CN204891293U - Oil backpressure oil water separator - Google Patents
Oil backpressure oil water separator Download PDFInfo
- Publication number
- CN204891293U CN204891293U CN201520552588.1U CN201520552588U CN204891293U CN 204891293 U CN204891293 U CN 204891293U CN 201520552588 U CN201520552588 U CN 201520552588U CN 204891293 U CN204891293 U CN 204891293U
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- oil
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- separation tank
- pipe
- communicating pipe
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Abstract
The utility model relates to an oil backpressure oil water separator belongs to the splitter field, including the water oil separating case, the bottom of water oil separating case is provided with charge -in pipeline, and the top of water oil separating case is provided with row oil pipe way, arranges the oil pipe way and is provided with the oil drain port with water oil separating case intercommunication department, and the top of oil drain port is provided with an emptying pipeline, the outside of water oil separating case is provided with the water tank, and the intermediate position of water oil separating case is provided with n shape communicating pipe, and the highest point of communicating pipe and the vertical height on ground are less than the vertical height on oil drain port and ground, and through the communicating pipe intercommunication between water oil separating case and the water tank, the below of the communicating pipe that links to each other with the water oil separating case is provided with the import, and the import sets up the top at charge -in pipeline, water tank one side is provided with drainage pipe, and drainage pipe's top is provided with the 2nd emptying pipeline. The device simple structure, it is with low costs, convenient operation, the practicality is strong, effectively guarantees the quality of the oil of oil water mixture after -separating, implements effectually.
Description
Technical field
The utility model relates to a kind of oil water separator, particularly relates to oily back pressure oil water separator.
Background technology
In densely populated big city, garbage disposal is a headachy problem.Common way is sent to landfill after collecting, or incinerate with incinerator.But both all can the problem of manufacturing environment protection, and stops overconsumption and can alleviate landfill degree of saturation further.Garbage disposal in landfill is improper polluted underground water and stinks, and a lot of city can be fewer and feweri for the area of landfill.Incinerate and then unavoidablely can produce toxic gas, harm organism.The method of rubbish generation is all reduced in most cities in research, and encourages resource reclaim.
Wherein, the materials such as the waste plastics in rubbish, scrap rubber, mainly refer to leftover bits and pieces and waste plastic, the broken material of rubber after recycling of plastic processes.China is second-biggest-in-the-world plastics, rubber producing country, and waste or used plastics, the rubber of generation are countless, and a large amount of waste plastics, rubber are difficult to decompose in natural environment, accumulate over a long period, cause serious white pollution, destroy ecological environment.The method that tradition waste plastics, rubber industry wastewater utilize is mainly regeneration recycling by mechanism; Heat energy is reclaimed in burning; Catalytic pyrolysis prepares fuel oil.In the international energy-conserving and environment-protective exhibition in May, 2012 Beijing, have expert to be proposed plastic garbage processing item, the plastic garbage of white is by pretreatment, cracking and refining three phases, and final " change " is product oil, and this product oil can be used for life and industrial production.Have report to show, converting plastic waste to oil can be used for diesel engine with direct injection completely.
In plastic garbage treatment process, the alkanes oil of plastics and arene wet goods hydrocarbon-type oil, can produce a large amount of oil water mixtures aborning, and meeting serious environment pollution directly discharged by this oil water mixture, and owing to wherein containing a large amount of hydrocarbon-type oils, direct discharge can cause waste.The main oily-water seperating equipment adopting top grade at present, this apparatus structure is complicated, and oil by oil sucking-off from water, then is extruded by the mode of extruding by the more oleophilic substance that adopts from oleophilic substance, and it implements comparatively complexity from principle, and cost is high.And need motor to drive completing of whole link, add the possibility that fault produces.Finally discarded oleophilic substance becomes again new pollutant.
Utility model content
The deficiency that the utility model exists for prior art, provide oily back pressure oil water separator, concrete technical scheme is as follows:
Oil back pressure oil water separator, comprise water separation tank, the bottom of water separation tank is provided with feed pipe, and the top of water separation tank is provided with oil-drain pipe, oil-drain pipe and water separation tank connectivity part are provided with oil drain out, and the top of oil drain out is provided with first row vacant duct; The arranged outside of water separation tank has water tank, the centre position of water separation tank is provided with n shape communicating pipe, the highest point of communicating pipe and the vertical height on ground are less than the vertical height on oil drain out and ground, be communicated with by communicating pipe between water separation tank and water tank, the bottom of the communicating pipe be connected with water separation tank is provided with import, and import is arranged on the top of feed pipe; Water tank side is provided with drainage pipeline, and the top of drainage pipeline is provided with second row vacant duct.
