CN206843411U - A kind of camellia seed oil production process alkali refining device - Google Patents
A kind of camellia seed oil production process alkali refining device Download PDFInfo
- Publication number
- CN206843411U CN206843411U CN201720765045.7U CN201720765045U CN206843411U CN 206843411 U CN206843411 U CN 206843411U CN 201720765045 U CN201720765045 U CN 201720765045U CN 206843411 U CN206843411 U CN 206843411U
- Authority
- CN
- China
- Prior art keywords
- alkali refining
- alkali
- tank body
- oil
- refining tank
- 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
- Tea And Coffee (AREA)
Abstract
The utility model discloses a kind of camellia seed oil production process alkali refining device, including alkali lye casing, tea seed crude oil casing and the inertia gas tank with being connected at the top of alkali refining tank body respectively, alkali refining tank base is provided with heater, alkali refining tank body madial wall is provided with temperature sensor, the signal output part of temperature sensor is connected with the signal input part of controller, controller control connection heater, alkali refining tank base is connected with acid detection means and centrifuge respectively, and centrifuge is connected with camellia seed oil casing and saponification tank body.The utility model can accurately measure the acidity of liquid in tea seed crude oil alkali refining course of reaction, and then the alkali refining degree of Precise Control of Oil tea seed crude oil, and the temperature of liquid in energy Precise Control of Oil tea seed crude oil alkali refining course of reaction, so as to prevent that the composition of camellia seed oil in itself changes in tea seed crude oil alkali refining process.
Description
Technical field
It the utility model is related to oil alkali refining technical field, and in particular to a kind of camellia seed oil production process alkali refining device.
Background technology
At present, during vegetable oil refining, alkali refining process plays very important effect.After alkali refining, the trip in grease
It is neutralized from aliphatic acid and generates soap, the acid number of grease is also minimized.Existing alkali refining device has the following disadvantages：When adding alkali
Added manually by worker, safety problem be present；Stir uneven, and then saponification degree etc. can be influenceed.
Alkali refining reaction pot in the oil alkali refining device of prior art does not connect acid detection means, thus can not essence
The acidity of liquid in alkali refining reaction pot really is controlled, therefore is unable to the alkali refining degree of Precise Control of Oil fat；And prior art
Temperature sensor is not provided with alkali refining reaction pot in oil alkali refining device, thus can not accurately be controlled in alkali refining reaction pot
The temperature of liquid, when the temperature of alkali refining reaction pot is higher, not only the free fatty in grease can be neutralized by alkali and produce soap,
And grease can also react with alkali in itself, can thus change the composition of grease in itself.
In order to accurately measure the acidity of liquid in alkali refining course of reaction, and then the alkali refining degree of Precise Control of Oil fat, and
In order to accurately control the temperature of liquid in alkali refining course of reaction, so as to prevent that the composition of grease in itself occurs in oil alkali refining process
Change, is highly desirable to design a kind of camellia seed oil production process alkali refining device.
Utility model content
The utility model provides a kind of camellia seed oil production process alkali refining device, and it is anti-accurately to measure tea seed crude oil alkali refining
The acidity of liquid during answering, and then the alkali refining degree of Precise Control of Oil tea seed crude oil, and can Precise Control of Oil tea seed crude oil
The temperature of liquid in alkali refining course of reaction, so as to prevent that the composition of camellia seed oil in itself occurs in tea seed crude oil alkali refining process
Change.
