CN2725275Y - Integrated oil removing settling filter - Google Patents
Integrated oil removing settling filter Download PDFInfo
- Publication number
- CN2725275Y CN2725275Y CN 200420041508 CN200420041508U CN2725275Y CN 2725275 Y CN2725275 Y CN 2725275Y CN 200420041508 CN200420041508 CN 200420041508 CN 200420041508 U CN200420041508 U CN 200420041508U CN 2725275 Y CN2725275 Y CN 2725275Y
- Authority
- CN
- China
- Prior art keywords
- chamber
- tank body
- oil removing
- oil
- coarse
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Abstract
The utility model relates to a sewage treatment plant, in particular to an integrated oil removing settling filter with high precision which can simultaneously realize the oil-water separation and the solid-liquid separation. A tank is sequentially divided into a buffering chamber (2), a coarse granulation chamber (3), the sloped-tube oil-removing chamber (4), a water collecting chamber (5), a flow guiding tube (10), the flocculating chamber (7) of the swirling flow reaction, the sloped-tube settling chamber (8), and the filter chamber (9) of the filtering core from the sealing head end of the tank body by a separator plate. A static mixer (12) is connected out the tank body, and an oil drain port is arranged on the top of the tank body. A soil discharging port (17) is arranged on the bottom of the tank body. The whole integrated oil removing settling filter adopts the horizontal tubular structure, and has the advantages that volume is small; the functions are full; the movable components do not have; the operation is simple; the operation is safe.
Description
Affiliated technical field: the utility model relates to a kind of waste disposal plant, particularly can realize the comprehensive oil removing sedimentation of the high precision strainer of oily water separation and solid-liquid separation simultaneously.
Background technology: existing equipment is that water treatment agents such as flocculation agent, coagulant aids are added before processing, and experiment shows that it is not fine processing efficient like this, and the medicament service efficiency is low, and the medicament add-on is also very big, is unfavorable for running cost control.Its two be equipment coarse material selection be haydite or the floating filter material of the about 3mm of diameter, the coarse void ratio that is made of the solid filtrate of this class small particle size is only about 50%, has the susceptible to plugging defective of filtering layer.Three what be that the equipment filtering unit adopts is walnut shell filtering material, quartz sand or fibrous nodules even-granular filtrate for it, this type of filter type all can not the better controlled final outflow water in the particle diameter of suspended solids, and rejection of oil flied effluent has higher requirements to this, especially low permeability oil field.
Summary of the invention: the purpose of this utility model is a kind of comprehensive oil removing sedimentation strainer of design, makes its crude oil when oily water separation and solid-liquid separation, reaches to add that medicament is few, processing efficiency is high, save cost, effect of settling, wash nonclogging purpose easily.
The purpose of this utility model is to realize like this, comprehensive oil removing sedimentation strainer, it is characterized in that: tank body is divided into buffer chamber, coarse chamber, inclined tube oil removal plant, the chamber that catchments, thrust-augmenting nozzle by dividing plate from the seal head end order, cyclone reaction flocculating chamber, inclined plate sedimentation device, filter element filtering chamber; Tank body connects static mixer outward, is provided with oil discharge outlet at the cylindrical shell top; In the cylindrical shell bottom mud discharging mouth is arranged.
The filter element filtering chamber comprises " O " type sealing filter core that is made of non-woven fabrics.
Described coarse chamber selects for use the multiaspect hollow ball as the coarse material.
The utility model is selected hydrophilic non-woven fabrics filter core for use, can be changed the filter core of different size according to the effluent quality requirement easily, and " O " type of filter core employing simultaneously sealing plug-in card is fixed, easy accessibility.
The utility model complete machine adopts horizontal tubular structure, has that volume is little, function is complete, no dynamic component, characteristics simple to operate, safe and reliable to operation, is the ideal equipment of handling oilfield sewage, and the while can be widely used in the oily water treatment of other industry.
The utility model is described in further detail below in conjunction with the embodiment accompanying drawing:
Description of drawings: Fig. 1 is the utility model example structure synoptic diagram;
Among the figure: 1, pipeline; 2, surge chamber; 3, coarse chamber; 4, inclined tube removes the grease chamber; 5, the chamber that catchments; 6, reaction chamber; 7, cyclone reaction flocculating chamber; 8, inclined tube settling pocket; 9, filter element filtering chamber; 10, thrust-augmenting nozzle; 11, dosing mouth; 12, static mixer; 13, diffusing opening; 14, filter core; 15, oil discharge outlet; 16, oil extraction; 17, mud discharging mouth; 18, water outlet.
Embodiment: as shown in Figure 1, oily(waste)water arrives surge chamber 2 by pipeline 1 after entering horizontal garden tube container, float to the equipment top here in the water on the oil slick, current enter coarse chamber 3 from the bottom, select for use the multiaspect hollow ball as the coarse material, current are by passing down in the process of coarse layer, the little oil droplet of dispersive contacts with the coarse material impacts in the water, caught by oil loving coarse material surface and assemble, when oil reservoir gathers to a certain degree, oil droplet breaks away from multiaspect hollow ball surface under buoyancy and sluicing, particle diameter become big oil droplet be easy to arrive equipment top oil reservoir, enter inclined tube with current and remove the oil droplet of grease chamber 4 by further come-up removal, 2,3, total oil removal efficiency about 80% of 4 three steps; The water that catchments in the chamber 5 is drawn by thrust-augmenting nozzle 10, and diversion pipeline is provided with dosing mouth 11, and flocculation agent is added by dosing mouth 11; Tangentially enter reaction chamber 6 after 12 pressures mix with water through static mixer then, current are the eddy flow attitude to prolong current through line in reaction chamber, guarantee the reaction times, then enter flocculating settling chamber 7 by diffusing opening 13, current are laminar flow regime in this chamber, be beneficial to the formation and the sedimentation of flocs unit, in inclined tube settling pocket 8 subsequently, little flocs unit is by further sedimentation removal, the suspended solids and the oil in water emulsion of removing that do not floated are caught by flocs unit in this process in the former water, select suitably by 6 as medicament, 7, suspended substance is all removed basically in the 8 three step water; The filtering chamber 9 that is located at the equipment end can do accurately control to effluent quality according to user's requirement, be not more than 1 micron as suspended solids particle diameter in the low permeability oil field requirement water outlet, then equipment is joined 1 micron filter core 14 and is got final product, filter core 14 selects for use hydrophilic to be beneficial to clean, " O type " sealing-ring card insert type connects, the convenient installation and replacing; Handle water footpath, back water outlet 18 remover apparatus at last;
The oil slick that is gathered in each chamber roof is discharged from oil discharge outlet 15 by control draining valve 16; The heavy body refuse that combines in device bottom is discharged by mud discharging mouth 17; For the benefit of the spoil disposal washpipe can be established in the soil discharging facility bottom.
Claims (4)
1, comprehensive oil removing sedimentation strainer, it is characterized in that: tank body is divided into buffer chamber (2), coarse chamber (3), inclined tube except that grease chamber (4), the chamber that catchments (5), thrust-augmenting nozzle (10), cyclone reaction flocculating chamber (7), inclined tube settling pocket (8), filter element filtering chamber (9) by dividing plate from the seal head end order; Tank body connects static mixer (12) outward, is provided with oil discharge outlet (15) at the cylindrical shell top; In the cylindrical shell bottom mud discharging mouth (17) is arranged.
2, comprehensive oil removing sedimentation strainer according to claim 1 is characterized in that: filter element filtering chamber (9) comprise " O " type sealing filter core (14) that is made of non-woven fabrics.
3, comprehensive oil removing sedimentation strainer according to claim 1, it is characterized in that: described coarse chamber (3) selects for use the multiaspect hollow ball as the coarse material.
4, comprehensive oil removing sedimentation strainer according to claim 1, it is characterized in that: the water in the chamber that catchments (5) is drawn by thrust-augmenting nozzle (10), and diversion pipeline is provided with dosing mouth (11), and flocculation agent is added by dosing mouth (11).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420041508 CN2725275Y (en) | 2004-03-01 | 2004-03-01 | Integrated oil removing settling filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420041508 CN2725275Y (en) | 2004-03-01 | 2004-03-01 | Integrated oil removing settling filter |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2725275Y true CN2725275Y (en) | 2005-09-14 |
Family
ID=35039997
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200420041508 Expired - Fee Related CN2725275Y (en) | 2004-03-01 | 2004-03-01 | Integrated oil removing settling filter |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2725275Y (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102485656A (en) * | 2010-12-02 | 2012-06-06 | 宜兴市星晨水汽净化设备有限公司 | Constant-current fiber ball degreaser |
CN102838225A (en) * | 2011-07-28 | 2012-12-26 | 南通天华和睿科技创业有限公司 | Water treatment device for oilfield well |
CN103910449A (en) * | 2014-03-29 | 2014-07-09 | 中原特种车辆有限公司 | Fracturing flow-back fluid treatment device |
CN104193041A (en) * | 2014-09-24 | 2014-12-10 | 厦门福润源环保科技有限公司 | Treatment method of processing wastewater of jade |
CN104193117A (en) * | 2014-09-24 | 2014-12-10 | 厦门福润源环保科技有限公司 | Treatment device of processing wastewater of jade |
CN105217831A (en) * | 2015-07-07 | 2016-01-06 | 南京国能环保工程有限公司 | Gravitational coagulation formula oily-water seperating equipment |
CN106542676A (en) * | 2017-01-12 | 2017-03-29 | 青岛双瑞海洋环境工程股份有限公司 | Marine exhaust washs water treatment facilities |
CN109052508A (en) * | 2018-09-04 | 2018-12-21 | 唐山学院 | A kind of lacquer spraying technique gives up water purifying means and purification method |
CN116444103A (en) * | 2023-06-12 | 2023-07-18 | 扬州澄露环境工程有限公司 | Vertical oil-water separator |
-
2004
- 2004-03-01 CN CN 200420041508 patent/CN2725275Y/en not_active Expired - Fee Related
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102485656A (en) * | 2010-12-02 | 2012-06-06 | 宜兴市星晨水汽净化设备有限公司 | Constant-current fiber ball degreaser |
CN102838225A (en) * | 2011-07-28 | 2012-12-26 | 南通天华和睿科技创业有限公司 | Water treatment device for oilfield well |
CN103910449A (en) * | 2014-03-29 | 2014-07-09 | 中原特种车辆有限公司 | Fracturing flow-back fluid treatment device |
CN103910449B (en) * | 2014-03-29 | 2016-03-30 | 中原特种车辆有限公司 | A kind of fracturing outlet liquid treatment unit |
CN104193041B (en) * | 2014-09-24 | 2016-02-03 | 厦门福润源环保科技有限公司 | A kind for the treatment of process of jade processing waste water |
CN104193117A (en) * | 2014-09-24 | 2014-12-10 | 厦门福润源环保科技有限公司 | Treatment device of processing wastewater of jade |
CN104193041A (en) * | 2014-09-24 | 2014-12-10 | 厦门福润源环保科技有限公司 | Treatment method of processing wastewater of jade |
CN104193117B (en) * | 2014-09-24 | 2017-04-26 | 厦门福润源环保科技有限公司 | Treatment device of processing wastewater of jade |
CN105217831A (en) * | 2015-07-07 | 2016-01-06 | 南京国能环保工程有限公司 | Gravitational coagulation formula oily-water seperating equipment |
CN106542676A (en) * | 2017-01-12 | 2017-03-29 | 青岛双瑞海洋环境工程股份有限公司 | Marine exhaust washs water treatment facilities |
CN109052508A (en) * | 2018-09-04 | 2018-12-21 | 唐山学院 | A kind of lacquer spraying technique gives up water purifying means and purification method |
CN116444103A (en) * | 2023-06-12 | 2023-07-18 | 扬州澄露环境工程有限公司 | Vertical oil-water separator |
CN116444103B (en) * | 2023-06-12 | 2023-09-26 | 扬州澄露环境工程有限公司 | Vertical oil-water separator |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100579917C (en) | Three-phase cyclone separator and cleaning treatment system for oil-containing water | |
AU2009344910B2 (en) | Apparatus and method for separation of phases in a multiphase flow | |
CN102642884B (en) | Oil-contained sewage treatment method and eddy energy fast-cyclone separating system of special equipment for method | |
CN106186387B (en) | A kind of separation equipment and method for separating and processing | |
CN103787527B (en) | A kind of oil-contaminated water air-float suspended layer filtration unit | |
CN102807291A (en) | Treatment method and equipment for oilfield produced water | |
CN203461894U (en) | Restaurant waste water purification device | |
CN105330069B (en) | Air-float filtration processing unit | |
CN107522310A (en) | Not agent-feeding treatment oil-polluted water re-injection technique | |
CN2725275Y (en) | Integrated oil removing settling filter | |
CN2936380Y (en) | Unpowered waste water filtering and sterilizing treating device | |
GB2423299A (en) | Oil/water separator for use in drainage systems | |
CN205709989U (en) | A kind of oilfield sewage oil removal sand removal sedimenting system | |
CN2892839Y (en) | Light oil polluted water integrated processing apparatus | |
CN202898076U (en) | Crude oil sewage treatment device | |
CN209178108U (en) | A kind of oily-water seperating equipment of waste oil | |
CN107961907B (en) | Automatic sand washing rotational flow sand remover and automatic sand washing system | |
CN109650677A (en) | A kind of oily-water seperating equipment | |
CN205258153U (en) | Air supporting and filtration integrated device | |
CN212151802U (en) | Pretreatment equipment for grinding oil stains and SS in wastewater | |
CN209128193U (en) | A kind of high speed degreasing unit and rapidly and efficiently oil removing Airfloat filtering pond | |
CN202865025U (en) | Multifunctional water treatment device | |
CN202466820U (en) | Novel oil-water separator | |
CN207483477U (en) | A kind of air-floating apparatus of high-efficient purification sewage | |
CN105347569B (en) | Air-float filtration membrane filtration processing unit |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20050914 Termination date: 20100301 |