CN207646166U - A kind of automation edible oil settler - Google Patents
A kind of automation edible oil settler Download PDFInfo
- Publication number
- CN207646166U CN207646166U CN201721630503.2U CN201721630503U CN207646166U CN 207646166 U CN207646166 U CN 207646166U CN 201721630503 U CN201721630503 U CN 201721630503U CN 207646166 U CN207646166 U CN 207646166U
- Authority
- CN
- China
- Prior art keywords
- tank
- thermoprecipitation
- cryoprecipitate
- controller
- oil
- 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
Landscapes
- Fats And Perfumes (AREA)
Abstract
A kind of automation edible oil settler, including oil inlet pipe, the oil inlet pipe are connected with thermoprecipitation tank, and thermoprecipitation tank is connected with cryoprecipitate tank by petroleum pipeline, and oil pump is equipped on the petroleum pipeline, and cryoprecipitate tank is equipped with flowline;The bottom of thermoprecipitation tank and cryoprecipitate tank is equipped with Drainage valve;The thermoprecipitation tank is equipped with electric heater, and the electric heater is connected with controller;The cryoprecipitate tank is equipped with refrigeration machine, and refrigeration machine is connect with controller;It is equipped with the temperature sensor being connect with controller in the thermoprecipitation tank and cryoprecipitate tank.
Description
Technical field
The utility model belongs to edible oil field more particularly to a kind of automation edible oil settler.
Background technology
Edible oil by filtering, wherein still contain a large amount of impurity, including insoluble particulate matter and phosphatide colloid, phosphatide it is tight
The quality of peanut oil is endangered again, it is necessary to be removed from finished product.Existing dephosphorization technique generally uses heating hydrate technology dephosphorization, but
A large amount of aroma substance can be taken away by being this method, reduce peanut oil flavor, this with my quality of company's high-quality peanut oil not
Symbol.And it is not in this problem to use cryoprecipitate rule.Therefore my company develops a kind of equipment of edible oil settler.
Utility model content
The utility model provides a kind of automation edible oil settler in order to solve the above problem.
The utility model is achieved by the following technical solution:
A kind of automation edible oil settler, including oil inlet pipe, the oil inlet pipe are connected with thermoprecipitation tank, thermoprecipitation tank
It is connected with cryoprecipitate tank by petroleum pipeline, oil pump is installed on the petroleum pipeline, cryoprecipitate tank is equipped with flowline;Thermoprecipitation tank
It is equipped with Drainage valve with the bottom of cryoprecipitate tank;
The thermoprecipitation tank is equipped with electric heater, and the electric heater is connected with controller;It is set on the cryoprecipitate tank
There are refrigeration machine, refrigeration machine to be connect with controller;
It is equipped with the temperature sensor being connect with controller in the thermoprecipitation tank and cryoprecipitate tank.
It is further to improve, it is covered with heat-barrier material outside the thermoprecipitation tank and cryoprecipitate tank.
Further to improve, the controller is singlechip controller.
Compared with prior art, the utility model has the following advantages:
The utility model removes the impurity in edible oil crude oil by the way of precipitation, remains the aroma substance in oil,
Improve the quality of oil.Crude oil by filtering is introduced into thermoprecipitation tank, after electric heater heats thermoprecipitation tank, oil temperature liter
The viscosity of height, edible oil reduces, and accelerates insoluble matter contamination precipitation.Thermoprecipitation terminates rear pump or output pump and oil is pumped into cryoprecipitate tank,
Refrigeration machine on cryoprecipitate tank cools to 15 degrees centigrades to oil, and precipitation is gradually precipitated in phosphatide colloid from oil at this time.It is cold heavy
The edible oil after oil pipe pump-and-treat system can be gone out after shallow lake.Above step has the controller in equipment to automatically control
At automatically adjusting to temperature, ensure that the consistency of precipitation temperature.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
Specific implementation mode
Embodiment 1
As a kind of automation edible oil settler of Fig. 1, including oil inlet pipe 2, the oil inlet pipe 2 are connected with thermoprecipitation tank
1, thermoprecipitation tank 1 is connected with cryoprecipitate tank 4 by petroleum pipeline, and oil pump 3 is equipped on the petroleum pipeline, and cryoprecipitate tank 4 is equipped with
Flowline 5;The bottom of thermoprecipitation tank 1 and cryoprecipitate tank 4 is equipped with Drainage valve;
The thermoprecipitation tank 1 is equipped with electric heater(Heater is not shown in figure in oil tank), the electric heater company
It is connected to controller;The cryoprecipitate tank is equipped with refrigeration machine, and refrigeration machine is connect with controller;
It is equipped with the temperature sensor being connect with controller in the thermoprecipitation tank 1 and cryoprecipitate tank 4.1 He of thermoprecipitation tank
It is covered with heat-barrier material outside cryoprecipitate tank 4.
