CN106833874A - A kind of tree peony edible oil squeezes technique - Google Patents

A kind of tree peony edible oil squeezes technique Download PDF

Info

Publication number
CN106833874A
CN106833874A CN201710143290.9A CN201710143290A CN106833874A CN 106833874 A CN106833874 A CN 106833874A CN 201710143290 A CN201710143290 A CN 201710143290A CN 106833874 A CN106833874 A CN 106833874A
Authority
CN
China
Prior art keywords
tree peony
temperature
peony
edible oil
reaction
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
Application number
CN201710143290.9A
Other languages
Chinese (zh)
Inventor
王新龙
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
HISHINE GROUP Ltd
Original Assignee
HISHINE GROUP Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by HISHINE GROUP Ltd filed Critical HISHINE GROUP Ltd
Priority to CN201710143290.9A priority Critical patent/CN106833874A/en
Publication of CN106833874A publication Critical patent/CN106833874A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/02Pretreatment
    • C11B1/04Pretreatment of vegetable raw material
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/10Production of fats or fatty oils from raw materials by extracting
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B3/00Refining fats or fatty oils
    • C11B3/001Refining fats or fatty oils by a combination of two or more of the means hereafter
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B3/00Refining fats or fatty oils
    • C11B3/008Refining fats or fatty oils by filtration, e.g. including ultra filtration, dialysis
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B3/00Refining fats or fatty oils
    • C11B3/02Refining fats or fatty oils by chemical reaction
    • C11B3/06Refining fats or fatty oils by chemical reaction with bases
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B3/00Refining fats or fatty oils
    • C11B3/10Refining fats or fatty oils by adsorption

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fats And Perfumes (AREA)

Abstract

Technique, including soaking flushing are squeezed the invention discloses a kind of tree peony edible oil, compacting crushing, immersion crude oil, depickling are decolourized and deodorant, and the technique obtains the edible oil that oil yield is high, is of high nutritive value.Without pyroreaction, composition preserves complete to the present invention in oil, not only improves and oil quality, while also improving the utilization rate of nutriment.

