CN108690713A - A kind of method of camellia seed kernel cold pressing production tea-seed oil - Google Patents
A kind of method of camellia seed kernel cold pressing production tea-seed oil Download PDFInfo
- Publication number
- CN108690713A CN108690713A CN201810778735.5A CN201810778735A CN108690713A CN 108690713 A CN108690713 A CN 108690713A CN 201810778735 A CN201810778735 A CN 201810778735A CN 108690713 A CN108690713 A CN 108690713A
- Authority
- CN
- China
- Prior art keywords
- tea
- camellia
- seed oil
- seed
- parts
- 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.)
- Pending
Links
- 239000010495 camellia oil Substances 0.000 title claims abstract description 78
- 235000018597 common camellia Nutrition 0.000 title claims abstract description 56
- 238000000034 method Methods 0.000 title claims abstract description 25
- 238000003825 pressing Methods 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 15
- 240000001548 Camellia japonica Species 0.000 title claims description 52
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 29
- 235000013399 edible fruits Nutrition 0.000 claims abstract description 21
- 241000526900 Camellia oleifera Species 0.000 claims abstract description 20
- 238000001914 filtration Methods 0.000 claims abstract description 17
- 238000001035 drying Methods 0.000 claims abstract description 13
- 239000003755 preservative agent Substances 0.000 claims abstract description 12
- 230000002335 preservative effect Effects 0.000 claims abstract description 12
- 241000209507 Camellia Species 0.000 claims abstract description 4
- 244000269722 Thea sinensis Species 0.000 claims description 39
- 235000013616 tea Nutrition 0.000 claims description 24
- 238000001816 cooling Methods 0.000 claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 21
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 20
- 239000003921 oil Substances 0.000 claims description 19
- 235000009569 green tea Nutrition 0.000 claims description 18
- 238000007654 immersion Methods 0.000 claims description 16
- 239000008367 deionised water Substances 0.000 claims description 12
- 229910021641 deionized water Inorganic materials 0.000 claims description 12
- 235000019441 ethanol Nutrition 0.000 claims description 10
- 239000002994 raw material Substances 0.000 claims description 10
- 229940094952 green tea extract Drugs 0.000 claims description 7
- 235000020688 green tea extract Nutrition 0.000 claims description 7
- 238000002360 preparation method Methods 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- CHHHXKFHOYLYRE-UHFFFAOYSA-M 2,4-Hexadienoic acid, potassium salt (1:1), (2E,4E)- Chemical compound [K+].CC=CC=CC([O-])=O CHHHXKFHOYLYRE-UHFFFAOYSA-M 0.000 claims description 5
- 229920002261 Corn starch Polymers 0.000 claims description 5
- 239000004287 Dehydroacetic acid Substances 0.000 claims description 5
- 235000009008 Eriobotrya japonica Nutrition 0.000 claims description 5
- PVNIIMVLHYAWGP-UHFFFAOYSA-N Niacin Chemical compound OC(=O)C1=CC=CN=C1 PVNIIMVLHYAWGP-UHFFFAOYSA-N 0.000 claims description 5
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 claims description 5
- BGNXCDMCOKJUMV-UHFFFAOYSA-N Tert-Butylhydroquinone Chemical compound CC(C)(C)C1=CC(O)=CC=C1O BGNXCDMCOKJUMV-UHFFFAOYSA-N 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 239000008120 corn starch Substances 0.000 claims description 5
- 229940099112 cornstarch Drugs 0.000 claims description 5
- 235000019258 dehydroacetic acid Nutrition 0.000 claims description 5
- JEQRBTDTEKWZBW-UHFFFAOYSA-N dehydroacetic acid Chemical compound CC(=O)C1=C(O)OC(C)=CC1=O JEQRBTDTEKWZBW-UHFFFAOYSA-N 0.000 claims description 5
- 229940061632 dehydroacetic acid Drugs 0.000 claims description 5
- PGRHXDWITVMQBC-UHFFFAOYSA-N dehydroacetic acid Natural products CC(=O)C1C(=O)OC(C)=CC1=O PGRHXDWITVMQBC-UHFFFAOYSA-N 0.000 claims description 5
- 235000012054 meals Nutrition 0.000 claims description 5
- 239000011259 mixed solution Substances 0.000 claims description 5
- 229960003512 nicotinic acid Drugs 0.000 claims description 5
- 235000001968 nicotinic acid Nutrition 0.000 claims description 5
- 239000011664 nicotinic acid Substances 0.000 claims description 5
- 239000004302 potassium sorbate Substances 0.000 claims description 5
- 235000010241 potassium sorbate Nutrition 0.000 claims description 5
- 229940069338 potassium sorbate Drugs 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 5
- 238000004064 recycling Methods 0.000 claims description 5
- 150000003839 salts Chemical class 0.000 claims description 5
- 239000001632 sodium acetate Substances 0.000 claims description 5
- 235000017281 sodium acetate Nutrition 0.000 claims description 5
- 239000004250 tert-Butylhydroquinone Substances 0.000 claims description 5
- 235000019281 tert-butylhydroquinone Nutrition 0.000 claims description 5
- 238000010792 warming Methods 0.000 claims description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 claims description 4
- 238000004042 decolorization Methods 0.000 claims description 4
- 235000013922 glutamic acid Nutrition 0.000 claims description 4
- 239000004220 glutamic acid Substances 0.000 claims description 4
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 244000061508 Eriobotrya japonica Species 0.000 claims 1
- PHYFQTYBJUILEZ-IUPFWZBJSA-N triolein Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(OC(=O)CCCCCCC\C=C/CCCCCCCC)COC(=O)CCCCCCC\C=C/CCCCCCCC PHYFQTYBJUILEZ-IUPFWZBJSA-N 0.000 claims 1
