily-water seperating equipment according to claim 1 is characterized in that, is provided with the dividing plate of vertical installation and the flow deflector that tilts to install in the described anaerobic baffled reactor district.
10. oily-water seperating equipment according to claim 1 is characterized in that the ingress of described water stream channel is provided with grid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020290100XU CN201770584U (en) | 2010-08-12 | 2010-08-12 | Oil-water separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020290100XU CN201770584U (en) | 2010-08-12 | 2010-08-12 | Oil-water separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201770584U true CN201770584U (en) | 2011-03-23 |
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ID=43750424
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201020290100XU Expired - Fee Related CN201770584U (en) | 2010-08-12 | 2010-08-12 | Oil-water separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201770584U (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104588396A (en) * | 2014-12-30 | 2015-05-06 | 苏州韩博厨房电器科技有限公司 | Garbage treatment equipment |
| CN104588395A (en) * | 2014-12-30 | 2015-05-06 | 苏州韩博厨房电器科技有限公司 | Integrated garbage treatment equipment |
| CN104588394A (en) * | 2014-12-30 | 2015-05-06 | 苏州韩博厨房电器科技有限公司 | Garbage continuous treatment equipment |
| CN104649368A (en) * | 2013-11-15 | 2015-05-27 | 天津今誉源环保设备有限公司 | Novel deodorant grease trap for decomposing fat |
| CN104649367A (en) * | 2013-11-15 | 2015-05-27 | 天津今誉源环保设备有限公司 | Ion microbubble aeration oil decomposition technology |
| CN107434323A (en) * | 2017-09-18 | 2017-12-05 | 广东普施德泽环保股份有限公司 | A kind of device that food and drink profit is handled using ion-oxygen |
| CN110526488A (en) * | 2018-05-24 | 2019-12-03 | 山东蓝卫环保科技有限公司 | The micro-nano ionic membrane grease resolving device of active oxygen and processing method |
| CN112939257A (en) * | 2021-02-09 | 2021-06-11 | 加中环境技术(天津)有限公司 | Grease, mud, sand and water separator |
| CN113754186A (en) * | 2021-09-02 | 2021-12-07 | 北京华夏大禹科技有限公司 | Oily wastewater treatment system |
-
2010
- 2010-08-12 CN CN201020290100XU patent/CN201770584U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104649368A (en) * | 2013-11-15 | 2015-05-27 | 天津今誉源环保设备有限公司 | Novel deodorant grease trap for decomposing fat |
| CN104649367A (en) * | 2013-11-15 | 2015-05-27 | 天津今誉源环保设备有限公司 | Ion microbubble aeration oil decomposition technology |
| CN104588396A (en) * | 2014-12-30 | 2015-05-06 | 苏州韩博厨房电器科技有限公司 | Garbage treatment equipment |
| CN104588395A (en) * | 2014-12-30 | 2015-05-06 | 苏州韩博厨房电器科技有限公司 | Integrated garbage treatment equipment |
| CN104588394A (en) * | 2014-12-30 | 2015-05-06 | 苏州韩博厨房电器科技有限公司 | Garbage continuous treatment equipment |
| CN107434323A (en) * | 2017-09-18 | 2017-12-05 | 广东普施德泽环保股份有限公司 | A kind of device that food and drink profit is handled using ion-oxygen |
| CN110526488A (en) * | 2018-05-24 | 2019-12-03 | 山东蓝卫环保科技有限公司 | The micro-nano ionic membrane grease resolving device of active oxygen and processing method |
| CN112939257A (en) * | 2021-02-09 | 2021-06-11 | 加中环境技术(天津)有限公司 | Grease, mud, sand and water separator |
| CN113754186A (en) * | 2021-09-02 | 2021-12-07 | 北京华夏大禹科技有限公司 | Oily wastewater treatment system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20121231 Granted publication date: 20110323 |
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| RINS | Preservation of patent right or utility model and its discharge | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20121231 Granted publication date: 20110323 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110323 Termination date: 20180812 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |