CN208545390U - A kind of camellia oil cold press and molecular distillation equipment - Google Patents
A kind of camellia oil cold press and molecular distillation equipment Download PDFInfo
- Publication number
- CN208545390U CN208545390U CN201820984465.9U CN201820984465U CN208545390U CN 208545390 U CN208545390 U CN 208545390U CN 201820984465 U CN201820984465 U CN 201820984465U CN 208545390 U CN208545390 U CN 208545390U
- Authority
- CN
- China
- Prior art keywords
- cold pressing
- twin
- molecular distillation
- pressing expeller
- circulating water
- 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
Abstract
The utility model relates to a kind of camellia oil cold press and molecular distillation equipments, including the cold pressing expeller and molecular distillation tower being sequentially connected in series, the cold pressing expeller is twin-screw cold pressing expeller, the feed hopper of twin-screw cold pressing expeller is equipped with microwave treatment chamber, microwave treatment chamber is equipped with the first microwave generator, it is equipped with the second microwave generator in the press chamber of twin-screw cold pressing expeller, is equipped with cooling water coil outside the press chamber of twin-screw cold pressing expeller.This programme uses twin-screw squeezer, and microwave generator is equipped in the feed hopper of twin-screw squeezer and press chamber, can use microwave and destroys plant cell wall, improves cold press oil yield.
Description
Technical field
The utility model relates to a kind of camellia oil cold press and molecular distillation equipments, belong to tea oil technical field of processing equipment.
Background technique
Camellia oil also known as camellia seed oil are obtained from plant of theaceae tea oil tree seed, are the most ancient biographies in China
It unites one of woody edible vegetable oil, fatty acid composition is very much like with olive oil, and be otherwise known as " east olive oil ".Camellia oil
In also containing the various actives substance such as tea polysaccharide, tsubakisaponin, flavones, tea polyphenols, vitamin and phytosterol, frequent food utensil
Having reduces cholesterol, improves high-density lipoprotein, reduce low-density lipoprotein, reducing blood lipid, prevent cardiovascular and cerebrovascular disease, raising from exempting from
Epidemic disease power, anti-radiation, removing free radical, pre- preventing tumor and other effects, international food and agricultural organization has been classified as the health of emphasis popularization
Edible oil.
The acquisition technique of camellia oil crude oil, which uses extraction liquefaction substantially or steams, at present fries squeezing method, the refinery practice base of crude oil
This uses aquation degumming-alkali-refining deacidification-washing-filtering decoloration-high temperature circulation water deodorization-winterization degreasing-product oil.It is logical
It crosses high temperature and steams the albumen and immobilized artificial membrane fried and can destroy oil droplet outer layer, to improve oil yield, and extracting technology then will lead to finished product
Dissolvent residual in oil.Steam processing temperature generally at 100 DEG C~140 DEG C, frying processing temperature generally at 200 DEG C~300 DEG C, and
Using the chamber hall temperature of pressafiner squeezing generally at 200 DEG C~250 DEG C, above-mentioned process can generate carcinogenic substance benzo
(a) pyrene, while extraction and steaming and frying technique can make to improve acid value, so as to cause in oil there are a large amount of free fatty acids in oil
Peroxide largely generates.Chemical refining needs to add in lye and free fatty acid, high temperature deodorization and etc., finished product can be made
The nutrition contents such as vitamin content, phytosterol are down to extremely low in oil, have both destroyed the nutrition of camellia oil, alkali refining waste liquid
Discharge will lead to environmental pollution again.
The higher tea oil of quality can be obtained using cold pressing process, but that there are oil yields is low for cold press equipment in the prior art
The problem of.
Utility model content
The purpose of this utility model is to provide a kind of camellia oil cold press and molecular distillation equipments, the specific scheme is that
A kind of camellia oil cold press and molecular distillation equipment, it is described cold including the cold pressing expeller and molecular distillation tower being sequentially connected in series
Crusher is twin-screw cold pressing expeller, and the feed hopper of twin-screw cold pressing expeller is equipped with microwave treatment chamber, and microwave treatment chamber is equipped with the first microwave
Generator, the press chamber of twin-screw cold pressing expeller is interior to be equipped with the second microwave generator, is equipped with cooling outside the press chamber of twin-screw cold pressing expeller
Water coil.