- 238000000605 extraction Methods 0.000 abstract description 7
- 229920006395 saturated elastomer Polymers 0.000 abstract description 6
- 239000012535 impurity Substances 0.000 abstract description 5
- 239000003960 organic solvent Substances 0.000 abstract description 3
- 235000012041 food component Nutrition 0.000 abstract description 2
- 235000019198 oils Nutrition 0.000 description 18
- 239000004615 ingredient Substances 0.000 description 6
- 235000015112 vegetable and seed oil Nutrition 0.000 description 6
- 235000016709 nutrition Nutrition 0.000 description 5
- 241001092070 Eriobotrya Species 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 125000001931 aliphatic group Chemical group 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 235000019197 fats Nutrition 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 235000018102 proteins Nutrition 0.000 description 3
- 102000004169 proteins and genes Human genes 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 238000004061 bleaching Methods 0.000 description 2
- HVYWMOMLDIMFJA-DPAQBDIFSA-N cholesterol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 HVYWMOMLDIMFJA-DPAQBDIFSA-N 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 2
- 235000008390 olive oil Nutrition 0.000 description 2
- 239000004006 olive oil Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 1
- FPIPGXGPPPQFEQ-UHFFFAOYSA-N 13-cis retinol Natural products OCC=C(C)C=CC=C(C)C=CC1=C(C)CCCC1(C)C FPIPGXGPPPQFEQ-UHFFFAOYSA-N 0.000 description 1
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 1
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 1
- 229930195730 Aflatoxin Natural products 0.000 description 1
- DPUOLQHDNGRHBS-UHFFFAOYSA-N Brassidinsaeure Natural products CCCCCCCCC=CCCCCCCCCCCCC(O)=O DPUOLQHDNGRHBS-UHFFFAOYSA-N 0.000 description 1
- 241000237942 Conidae Species 0.000 description 1
- 244000147058 Derris elliptica Species 0.000 description 1
- URXZXNYJPAJJOQ-UHFFFAOYSA-N Erucic acid Natural products CCCCCCC=CCCCCCCCCCCCC(O)=O URXZXNYJPAJJOQ-UHFFFAOYSA-N 0.000 description 1
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- 235000014443 Pyrus communis Nutrition 0.000 description 1
- 241001062811 Stewartia malacodendron Species 0.000 description 1
- FPIPGXGPPPQFEQ-BOOMUCAASA-N Vitamin A Natural products OC/C=C(/C)\C=C\C=C(\C)/C=C/C1=C(C)CCCC1(C)C FPIPGXGPPPQFEQ-BOOMUCAASA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000005409 aflatoxin Substances 0.000 description 1
- FPIPGXGPPPQFEQ-OVSJKPMPSA-N all-trans-retinol Chemical compound OC\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)CCCC1(C)C FPIPGXGPPPQFEQ-OVSJKPMPSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000003115 biocidal effect Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 230000036772 blood pressure Effects 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 235000012000 cholesterol Nutrition 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 230000002526 effect on cardiovascular system Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- DPUOLQHDNGRHBS-KTKRTIGZSA-N erucic acid Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(O)=O DPUOLQHDNGRHBS-KTKRTIGZSA-N 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 235000003642 hunger Nutrition 0.000 description 1
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 1
- 150000002617 leukotrienes Chemical class 0.000 description 1
- 235000020778 linoleic acid Nutrition 0.000 description 1
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 210000001161 mammalian embryo Anatomy 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 1
- 230000001151 other effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 235000019871 vegetable fat Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 235000019155 vitamin A Nutrition 0.000 description 1
- 239000011719 vitamin A Substances 0.000 description 1
- 229940045997 vitamin a Drugs 0.000 description 1
- 150000003722 vitamin derivatives Chemical class 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/06—Production of fats or fatty oils from raw materials by pressing
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/02—Pretreatment
- C11B1/04—Pretreatment of vegetable raw material
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Medicines Containing Plant Substances (AREA)
- Edible Oils And Fats (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
Abstract
The invention discloses a kind of methods that camellia seed kernel cold pressing produces tea-seed oil, are related to tea-seed oil production field;Fresh camellia oleifera fruit is coated with preservative film, saturated vapour pressure processing is put into, then shells, camellia seed kernel is immersed in inorganic agent, with being stirred by slow fire after drying, impregnated again with inorganic agent after stir-frying, finally use squeezer cold press fuel-displaced, after refined filtration, tea-seed oil is made;Organic solvent extract need not be added in extraction process, also high temperature need not be utilized to squeeze, tea-seed oil is squeezed out under conditions of low temperature is additive-free, the multiple nutritional components for remaining tea-seed oil are not destroyed, and tea-seed oil purity is high, yield is high, no objectionable impurities generates.
Description
Technical field:
The present invention relates to tea-seed oil production fields, and in particular to a kind of side of camellia seed kernel cold pressing production tea-seed oil
Method.
Background technology:
Tea-seed oil also known as camellia oil, tea pear oil, Wild camellia seed oil, camellia seed oil, tea oil seeds of trees oil.Camellia is Chinese big other
The ground specialty such as mountain, Fujian, Jiangxi, Hunan (Changning) can extract good camellia oil, i.e. tea-seed oil in fruit.Method one:Pressure
It squeezes.It is derived from the seed of tea oil tree.The manufacturing process of tea-seed oil can be divided into:Oil expression, filtering.Method two:Subcritical abstraction.It is subcritical
Low-temperature extraction technology is tea seed decladding, crushes, rolls embryo, subcritical low-temperature extraction, and finished product tea-seed oil is obtained after oil and fat refining.
Erucic acid, cholesterol, aflatoxins and other additives are free of in camellia seed oil.After tested:Insatiable hunger in camellia seed oil
Be up to 90% or more with aliphatic acid, oleic acid reaches 80-83%, and linoleic acid reaches 7-13%, and rich in protein and vitamin A,
B, D, E etc., the especially abundant leukotrienes contained by it are needed by human and cannot synthesize.The effect tea oil of camellia seed oil
It is the distinctive woody grease in China, aliphatic acid composition is similar to the best vegetable fat olive oil generally acknowledged in the world, there is " east
The laudatory title of square olive oil " contains several functions composition in tea oil, is eaten for a long time, and has the hardening of apparent prevention of cardiovascular, drop
The special efficacy of blood pressure, reducing blood lipid and other effects and cancer-resisting.
Currently, the preparation method that China produces camellia seed oil mainly has machinery pressure hot moulding method and solvent extraction method, squeezing method
Equipment is more, and fat residue rate is high, and conventional high-temperature hot moulding tea oil is easy that vitamin isoreactivity substance is made to be destroyed.Lixiviation process
Using 6# solvents, although having at low cost, the high advantage of oil yield, there are security risks for organic solvent, and the solvent discharged
Gas is unfriendly to environment.Therefore, how to research and develop and new squeeze technique so that can be effectively retained on the basis of additive-free
The nutritional ingredient of tea-seed oil, the problem of becoming urgent need to resolve.
Invention content:
Technical problem to be solved by the present invention lies in a kind of method for providing camellia seed kernel cold pressing and producing tea-seed oil,
Organic solvent extract need not be added in extraction process, need not also high temperature be utilized to squeeze, in the additive-free item of low temperature
Tea-seed oil is squeezed out under part, the multiple nutritional components for remaining tea-seed oil are not destroyed, and tea-seed oil purity is high, yield is high, nothing
Objectionable impurities generates.
The technical problems to be solved by the invention are realized using technical solution below:
A kind of method of camellia seed kernel cold pressing production tea-seed oil, includes the following steps:
(1) fresh camellia oleifera fruit is picked, one layer of preservative film is coated on camellia oleifera fruit surface, camellia oleifera fruit is put into 70 DEG C of vapor
60-90min is handled in saturated vapour pressure, naturally dry after cooling removes preservative film;
(2) tea seed after drying, which is sent into hulling machine, to shell, then is detached camellia seed kernel and shell with winnowing machine,
Collect camellia seed kernel;
(3) camellia seed kernel is immersed in inorganic agent the immersion 3-4h at 35-45 DEG C, 3-5 is cleaned with deionized water after immersion
It is secondary, it is put into curer and is dried at 55-65 DEG C;
(4) camellia seed kernel after drying is put into pot with being stirred by slow fire, camellia seed kernel quality is added during stir-frying
0.05% salt, stir-fry 3-5min, natural cooling;
(5) camellia seed kernel after cooling that will stir-fry crushes, and crosses 10 mesh sieve, is placed again into inorganic agent and is impregnated at 35-45 DEG C
120-150min is cleaned 3-5 times after immersion with deionized water, is put into curer and is dried at 55-65 DEG C;
(6) treated camellia seed kernel is sent into progress cold press in squeezer and obtains oil meal and thick tea-seed oil, it will be thick
Tea-seed oil is made in tea-seed oil refined filtration.
