CN205569829U - Go out water oil water separator in succession - Google Patents
Go out water oil water separator in succession Download PDFInfo
- Publication number
- CN205569829U CN205569829U CN201620298972.8U CN201620298972U CN205569829U CN 205569829 U CN205569829 U CN 205569829U CN 201620298972 U CN201620298972 U CN 201620298972U CN 205569829 U CN205569829 U CN 205569829U
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- outer tube
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- water
- dividing plate
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Abstract
The utility model discloses a go out water oil water separator in succession, include multistage separator and go out water mechanism in succession, multistage separator includes the baffle that sets up in the box, box, the baffle divide into body cavity forward in feed liquor chamber, middle chamber and goes out the water cavity after by, going out water mechanism in succession and including outer tube and setting the inner tube outer tube in of vertical setting in a water cavity, inner tube and outer tube coaxial line set up, and outer internal diameter of pipe is greater than interior external diameter of pipe, the inner tube top is located box upper portion, and the outer tube top is higher than the inner tube top and the outer tube bottom is equipped with the intercommunication mouth that communicates the outer tube and go out the water cavity, all smooth mouthful of settings of top of outer tube and inner tube, the inner tube bottom is connected with the continuous outlet pipe that the level set up, and the outlet pipe stretches out outer tube and box forward in succession. The utility model discloses water oil separating is rateed higher, waste water outlet pipe and can be opened always and can keep the liquid level to be in always and stabilize the state, and it is very convenient to use.
Description
Technical field
This utility model relates to a kind of by the device that separates with water of oil, it is adaptable to factory that oily waste water is many and restaurant.
Background technology
Oily-water seperating equipment tool has been widely used.Industrially, containing a large amount of waste oil in the industrial wastewater of many application scenarios, if not reclaimed directly discharge, both polluting environment, having wasted again resource.Many civilian occasions also have the demand separating oil and water.As there is substantial amounts of kitchen waste water every day in restaurant, containing many oil contents in these waste water；As being directly discharged to sewer, city can be increased and process the cost of sanitary sewage.Existing oily-water seperating equipment has following limitation: 1. the effect of its oil-water separation is limited, and oil-water separation is poor.2., for keeping the waste water flowed out to have certain hydraulic pressure, waste water effuser is generally located on bottom liquid level.But such setting, waste water effuser can not be constantly in the state opened, and otherwise waste water will can not accumulate higher liquid level in oil water separator.Batch (-type) is opened waste water effuser and is brought the biggest inconvenience to using, and needs artificial often observation and operation.Some factory is simply not provided with waste water effuser, when liquid level is higher, is directly extracted out by waste water with water pump, uses also inconvenient, needs artificial often observation and manual operation.
Utility model content
The purpose of this utility model is to provide that a kind of oil-water separation rate is higher, waste water effuser can be always on and liquid level can be kept to be constantly in steady statue, avoid bringing adverse effect into water to oil-water separation and mechanization can removing the continuous effluent oil water separator of impurity.
For achieving the above object, continuous effluent oil water separator of the present utility model includes multiple-stage separator and continuous effluent mechanism；Multiple-stage separator includes the casing of the smooth mouth in top, with liquid flowing direction as forward direction, be uniformly provided with two or more dividing plate in casing in the longitudinal direction, cabinets cavity is divided into admission chamber, intermediate cavity and water chamber before backward by dividing plate；Each dividing plate top flushes with casing top, is communicated with the opening of admission chamber, intermediate cavity and water chamber between each dividing plate bottom and casing diapire；
Continuous effluent mechanism includes the outer tube being vertically provided in water chamber and arranges inner tube within the outer tube, and inner and outer tubes are coaxially set, and outer tube diameter is more than inner tube external diameter；Inner tube top is positioned at casing top, and outer tube top is higher than inner tube top and is communicated with the connected entrance of outer tube and water chamber between outer tube bottom and casing diapire；The all smooth mouth in the top of outer tube and inner tube is arranged, and inner tube bottom connects horizontally disposed continuous effluent pipe, and continuous effluent pipe forward extends out outer tube and casing.
