CN108085131A - Cryogenic technique integrates the method for preparing high-quality rapeseed oil - Google Patents
Cryogenic technique integrates the method for preparing high-quality rapeseed oil Download PDFInfo
- Publication number
- CN108085131A CN108085131A CN201711417078.3A CN201711417078A CN108085131A CN 108085131 A CN108085131 A CN 108085131A CN 201711417078 A CN201711417078 A CN 201711417078A CN 108085131 A CN108085131 A CN 108085131A
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- Prior art keywords
- phospholipase
- oil
- rapeseed oil
- enzyme
- linked
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Classifications
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- 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
-
- 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
- C11B3/00—Refining fats or fatty oils
- C11B3/001—Refining fats or fatty oils by a combination of two or more of the means hereafter
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- 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)
- Microbiology (AREA)
- Edible Oils And Fats (AREA)
Abstract
The method for preparing high-quality rapeseed oil is integrated the invention discloses cryogenic technique, belongs to Oil processing technical field.The produced in series techniques such as innovative development of the present invention cold pressing degumming of rape oil, decoloration.Using the double enzyme-linked Integration ofTechnologies such as biological degumming, the decoloration of one steps of low activity decolorising agent of phospholipase A phospholipase C (PLA PLC), rapeseed oil appropriateness Refining Technology is established, the trans-fatty acid in grease is reduced while remaining the natural lipids active material such as vitamin E, phytosterol to greatest extent.The target of consumption reduction emission reduction is effectively realized while rapeseed oil quality is improved, the denaturation of byproduct dregs of rapeseed cake albumen is significantly reduced, improves its value of exploiting and utilizing.
Description
Technical field
The method for preparing high-quality rapeseed oil is integrated the present invention relates to cryogenic technique, belongs to Oil processing technical field.
Background technology
China is not only oil seed production big country and grease consumption big country, while is also oil plant fats and oils processing big country.With regard to grease
For processing, the fats and oils processing ability in China is big, as many as number of the enterprise belongs to the first in the world.According to statistics, 2008 are ended, entirely
100,000,000 tons of state's Oil processing ability, 30,000,000 tons of affinability, edible vegetable oil total output are 24,000,000 tons, and refining oil yield is
18000000 tons, 236,200,000,000 yuan of scale more than Oils and fats enterprise sales volume, oil and fat product total value is up to 14,000,000,000 yuan/year.Oil prodution industry has become
To be only second to butcher and the second largest agricultural and sideline food processing industry of meat industry, its 20% share is accounted for, in Chinese national economy
In have highly important status and effect.Edible oil industry is the mainstay industry concerning national economy and the people's livelihood, is food industry
Important component, the gross output value accounts for the 1/10 of the food industry output value up to more than 4,400 hundred million, while is also to be related to state food safety
With the important industry of national health.However, China's edible vegetable oil industry problem encountered should not be underestimated, the production of China's edible oil
Industry dependence on external supply is serious, and edible oil safety is classified as one of national strategy safety by China.
In traditional refining pattern of China's rapeseed oil, nutrition destruction, high energy consumption, contaminant capacity existing for chemical refining are big etc. asks
Topic;Only in refining procedure, more than crude oil power consumption 20kwh, more than coal consumption 30kg per ton generate more than 210L oil-containings and give up containing alkali
Water, also there are soap stock, waste oil, spent bleaching clay, hazardous solvent gas, dead catalyst discharge, enterprise is that discharge waste material is made to meet environmental protection
It is required that, it has to oil and fat product cost is significantly increased in flower substantial contribution input waste disposal.Therefore, exploitation has traditional dish
The nutrient retention rates such as the cold press rapeseed oil and vitamin E, sterol of seed oil peculiar flavour have up to 90% appropriate refined rapeseed oil
Help improve China's edible oil degree of self-sufficiency, ensure resident's edible oil safety.
It is a very important ring in food service industry to toast flavouring, has and extends effective period of food quality, sterilization, improves flavor etc.
Effect.The method for being usually used in food heating at present has convective drying --- including heated-air drying, heat pump drying and superheated steam
Dry, radiant drying --- including microwave drying and infra-red drying, a good roasting mode should have at low cost, baking
The characteristics of speed is fast, baking quality is high and bactericidal effect is good.Convection current heated-air drying is using more in current industrial production
A kind of baking mode, it is low for equipment requirements, have the characteristics that easy to operate, rate of drying is relatively fast, sterilization effect is preferable, but
It is its high energy consumption, energy utilization rate is low, and due to needing high temperature in the drying process, it can be to the mouthfeel, appearance and battalion of product
It forms to grade and can cause a degree of destruction, be not a kind of efficiently effective drying mode;Microwave drying has many advantages, such as,
Penetrating medium using electromagnetic wave makes its interior molecules vibrate heat production, and heat is generated inside material so that each position of material
The rate of heat addition is identical, and rate of drying is fast, low energy consumption, dry from spatio-temporal influence, can carry out large-scale industry
A kind of more drying modes is applied in dry production and at present research, but microwave drying influences ratio to the quality of material
It is larger, fragrance and texture of the bad drying parameter often to material is controlled to cause big damage, and due to microwave radiation pair
Human body is harmful to, and the spilling of microwave is avoided in microwave drying process, and higher requirement is proposed to drying equipment, is caused high
Initial cost.
The content of the invention
First purpose of the present invention is to provide a kind of preparation method of high-quality rapeseed oil, and the method is to increase vegetable seed
Fragrant technology, cold pressing technology and phospholipase A-phospholipase C it is double it is enzyme-linked be combined with biological degumming, prepare soft refined type rapeseed oil.
In one embodiment of the invention, the vegetable seed aromatizing technology is to handle vegetable seed using medium-wave infrared.
In one embodiment of the invention, the method is that vegetable seed is heated 30~40min at 120~130 DEG C,
2.0~2.8 μm of infrared wavelength handles 15~20cm of distance, 4~6cm of material thickness.
In one embodiment of the invention, the phospholipase A-phospholipase C it is double it is enzyme-linked with biological degumming be with 200~
The additive amount of 500U/mg vegetable seed adds in phospholipase A, and adds in phospholipase C with the additive amount of 10000~30000U/g vegetable seed,
When reaction 1~2 is small at a temperature of 45~50 DEG C.
In one embodiment of the invention, the phospholipase A-phospholipase C it is double it is enzyme-linked with biological degumming be with 200U/
The additive amount of mg adds in phospholipase A, and adds in phospholipase C with the additive amount of 30000U/g, when being reacted 1 hour at a temperature of 50 DEG C
Between.
In one embodiment of the invention, the double enzyme-linked use of the phospholipase A-phospholipase C are the conditions in pH5~6
Lower progress.
In one embodiment of the invention, pH is adjusted by adding in HCl or NaOH.
In one embodiment of the invention, the citric acid that crude oil and mass concentration are 40~50% is with 2~5% body
Product ratio is mixed.
In one embodiment of the invention, crude oil and mass concentration be 50% citric acid with 2% volume ratio into
Row mixing.
In one embodiment of the invention, the method further includes decoloration process, and the decoloration process is:Addition is pressed
The attapulgite of quality meter 0.5~1% carries out seed oil decolorization technique, 100-110 DEG C of bleaching temperature, bleaching time 30-
50mins。
In one embodiment of the invention, the squeezing is using fluid pressure type oil expression mode.
In one embodiment of the invention, the method includes successively:The processing of medium-wave infrared flavouring, cold pressing,
PLA-PLC double enzyme-linked processing and decolorizations.
The soft refined fragrance rapeseed oil of the method preparation is also claimed in the present invention.
Beneficial effects of the present invention:
(1) innovative development is suitable for the low temperature aromatizing technology of rapeseed, and the technique that optimizes vegetable seed flavouring improves dish
The quality of seed oil;
(2) it is integrated with the quality for suitable for rapeseed cold pressing technology and equipment, improving cold pressing rapeseed oil;
(3) the produced in series technique such as innovative development cold pressing degumming of rape oil, decoloration.Using phospholipase A-phosphatidase
The double enzyme-linked Integration ofTechnologies such as biological degumming, the decoloration of one steps of low activity decolorising agent of C (PLA-PLC), establish rapeseed oil appropriateness essence
Sweetening process technology is reduced while remaining the natural lipids active material such as vitamin E, phytosterol to greatest extent in grease
Trans-fatty acid.
(4) target of consumption reduction emission reduction while ensureing rapeseed oil nutritional quality and value is effectively realized, significantly reduces pair
The denaturation of product dregs of rapeseed cake albumen, improves its value of exploiting and utilizing.
Description of the drawings
Fig. 1 is combined biological degumming technique flow for PLA-PLC;
Fig. 2 is low activity decolorising agent two-step bleaching technological process;
Fig. 3 is the process flow chart of the present invention.