In order to solve the above-mentioned technical problem, the utility model adopts the following technical scheme that：
A kind of camellia seed oil production process alkali refining device, including alkali refining tank body, alkali refining tank body top is by going deep into alkali refining tank
The alkali lye pipeline of body is connected with alkali lye bottom half, and the height of alkali lye bottom half is higher than the height at the top of alkali refining tank body, alkali
The lower end in liquid pipe road is connected with alkali lye shower nozzle multiple identical and in sustained height, alkali refining tank body top and alkali lye bottom half
Between alkali lye pipeline be provided with alkali lye valve；It is former by the inflow pipeline and tea seed that go deep into alkali refining tank body at the top of alkali refining tank body
Oil box bottom is connected, and the height of tea seed crude oil bottom half is higher than the height at the top of alkali refining tank body, under inflow pipeline
End is connected with into oil nozzle, and the inflow pipeline between alkali refining tank body top and tea seed crude oil bottom half is provided with inlet valve
Door；It is connected at the top of alkali refining tank body by admission line with inertia gas tank, admission line is provided with air intake valve；In alkali refining tank body
Provided with agitator；Alkali refining tank base is provided with heater, and alkali refining tank body madial wall is provided with temperature sensor, temperature sensor
Signal output part is connected with the signal input part of controller, controller control connection heater；Alkali refining tank base is by treating
Inspection liquid pipe road is connected with acid detection means, and liquid pipe road to be checked is provided with fluid valve to be checked；Alkali refining tank base is by going out liquid
For pipeline with being connected at the top of centrifuge, drain pipe road is provided with liquid valve door, and centrifugation motor spindle passes through flowline and tea seed
It is connected at the top of oil box, the height for centrifuging motor spindle is higher than the height of camellia seed oil casing top, and flowline is provided with out
Fuel tap door, for centrifugation motor spindle by soap stock pipeline with being connected at the top of saponification tank body, the height for centrifuging motor spindle is higher than saponification tank
Height at the top of body, soap stock pipeline are provided with soap stock valve.
Further, the alkali lye shower nozzle has four, and four alkali lye shower nozzles are symmetricly set on the inside of alkali refining tank body.
Further, the alkali lye shower nozzle is alkali lye rotary-atomizing shower nozzle.
Further, it is described enter oil nozzle be on the axis of alkali refining tank body, and it is oil-feed rotary-atomizing to enter oil nozzle
Shower nozzle.
Further, the agitator includes being stirred by motor-driven agitating shaft and multiple identicals on agitating shaft
Blade is mixed, agitating shaft is on the axis of alkali refining tank body, and multiple stirrer paddles are symmetricly set on the left and right sides of agitating shaft.
Further, the motor is arranged at the lower section of alkali refining tank body.
Further, the temperature sensor is thermocouple.
The course of work of the present utility model is：Air intake valve is opened, inert gas is entered by admission line from inertia gas tank
Enter alkali refining tank body and take a breath, it is inert gas to make the gas in alkali refining tank body, is then shut off air intake valve；Open inlet valve
, the tea seed crude oil in tea seed crude oil casing enters inflow pipeline and sprayed into by entering oil nozzle in alkali refining tank body, then
Close oil inlet valve and open heater, when the temperature of tea seed crude oil in the alkali refining tank body shown on controller reaches suitable
During temperature, heater is controlled, heater is no longer heated to alkali refining tank body and alkali refining tank body is incubated；Then alkali lye is opened
Valve, the alkali lye in alkali lye casing enter alkali lye pipeline and sprayed into by alkali lye shower nozzle in alkali refining tank body, are then shut off alkali lye valve
Door simultaneously opens motor, and agitator stirs the tea seed crude oil in alkali refining tank body with alkali lye, when tea seed crude oil and alkali lye
After reacting a period of time, fluid valve to be checked is opened, the mixing liquid in alkali refining tank body passes through liquid pipe road to be checked and enters acid detect
In device, fluid valve to be checked is then shut off, when the acidity for the mixing liquid that detection is drawn reaches appropriate acid, closes motor,
Agitator stops stirring, and opens liquid valve door, and the soap stock liquid in alkali refining tank body is entered in centrifuge by drain pipe road, centrifugation
Soap stock liquid is centrifuged and obtains camellia seed oil and soap stock by machine, opens fuel-displaced valve, and camellia seed oil enters oil tea by flowline
Seed oil box, opens soap stock valve, and soap stock enters saponification tank body by soap stock pipeline.