Description

A kind of tree peony edible oil squeezes technique
Technical field
The invention belongs to food processing technology field, and in particular to a kind of tree peony edible oil squeezes technique.
Background technology
Tree peony, is Ranunculaceae, Chinese herbaceous peony platymiscium, is perennial machaka, spends beautiful in colour, and jade laughs at pearl perfume, distinguished and admirable It is graceful, it is splendid, have the good reputation of " king in spending ".Varieties of Peony is various, and oil therein is with tree peony except with viewing and admiring valency Value, its fruit peony seeds can also be used to make peony seed oil;Peony seed oil is because its is nutritious and unique and with health care Effect, is the treasure in vegetable oil, is referred to as " liquid golden ", and peony seed oil is best suitable in the grease for being found so far The grease of human nutrition, is the most rational total nutritive value highest of all edible oil, constituent structure, and it contains abundant many insatiable hungers And aliphatic acid, considerably beyond " oil of human health " olive oil is referred to as, wherein linolenic acid content is olive oil to its nutritive value More than 200 times, many index also all higher than other oil plant, oxide deposition is difficult again in human vas wall, heart coronary artery etc. Position.Exactly these compositions make it play important function in medical science and nutrition and turn into preferable edible oil.
At present, the preparation of peony seed oil, still takes traditional Technology in Pressing mostly, and combine degumming, depickling, decolouring, The technique of deodorization is made, but the technique oil yield is not high, and especially the recovery rate of linoleic acid plus linolenic acid is relatively low, male so as to cause Nutritional ingredient utilization rate in red seed is low.
The content of the invention
It is an object of the invention to provide a kind of technique of squeezing of tree peony edible oil, the present invention is without pyroreaction, composition in oil Preserve complete, not only improve and oil quality, while also improving the utilization rate of nutriment.
A kind of tree peony edible oil squeezes technique, and its step is as follows:
Step 1, peony seeds are dipped in water, carry out aeration flushing, are filtered using screen after being rinsed through 3-4h;
Peony seeds after cleaning are carried out low temperature compacting by step 2, and through constant temperature drying 6-8h, then secondary compacting obtains male Red powder of seeds;
Step 3, tree peony powder of seeds is put into reactor, adds ethanol to be stirred immersion 2-4h;
Step 4, gas is thermally formed by ethyl acetate, is passed through aerated reaction in reactor, until ethyl acetate is all noted In entering reactor;
Step 5, water-bath distillation reaction is carried out by reaction solution, until abjection ethyl acetate and ethanol, obtain crude oil;
Step 6, crude oil is put into after carrying out filter cleaner in filter, obtains crude oil;
Step 7, crude oil is put into sodium hydroxide lye, constant temperature stirring 2-3h, stands reaction 2-3h, is subsequently adding activity Carclazyte, stirs 1-2h, and suction filtration obtains the edible crude oil of tree peony;
Step 8, carries out batch deodorization method deodorant, you can obtain tree peony edible oil by the edible crude oil of tree peony.
Aerating gas in the step 1 use air, and aerated reaction air velocity is 10-15mL/min.
The temperature of the low temperature compacting in the step 2 is 30-40 DEG C, and the temperature of the constant temperature drying is 60-70 DEG C.
Amount of alcohol added in the step 3 is 2-4 times of peony seeds quality, and the mixing speed of the stirring immersion is 400-600r/min。
Ethyl acetate amount in the step 4 is 0.3-1.1 times of peony seeds quality, the heating-up temperature of the ethyl acetate It it is 80-100 DEG C, the temperature of the aerated reaction is 50-65 DEG C, the air-flow velocity of the aerated reaction is 3-7mL/min.
Water-bath temperature in the step 5 is 70-80 DEG C, and the condensing mode of the distillation reaction uses air setting Method.
The concentration of the sodium hydroxide lye in the step 7 is 3-13%, and the temperature of the constant temperature stirring is 70-100 DEG C, Mixing speed is 800-1400r/min.
The addition of the sodium hydroxide lye in the step 7 is 11-17 times of peony seeds, and atlapulgite addition is male The 10-17% of red seed.
The temperature for doing deodorant in the step 8 is 130-160 DEG C, and pressure is 2-8MPa, and the deodorant reaction time is 4-8h。
Compared with prior art, the invention has the advantages that:
1st, present invention process equipment requirement is relatively low, it is small to put into, it is easy to carry out large-scale production.
2nd, the present invention can improve the oil yield of peony seeds and the recovery rate of linoleic acid plus linolenic acid, and the tree peony of output eats Oily oil yield reaches always in reaching 28.9-30.0%, and peony seed oil rich in unrighted acid, linoleic acid plus linolenic acid content The 86.0-87.1% of oil mass, improves the utilization rate of nutriment in peony seeds, with wide market prospects.-
3rd, without pyroreaction, composition preserves complete to the present invention in oil, not only improves and oil quality, while also improving battalion Support the utilization rate of material.
Specific embodiment
The present invention is described further with reference to embodiment:
Embodiment 1
A kind of tree peony edible oil squeezes technique, and its step is as follows:
Step 1, peony seeds are dipped in water, carry out aeration flushing, are filtered using screen after being rinsed through 3-4h;
Peony seeds after cleaning are carried out low temperature compacting by step 2, and through constant temperature drying 6-8h, then secondary compacting obtains male Red powder of seeds;
Step 3, tree peony powder of seeds is put into reactor, adds ethanol to be stirred immersion 2-4h;