Further, the heating plate of the molecular distillation tower is circulating water heating plate, and the circulating water heating plate is equipped with and follows
Ring water inlet and circulating water outlet, circulating water intake are connect with circulating water heater.
Further, the circulating water outlet of the circulating water heating plate and the water inlet of circulating water heater and cold pressing expeller
Cooling water coil connection.
Further, the microwave treatment chamber is the cylindrical cavity set on feed hopper lower part, and the bottom of cylindrical cavity is equipped with
Sluice gate, first microwave generator are set to the side of cylindrical cavity.
Further, second microwave generator has multiple, and between length direction of twin-screw cold pressing expeller press chamber etc.
Away from distribution.
The beneficial point of the utility model is: this programme uses twin-screw squeezer, and in the charging of twin-screw squeezer
It is equipped with microwave generator in bucket and press chamber, can use microwave and destroy plant cell wall, improve cold press oil yield.In addition, by
There is heating effect simultaneously in microwave treatment, cold pressing expeller can be cooled down, be prevented cold by the cooling water coil outside press chamber
Temperature is excessively high during squeezing.
This programme carries out distillation processing to pressed oil by matched molecular distillation tower, can remove free in pressed oil
The heating of fatty acid, molecular distillation tower is carried out using recirculated water.By the heat recovery to cold pressing expeller, it can also reduce recirculated water and add
The heat consumption of hot device.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Specific embodiment
A kind of camellia oil cold press as shown in Figure 1 and molecular distillation equipment, steam including the cold pressing expeller 1 being sequentially connected in series and molecule
Tower 2 is evaporated, the cold pressing expeller 1 is twin-screw cold pressing expeller, and the feed hopper 3 of twin-screw cold pressing expeller is equipped with microwave treatment chamber 4, microwave treatment
Chamber 4 is equipped with the first microwave generator 5, is equipped with the second microwave generator 6 in the press chamber of twin-screw cold pressing expeller, twin-screw cold pressing expeller
Cooling water coil 7 is equipped with outside press chamber.The heating plate of the molecular distillation 2 is circulating water heating plate 8, the circulating water heating plate
8 are equipped with circulating water intake and circulating water outlet, and circulating water intake is connect with circulating water heater 9.The circulating water heating plate 8
The water inlet of circulating water outlet and circulating water heater 9 is connect with the cooling water coil 7 of cold pressing expeller 1.The microwave treatment chamber 4 is
Cylindrical cavity set on 3 lower part of feed hopper, the bottom of cylindrical cavity are equipped with sluice gate 10, and first microwave generator 5 is set to cylinder
The side of shape cavity.Second microwave generator 6 have it is multiple, and along the equal spacing in length direction of twin-screw cold pressing expeller press chamber point
Cloth.
In the present embodiment, the other structures of twin-screw squeezer and molecular distillation tower are all made of routine in the art
Structure.The first microwave generator and the second microwave generator in the present embodiment equally use the installation of conventional microwave generator
Structure.The present embodiment focuses on setting position of the microwave generator on twin-screw squeezer, and by setting to press chamber
Set the heat recovery that cooling water coil carries out pressing temperature control and microwave treatment.
Claims (5)
1. a kind of camellia oil cold press and molecular distillation equipment exist including the cold pressing expeller being sequentially connected in series and molecular distillation tower, feature
In: the cold pressing expeller is twin-screw cold pressing expeller, and the feed hopper of twin-screw cold pressing expeller is equipped with microwave treatment chamber, and microwave treatment chamber is equipped with
First microwave generator, is equipped with the second microwave generator in the press chamber of twin-screw cold pressing expeller, outside the press chamber of twin-screw cold pressing expeller
Equipped with cooling water coil.
