CN110055129A - A kind of method that aqua method extracts melon seeds in August oil - Google Patents
A kind of method that aqua method extracts melon seeds in August oil Download PDFInfo
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- CN110055129A CN110055129A CN201910418084.3A CN201910418084A CN110055129A CN 110055129 A CN110055129 A CN 110055129A CN 201910418084 A CN201910418084 A CN 201910418084A CN 110055129 A CN110055129 A CN 110055129A
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- seeds
- august
- oil
- melon seeds
- powder
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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
- C11B1/02—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
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
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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)
- Fats And Perfumes (AREA)
- Edible Oils And Fats (AREA)
Abstract
The invention discloses a kind of methods that aqua method extracts melon seeds in August oil, it includes: dry 48 hours in the drying box for be placed in melon seeds in August 55 DEG C, removes impurity, is crushed with pulverizer;Stauntonia latifolia powder of seeds is placed in glass spinner flask, constantly being stirred using the thermostat water bath with magnetic stirring function makes the fuel-displaced formation leaching liquor of Stauntonia latifolia powder of seeds;Leaching liquor is put into centrifuge tube, 20min is centrifugated by centrifuge;Under the influence of centrifugal force, grease is split into upper layer, and lower layer is emulsion layer;Draw upper layer grease;Using freeze-thaw demulsification method, emulsification is placed in the environment of -20 DEG C and freezes 12h, is demulsified after 80 DEG C of defrostings by centrifuge separation, again absorption upper layer edible vegetable oil;It solves threeleaf akebia seed but to be discarded as agricultural wastes, however the edible rate of Trilobed Caulis Akebiae fruit is lower, seed proportion is larger, and threeleaf akebia seed is abandoned the problems such as causing a large amount of wasting of resources.
Description
Technical field
The invention belongs to a kind of methods that seed oil extract technology more particularly to aqua method extract melon seeds in August oil.
Background technique
It is the perennial half fallen leaves bejuco of Lardizabalaceae that threeleaf akebia Akebia trifoliate, which is also Stauntonia latifolia,
Japan and China are originated in, in China, main integrated distribution is in the Hunan of the Yangtze river basin and southwest, Jiangxi, Hubei, four
River, Yunnan and Guizhou etc. are regional, are a kind of typical medicinal and edible plants.Threeleaf akebia have high medical value, root,
Stem, fruit and seed can be used as medicine, and be the civil common Chinese traditional herbs in China, continue to use in China's traditional Chinese medicine history super
Spent for more than 2000 years.Threeleaf akebia is also for natural green wild fruit, and pulp accounts for fresh fruit weight nearly 50%, is rich in sugar, VC, minerals
With 15 kinds of amino acid etc., fruit meat is white, and juice sweet taste is dense, and faint scent is unique, can eat raw, can also make wine, vinegar processed, be processed into jelly and fruit
The food such as dried meat;Threeleaf akebia annidation is strong, drought resisting impoverishment tolerant, to the stony desertification ecosystem of the few soil of Southwestern China area arid
System has good adaptability, and has certain shade tolerance, can be to develop forest economy to produce with the mating planting of other economic forests
The vanguard tree seed of industry.In recent years, Southwestern China Karst region threeleaf akebia cultivated area sharply rises violently, from the lake initially planted
The provinces such as south, Guizhou are quickly extended to periphery province, have multiple provinces and cities so far using threeleaf akebia as medicinal plant or work
The plantation and exploitation of large area are carried out for a kind of novel fruits;Trilobed Caulis Akebiae fruit mainly as fresh fruit or is processed into drink at present
Expect product sale, threeleaf akebia seed is but discarded as agricultural wastes, however the edible rate of Trilobed Caulis Akebiae fruit is lower, kind
Seed proportion is larger, and the discarding of threeleaf akebia seed is caused a large amount of wasting of resources.
Summary of the invention
The technical problem to be solved by the present invention is a kind of method that aqua method extracts melon seeds in August oil is provided, it is existing to solve
There is in technology Trilobed Caulis Akebiae fruit mainly as fresh fruit or be processed into beverage products sale, threeleaf akebia seed is but by as agriculture
Industry waste discards, however the edible rate of Trilobed Caulis Akebiae fruit is lower, and seed proportion is larger, and threeleaf akebia seed is abandoned
The problems such as causing a large amount of wasting of resources.