Connecting on the casing diapire in described each dividing plate front and have baffle plate, baffle plate is higher than dividing plate bottom with casing with wide and its top in the lateral direction.
Said inner tube sidewall is arranged at intervals with some Liquid level holes up and down, is mounted on plug at each Liquid level hole.
This utility model has the advantage that
1. the design of continuous effluent mechanism is ingenious, can the liquid level kept certain height of the liquid in guard box body, again can be in box bottom continuous effluent, water outlet has certain hydraulic pressure (pressure that liquid level brings).Use continuous effluent mechanism, continuous effluent pipe can be connected with municipal drain or next stage water treatment facilities, without the liquid level in direct surveillance's casing hand-actuated or use pumping for water pump, use very convenient.The setting of the plug in Liquid level hole, can the liquid level in control chamber body the most neatly.
2. owing to have employed multistage separation structure, oil water mixture all can carry out the process of oil-water separation at admission chamber, intermediate cavity and water chamber, therefore the efficiency of oil-water separation is substantially increased, on the one hand the process of oil-water separation can be accelerated, more oil water mixture is processed within the unit interval, on the other hand oil water mixture has obtained separating more thoroughly, and in the liquid finally gone out by continuous effluent pipe flow, oil content is less.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model embodiment one；
Fig. 2 is the A-A sectional view of Fig. 1；
The structural representation that Fig. 3 is inner tube and continuous effluent pipe links together；
Fig. 4 is the structural representation of fixed network board；
Fig. 5 is the structural representation of this utility model embodiment two.
Detailed description of the invention
Embodiment one
In Fig. 1, direction shown in arrow is the flow direction of liquid at this.
As shown in Figures 1 to 4, continuous effluent oil water separator of the present utility model includes multiple-stage separator, mechanical purifying mechanism, continuous effluent mechanism and two-stage buffering water intake mechanism；
Multiple-stage separator includes the casing 1 of the smooth mouth in top, with liquid flowing direction as forward direction, be uniformly provided with two or more dividing plate 2 in casing 1 in the longitudinal direction, casing 1 inner chamber is divided into admission chamber 3, intermediate cavity 4 and water chamber 5 before backward by dividing plate 2；Each dividing plate 2 top flushes with casing 1 top, is communicated with the opening 6 of admission chamber 3, intermediate cavity 4 and water chamber 5 between each dividing plate 2 bottom and casing 1 diapire；
Continuous effluent mechanism includes that the outer tube 7 being vertically provided in water chamber 5 and the inner tube 8 being arranged in outer tube 7, inner tube 8 and outer tube 7 are coaxially set, and outer tube 7 internal diameter is more than inner tube 8 external diameter, thus forms Ring-cylindrical space between inner tube 8 and outer tube 7；Inner tube 8 top is positioned at casing 1 top, and outer tube 7 top higher than inner tube 8 top and flushes with casing 1 top, it is also possible to slightly below casing 1 top.The connected entrance 9 of outer tube 7 and water chamber 5 it is communicated with between outer tube 7 bottom and casing 1 diapire；The all smooth mouth in the top of outer tube 7 and inner tube 8 is arranged, and inner tube 8 bottom connects horizontally disposed continuous effluent pipe 10, and continuous effluent pipe 10 forward extends out outer tube 7 and casing 1；The bottom of outer tube 7 is also that smooth mouth is arranged.
Mechanical purifying mechanism includes fixed network board 11, movable screen 12, hydraulic cylinder 13, hoist engine 14 and drags for miscellaneous web plate 15；Fixed network board 11 is in being connected to admission chamber 3 on the casing 1 of neighbouring dividing plate 2, and fixed network board 11 is homogeneously connected with diapire and the left and right sidewall of casing 1；The upper end of fixed network board 11 and movable screen 12 is above inner tube 8 upper end, so that the upper end of fixed network board 11 upper end and movable screen 12 is necessarily higher than liquid level, ensure that including showy impurity is gathered, prevent impurity from crossing in the casing 1 that fixed network board 11 enters fixed network board 11 front.The upper end of movable screen 12 is higher than inner tube 8 upper end, it is possible to prevents impurity from crossing movable screen 12 and comes the rear of movable screen 12.