Specific embodiment
Acid value determination method:National standard GB/T 5530-2005;
Lovibond color measuring method:GB/T22460-2008;
VE content assaying methods:HPLC;
Oxidation stability assay method:GB/T 21121-2007;
Determination Methods of Aflatoxins:GB/T 5009.23-2006.
The preparation of 1 rapeseed oil of embodiment
(1) vegetable seed 25kg is taken, the vegetable seed screened is added in by vacuum intake mode in infrared heating machine and is handled
(heating 40min at 130 DEG C, handle distance 20cm, material thickness 5cm, 2.5 μm or so of infrared wavelength)
(2) using three column fluid pressure type oil presses it is infrared to step (1) treated that vegetable seed extracts oil, gradient promotes pressure
Power prepares rapeseed oil:
First stage:10~12bar handles 30mins;
Second stage:25~28bar handles 30mins;
Phase III:45~48bar handles 30min;
Fourth stage:95~98bar handles 30mins;
5th stage:290~295bar handles 30mins;
6th stage:570~585bar handles 30mins.
It is centrifuged through 4500r/min room temperatures in centrifuge to get to rapeseed oil crude oil.
(3) 1%PLA-PLC is added when reaction 3 is small under the conditions of 60 DEG C, and after centrifugation, edible vegetable oil adds in by mass 1% decoloration
105 DEG C of heating 40mins of agent, filter to obtain high-quality rapeseed oil, oil yield 85%, Residual oil 15%.To the rapeseed oil prepared
Quality is detected, as a result as shown in table 1~2.
It is 80% according to the peanut oil oil yield of the present embodiment method, Residual oil 20%.
1 rapeseed oil quality index of table
2 rapeseed oil safety index of table
The preparation of 1 low temperature rapeseed oil of reference examples
Specific embodiment is with embodiment 2, and difference lies in the edible vegetable oil after cold pressing without refining and PLA-PLC
Enzymatic treatment, oil yield 60%, Residual oil 40%, oily insoluble impurities and content of trans fatty acids are exceeded.
2 cold pressing of reference examples combines double enzyme-linked processing
Specific embodiment with embodiment 2, difference lies in, after cold pressing before handled without low temperature flavouring, obtain oily
Rate is about 75%, but rapeseed oil fragrance deficiency.
Although the present invention has been described by way of example and in terms of the preferred embodiments, it is not limited to the present invention, any to be familiar with this skill
The people of art without departing from the spirit and scope of the present invention, can do various change and modification, therefore the protection model of the present invention
Enclosing be subject to what claims were defined.
Claims (10)
1. a kind of preparation method of high-quality rapeseed oil, which is characterized in that by vegetable seed aromatizing technology, cold pressing technology and phosphatide
Enzyme A- phospholipase Cs pair are enzyme-linked to be combined with biological degumming, prepares soft refined type rapeseed oil.
2. according to the method described in claim 1, it is characterized in that, the vegetable seed aromatizing technology is to handle dish using medium-wave infrared
Seed.
3. according to the method described in claim 2, it is characterized in that, medium-wave infrared processing is at 120~130 DEG C by vegetable seed
30~40min of lower heating, 2.0~2.8 μm of infrared wavelength handle 15~20cm of distance, 4~6cm of material vegetable seed thickness.
4. according to the method described in claim 1, it is characterized in that, the phospholipase A-phospholipase C pair is enzyme-linked to use biological degumming
It is that phospholipase A is added in the additive amount of 200~500U/mg vegetable seed, and phosphorus is added in the additive amount of 10000~30000U/g vegetable seed
Lipase C, when reaction 1~2 is small at a temperature of 45~50 DEG C.
5. according to the method described in claim 4, it is characterized in that, the phospholipase A-phospholipase C pair is enzyme-linked to use biological degumming
It is that phospholipase A is added in the additive amount of 200U/mg, and phospholipase C is added in the additive amount of 30000U/g, it is anti-at a temperature of 50 DEG C
Answer 1 it is small when the time.
6. method according to claim 4 or 5, which is characterized in that the phospholipase A-phospholipase C it is double it is enzyme-linked be
It is carried out under conditions of pH5~6.
7. according to the method described in claim 1, it is characterized in that, double enzyme-linked with after biological degumming, decoloration process is also carried out.
8. the method according to the description of claim 7 is characterized in that the decoloration process is:It adds in 0.5 based on raw material oil quality
~1% attapulgite carries out seed oil decolorization technique, 100-110 DEG C of bleaching temperature, bleaching time 30-50mins.
9. according to the method described in claim 1, it is characterized in that, the squeezing is using fluid pressure type oil expression mode.