The technical scheme is that
A kind of method that aqua method extracts melon seeds in August oil, it includes:
Melon seeds in August is placed in 55 DEG C of drying box dry 48 hours by step 1, is removed impurity, is crushed with pulverizer,
Smashed Stauntonia latifolia powder of seeds is placed at 4 DEG C and is saved backup;
Stauntonia latifolia powder of seeds is placed in glass spinner flask by step 2, uses the thermostat water bath with magnetic stirring function
Continuous stirring makes the fuel-displaced formation leaching liquor of Stauntonia latifolia powder of seeds;
Step 2 is obtained leaching liquor and is put into centrifuge tube by step 3, is centrifugated 20min by centrifuge;In centrifugal force
Under effect, grease is split into upper layer, and lower layer is emulsion layer;
Step 4 draws upper layer grease;
Step 5, be demulsified method using freeze-thaw, and emulsification is placed in the environment of -20 DEG C and freezes 12h, 80 DEG C of defrostings
Afterwards by centrifuge separation demulsification, upper layer edible vegetable oil is drawn again.
The method for obtaining Stauntonia latifolia powder of seeds is crushed with pulverizer described in step 1 are as follows: is crushed using high speed Universal pulverizer
After August melon seeds, Stauntonia latifolia powder of seeds is crossed into 40 meshes.
Constantly being stirred described in step 2 using the thermostat water bath with magnetic stirring function keeps Stauntonia latifolia powder of seeds fuel-displaced
When forming leaching liquor, the ratio of Stauntonia latifolia powder of seeds and water are as follows: 1:5g/mL.
When constantly stirring thermostat water bath using the thermostat water bath with magnetic stirring function described in step 2, extract
Temperature is 65 DEG C.
Constantly being stirred described in step 2 using the thermostat water bath with magnetic stirring function keeps Stauntonia latifolia powder of seeds fuel-displaced
When forming leaching liquor, extraction time is 1 hour.
20min, the centrifuge speed are centrifugated by centrifuge described in step 3 are as follows:
5500r/min。
The medicine have the advantages that
The present invention by thermostat water bath extracting at constant temperature obtains leaching liquor after crushing melon seeds in August, and leaching liquor is led to
The isolated grease of centrifuge and emulsion layer are crossed, after grease is extracted, remaining emulsion layer is carried out using freeze-thaw demulsification method
Oil is mentioned again;Eventually by oil extraction for second, the oil yield of melon seeds in August is improved as far as possible;Solves three leaf in the prior art
Caulis Akebiae fruit is mainly as fresh fruit or is processed into beverage products sale, and threeleaf akebia seed is but abandoned as agricultural wastes
It goes, however the edible rate of Trilobed Caulis Akebiae fruit is lower, seed proportion is larger, the discarding of threeleaf akebia seed is caused a large amount of
The wasting of resources the problems such as.
Detailed description of the invention:
Fig. 1 is influence schematic diagram of the liquid-to-solid ratio to melon seeds oil extract rate in August;
Fig. 2 is influence schematic diagram of the Extracting temperature to melon seeds oil extract rate in August;
Fig. 3 is influence schematic diagram of the extraction time to melon seeds oil extract rate in August;
Fig. 4 is influence schematic diagram of the centrifugal rotational speed to melon seeds oil extract rate in August.
Specific embodiment
A kind of method that aqua method extracts melon seeds in August oil, it includes:
Melon seeds in August is placed in 55 DEG C of drying box dry 48 hours by step 1, is removed impurity, is crushed with pulverizer,
Smashed Stauntonia latifolia powder of seeds is placed at 4 DEG C and is saved backup;
The method for obtaining Stauntonia latifolia powder of seeds is crushed with pulverizer described in step 1 are as follows: is crushed using high speed Universal pulverizer
After August melon seeds, Stauntonia latifolia powder of seeds is crossed into 40 meshes.
The high speed Universal pulverizer is the DFT-200 of Shanghai Lei Gu Instrument Ltd.;Drying box is electric heating constant temperature drum
Wind drying box, Shanghai Hui Tai instrument manufacturing Co., Ltd DHG-9030A.