Casing 1 rearward end is provided with chute 16 along the longitudinal direction, slidably connects movable screen 12 in chute 16, and movable screen 12 is homogeneously abutted against with diapire and the left and right sidewall of casing 1；Casing 1 rear is provided with hydraulic cylinder 13, and extension bar 18 slipper seal of hydraulic cylinder 13 is through described casing 1 rear wall and fixing with described movable screen 12 is connected；Multiple mesh 17 it is uniformly provided with respectively in fixed network board 11 and movable screen 12.The front extreme position of movable screen 12 is with described to drag for miscellaneous web plate 15 adjacent, and the rear extreme position of movable screen 12 is adjacent with the rear wall of described casing 1；
Admission chamber 3 is arranged over described hoist engine 14, and casing 1 diapire at the trailing flank of fixed network board 11 is provided with and drags for miscellaneous web plate 15, and dragging for the connection of miscellaneous web plate 15 has lifting rope 20, lifting rope 20 upper end to be connected on the reel 19 of described hoist engine 14；Drag for and on miscellaneous web plate, be preferably provided with multiple mesh, drag for and mesh on miscellaneous web plate, can also be not provided with.
Described two-stage buffering water intake mechanism includes the buffer barrel 21 being located at casing 1 rear and is arranged on the buffer board 22 at admission chamber 3 top；Buffer barrel 21 is higher than described casing 1 top, and buffer barrel 21 is provided with the feed tube 23 for connecting waste stream source and for the drain pipe 24 to admission chamber 3 feed flow；Buffer board 22 is horizontally disposed with and is higher than said inner tube 8 top, described drain pipe 24 is curved pipe (liquid is milder arc Bottomhole pressure) and its outlet is positioned at the top of buffer board 22 adjacent with buffer board 22, so make liquid just flow out from drain pipe 24 and i.e. fall on buffer board 22, it is to avoid the excessive phenomenon causing liquid splash of the discrepancy in elevation.
Connecting on casing 1 diapire in described each dividing plate 2 front and have baffle plate 25, baffle plate 25 is slightly above dividing plate 2 bottom with casing 1 with wide and its top in the lateral direction.So, liquid is when flowing into next chamber (intermediate cavity 4 or water chamber 5) by the opening 6 between dividing plate 2 bottom and casing 1 diapire, to be stopped by baffle plate 25, front can not be flowed directly into along casing 1 diapire, but after just carrying out more sufficiently oil-water separation completely into next chamber, beneficially liquid in next chamber after being folded upward at flowing just continuation flow forward to next one chamber in front.
Said inner tube 8 sidewall is arranged at intervals with some Liquid level holes 26 up and down, is mounted on plug at each Liquid level hole 26.Plug is conventional components, not shown.
Need regulate liquid level to a certain height time, can take off at corresponding height plug, such liquid will be entered inner tube 8 by the Liquid level hole 26 at this and flowed out, making liquid level be maintained at the height in this Liquid level hole 26.This set can control the liquid level in casing 1 the most neatly.
The extension bar 18 of described hydraulic cylinder 13 is embedded with sealing ring with coordinating of casing 1 rear wall at face；Sealing ring is routine techniques, not shown.Described hydraulic cylinder 13 is supported on ground by small rack 27, and described buffer barrel 21 is supported on the ground by big support 28.
The smooth mouth in outer tube 7 top is arranged, and therefore when water is entered outer tube 7 by water chamber 5 by connected entrance 9, the air accumulated in outer tube 7 can be to discharge at the smooth mouth in outer tube 7 top, consequently facilitating water enters outer tube 7 swimmingly.Water chamber 5, intermediate cavity 4 and admission chamber 3 in casing 1 are interconnected by the opening 6 arranged between dividing plate 2 bottom and casing 1 diapire, and so, in casing 1, liquid level all flushes everywhere.Being communicated with the connected entrance 9 of outer tube 7 and water chamber 5 between outer tube 7 bottom and casing 1 diapire, the liquid level in such outer tube 7 also flushes with liquid level everywhere in casing 1.
During use, after in casing 1, persistently water inlet, water level arrive inner tube 8 top, liquid starts to gradually pass through the mode of overflow and enters inner tube 8, and then discharges from continuous effluent pipe 10.So, the height of hydrops in the height on inner tube 8 top i.e. casing 1, by controlling the height on inner tube 8 top, the liquid level in casing 1 can be controlled.Certainly, the sidewall of the inner tube 8 in this utility model is arranged at intervals with some Liquid level holes 26 up and down, is mounted on plug at each Liquid level hole 26, and this structure is more convenient for the control of liquid level.Take off the plug needed at height, the overall liquid level in height in Liquid level hole 26 i.e. determines casing 1 at this.
In work, oily waste water is introduced into buffer barrel 21 at its source, and owing to buffer barrel 21 volume is relatively big, when therefore oily waste water enters buffer barrel 21, flow velocity reduces, and obtains buffering for the first time.Oily waste water obtains second time and buffers when being flow to buffer board 22 by drain pipe 24, oily waste water is wandered on the liquid in admission chamber 3 in buffer board 22 overflow, and oily waste water of fundamentally having stopped compared with the past directly rushes in liquid level depths, the phenomenon again mixed by the You Heshui of initial gross separation originally when entering.
In admission chamber 3, lighter oil content rises to top, and heavier moisture content sinks down into bottom and flows into intermediate cavity 4 by the opening 6 below dividing plate 2.When liquid entrance intermediate cavity 4 and liquid enter water chamber 5 by intermediate cavity 4, can be stopped by baffle plate 25, prevent liquid from directly flowing forwardly into next chamber (intermediate cavity 4 or water chamber 5) along casing 1 diapire.Proceeding the process of oil-water separation in intermediate cavity 4, lighter oil content rises to liquid top, and heavier moisture content sinks down into liquid bottom.The moisture content that final bottom oil content is substantially reduced is flowed into water chamber 5 by the opening 6 below dividing plate 2, and carries out the process of oil-water separation in water chamber 5 further.The water that bottom water chamber 5, oil-containing is little enters outer tube 7 by connected entrance 9, liquid level in outer tube 7 keeps flushing owing to being interconnected with the liquid level in casing 1, i.e. it is maintained at the height (when the plug removed on certain Liquid level hole, the liquid level in casing 1 is maintained at the height in this Liquid level hole) of inner tube 8 upper end.Along with admission chamber 3 is ceaselessly intake, water annular space between outer tube 7 and inner tube 8 enters inner tube 8 by inner tube top or the overflow of Liquid level hole, and discharges through continuous effluent pipe 10.Need not arrange valve on continuous effluent pipe 10, can realize continuous drainage while keeping there is certain liquid level in casing, compared with the past greatly facilitate operation, it is to avoid conventional batch (-type) opens the inconvenience that waste water effuser brings to user.It is no longer water when flow out from continuous effluent pipe 10, but during the more oil water mixture of oil content, it is meant that in casing 1, the waste oil separated expired clearly by collection.Now continuous effluent pipe can be connected with oil collector sump tank, and pull up the plug of bottom in inner tube 8, waste oil in casing 1 be concentrated and discharges.