10. Claims 1 to 5, soft refined fragrance rapeseed oil prepared by 7~9 any the methods.
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CN201711417078.3A CN108085131A (en) | 2017-12-25 | 2017-12-25 | Cryogenic technique integrates the method for preparing high-quality rapeseed oil |
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CN201711417078.3A CN108085131A (en) | 2017-12-25 | 2017-12-25 | Cryogenic technique integrates the method for preparing high-quality rapeseed oil |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110964596A (en) * | 2019-12-05 | 2020-04-07 | 山东省农业科学院农产品研究所 | A kind of preparation method of acetyl triglyceride |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101663382A (en) * | 2007-01-30 | 2010-03-03 | 邦奇油类公司 | Enzymatic degumming utilizing a mixture of pla and plc phospholipases |
CN102399627A (en) * | 2011-09-26 | 2012-04-04 | 华南理工大学 | Improved vegetable oil enzymatic degumming method |
CN102517142A (en) * | 2011-12-20 | 2012-06-27 | 山东渤海实业股份有限公司 | Zero trans-fatty acid multi-vitamin first-grade soybean oil and preparation method thereof |
CN104178334A (en) * | 2013-05-24 | 2014-12-03 | 北京中天金谷粮油工程技术有限公司 | Process for infrared baking of sesame to produce oil |
CN104651040A (en) * | 2015-01-30 | 2015-05-27 | 国粮武汉科学研究设计院有限公司 | Method for degumming fragrant rap oil through enzymic process |
CN104893813A (en) * | 2015-06-30 | 2015-09-09 | 武汉轻工大学 | Rapeseed oil processing method |
CN105038978A (en) * | 2007-01-30 | 2015-11-11 | 邦奇油类公司 | Enzymatic degumming utilizing a mixture of pla and plc phospholipases |
CN106367196A (en) * | 2016-08-29 | 2017-02-01 | 无锡德合食品科技有限公司 | Method for obtaining peanut oil with soft and refined fragrance and high-quality protein powder simultaneously |
CN106359626A (en) * | 2016-08-29 | 2017-02-01 | 无锡德合食品科技有限公司 | Making method of peanut juice with soft and refined fragrance |
CN106433945A (en) * | 2016-08-10 | 2017-02-22 | 无锡德合食品科技有限公司 | Press prepared peanut oil pretreatment method |
CN109694776A (en) * | 2018-12-28 | 2019-04-30 | 合肥工业大学 | The method of vegetable oil degumming |
-
2017
- 2017-12-25 CN CN201711417078.3A patent/CN108085131A/en active Pending
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101663382A (en) * | 2007-01-30 | 2010-03-03 | 邦奇油类公司 | Enzymatic degumming utilizing a mixture of pla and plc phospholipases |
CN105038978A (en) * | 2007-01-30 | 2015-11-11 | 邦奇油类公司 | Enzymatic degumming utilizing a mixture of pla and plc phospholipases |
CN102399627A (en) * | 2011-09-26 | 2012-04-04 | 华南理工大学 | Improved vegetable oil enzymatic degumming method |
CN102517142A (en) * | 2011-12-20 | 2012-06-27 | 山东渤海实业股份有限公司 | Zero trans-fatty acid multi-vitamin first-grade soybean oil and preparation method thereof |
CN104178334A (en) * | 2013-05-24 | 2014-12-03 | 北京中天金谷粮油工程技术有限公司 | Process for infrared baking of sesame to produce oil |
CN104651040A (en) * | 2015-01-30 | 2015-05-27 | 国粮武汉科学研究设计院有限公司 | Method for degumming fragrant rap oil through enzymic process |
CN104893813A (en) * | 2015-06-30 | 2015-09-09 | 武汉轻工大学 | Rapeseed oil processing method |
CN106433945A (en) * | 2016-08-10 | 2017-02-22 | 无锡德合食品科技有限公司 | Press prepared peanut oil pretreatment method |
CN106367196A (en) * | 2016-08-29 | 2017-02-01 | 无锡德合食品科技有限公司 | Method for obtaining peanut oil with soft and refined fragrance and high-quality protein powder simultaneously |
CN106359626A (en) * | 2016-08-29 | 2017-02-01 | 无锡德合食品科技有限公司 | Making method of peanut juice with soft and refined fragrance |
CN109694776A (en) * | 2018-12-28 | 2019-04-30 | 合肥工业大学 | The method of vegetable oil degumming |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110964596A (en) * | 2019-12-05 | 2020-04-07 | 山东省农业科学院农产品研究所 | A kind of preparation method of acetyl triglyceride |
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