2. camellia oil cold press according to claim 1 and molecular distillation equipment, it is characterised in that: the molecular distillation tower
Heating plate be circulating water heating plate, the circulating water heating plate be equipped with circulating water intake and circulating water outlet, circulating water intake with
Circulating water heater connection.
3. camellia oil cold press according to claim 2 and molecular distillation equipment, it is characterised in that: the circulating water heating plate
Circulating water outlet and circulating water heater water inlet and cold pressing expeller cooling water coil connect.
4. camellia oil cold press according to claim 1 and molecular distillation equipment, it is characterised in that: the microwave treatment chamber is
Cylindrical cavity set on feed hopper lower part, the bottom of cylindrical cavity are equipped with sluice gate, and first microwave generator is set to cylindrical chamber
The side of body.
5. camellia oil cold press according to claim 1 and molecular distillation equipment, it is characterised in that: second microwave occurs
Device have it is multiple, and along the equal spacing in length direction of twin-screw cold pressing expeller press chamber be distributed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820984465.9U CN208545390U (en) | 2018-06-26 | 2018-06-26 | A kind of camellia oil cold press and molecular distillation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820984465.9U CN208545390U (en) | 2018-06-26 | 2018-06-26 | A kind of camellia oil cold press and molecular distillation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208545390U true CN208545390U (en) | 2019-02-26 |
Family
ID=65423405
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820984465.9U Expired - Fee Related CN208545390U (en) | 2018-06-26 | 2018-06-26 | A kind of camellia oil cold press and molecular distillation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208545390U (en) |
-
2018
- 2018-06-26 CN CN201820984465.9U patent/CN208545390U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102329690B (en) | Low-temperature cold-pressing and bivariate continuous refining and processing method for oiltea camellia seed oil | |
| CN102517141B (en) | Method for purely physically preparing camellia oil at low temperature | |
| CN101554211B (en) | Technique and industrial device for refining rice by supercritical polybasic fluid | |
| CN104109584B (en) | The liquefaction of tea-seed or tea seed and refining production method | |
| CN103289816A (en) | Tea oil processing method and device special for tea oil processing method | |
| CN102533426A (en) | Processing method for improving flavor and nutritional quality of colza oil | |
| CN100427576C (en) | Extraction of hickory nut oil from water enzyme | |
| CN103834463A (en) | Low temperature cold-pressing production technology for tea oil | |
| CN102757515B (en) | Method for extracting high-purity flavonoid and pectin from citrus peel | |
| CN104031736B (en) | A kind of preparation method of fructus cannabis oil of low tetrahydrocannabinol content | |
| CN103351944A (en) | Method for extracting grape seed oil by cold pressing | |
| CN107011988B (en) | A kind of coconut oil extraction process and its coconut oil | |
| CN104928018A (en) | Method for extracting tea-seed oil by microwave expansion assisted biological enzymolysis | |
| CN105685260A (en) | Nutritious health-care peony seed blend oil and preparing process thereof | |
| CN105707294A (en) | Refining method for snake gourd seed oil with stomach nourishing and yin replenishing effects | |
| CN104342282A (en) | Method for preparing functional grease and active protein powder from abelmoschus manilhot | |
| CN104987948A (en) | Improved freshness retaining squeezing method | |
| CN102191125B (en) | Process for preparing tussah pupa oil having the function of adjusting blood fat | |
| CN105132138A (en) | Processing technology for camellia seeds | |
| CN105419930A (en) | Method for extracting peanut oil and peanut butter through aqueous enzymatic method | |
| CN109294726A (en) | A kind of processing refinement method of rapeseed oil | |
| CN208545390U (en) | A kind of camellia oil cold press and molecular distillation equipment | |
| CN202430195U (en) | Dimethyl ether subcritical leaching tea-seed oil device | |
| CN203768325U (en) | Grease production line | |
| CN104095081B (en) | A kind of seed of Flos Moutan mixed oil of rich in vitamin E and preparation method thereof |
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: 20190226 Termination date: 20210626 |