Relative to prior art, the beneficial effects of the utility model are：
Alkali refining tank base is connected by liquid pipe road to be checked with acid detection means in the utility model, when tea seed is former
Oil and alkaline reaction for a period of time after, open fluid valve to be checked, the mixing liquid in alkali refining tank body is entered by liquid pipe road to be checked
In acid detection means, acid detection means can accurately measure the acidity of mixing liquid in alkali refining tank body, and then can accurately control
The alkali refining degree of tea seed crude oil；Alkali refining tank body madial wall is provided with temperature sensor in the utility model, can Precise Control of Oil tea
The temperature of liquid in seed crude oil alkali refining course of reaction, so as to prevent camellia seed oil in tea seed crude oil alkali refining process in itself into
Divide and change；It is connected in the utility model at the top of alkali refining tank body by admission line with inertia gas tank, can thus makes alkali
Mixing liquid in refining tank body is isolated with air；The height of alkali lye bottom half is higher than at the top of alkali refining tank body in the utility model
Height, and the height of tea seed crude oil bottom half is higher than the height at the top of alkali refining tank body, alkali lye and the equal energy of tea seed crude oil
Smoothly enter by the gravity of itself in alkali refining tank body, the height that motor spindle is centrifuged in the utility model is higher than camellia seed oil casing
The height at top, and the height of centrifugation motor spindle can rely on certainly higher than the height at the top of saponification tank body, camellia seed oil with soap stock
The gravity of body smoothly enters in camellia seed oil casing and saponification tank body respectively, so there is no need to special pump to alkali lye, oil tea
Seed crude oil, camellia seed oil and soap stock are pumped, therefore energy consumption is low.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
In order that the utility model purpose, technical scheme and advantage are clearer, below in conjunction with the accompanying drawings to the utility model
It is described in further detail.
The utility model includes alkali refining tank body 1, and the top of alkali refining tank body 1 is by going deep into the alkali lye pipeline 2 and alkali of alkali refining tank body 1
The bottom of liquid case body 3 is connected, and the height of the bottom of alkali lye casing 3 is higher than the height at the top of alkali refining tank body 1, the lower end of alkali lye pipeline 2
Alkali lye shower nozzle 4 multiple identical and in sustained height is connected with, the alkali lye shower nozzle 4 there are four, and four alkali lye shower nozzles 4 are symmetrical
The inside of alkali refining tank body 1 is arranged on, and alkali lye shower nozzle 4 is alkali lye rotary-atomizing shower nozzle, the top of alkali refining tank body 1 and alkali lye casing 3
Alkali lye pipeline 2 between bottom is provided with alkali lye valve 5；The top of alkali refining tank body 1 is by going deep into the inflow pipeline 6 of alkali refining tank body 1
It is connected with the bottom of tea seed crude oil casing 7, the height of the bottom of tea seed crude oil casing 7 is higher than the height at the top of alkali refining tank body 1,
The lower end of inflow pipeline 6 is connected with into oil nozzle 8, it is described enter oil nozzle 8 be on the axis of alkali refining tank body 1, and oil-feed is sprayed
First 8 be oil-feed rotary-atomizing shower nozzle, and the inflow pipeline 6 between the top of alkali refining tank body 1 and the bottom of tea seed crude oil casing 7 is provided with
Oil inlet valve 9；The top of alkali refining tank body 1 is connected by admission line 10 with inertia gas tank 11, and admission line 10 is provided with air inlet
Valve 12；Agitator 13 is provided with alkali refining tank body 1；The bottom of alkali refining tank body 1 is provided with heater 14, and the madial wall of alkali refining tank body 1 is set
There is temperature sensor（Thermocouple）15, the signal output part and controller of temperature sensor 15（Do not shown in figure）Signal input
End is connected, controller control connection heater 14；The bottom of alkali refining tank body 1 passes through liquid pipe road 16 to be checked and acid detection means 17
It is connected, liquid pipe road 16 to be checked is provided with fluid valve 18 to be checked；Pushed up by drain pipe road 19 and centrifuge 20 bottom of alkali refining tank body 1
Portion is connected, and drain pipe road 19 is provided with liquid valve door 21, and the bottom of centrifuge 20 passes through flowline 22 and camellia seed oil casing
23 tops are connected, and the height of the bottom of centrifuge 20 is provided with higher than the height at the top of camellia seed oil casing 23, flowline 22
Fuel-displaced valve 24, the bottom of centrifuge 20 are connected by soap stock pipeline 25 with the top of saponification tank body 26, the height of the bottom of centrifuge 20
Degree is provided with soap stock valve 27 higher than the height at the top of saponification tank body 26, soap stock pipeline 25.
Wherein, the agitator 13 includes multiple identical with agitating shaft 29 by the agitating shaft 29 that motor 28 drives
Stirrer paddle 30, agitating shaft 29 is on the axis of alkali refining tank body 1, and multiple stirrer paddles 30 are symmetricly set on agitating shaft 29
The left and right sides, so evenly, and motor 28 is arranged at the lower section of alkali refining tank body 1 for stirring.