The inorganic agent is made of the raw material of following parts by weight:12-16 parts of potassium sorbate, 8-10 parts of cornstarch, paddy ammonia
6-8 parts sour, 18-22 parts of loquat dew, 14-16 parts of sodium acetate, 22-26 parts of green tea, 3-5 parts of niacin, tert-butylhydroquinone 9-
12 parts, 15-20 parts of dehydroacetic acid, 300-350 parts of deionized water.
The preparation method of the inorganic agent is:
(1) green tea is added to the water, is put into 3-5 DEG C of environment and handles 20-30min, after being warming up to room temperature, filtered, it is dry,
It is added in the ethyl alcohol of 12-15 times of green tea weight, flow back 40-50min at 82-85 DEG C, centrifugal filtration, and recycling ethyl alcohol is concentrated under reduced pressure,
Green-tea extract is made;
(2) green-tea extract and other raw materials are mixed, 20- is stirred under 80-90 DEG C, 200-300r/min rotating speeds
30min;
(3) above-mentioned mixed solution is put into reaction kettle, 2-2.5h is handled at 60-80 DEG C, ultra violet lamp is used after cooling
Inorganic agent is made in 5-8min.
Further include decoloration process after the step (6):Tea-seed oil after refined filtration is subjected to decolorization with medicinal carbon,
Tea-seed oil after decoloration is put into nitrogen environment in 120-160 DEG C of isothermal holding 20-30min, Temperature fall to room temperature.
The present invention provides a kind of method that camellia seed kernel cold pressing produces tea-seed oil, advantage is:
(1) fresh camellia oleifera fruit is covered with preservative film, is put into 70 DEG C of saturated vapour pressures and handles, camellia oleifera fruit can be accelerated
Curing keeps the nutriment in camellia oleifera fruit more abundant, while can reduce the aliphatic acid saturation degree of tea-seed oil in camellia oleifera fruit, will
Tea seed kernel is immersed in inorganic agent and handles, and can soften tea seed kernel, while the nutritional ingredient for retaining tea seed kernel is not destroyed, softening
Afterwards by stir-frying, tea seed oil component is made to be precipitated in advance, is progressively disengaged with other ingredients such as protein inside tea seed kernel, powder after stir-frying
It is broken, it impregnates again, other ingredients such as oil component and protein is made thoroughly to be detached from, be conducive to carry in postorder low-temperature cold pressing technical process
Height squeezes rate, improves the purity of tea-seed oil, and does not destroy the nutritional ingredient of tea-seed oil, and the tea-seed oil of preparation is full of nutrition, production
Amount is high, purity is high, no objectionable impurities.
(2) inorganic agent selects special formulation, is not only safe from harm to tea seed kernel, but also can promote the precipitation of oil, together
When ensure tea-seed oil nutritional ingredient be not destroyed.
(3) the medicinal activated carbon decolorizing of tea-seed oil is handled and is put into isothermal holding in nitrogen nitrogen environment, it can not only be right
Tea-seed oil plays the purpose of decoloration, removal of impurities, moreover it is possible to which stability, the antibiotic property for enhancing tea-seed oil extend the shelf-life of tea-seed oil.
Specific implementation mode:
In order to make the technical means, the creative features, the aims and the efficiencies achieved by the present invention be easy to understand, tie below
Specific embodiment is closed, the present invention is further explained.
Embodiment 1:
A kind of method of camellia seed kernel cold pressing production tea-seed oil, includes the following steps:
(1) fresh camellia oleifera fruit is picked, one layer of preservative film is coated on camellia oleifera fruit surface, camellia oleifera fruit is put into 70 DEG C of vapor
60min is handled in saturated vapour pressure, naturally dry after cooling removes preservative film;
(2) tea seed after drying, which is sent into hulling machine, to shell, then is detached camellia seed kernel and shell with winnowing machine,
Collect camellia seed kernel;
(3) camellia seed kernel is immersed in inorganic agent the immersion 3h at 35 DEG C, is cleaned 3 times, is put into deionized water after immersion
It is dried at 55 DEG C in curer;
(4) camellia seed kernel after drying is put into pot with being stirred by slow fire, camellia seed kernel quality is added during stir-frying
0.05% salt, stir-fry 3min, natural cooling;
(5) camellia seed kernel after cooling that will stir-fry crushes, and crosses 10 mesh sieve, is placed again into inorganic agent and is impregnated at 35 DEG C
120min is cleaned 3 times after immersion with deionized water, is put into curer and is dried at 55 DEG C;
(6) treated camellia seed kernel is sent into progress cold press in squeezer and obtains oil meal and thick tea-seed oil, it will be thick
Tea-seed oil is made in tea-seed oil refined filtration.