Stauntonia latifolia powder of seeds is placed in glass spinner flask by step 2, uses the thermostat water bath with magnetic stirring function
Continuous stirring makes the fuel-displaced formation leaching liquor of Stauntonia latifolia powder of seeds;
Thermostat water bath uses the SHJ-6AB of Changzhou Jintan beneficial friend Instrument Ltd..
Step 2 is obtained leaching liquor and is put into centrifuge tube by step 3, is centrifugated 20min by centrifuge;In centrifugal force
Under effect, grease is split into upper layer, and lower layer is emulsion layer;
Centrifuge uses high speed freezing centrifuge;The Sigma 3-18ks of Beijing Five continents east development in science and technology Co., Ltd.
Step 4 draws upper layer grease, is denoted as edible vegetable oil I;
Step 5, be demulsified method using freeze-thaw, and emulsification is placed in the environment of -20 DEG C and freezes 12h, 80 DEG C of defrostings
Afterwards by centrifuge separation demulsification, upper layer edible vegetable oil is drawn again;It is denoted as edible vegetable oil II;
Merge edible vegetable oil twice to weigh, August, melon seeds oil yield calculated as follows:
Wherein, total oil quality=material quality × raw material crude fat content of raw material.
Constantly being stirred described in step 2 using the thermostat water bath with magnetic stirring function keeps Stauntonia latifolia powder of seeds fuel-displaced
When forming leaching liquor, the ratio of Stauntonia latifolia powder of seeds and water are as follows: 1:5g/mL.
All determining solid-liquid ratios of the present invention are 1:5;It is because finding melon seeds in August oil extract rate with the increasing of liquid-to-solid ratio
Big is in downward trend after first rising.When liquid-to-solid ratio progressively increases to 5:1 from 2:1, recovery rate progressively increases to maximum value
Oil yield under (64.59% ± 0.63), with other levels has significant difference (P < 0.05).When liquid material is smaller, mention
Take rate not high, it may be possible to which, because the amount of extractant is less, system is excessively sticky, and intracellular grease is not easy from albumen emulsus system
It is middle replaced water so that extracting incomplete.And liquid material ratio it is excessively high when, oil with screenings emulsification degree increasing is not easy from, influence
Fuel-displaced effect, recovery rate decline, therefore, solid-liquid ratio the most suitable is 1:5g/mL.
When constantly stirring thermostat water bath using the thermostat water bath with magnetic stirring function described in step 2, extract
Temperature is 65 DEG C.
Why Extracting temperature is selected in 65 DEG C by the present invention;It is because when Extracting temperature is increased to 65 DEG C from 35 DEG C eight
Month melon seeds oil extract rate is in rising trend, when extraction temperature is 65 DEG C, oil yield reach maximum value (67.93% ±
0.91), have with the oil yield under other levels significant difference (P < 0.05).This is because as the temperature rises, molecule
Movement velocity is accelerated, and grease is easier to be transferred to out from cell, accelerates dissolution of the aqueous solution to melon seeds oil in August.Work as extraction
When temperature is more than 65 DEG C, oil yield is declined, this may be because temperature raising causes the solubility of protein to increase, to three
The adsorption rate of leaf akebia seed oil increases so that the grease in August melon seeds be not easy by it is water-soluble go out caused by.It is most suitable for when therefore extracting
Extracting temperature be 65 DEG C.
Constantly being stirred described in step 2 using the thermostat water bath with magnetic stirring function keeps Stauntonia latifolia powder of seeds fuel-displaced
When forming leaching liquor, extraction time is 1 hour.
Melon seeds in August oil extract rate of the invention reduces afterwards as the extension of extraction time first increases, and constant temperature stirs 2h, so that
Oil yield reaches maximum value (67.96% ± 0.68), has significant difference (P < 0.05) with the oil yield under other levels.
Heating stirring can preferably destroy melon seeds cell in August, allow the water to replace the grease being wrapped in homogenate, grease can be maximum
Limit it is released.Extraction time is more than 1h, and recovery rate is on a declining curve, this is because the time is longer, will cause moisture
Evaporation is excessive, so that slurries are more and more sticky, extraction effect is bad, it is contemplated that the efficiency of actual production, optimum extraction eight
The time of the melon seeds oil moon is 1h.
20min, the centrifuge speed are as follows: 5500r/min are centrifugated by centrifuge described in step 3.