Further to improve, the controller is singlechip controller.
Crude oil by filtering is introduced into thermoprecipitation tank, and after electric heater heats thermoprecipitation tank, oil temperature increases, edible oil
Viscosity reduce, accelerate insoluble matter contamination precipitation.Thermoprecipitation terminates rear pump or output pump and oil is pumped into cryoprecipitate tank, on cryoprecipitate tank
Refrigeration machine 15 degrees centigrades are cooled to oil, at this time phosphatide colloid gradually from oil be precipitated precipitation.After cryoprecipitate i.e.
The edible oil after oil pipe pump-and-treat system can be gone out.Above step has the controller in equipment to automatically control completion, to temperature
It automatically adjusts, ensure that the consistency of precipitation temperature.When cleaning precipitation, the precipitation for precipitating pot bottom can be from Drainage valve
Outflow.
Above example is merely to illustrate the utility model, but is not intended to limit the scope of the present invention, every foundation
The technical essence of the utility model still falls within this reality to any simple modification, equivalent change and modification made by following instance
In the range of new technique scheme.
Claims (3)
1. a kind of automation edible oil settler, including oil inlet pipe, which is characterized in that the oil inlet pipe is connected with thermoprecipitation
Tank, thermoprecipitation tank are connected with cryoprecipitate tank by petroleum pipeline, and oil pump is equipped on the petroleum pipeline, and cryoprecipitate tank is equipped with fuel-displaced
Pipe;The bottom of thermoprecipitation tank and cryoprecipitate tank is equipped with Drainage valve;
The thermoprecipitation tank is equipped with electric heater, and the electric heater is connected with controller;The cryoprecipitate tank is equipped with system
Cold, refrigeration machine are connect with controller;
It is equipped with the temperature sensor being connect with controller in the thermoprecipitation tank and cryoprecipitate tank.
2. a kind of automation edible oil settler as described in claim 1, which is characterized in that the thermoprecipitation tank and cold sink
It is covered with heat-barrier material outside the tank of shallow lake.
3. a kind of automation edible oil settler as described in claim 1, which is characterized in that the controller is microcontroller
Controller.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721630503.2U CN207646166U (en) | 2017-11-29 | 2017-11-29 | A kind of automation edible oil settler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721630503.2U CN207646166U (en) | 2017-11-29 | 2017-11-29 | A kind of automation edible oil settler |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207646166U true CN207646166U (en) | 2018-07-24 |
Family
ID=62882149
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721630503.2U Expired - Fee Related CN207646166U (en) | 2017-11-29 | 2017-11-29 | A kind of automation edible oil settler |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207646166U (en) |
-
2017
- 2017-11-29 CN CN201721630503.2U patent/CN207646166U/en not_active Expired - Fee Related
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN207646166U (en) | A kind of automation edible oil settler | |
CN104292198B (en) | During maltol produces, grignard is hydrolyzed two-phase laminated flow synthetic method and device | |
CN203815884U (en) | Full automatic traditional black plaster coating forming machine | |
CN204032254U (en) | The bold and resolute sub-producing device of a kind of oil | |
CN205014734U (en) | Open cooling water circulation device | |
CN201650935U (en) | Circulatory flushing device of hydraulic system pipeline | |
CN204051648U (en) | The hot water temperature keeping device of reactor | |
CN207811706U (en) | A kind of automatic hydrating apparatus of edible oil | |
CN202688299U (en) | Low-temperature dehydration device for refined vegetable oil in hydration and salinization process | |
CN208120882U (en) | It is a kind of by increase pressure difference improve after recirculating cooling water system | |
CN207631852U (en) | A kind of lube base oil pre-heating system | |
CN106432596A (en) | Method for preparing water clarifier for light crude water of offshore platform | |
CN206652935U (en) | One kind penetrates wax machine | |
CN205340771U (en) | Oily conveyor of circulation heat of phosphate ester starch | |
CN204535191U (en) | A kind of self-loopa water-cooled constant temperature machine group | |
CN206620800U (en) | Leaching equipment is poured for soy sauce production | |
CN206518966U (en) | Biology enzyme separates special pumping and filtering device | |
CN205270729U (en) | Intelligent resin sand processing apparatus | |
CN204963603U (en) | Lubricating grease production heat conduction oil furnace system heat sink | |
CN109777522A (en) | Half negative pressure benzene removal device of coking of coal | |
CN204198641U (en) | Grignard hydrolysis two-phase laminated flow synthesizer in voitol production | |
CN201704306U (en) | Multi-layer deacidification tower | |
CN203939612U (en) | For the constant temperature hydraulic system of electrical control oil spray pump flow test stand | |
CN106944593A (en) | A kind of investment casting formwork water boils dewaxing duration control method | |
CN204447382U (en) | Novel grading type crystallizer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
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: 20180724 Termination date: 20181129 |