The inorganic agent is made of the raw material of following parts by weight:12 parts of potassium sorbate, 8 parts of cornstarch, 6 parts of glutamic acid,
18 parts of loquat dew, 14 parts of sodium acetate, 22 parts of green tea, 3 parts of niacin, 9 parts of tert-butylhydroquinone, 15 parts of dehydroacetic acid, go from
300 parts of sub- water.
The preparation method of the inorganic agent is:
(1) green tea is added to the water, is put into 3 DEG C of environment and handles 20-30min, after being warming up to room temperature, filtered, it is dry, add
In the ethyl alcohol for entering 12 times of green tea weight, flow back 40min at 82 DEG C, centrifugal filtration, and recycling ethyl alcohol is concentrated under reduced pressure, and green tea extraction is made
Object;
(2) green-tea extract and other raw materials are mixed, 20min is stirred under 80 DEG C, 200r/min rotating speeds;
(3) above-mentioned mixed solution is put into reaction kettle, 2h is handled at 60 DEG C, ultra violet lamp 5min, system are used after cooling
Obtain inorganic agent.
Embodiment 2:
A kind of method of camellia seed kernel cold pressing production tea-seed oil, includes the following steps:
(1) fresh camellia oleifera fruit is picked, one layer of preservative film is coated on camellia oleifera fruit surface, camellia oleifera fruit is put into 70 DEG C of vapor
90min is handled in saturated vapour pressure, naturally dry after cooling removes preservative film;
(2) tea seed after drying, which is sent into hulling machine, to shell, then is detached camellia seed kernel and shell with winnowing machine,
Collect camellia seed kernel;
(3) camellia seed kernel is immersed in inorganic agent the immersion 4h at 45 DEG C, is cleaned 5 times, is put into deionized water after immersion
It is dried at 65 DEG C in curer;
(4) camellia seed kernel after drying is put into pot with being stirred by slow fire, camellia seed kernel quality is added during stir-frying
0.05% salt, stir-fry 5min, natural cooling;
(5) camellia seed kernel after cooling that will stir-fry crushes, and crosses 10 mesh sieve, is placed again into inorganic agent and is impregnated at 45 DEG C
150min is cleaned 5 times after immersion with deionized water, is put into curer and is dried at 65 DEG C;
(6) treated camellia seed kernel is sent into progress cold press in squeezer and obtains oil meal and thick tea-seed oil, it will be thick
Tea-seed oil is made in tea-seed oil refined filtration;
(7) tea-seed oil after refined filtration is subjected to decolorization with medicinal carbon, the tea-seed oil after decoloration is put into nitrogen ring
In 160 DEG C of isothermal holding 30min, Temperature fall to room temperature in border.
The inorganic agent is made of the raw material of following parts by weight:16 parts of potassium sorbate, 10 parts of cornstarch, 8 parts of glutamic acid,
22 parts of loquat dew, 16 parts of sodium acetate, 26 parts of green tea, 5 parts of niacin, 12 parts of tert-butylhydroquinone, 20 parts of dehydroacetic acid, go from
350 parts of sub- water.
The preparation method of the inorganic agent is:
(1) green tea is added to the water, is put into 5 DEG C of environment and handles 30min, after being warming up to room temperature, filtered, it is dry, it is added
In the ethyl alcohol that 15 times of green tea weight, flow back 50min at 85 DEG C, centrifugal filtration, and recycling ethyl alcohol is concentrated under reduced pressure, and green tea extraction is made
Object;
(2) green-tea extract and other raw materials are mixed, 30min is stirred under 90 DEG C, 300r/min rotating speeds;
(3) above-mentioned mixed solution is put into reaction kettle, 2.5h is handled at 80 DEG C, ultra violet lamp 8min is used after cooling,
Inorganic agent is made.