With the increase of centrifugal force, Akebia trifoliata seed oil yield is gradually increasing.When centrifugal force increases, it is wrapped in slurries
Grease can be easier to be separated, the emulsion layer that centrifugal force more ambassador must be distributed in top layer is thinner, has certain broken
Newborn effect, recovery rate can be higher.Therefore, centrifuge RPMs maximum is selected in 5500r/min by the present invention.
The present invention extracts melon seeds in August oil using aqua method, on the basis of experiment of single factor, it is determined that natural pure water is
Extraction solvent, centrifugal rotational speed 5500r/min have selected to extract temperature to the liquid-to-solid ratio that August, melon seeds oil extract rate was affected
Degree and these three factors of extraction time to melon seeds oil extract rate influence size in August successively are as follows: extraction time > Extracting temperature
> liquid-to-solid ratio, and extraction time, Extracting temperature and solid-liquid ratio make a significant impact melon seeds oil extract rate in August.
By obtaining the optimised process item of melon seeds grease agent method in August extraction after experiment of single factor and response surface analysis optimization
Part are as follows: Stauntonia latifolia powder of seeds crosses 40 meshes, and with natural Aqua pure extract solvent, liquid-to-solid ratio 5:1, Extracting temperature is 65 DEG C, extracts
Under conditions of time 1.2h, August melon seeds oil recovery rate up to 68.85 ± 0.75%.Realization proposes the maximum of melon seeds oil in August
It takes.Reduce waste.
Claims (6)
1. a kind of method that aqua method extracts melon seeds in August oil, it includes:
Melon seeds in August is placed in 55 DEG C of drying box dry 48 hours by step 1, is removed impurity, is crushed with pulverizer, by powder
Stauntonia latifolia powder of seeds after broken, which is placed at 4 DEG C, to be saved backup;
Stauntonia latifolia powder of seeds is placed in glass spinner flask by step 2, continuous using the thermostat water bath with magnetic stirring function
Stirring make the fuel-displaced formation leaching liquor of Stauntonia latifolia powder of seeds;
Step 2 is obtained leaching liquor and is put into centrifuge tube by step 3, is centrifugated 20min by centrifuge;In the effect of centrifugal force
Under, grease is split into upper layer, and lower layer is emulsion layer;
Step 4 draws upper layer grease;
Step 5, be demulsified method using freeze-thaw, and emulsification is placed in the environment of -20 DEG C and freezes 12h, is led to after 80 DEG C of defrostings
Centrifuge separation demulsification is crossed, draws upper layer edible vegetable oil again.
2. the method that a kind of aqua method according to claim 1 extracts melon seeds in August oil, it is characterised in that:
The method for obtaining Stauntonia latifolia powder of seeds is crushed with pulverizer described in step 1 are as follows: crushes August using high speed Universal pulverizer
After melon seeds, Stauntonia latifolia powder of seeds is crossed into 40 meshes.
3. the method that a kind of aqua method according to claim 1 extracts melon seeds in August oil, it is characterised in that: described in step 2
It is constantly stirred using the thermostat water bath with magnetic stirring function when making the fuel-displaced formation leaching liquor of Stauntonia latifolia powder of seeds, August
The ratio of melon seeds powder and water are as follows: 1:5g/mL.
4. the method that a kind of aqua method according to claim 1 extracts melon seeds in August oil, it is characterised in that: described in step 2
It is constantly stirred when making the fuel-displaced formation leaching liquor of Stauntonia latifolia powder of seeds, is extracted using the thermostat water bath with magnetic stirring function
Temperature is 65 DEG C.
5. the method that a kind of aqua method according to claim 1 extracts melon seeds in August oil, it is characterised in that: described in step 2
It is constantly stirred when making the fuel-displaced formation leaching liquor of Stauntonia latifolia powder of seeds, is extracted using the thermostat water bath with magnetic stirring function
Time is 1 hour.
6. the method that a kind of aqua method according to claim 1 extracts melon seeds in August oil, it is characterised in that: described in step 3
20min, the centrifuge speed are as follows: 5500r/min are centrifugated by centrifuge.
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN116064193A (en) * | 2023-02-21 | 2023-05-05 | 贵州农业职业学院 | Extraction method of seed oil of holboellia latifolia |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116064193A (en) * | 2023-02-21 | 2023-05-05 | 贵州农业职业学院 | Extraction method of seed oil of holboellia latifolia |
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