As the improvement of technique scheme, described feed pipe is provided with magnetic valve and flowmeter.
Oily back pressure oil water separator described in the utility model, utilizes the structures such as n shape communicating pipe, water separation tank, water tank, ensures that oil water mixture realizes being separated, utilizes magnetic valve and flowmeter, realize automation, serialization controls.This apparatus structure is simple, and cost is low, easy to operate, practical, and effectively ensure the quality of the oil after oil water mixture separation, implementation result is good.
Accompanying drawing explanation
Fig. 1 is oily back pressure structure of oil water separator schematic diagram described in the utility model;
Fig. 2 is oily back pressure structure of oil water separator schematic diagram (before water-oil separating) described in the utility model;
Fig. 3 is oily back pressure structure of oil water separator schematic diagram (in water-oil separating) described in the utility model;
Fig. 4 is oily back pressure structure of oil water separator schematic diagram (after water-oil separating) described in the utility model.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
As shown in Figure 1, Fig. 1 is oily back pressure structure of oil water separator schematic diagram described in the utility model.Described oily back pressure oil water separator, comprises water separation tank 10, and the bottom of water separation tank 10 is provided with feed pipe 11, and the oil water mixture produced in production process enters in water separation tank 10 by feed pipe 11; The top of water separation tank 10 is provided with oil-drain pipe 12, and oil-drain pipe 12 and water separation tank 10 connectivity part are provided with oil drain out 12a, and the oil after separation flows into oil-drain pipe 12 by oil drain out 12a and discharges.For ensureing that oil water mixture flows into the inside of water separation tank 10 smoothly, water separation tank 10 is provided with first row vacant duct 13, and for preventing the oil after being separated from flowing out from first row vacant duct 13, first row vacant duct 13 is arranged on the top of oil drain out 12a; Oil water mixture enters the inside of water separation tank 10 by feed pipe 11, and the air of water separation tank 10 inside discharges from first row vacant duct 13, ensures that oil water mixture flows into smoothly.
Have water tank 20 in the arranged outside of water separation tank 10, the centre position of water separation tank 10 is provided with n shape communicating pipe 14, and the highest point of communicating pipe 14 and the vertical height on ground are less than the vertical height on oil drain out 12a and ground; Be communicated with by communicating pipe 14 between water separation tank 10 and water tank 20, the bottom of the communicating pipe 14 be connected with water separation tank 10 is provided with import 14a, and import 14a is arranged on the top of feed pipe 11.
Water tank 20 side is provided with drainage pipeline 22, for discharging the water after separation.Above drainage pipeline 22, arrange second row vacant duct 21, the water after separation was entered in water tank 20 by communicating pipe 14, and the air of water tank 20 inside discharges from second row vacant duct 21, ensured that profit flows in water tank 20 smoothly.
Described feed pipe 11 is provided with magnetic valve 15 and flowmeter 16, is used for controlling the flow velocity of oil water mixture and flow and flowing time.
As shown in Figure 2, Fig. 2 is oily back pressure structure of oil water separator schematic diagram (before water-oil separating) described in the utility model.Under the control of magnetic valve 15 and flowmeter 16, oil water mixture enters water separation tank 10 from feed pipe 11, until the liquid level of oil water mixture, lower than import 14a, leaves standstill a period of time in water separation tank 10, because oil density is less than the density of water, liquid level upper strata is oil reservoir.Liquid level lower floor is water layer.Along with oil water mixture constantly enters from feed pipe 11, water separation tank 10 internal liquid level raises, and the oil in oil water mixture is to floating under the effect of buoyancy, and water is heavy under gravity to be collected in lower floor;
As shown in Figure 3, Fig. 3 is oily back pressure structure of oil water separator schematic diagram (in water-oil separating) described in the utility model; When highest point higher than communicating pipe 14 of the liquid level of oil water mixture, the water of oil water mixture lower floor flows into from communicating pipe 14 in water tank 20, and the oil on oil water mixture upper strata, due to higher than import 14a, is avoided flowing in water tank 20 from communicating pipe 14.