Embodiment 3:
A kind of method of camellia seed kernel cold pressing production tea-seed oil, includes the following steps:
(1) fresh camellia oleifera fruit is picked, one layer of preservative film is coated on camellia oleifera fruit surface, camellia oleifera fruit is put into 70 DEG C of vapor
80min is handled in saturated vapour pressure, naturally dry after cooling removes preservative film;
(2) tea seed after drying, which is sent into hulling machine, to shell, then is detached camellia seed kernel and shell with winnowing machine,
Collect camellia seed kernel;
(3) camellia seed kernel is immersed in inorganic agent the immersion 3h at 40 DEG C, is cleaned 4 times, is put into deionized water after immersion
It is dried at 60 DEG C in curer;
(4) camellia seed kernel after drying is put into pot with being stirred by slow fire, camellia seed kernel quality is added during stir-frying
0.05% salt, stir-fry 4min, natural cooling;
(5) camellia seed kernel after cooling that will stir-fry crushes, and crosses 10 mesh sieve, is placed again into inorganic agent and is impregnated at 40 DEG C
130min is cleaned 4 times after immersion with deionized water, is put into curer and is dried at 60 DEG C;
(6) treated camellia seed kernel is sent into progress cold press in squeezer and obtains oil meal and thick tea-seed oil, it will be thick
Tea-seed oil is made in tea-seed oil refined filtration;
(7) tea-seed oil after refined filtration is subjected to decolorization with medicinal carbon, the tea-seed oil after decoloration is put into nitrogen ring
In 120 DEG C of isothermal holding 20min, Temperature fall to room temperature in border.
The inorganic agent is made of the raw material of following parts by weight:14 parts of potassium sorbate, 9 parts of cornstarch, 7 parts of glutamic acid,
20 parts of loquat dew, 15 parts of sodium acetate, 24 parts of green tea, 4 parts of niacin, 10 parts of tert-butylhydroquinone, 18 parts of dehydroacetic acid, go from
320 parts of sub- water.
The preparation method of the inorganic agent is:
(1) green tea is added to the water, is put into 4 DEG C of environment and handles 25min, after being warming up to room temperature, filtered, it is dry, it is added
In the ethyl alcohol that 13 times of green tea weight, flow back 45min at 85 DEG C, centrifugal filtration, and recycling ethyl alcohol is concentrated under reduced pressure, and green tea extraction is made
Object;
(2) green-tea extract and other raw materials are mixed, 25min is stirred under 85 DEG C, 250r/min rotating speeds;
(3) above-mentioned mixed solution is put into reaction kettle, 2h is handled at 70 DEG C, ultra violet lamp 7min, system are used after cooling
Obtain inorganic agent.
Comparative example:
Refine cold press tea-seed oil
Oil tea cone is harvested, threshing ground drying is dry, manually removes cone shell, and tea seed is placed in low temperature in 5 DEG C of freezer
Storage 25 days.The impurity such as rubble, weeds to clean in grader removal tea seed obtain the uniform pure nothing of size and go mouldy oil tea
Seed.Hulling machine combination pneumatic jig carries out shelling and separation of hull from kernel to tea seed, and it is suitable so that shelling rate is reached 20%.By decladding
20kg tea seeds are placed in 60 DEG C of baking ovens and are dried, and are taken out after tea seed is dried to moisture 8% and carry out precrushing processing.It adopts
The tea seed after drying is crushed with double-roll crusher, control degree of fragmentation to 1/4~1/8 valve of tea seed.By broken oil
Tea seed is put into cold pressing machine, and setup parameter pressing temperature is 65 DEG C, rotating speed 30r/min, press chamber pressure 3.5MPa;It is squeezed
Crude oil.Crude oil is first passed through natural filter cloth removal part filter residue uses filter opening for 60,80,100 mesh specifications then at 10 DEG C
Filter by above-mentioned coarse tea oil carry out multi-filtering, obtain cold press tea oil.Filtered cold press tea oil will be refined in time
50kg cold press tea oil is placed in the inorganic ceramic membrane separation plant that molecular cut off is 20,000 and carries out degumming process, degumming by processing
Temperature is 40 DEG C, operating pressure 0.4MPa, usually time 1.5h, and degumming caudacoria will be cleaned in time.Tea after degumming
4% atlapulgite is added in oil, tea oil is placed in vacuum decoloration tower, bleaching temperature is 80 DEG C, and bleaching time 30min is filtered
The tea oil substantially colorless to appearance.Under the vacuum degree of 0.1MPa, when Colorless Camellia Oil is heated to 140 DEG C, it is passed through a small amount of water and steams
Gas is continuously heating to 180 DEG C, and constant temperature distills 1h, stops heating, and cooling, when temperature drops to 50 DEG C, vacuum breaker takes out oil,
Filter to obtain deodorised oil.Deodorization tea oil gas force feed is entered into freezing and crystallizing tank, so that oil is cooled to 6 DEG C, 8h, hydraulic filtering is kept to go
Except crystalline solid fat, the refined tea oil of clear is obtained.