The course of work of the present utility model is：Air intake valve 12 is opened, inert gas is by admission line 10 from indifferent gas
Tank 11 enters alkali refining tank body 1 and taken a breath, and it is inert gas to make the gas in alkali refining tank body 1, is then shut off air intake valve 12；Beat
Open oil inlet valve 9, the tea seed crude oil in tea seed crude oil casing 7 enters inflow pipeline 6 and sprays into alkali refining by entering oil nozzle 8
In tank body 1, it is then shut off oil inlet valve 9 and opens heater 14, when tea seed is former in the alkali refining tank body 1 shown on controller
When the temperature of oil reaches preference temperature, heater 14 is controlled, heater 14 is no longer heated and alkali refining tank body 1 to alkali refining
Tank body 1 is incubated；Then alkali lye valve 5 is opened, the alkali lye in alkali lye casing 3 enters alkali lye pipeline 2 and sprayed into by alkali lye shower nozzle 4
In alkali refining tank body 1, be then shut off alkali lye valve 5 and open motor 28, agitator 13 by the tea seed crude oil in alkali refining tank body 1 with
Alkali lye stirs, when tea seed crude oil and alkaline reaction for a period of time after, fluid valve 18 to be checked is opened, in alkali refining tank body 1
Mixing liquid is entered in acid detection means 17 by liquid pipe road 16 to be checked, fluid valve 18 to be checked is then shut off, when detection is drawn
The acidity of mixing liquid when reaching appropriate acid, close motor 28, agitator 13 stops stirring, and opens liquid valve door 21,
Soap stock liquid in alkali refining tank body 1 is entered in centrifuge 20 by drain pipe road 19, and soap stock liquid is centrifuged and obtains oil by centrifuge 20
Tea-seed oil and soap stock, fuel-displaced valve 24 is opened, camellia seed oil enters camellia seed oil casing 23 by flowline 22, opens soap stock
Valve 27, soap stock enter saponification tank body 26 by soap stock pipeline 25.
Above-described is only preferred embodiment of the present utility model, it is noted that for those skilled in the art
For, under the premise of the utility model general idea is not departed from, some changes and improvements can also be made, these should also be considered as
The scope of protection of the utility model.
Claims (7)
- A kind of 1. camellia seed oil production process alkali refining device, it is characterised in that：Including alkali refining tank body, pass through depth at the top of alkali refining tank body The alkali lye pipeline for entering alkali refining tank body is connected with alkali lye bottom half, and the height of alkali lye bottom half is higher than at the top of alkali refining tank body Highly, the lower end of alkali lye pipeline is connected with alkali lye shower nozzle multiple identical and in sustained height, alkali refining tank body top and alkali lye Alkali lye pipeline between bottom half is provided with alkali lye valve；At the top of alkali refining tank body by go deep into the inflow pipeline of alkali refining tank body with Tea seed crude oil bottom half is connected, and the height of tea seed crude oil bottom half is higher than the height at the top of alkali refining tank body, oil-feed The lower end of pipeline is connected with into oil nozzle, and the inflow pipeline between alkali refining tank body top and tea seed crude oil bottom half is provided with Oil inlet valve；It is connected at the top of alkali refining tank body by admission line with inertia gas tank, admission line is provided with air intake valve；Alkali refining Agitator is provided with tank body；Alkali refining tank base is provided with heater, and alkali refining tank body madial wall is provided with temperature sensor, and temperature passes The signal output part of sensor is connected with the signal input part of controller, controller control connection heater；Alkali refining tank base It is connected by liquid pipe road to be checked with acid detection means, liquid pipe road to be checked is provided with fluid valve to be checked；Alkali refining tank base is led to Cross at the top of drain pipe road and centrifuge and be connected, drain pipe road is provided with liquid valve door, centrifugation motor spindle by flowline and Camellia seed oil casing top is connected, and the height for centrifuging motor spindle is higher than the height of camellia seed oil casing top, on flowline Provided with fuel-displaced valve, by soap stock pipeline with being connected at the top of saponification tank body, the height for centrifuging motor spindle is higher than centrifugation motor spindle Height at the top of saponification tank body, soap stock pipeline are provided with soap stock valve.