As shown in Figure 4, Fig. 4 is oily back pressure structure of oil water separator schematic diagram (after water-oil separating) described in the utility model.Oil water mixture continues to enter from feed pipe 11, water separation tank 10 internal liquid level continues to rise, until the liquid level of oil water mixture flushes with oil drain out 12a, oil in oil water mixture is under constantly floating for a long time, the superiors' liquid level forms oil reservoir, the oil reservoir of the superiors flows to oil-drain pipe 12 from oil drain out 12a, until be collected.Under the effect of flowmeter 16, by the aperture of Controlling solenoid valve 15, control the flow velocity of oil water mixture in feed pipe 11, the time that in flow and water separation tank 10, oil water mixture leaves standstill, oil and water hydraulic in oil water mixture is allowed to balance with this, You Heshui is in, the released state of lower floor, realize automation, serialization is separated, and this device is owing to utilizing the buoyancy of oil, hydraulic pressure between oil and water and the gravity of water, physical method is adopted to realize automatically being separated, do not add other reagent, oil after separation can utilize again, cost-saving, effective guarantee is separated rear oily quality.This apparatus structure is simple, and using method is simple, and cost is low.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (2)
1. oily back pressure oil water separator, comprise water separation tank 10, it is characterized in that: the bottom of described water separation tank (10) is provided with feed pipe (11), the top of water separation tank (10) is provided with oil-drain pipe (12), oil-drain pipe (12) and water separation tank (10) connectivity part are provided with oil drain out (12a), and the top of oil drain out (12a) is provided with first row vacant duct (13); The arranged outside of water separation tank (10) has water tank (20), the centre position of water separation tank (10) is provided with n shape communicating pipe (14), the highest point of communicating pipe (14) and the vertical height on ground are less than the vertical height on oil drain out (12a) and ground, be communicated with by communicating pipe (14) between water separation tank (10) and water tank (20), the bottom of the communicating pipe (14) be connected with water separation tank (10) is provided with import (14a), and import (14a) is arranged on the top of feed pipe (11); Water tank (20) side is provided with drainage pipeline (22), and the top of drainage pipeline (22) is provided with second row vacant duct (21).
2. oily back pressure oil water separator according to claim 1, is characterized in that: described feed pipe (11) is provided with magnetic valve (15) and flowmeter (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520552588.1U CN204891293U (en) | 2015-07-28 | 2015-07-28 | Oil backpressure oil water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520552588.1U CN204891293U (en) | 2015-07-28 | 2015-07-28 | Oil backpressure oil water separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204891293U true CN204891293U (en) | 2015-12-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520552588.1U Expired - Fee Related CN204891293U (en) | 2015-07-28 | 2015-07-28 | Oil backpressure oil water separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204891293U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107008034A (en) * | 2017-05-19 | 2017-08-04 | 今麦郎面品有限公司 | A kind of oily water separating equipment |
| CN107281779A (en) * | 2017-08-07 | 2017-10-24 | 山东钢铁股份有限公司 | A kind of solvent separation unit |
| CN107469408A (en) * | 2017-06-30 | 2017-12-15 | 安乡欣瑞生物科技有限公司 | Oily-water seperating equipment |
| CN113274808A (en) * | 2021-04-25 | 2021-08-20 | 浙江农林大学 | Torreya grandis essential oil extraction and separation system |
-
2015
- 2015-07-28 CN CN201520552588.1U patent/CN204891293U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107008034A (en) * | 2017-05-19 | 2017-08-04 | 今麦郎面品有限公司 | A kind of oily water separating equipment |
| CN107469408A (en) * | 2017-06-30 | 2017-12-15 | 安乡欣瑞生物科技有限公司 | Oily-water seperating equipment |
| CN107281779A (en) * | 2017-08-07 | 2017-10-24 | 山东钢铁股份有限公司 | A kind of solvent separation unit |
| CN113274808A (en) * | 2021-04-25 | 2021-08-20 | 浙江农林大学 | Torreya grandis essential oil extraction and separation system |
| CN113274808B (en) * | 2021-04-25 | 2022-08-19 | 浙江农林大学 | Torreya grandis essential oil extraction and separation system |
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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 |
Granted publication date: 20151223 Termination date: 20190728 |
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| CF01 | Termination of patent right due to non-payment of annual fee |