Mechanization dedoping step is: oil water mixture flows into admission chamber 3 from buffer barrel 21, and the impurity in oil water mixture enters admission chamber 3 the most therewith.Liquid can flow forwardly into intermediate cavity by the mesh 17 in fixed network board 11, and solid impurity is then blocked by fixed network board 11, stays in admission chamber 3.After working time is longer, in admission chamber 3, more impurity can be accumulated.Now starting hydraulic cylinder 13, the extension bar 18 of hydraulic cylinder 13 promotes movable screen 12 to move forward, and in moving process, the liquid in admission chamber 3 can flow to the rear of movable screen 12 by the mesh 17 on movable screen 12, and impurity is then promoted forward by movable screen 12.When movable screen 12 moves forward to front extreme position adjacent with dragging for miscellaneous web plate, now drag for miscellaneous web plate 15 between fixed network board 11 and movable screen 12, the impurity in admission chamber 3 is also gathered under the promotion of movable screen 12 and is being dragged for above miscellaneous web plate 15.Starting hoist engine 14, lifting rope 20 will drag for miscellaneous web plate 15 the most in advance, drag for miscellaneous web plate 15 when rising by it above impurity together raise up, thus realize the clear auxiliary work of mechanization.
Embodiment two
As it is shown in figure 5, the present embodiment is with the difference of embodiment one: described dividing plate 2 is provided with more than three, casing 1 inner chamber is divided into an admission chamber 3, two or more intermediate cavity 4 and a water chamber 5 before backward.
Claims (3)
1. continuous effluent oil water separator, it is characterised in that: include multiple-stage separator and continuous effluent mechanism；
Multiple-stage separator includes the casing of the smooth mouth in top, with liquid flowing direction as forward direction, be uniformly provided with two or more dividing plate in casing in the longitudinal direction, cabinets cavity is divided into admission chamber, intermediate cavity and water chamber before backward by dividing plate；Each dividing plate top flushes with casing top, is communicated with the opening of admission chamber, intermediate cavity and water chamber between each dividing plate bottom and casing diapire；
Continuous effluent mechanism includes the outer tube being vertically provided in water chamber and arranges inner tube within the outer tube, and inner and outer tubes are coaxially set, and outer tube diameter is more than inner tube external diameter；Inner tube top is positioned at casing top, and outer tube top is higher than inner tube top and is communicated with the connected entrance of outer tube and water chamber between outer tube bottom and casing diapire；The all smooth mouth in the top of outer tube and inner tube is arranged, and inner tube bottom connects horizontally disposed continuous effluent pipe, and continuous effluent pipe forward extends out outer tube and casing.
Continuous effluent oil water separator the most according to claim 1, it is characterised in that: connecting on the casing diapire in described each dividing plate front and have baffle plate, baffle plate is higher than dividing plate bottom with casing with wide and its top in the lateral direction.
Continuous effluent oil water separator the most according to claim 1 and 2, it is characterised in that: said inner tube sidewall is arranged at intervals with some Liquid level holes up and down, is mounted on plug at each Liquid level hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620298972.8U CN205569829U (en) | 2016-04-12 | 2016-04-12 | Go out water oil water separator in succession |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620298972.8U CN205569829U (en) | 2016-04-12 | 2016-04-12 | Go out water oil water separator in succession |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205569829U true CN205569829U (en) | 2016-09-14 |
Family
ID=56865532
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620298972.8U Expired - Fee Related CN205569829U (en) | 2016-04-12 | 2016-04-12 | Go out water oil water separator in succession |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205569829U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106818695A (en) * | 2017-02-27 | 2017-06-13 | 四川雷神空天科技有限公司 | Storing apparatus |
| CN107376425A (en) * | 2017-08-22 | 2017-11-24 | 浙江美纳环保科技有限公司 | A kind of floating oil collecting seperator |
| CN112569639A (en) * | 2019-09-28 | 2021-03-30 | 成都市赛沃德意环保科技有限公司 | Oil-water separator convenient for replacing oil receiving box |
-
2016
- 2016-04-12 CN CN201620298972.8U patent/CN205569829U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106818695A (en) * | 2017-02-27 | 2017-06-13 | 四川雷神空天科技有限公司 | Storing apparatus |
| CN107376425A (en) * | 2017-08-22 | 2017-11-24 | 浙江美纳环保科技有限公司 | A kind of floating oil collecting seperator |
| CN112569639A (en) * | 2019-09-28 | 2021-03-30 | 成都市赛沃德意环保科技有限公司 | Oil-water separator convenient for replacing oil receiving box |
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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: 20160914 Termination date: 20170412 |