- 2. camellia seed oil production process alkali refining device according to claim 1, it is characterised in that：The alkali lye shower nozzle has four It is individual, and four alkali lye shower nozzles are symmetricly set on the inside of alkali refining tank body.
- 3. camellia seed oil production process alkali refining device according to claim 1 or 2, it is characterised in that：The alkali lye shower nozzle For alkali lye rotary-atomizing shower nozzle.
- 4. camellia seed oil production process alkali refining device according to claim 2, it is characterised in that：It is described enter oil nozzle be in On the axis of alkali refining tank body, and it is oil-feed rotary-atomizing shower nozzle to enter oil nozzle.
- 5. camellia seed oil production process alkali refining device according to claim 1, it is characterised in that：The agitator include by Motor-driven agitating shaft is in the axis of alkali refining tank body with multiple identical stirrer paddles on agitating shaft, agitating shaft On, multiple stirrer paddles are symmetricly set on the left and right sides of agitating shaft.
- 6. camellia seed oil production process alkali refining device according to claim 5, it is characterised in that：The motor is arranged at alkali Refine the lower section of tank body.
- 7. camellia seed oil production process alkali refining device according to claim 1, it is characterised in that：The temperature sensor is Thermocouple.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720765045.7U CN206843411U (en) | 2017-06-28 | 2017-06-28 | A kind of camellia seed oil production process alkali refining device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720765045.7U CN206843411U (en) | 2017-06-28 | 2017-06-28 | A kind of camellia seed oil production process alkali refining device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206843411U true CN206843411U (en) | 2018-01-05 |
Family
ID=60802959
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720765045.7U Expired - Fee Related CN206843411U (en) | 2017-06-28 | 2017-06-28 | A kind of camellia seed oil production process alkali refining device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206843411U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110819448A (en) * | 2019-11-22 | 2020-02-21 | 湖南神农国油生态农业发展有限公司 | Oil tea seed oil production process alkali refining device |
-
2017
- 2017-06-28 CN CN201720765045.7U patent/CN206843411U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110819448A (en) * | 2019-11-22 | 2020-02-21 | 湖南神农国油生态农业发展有限公司 | Oil tea seed oil production process alkali refining device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101843988B (en) | Continuous extracting device | |
| CN204911329U (en) | Material mixing tank | |
| CN205007883U (en) | Fluid reservoir is joined in marriage to high efficiency | |
| CN203648423U (en) | Mixing tank | |
| CN205868097U (en) | Heating agitator tank of dedicated steerable temperature of honey processing | |
| CN206843411U (en) | A kind of camellia seed oil production process alkali refining device | |
| CN203828057U (en) | Tobacco sheet raw material digestion extraction tank | |
| CN211586620U (en) | Reation kettle system suitable for bio-resin is synthetic | |
| CN210473122U (en) | Automatic extraction element of compound red clothing tonifying blood oral liquid production | |
| CN208465735U (en) | A kind of hot type lubricating oil agitator tank | |
| CN206853514U (en) | Yoghourt Production agitating device | |
| CN202983560U (en) | Intermittent high shear emulsifying machine | |
| CN205676471U (en) | The large-scale anaerobic fermentation vertical plug-flow circulatory system | |
| CN215693956U (en) | Honey refining reaction kettle with temperature regulation function | |
| CN206549629U (en) | A kind of chemical reaction kettle | |
| CN203916531U (en) | A kind of constant-temperature paint agitating device | |
| CN205672901U (en) | A kind of stirring reaction unit producing fast red KD base | |
| CN204448012U (en) | Reactor | |
| CN205517710U (en) | Reation kettle is used in production of water -soluble organosilicon modified acrylic resin | |
| CN208599709U (en) | It is a kind of for producing the reaction kettle of anti-incrustation corrosion inhibitor | |
| CN107617410A (en) | Highly effective reaction device | |
| CN104162400B (en) | Washed reaction still and washed reaction method | |
| CN206244751U (en) | A kind of new alkali-refining pot | |
| CN207769784U (en) | A kind of highly effective reaction kettle | |
| CN205797064U (en) | A kind of double-stirring mixing tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180105 Termination date: 20200628 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |