CN206924486U - Oil filtration system - Google Patents
Oil filtration system Download PDFInfo
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- CN206924486U CN206924486U CN201720698827.3U CN201720698827U CN206924486U CN 206924486 U CN206924486 U CN 206924486U CN 201720698827 U CN201720698827 U CN 201720698827U CN 206924486 U CN206924486 U CN 206924486U
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Abstract
The utility model discloses a kind of oil filtration system, including filtration system, filter membrane precoating system, the filtration system includes feed tube, filtering tank and the drain pipe being sequentially connected, the feed tube is provided with liquid feeding pump, the filter membrane precoating system includes blending tank, with mixing tank connected oil inlet pipe, charge pipe, discharge nozzle, recovery tube and blow-off pipe, the oil inlet pipe connects the feed tube, the charge pipe connection addition pump, the discharge nozzle is connected in the filtering tank, the recovery tube connects the drain pipe, recovery precoating oil plant.A kind of oil filtration system of the utility model, diatomite is mixed in precoating system and precoats cake layer in the filtering tank of filtration system, the continuous filtering of liquid can be achieved by once precoating, when filtering reaches saturation, add new diatomite, to be constantly formed continuously new cake layer, or cake layer is changed, improve the filter capacity and efficiency of equipment.
Description
Technical field
The utility model belongs to edible oil processing technique field, specifically, is related to a kind of oil filtration system.
Background technology
Edible oil filtering at present is mostly using filter types such as precipitation, filter bag, sheet frames, and its filter efficiency is low, filtering accuracy
Difference, production environment is poor, and hygienic conditions control difficulty is big, and edible oil economic value is high, is lost in filter process and requires low.In order to
Edible oil filter efficiency is improved, filtration Quality is improved, improves production environment, it is necessary to seek new edible oil filtering scheme.It is existing
Usually diatomite is selected to be filtered in technology, but diatomite is not easily cleaned, and usually need to change in use, and make life
Producing line stops, and is unfavorable for the requirement of continuous production in industrial production, reduces production efficiency.
Utility model content
It is to provide a kind of oil filtration system to solve above technical problem and problem, the purpose of this utility model, can
Solves the problems, such as edible oil filtration Quality difference, moreover it is possible to solve the problems, such as that oily filter efficiency is low.
The utility model purpose is realized in：A kind of oil filtration system, its key are：Including filtration system, filter
Film precoats system, and the filtration system includes the feed tube, filtering tank and the drain pipe that are sequentially connected, the feed tube be provided with into
Liquid pump, the filter membrane precoating system include blending tank, with mixing tank connected oil inlet pipe, charge pipe, discharge nozzle, recovery tube and row
Dirt pipe, the oil inlet pipe connect the feed tube, the charge pipe connection addition pump, and the discharge nozzle connects the filtering tank
Interior, the recovery tube connects the drain pipe, recovery precoating oil plant.Using said structure, the system is situated between by filtering of diatomite
Matter, diatomite is added into blending tank by adding pump, edible oil is added into blending tank by oil inlet pipe, by diatomite and food
Stirred and evenly mixed, be then added to by discharge nozzle in the filtering tank for filling oil, the filter house in filtering tank is formed uniformly with oil
Cake layer, complete diatomaceous precoating, cake layer can realize the interception filtering to edible oil impurity, pass through filter cake in precoating
The oil of layer is then recycled by recovery tube.Pass through pipe-line system, blending tank, filtering tank, the closing for realizing edible oil simultaneously
Circulating filtration, its filtration Quality, filter efficiency, production environment, which are obtained for, greatly to be improved.
Further, above-mentioned filtering tank includes tank body, the central tube in tank body, distribution plate and filtering table, described point
It is sheathed on the central tube with disk and filtering table, the filtering table is uniformly distributed in below distribution plate, the filtering table inner chamber
Communicated with the central tube, the drain pipe connects the central tube.Using said structure, when precoating cake layer, distribution plate will
The mixed liquor of diatomite and edible oil is evenly spread on the filtering table of tank body, to form cake layer on filtering table, and in
Heart pipe then connects filtering table and concentrates the oil passed through, then is recycled in blending tank and recycled by recovery tube；During filtering, oil passes through
Cake layer is filtered, and filtering gained supernatant liquid is focused in central tube, is then sent out by drain pipe.
Preferably, above-mentioned tank body is externally provided with centrifugation motor, central tube described in the centrifugation motor connection, makes central tube centrifugal rotary
Turn.Using said structure, when changing cake layer, central tube can be driven to rotate by centrifuging motor, so as to by filtering table
Cake layer centrifugation depart from, then from filtering pot bottom sewage draining exit discharge.
Preferably, above-mentioned filtering top tank structure is provided with cleaning jet pipe, and filtering panel surface described in the cleaning jet pipe face is provided with clearly
Wash nozzle.Using said structure, the efficiency to filtering table cleaning can be further improved.
Further, above-mentioned addition pump connects feed tube by the first cleaning pipe, and the addition parallel connection of pumps has the second cleaning
Pipe, the second cleaning pipe both ends are respectively communicated with feed tube and charge pipe, the oil inlet pipe, charge pipe, discharge nozzle, recovery tube, row
Dirt pipe, the first cleaning pipe and the second cleaning pipe are equipped with magnetic valve.Using said structure, opening for magnetic valve is controlled by system
Close, so as to realize precoating system and filtration system separate or synchronous operation, and when water is conveyed in feed tube, can to blending tank,
Filtering tank, each pipeline are cleaned, and can improve the automatic cleaning efficiency of whole system.
Preferably, on one section of feed tube after above-mentioned first cleaning pipe connects liquid feeding pump with the second cleaning pipe.Using upper
Structure is stated, beneficial to control.
Further, feed tube described in the last period of above-mentioned liquid feeding pump is provided with feed liquor main valve, and the oil inlet pipe connects institute
State one section of feed tube between feed liquor main valve and liquid feeding pump.Using said structure, controlled beneficial to manual or automaticization.
Beneficial effect：
A kind of oil filtration system of the utility model, diatomite is mixed and in the filtering tank of filtration system in precoating system
Middle precoating cake layer, the continuous filtering of liquid can be achieved by once precoating, when filtering reaches saturation, add new diatom
Soil, to be constantly formed continuously new cake layer, or cake layer is changed, improve the filter capacity and efficiency of equipment.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
Wherein 1a is feed tube, 1b be filtering tank, 11 be pipe centered on tank body, 12,13 be distribution plate, 14 be filtering table,
1c is drain pipe, 1d is liquid feeding pump, 2a is blending tank, 2b is oil inlet pipe, 2c is charge pipe, 2d is discharge nozzle, 2e be recovery tube,
2f is blow-off pipe, 3 is addition pump, 4 is centrifugation motor, 5 is cleaning jet pipe, 6 is the first cleaning pipe, 7 is the second cleaning pipe, 8 is
Magnetic valve, 9 are feed liquor main valve.
Embodiment
With reference to embodiment and accompanying drawing, the utility model is described in further detail.
Embodiment：
As shown in Figure 1：A kind of oil filtration system, by filtration system, filter membrane precoating system form, the filtration system by according to
Feed tube 1a, filtering tank 1b and drain pipe the 1c composition of secondary connection, the feed tube 1a are provided with liquid feeding pump 1d, the liquid feeding pump
Feed tube 1a described in 1d the last period is provided with feed liquor main valve 9, and the oil inlet pipe 2b connects the feed liquor main valve 9 and liquid feeding pump 1d
Between one section of feed tube 1a.
The filtering tank 1b is made up of tank body 11, the central tube 12 in tank body 11, distribution plate 13 and filtering table 14, institute
State distribution plate 13 and filtering table 14 is sheathed on the central tube 12, the filtering table 14 is uniformly distributed under distribution plate 13
Side, the inner chamber of filtering table 14 communicate with the central tube 12, and the drain pipe 1c connects the central tube 12.Outside the tank body 11
Provided with centrifugation motor 4, the centrifugation motor 4 connects the central tube 12, makes the centrifugal rotation of central tube 12.The filtering tank 1b inwalls
Provided with cleaning jet pipe 5, the surface of filtering table 14 described in the face of cleaning jet pipe 5 is provided with washer jet.
The filter membrane precoats system by blending tank 2a, the oil inlet pipe 2b being connected with blending tank 2a, charge pipe 2c, discharge nozzle
2d, recovery tube 2e and blow-off pipe 2f compositions, the oil inlet pipe 2b connect the feed tube 1a, the charge pipe 2c connections addition pump
3, the discharge nozzle 2d is connected in the filtering tank 1b, the recovery tube 2e connections drain pipe 1c, recovery precoating oil plant.Institute
State addition pump 3 and feed tube 1a is connected by the first cleaning pipe 6, the addition pump 3 is parallel with the second cleaning pipe 7, second cleaning
The both ends of pipe 7 are respectively communicated with feed tube 1a and charge pipe 2c, the first cleaning pipe 6 connected with the second cleaning pipe 7 liquid feeding pump 1d it
On one section of feed tube 1a afterwards.