The tea-seed oil purity and yield prepared to the above various embodiments and comparative example counts, as a result as follows:
Purity (%) | Yield (kg/100kg) | Unsaturated fatty acid content (%) | |
Embodiment 1 | 99.8 | 42.5 | 93 |
Embodiment 2 | 99.8 | 42.5 | 93 |
Embodiment 3 | 99.9 | 42.6 | 93 |
Comparative example | 98.2 | 32.8 | 90 |
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this
The principle of invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its
Equivalent thereof.
Claims (4)
1. a kind of method of camellia seed kernel cold pressing production tea-seed oil, which is characterized in that include the following steps:
(1) fresh camellia oleifera fruit is picked, one layer of preservative film is coated on camellia oleifera fruit surface, camellia oleifera fruit is put into 70 DEG C of steam-ladens
60-90min is handled in vapour pressure, naturally dry after cooling removes preservative film;
(2) tea seed after drying, which is sent into hulling machine, to shell, then is detached camellia seed kernel and shell with winnowing machine, collects
Camellia seed kernel;
(3) camellia seed kernel is immersed in inorganic agent the immersion 3-4h at 35-45 DEG C, is cleaned 3-5 times, is put with deionized water after immersion
Enter in curer and is dried at 55-65 DEG C;
(4) camellia seed kernel after drying is put into pot with being stirred by slow fire, camellia seed kernel quality is added during stir-frying
0.05% salt, stir-fry 3-5min, natural cooling;
(5) camellia seed kernel after cooling that will stir-fry crushes, and crosses 10 mesh sieve, is placed again into inorganic agent the immersion 120- at 35-45 DEG C
150min is cleaned 3-5 times after immersion with deionized water, is put into curer and is dried at 55-65 DEG C;
(6) treated camellia seed kernel is sent into progress cold press in squeezer and obtains oil meal and thick tea-seed oil, by thick tea seed
Olein is filtered, and tea-seed oil is made.
2. the method for camellia seed kernel cold pressing production tea-seed oil according to claim 1, which is characterized in that the processing
Agent is made of the raw material of following parts by weight:12-16 parts of potassium sorbate, 8-10 parts of cornstarch, 6-8 parts of glutamic acid, loquat dew 18-
22 parts, 14-16 parts of sodium acetate, 22-26 parts of green tea, 3-5 parts of niacin, 9-12 parts of tert-butylhydroquinone, dehydroacetic acid 15-20
Part, 300-350 parts of deionized water.
3. the method for camellia seed kernel cold pressing production tea-seed oil according to claim 2, which is characterized in that the processing
The preparation method of agent is:
(1) green tea is added to the water, is put into 3-5 DEG C of environment and handles 20-30min, after being warming up to room temperature, filtered, it is dry, it is added
In the ethyl alcohol of 12-15 times of green tea weight, flow back 40-50min at 82-85 DEG C, centrifugal filtration, and recycling ethyl alcohol is concentrated under reduced pressure, is made
Green-tea extract;
(2) green-tea extract and other raw materials are mixed, 20-30min is stirred under 80-90 DEG C, 200-300r/min rotating speeds;
(3) above-mentioned mixed solution is put into reaction kettle, 2-2.5h is handled at 60-80 DEG C, ultra violet lamp 5- is used after cooling
Inorganic agent is made in 8min.