The oil inlet pipe 2b, charge pipe 2c, discharge nozzle 2d, recovery tube 2e, blow-off pipe 2f, the first cleaning pipe 6 and second are clear
Wash pipe 7 and be equipped with magnetic valve 8.
Operation principle：
During precoating, first oil is conveyed into filtering tank and filled by liquid feeding pump, will be by feeding blending tank by oil inlet pipe, will be mixed
After the oil of conjunction tank is attached to setting liquid level, related valve is closed, appropriate diatomite is added in blending tank by adding pump, by oil
Uniform diatomite liquid is stirred into diatomite, the diatomite liquid after mixing delivers to filtering tank, will by distribution plate
Diatomite mixed liquor is dispersed to be opened, and the diatomite now added can be uniformly adhered on filtering table, forms cake layer, clarification
Liquid then by diatomite cake layer, by filtering table, collect into central tube, from central tube export top outlet outflow, lead to
Cross recovery tube and be recycled to blending tank.By the switch of related valve in pipe-line system, the liquid iterative cycles of precoating can be allowed, pass through
Some time, uniform and stable cake layer is formed, complete diatomaceous precoating.
After the completion of precoating, it is possible to start the filtering of oil, oil to be filtered was continuously pumped into by liquid feeding pump
Filter tank, fluid filtering table, are pooled to central tube, by being exported above central tube, will filter gained by diatomite cake layer
Supernatant liquid is transported to storage tank or filling apparatus, that is, realizes the continuous filtering of fluid.The system by precoating once just
The continuous filtering of liquid can be realized, when being filled into the debris content saturation of cake layer, now the pressure of filtering tank will rise
Height, when reaching setup pressure value, system is automatically stopped filtering., can be by adding pump on-line continuous in continuous filtration process
The new diatomite of addition, to be constantly formed continuously new cake layer, improve the filter capacity of equipment.
After filtering contacts, disc spins are filtered by centrifuging motor driven, by centrifugal action, by waste diatomite filter cake
Lower filtering table is got rid of, then is given off by filtering tank down discharge mouth.Last CIP cleaning fluids are by cleaning jet pipe by filtering tank and mistake
Filter disc cleans up, and is managed by the first cleaning, the second cleaning pipe cleans up blending tank and addition pump.
Finally it should be noted that foregoing description is only preferred embodiment of the present utility model, the common skill of this area
Art personnel on the premise of without prejudice to the utility model aims and claim, can make under enlightenment of the present utility model
Expression, such conversion are each fallen within the scope of protection of the utility model as multiple types.
Claims (7)
- A kind of 1. oil filtration system, it is characterised in that：Including filtration system, filter membrane precoating system, the filtration system include according to Feed tube (1a), filtering tank (1b) and the drain pipe (1c) of secondary connection, the feed tube (1a) is provided with liquid feeding pump (1d), described Filter membrane precoating system includes blending tank (2a), the oil inlet pipe (2b) being connected with blending tank (2a), charge pipe (2c), discharge nozzle (2d), recovery tube (2e) and blow-off pipe (2f), the oil inlet pipe (2b) connect the feed tube (1a), and the charge pipe (2c) is even Logical addition pump (3), the discharge nozzle (2d) are connected in the filtering tank (1b), and the recovery tube (2e) connects the drain pipe (1c), recovery precoating oil plant.
- 2. oil filtration system according to claim 1, it is characterised in that：The filtering tank (1b) includes tank body (11), set In the central tube (12) in tank body (11), distribution plate (13) and filtering table (14), the distribution plate (13) and filtering table (14) are equal It is sheathed on the central tube (12), the filtering table (14) is uniformly distributed in below distribution plate (13), in the filtering table (14) Chamber communicates with the central tube (12), and the drain pipe (1c) connects the central tube (12).
- 3. oil filtration system according to claim 2, it is characterised in that：The tank body (11) is externally provided with centrifugation motor (4), The centrifugation motor (4) connects the central tube (12), makes central tube (12) centrifugal rotation.
- 4. the oil filtration system according to Claims 2 or 3, it is characterised in that：Filtering tank (1b) inwall is provided with cleaning Jet pipe (5), filtering table (14) surface described in cleaning jet pipe (5) face are provided with washer jet.
- 5. oil filtration system according to claim 1, it is characterised in that：The addition pump (3) manages (6) by the first cleaning Connect feed tube (1a), it is described addition pump (3) be parallel with the second cleaning pipe (7), this second cleaning pipe (7) both ends be respectively communicated with into Liquid pipe (1a) and charge pipe (2c), the oil inlet pipe (2b), charge pipe (2c), discharge nozzle (2d), recovery tube (2e), blow-off pipe (2f), the first cleaning pipe (6) and the second cleaning pipe (7) are equipped with magnetic valve (8).
- 6. oil filtration system according to claim 5, it is characterised in that：The first cleaning pipe (6) and the second cleaning pipe (7) on one section of feed tube (1a) after connection liquid feeding pump (1d).
- 7. oil filtration system according to claim 1, it is characterised in that：Feed liquor described in the last period of the liquid feeding pump (1d) Pipe (1a) is provided with feed liquor main valve (9), and the oil inlet pipe (2b) connects one between the feed liquor main valve (9) and liquid feeding pump (1d) Section feed tube (1a).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720698827.3U CN206924486U (en) | 2017-06-16 | 2017-06-16 | Oil filtration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720698827.3U CN206924486U (en) | 2017-06-16 | 2017-06-16 | Oil filtration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206924486U true CN206924486U (en) | 2018-01-26 |
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ID=61345891
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|---|---|---|---|
| CN201720698827.3U Active CN206924486U (en) | 2017-06-16 | 2017-06-16 | Oil filtration system |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108926884A (en) * | 2018-07-23 | 2018-12-04 | 上海兖矿能源科技研发有限公司 | A kind of filter device for the filtering of high temperature fischer-tropsch synthetic oil |
| CN109432869A (en) * | 2018-12-14 | 2019-03-08 | 广东百维生物科技有限公司 | For filtering the diatomite filter group and its control method of collagen |
| CN110354582A (en) * | 2019-06-27 | 2019-10-22 | 重庆中轻装备有限公司 | A kind of soy sauce filtration process |
| CN113509788A (en) * | 2021-06-30 | 2021-10-19 | 重庆中轻装备有限公司 | Diatomite recovery method of disc filter |
| CN113996112A (en) * | 2021-11-10 | 2022-02-01 | 龙岩卓越生物基材料有限公司 | Alkyd resin filtering method |
| CN114307360A (en) * | 2021-12-13 | 2022-04-12 | 宁夏恒生西夏王酒业有限公司 | Raw wine fining, clarifying and filtering equipment and using method |
| CN115253463A (en) * | 2022-07-27 | 2022-11-01 | 宁波长荣酿造设备有限公司 | Filtering system and control method |
| CN115554751A (en) * | 2022-12-06 | 2023-01-03 | 江苏威泽智能科技股份有限公司 | Machine tool with cutting fluid rapid filtering device |
-
2017
- 2017-06-16 CN CN201720698827.3U patent/CN206924486U/en active Active
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108926884A (en) * | 2018-07-23 | 2018-12-04 | 上海兖矿能源科技研发有限公司 | A kind of filter device for the filtering of high temperature fischer-tropsch synthetic oil |
| CN109432869A (en) * | 2018-12-14 | 2019-03-08 | 广东百维生物科技有限公司 | For filtering the diatomite filter group and its control method of collagen |
| CN110354582A (en) * | 2019-06-27 | 2019-10-22 | 重庆中轻装备有限公司 | A kind of soy sauce filtration process |
| CN113509788A (en) * | 2021-06-30 | 2021-10-19 | 重庆中轻装备有限公司 | Diatomite recovery method of disc filter |
| CN113509788B (en) * | 2021-06-30 | 2022-08-05 | 重庆中轻装备有限公司 | Diatomite recovery method of disc filter |
| CN113996112A (en) * | 2021-11-10 | 2022-02-01 | 龙岩卓越生物基材料有限公司 | Alkyd resin filtering method |
| CN114307360A (en) * | 2021-12-13 | 2022-04-12 | 宁夏恒生西夏王酒业有限公司 | Raw wine fining, clarifying and filtering equipment and using method |
| CN115253463A (en) * | 2022-07-27 | 2022-11-01 | 宁波长荣酿造设备有限公司 | Filtering system and control method |
| CN115554751A (en) * | 2022-12-06 | 2023-01-03 | 江苏威泽智能科技股份有限公司 | Machine tool with cutting fluid rapid filtering device |
| CN115554751B (en) * | 2022-12-06 | 2023-03-03 | 江苏威泽智能科技股份有限公司 | Machine tool with cutting fluid rapid filtering device |
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