4. the method for camellia seed kernel cold pressing production tea-seed oil according to claim 1, which is characterized in that the step
(6) further include decoloration process after:Tea-seed oil after refined filtration is subjected to decolorization with medicinal carbon, the tea-seed oil after decoloration is put
Enter in nitrogen environment in 120-160 DEG C of isothermal holding 20-30min, Temperature fall to room temperature.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810778735.5A CN108690713A (en) | 2018-07-16 | 2018-07-16 | A kind of method of camellia seed kernel cold pressing production tea-seed oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810778735.5A CN108690713A (en) | 2018-07-16 | 2018-07-16 | A kind of method of camellia seed kernel cold pressing production tea-seed oil |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108690713A true CN108690713A (en) | 2018-10-23 |
Family
ID=63851598
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810778735.5A Pending CN108690713A (en) | 2018-07-16 | 2018-07-16 | A kind of method of camellia seed kernel cold pressing production tea-seed oil |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108690713A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109943408A (en) * | 2019-04-10 | 2019-06-28 | 中国热带农业科学院农产品加工研究所 | A kind of oil tea seed kernel stripping method |
CN110819438A (en) * | 2019-11-29 | 2020-02-21 | 湖南杨家将茶油股份有限公司 | Preparation method of tea seed oil |
CN116144421A (en) * | 2022-09-05 | 2023-05-23 | 青岛天祥食品集团有限公司 | A kind of processing technology of flavor peanut oil |
CN116640619A (en) * | 2023-06-01 | 2023-08-25 | 中粮营养健康研究院有限公司 | Peanut oil and preparation method thereof |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104232292A (en) * | 2014-09-16 | 2014-12-24 | 锦屏县食为天农产品有限公司 | Cold pressing and refining method of camellia oil |
CN105886107A (en) * | 2014-12-19 | 2016-08-24 | 贵州省黎平县黔香园油脂有限公司 | Strong-flavor camellia oil cold-pressing process |
CN106190532A (en) * | 2016-08-14 | 2016-12-07 | 林亚东 | A kind of Oleum Camelliae preparation method |
CN106244316A (en) * | 2016-08-31 | 2016-12-21 | 蚌埠市江淮粮油有限公司 | A kind of processing method of giving off a strong fragrance Oleum Brassicae campestris |
CN107242583A (en) * | 2017-07-29 | 2017-10-13 | 湖南大三湘油茶生态产业有限公司 | The quick heat treatment method of camellia oleifera fruit |
-
2018
- 2018-07-16 CN CN201810778735.5A patent/CN108690713A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104232292A (en) * | 2014-09-16 | 2014-12-24 | 锦屏县食为天农产品有限公司 | Cold pressing and refining method of camellia oil |
CN105886107A (en) * | 2014-12-19 | 2016-08-24 | 贵州省黎平县黔香园油脂有限公司 | Strong-flavor camellia oil cold-pressing process |
CN106190532A (en) * | 2016-08-14 | 2016-12-07 | 林亚东 | A kind of Oleum Camelliae preparation method |
CN106244316A (en) * | 2016-08-31 | 2016-12-21 | 蚌埠市江淮粮油有限公司 | A kind of processing method of giving off a strong fragrance Oleum Brassicae campestris |
CN107242583A (en) * | 2017-07-29 | 2017-10-13 | 湖南大三湘油茶生态产业有限公司 | The quick heat treatment method of camellia oleifera fruit |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109943408A (en) * | 2019-04-10 | 2019-06-28 | 中国热带农业科学院农产品加工研究所 | A kind of oil tea seed kernel stripping method |
CN110819438A (en) * | 2019-11-29 | 2020-02-21 | 湖南杨家将茶油股份有限公司 | Preparation method of tea seed oil |
CN116144421A (en) * | 2022-09-05 | 2023-05-23 | 青岛天祥食品集团有限公司 | A kind of processing technology of flavor peanut oil |
CN116640619A (en) * | 2023-06-01 | 2023-08-25 | 中粮营养健康研究院有限公司 | Peanut oil and preparation method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2020101704A4 (en) | A Physical Refining Method of Original Camellia Oil | |
CN104194920B (en) | A kind of preparation method of fructus cannabis oil | |
CN103725408B (en) | Processing technology of camellia oil | |
CN104388182A (en) | Physically pressed tea seed oil and extracting preparation method thereof | |
CN108690713A (en) | A kind of method of camellia seed kernel cold pressing production tea-seed oil | |
CN100535093C (en) | Aromatic sunflower oil | |
CN102766524B (en) | Method for squeezing edible tea seed oil at normal temperature | |
CN104789345B (en) | A kind of method that twice pressing prepares shinyleaf yellowhorn oil | |
CN103305334A (en) | Method for extracting tea oil by cold pressing and solvent leaching technique in stages | |
CN110437931A (en) | A kind of processing technology of low acid value Fructus Zanthoxyli oil | |
CN104560366A (en) | Hydraulic and cold pressing method for preparing non-refined original-flavor tea oil | |
CN107011988B (en) | A kind of coconut oil extraction process and its coconut oil | |
CN106665890A (en) | Preparation method of walnut oil | |
CN107488499A (en) | A kind of cold press tea-seed oil method | |
CN105670778A (en) | Method for extracting peony seed oil from peony seeds | |
CN106867655B (en) | A kind of production method of low temperature pressing torreya oil | |
CN103396878A (en) | Preparation method of low-temperature cold-pressed peanut oil | |
CN105886108A (en) | Pure camellia oil processing technology | |
CN107904000B (en) | A kind of processing method of high stability flavor type kenaf oil | |
CN104560370A (en) | Preparation method of original ecological tea seed oil | |
CN1396249B (en) | Tea leaf tea-seed oil processing method | |
CN107653056A (en) | A kind of deep working method of camellia oil | |
CN107287026A (en) | A kind of peony seed oil depickling extracting method | |
CN106833877A (en) | A kind of colding pressing squeezes the method that combining ultrasonic ripple method extracts linseed oil | |
CN102766525B (en) | Method for squeezing tea seed oil at normal temperature |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181023 |