Step 4, gas is thermally formed by ethyl acetate, is passed through aerated reaction in reactor, until ethyl acetate is all noted In entering reactor;
Step 5, water-bath distillation reaction is carried out by reaction solution, until abjection ethyl acetate and ethanol, obtain crude oil;
Step 6, crude oil is put into after carrying out filter cleaner in filter, obtains crude oil;
Step 7, crude oil is put into sodium hydroxide lye, constant temperature stirring 2-3h, stands reaction 2-3h, is subsequently adding activity Carclazyte, stirs 1-2h, and suction filtration obtains the edible crude oil of tree peony;
Step 8, carries out batch deodorization method deodorant, you can obtain tree peony edible oil by the edible crude oil of tree peony.
Aerating gas in the step 1 use air, and aerated reaction air velocity is 10mL/min.
The temperature of the low temperature compacting in the step 2 is 30 DEG C, and the temperature of the constant temperature drying is 60 DEG C.
Amount of alcohol added in the step 3 is 2 times of peony seeds quality, and the mixing speed of the stirring immersion is 400r/min。
Ethyl acetate amount in the step 4 is 0.3 times of peony seeds quality, and the heating-up temperature of the ethyl acetate is 80 DEG C, the temperature of the aerated reaction is 50 DEG C, and the air-flow velocity of the aerated reaction is 3mL/min.
Water-bath temperature in the step 5 is 70 DEG C, and the condensing mode of the distillation reaction uses air setting method.
The concentration of the sodium hydroxide lye in the step 7 is 3%, and the temperature of the constant temperature stirring is 70 DEG C, stirring speed It is 800r/min to spend.
The addition of the sodium hydroxide lye in the step 7 is 11 times of peony seeds, and atlapulgite addition is tree peony The 10% of seed.
The temperature for doing deodorant in the step 8 is 130 DEG C, and pressure is 2MPa, and the deodorant reaction time is 4h.
Embodiment 2
A kind of tree peony edible oil squeezes technique, and its step is as follows:
Step 1, peony seeds are dipped in water, carry out aeration flushing, are filtered using screen after being rinsed through 4h;
Peony seeds after cleaning are carried out low temperature compacting by step 2, and through constant temperature drying 8h, then secondary compacting, obtains tree peony Powder of seeds;
Step 3, tree peony powder of seeds is put into reactor, adds ethanol to be stirred immersion 4h;
Step 4, gas is thermally formed by ethyl acetate, is passed through aerated reaction in reactor, until ethyl acetate is all noted In entering reactor;
Step 5, water-bath distillation reaction is carried out by reaction solution, until abjection ethyl acetate and ethanol, obtain crude oil;
Step 6, crude oil is put into after carrying out filter cleaner in filter, obtains crude oil;
Step 7, crude oil is put into sodium hydroxide lye, constant temperature stirring 3h, stands reaction 3h, is subsequently adding active white Soil, stirs 2h, and suction filtration obtains the edible crude oil of tree peony;
Step 8, carries out batch deodorization method deodorant, you can obtain tree peony edible oil by the edible crude oil of tree peony.
Aerating gas in the step 1 use air, and aerated reaction air velocity is 15mL/min.
The temperature of the low temperature compacting in the step 2 is 40 DEG C, and the temperature of the constant temperature drying is 70 DEG C.
Amount of alcohol added in the step 3 is 4 times of peony seeds quality, and the mixing speed of the stirring immersion is 600r/min。
Ethyl acetate amount in the step 4 is 1.1 times of peony seeds quality, and the heating-up temperature of the ethyl acetate is 100 DEG C, the temperature of the aerated reaction is 65 DEG C, and the air-flow velocity of the aerated reaction is 7mL/min.
Water-bath temperature in the step 5 is 80 DEG C, and the condensing mode of the distillation reaction uses air setting method.
The concentration of the sodium hydroxide lye in the step 7 is 13%, and the temperature of the constant temperature stirring is 100 DEG C, stirring Speed is 1400r/min.
The addition of the sodium hydroxide lye in the step 7 is 17 times of peony seeds, and atlapulgite addition is tree peony The 17% of seed.
The temperature for doing deodorant in the step 8 is 160 DEG C, and pressure is 2-8MPa, and the deodorant reaction time is 8h.
Embodiment 3
A kind of tree peony edible oil squeezes technique, and its step is as follows:
Step 1, peony seeds are dipped in water, carry out aeration flushing, are filtered using screen after being rinsed through 3h;
Peony seeds after cleaning are carried out low temperature compacting by step 2, and through constant temperature drying 7h, then secondary compacting, obtains tree peony Powder of seeds;
Step 3, tree peony powder of seeds is put into reactor, adds ethanol to be stirred immersion 3h;
Step 4, gas is thermally formed by ethyl acetate, is passed through aerated reaction in reactor, until ethyl acetate is all noted In entering reactor;
Step 5, water-bath distillation reaction is carried out by reaction solution, until abjection ethyl acetate and ethanol, obtain crude oil;
Step 6, crude oil is put into after carrying out filter cleaner in filter, obtains crude oil;
Step 7, crude oil is put into sodium hydroxide lye, constant temperature stirring 2h, stands reaction 3h, is subsequently adding active white Soil, stirs 1h, and suction filtration obtains the edible crude oil of tree peony;
Step 8, carries out batch deodorization method deodorant, you can obtain tree peony edible oil by the edible crude oil of tree peony.
Aerating gas in the step 1 use air, and aerated reaction air velocity is 13mL/min.
The temperature of the low temperature compacting in the step 2 is 35 DEG C, and the temperature of the constant temperature drying is 65 DEG C.
Amount of alcohol added in the step 3 is 3 times of peony seeds quality, and the mixing speed of the stirring immersion is 500r/min。
Ethyl acetate amount in the step 4 is 0.7 times of peony seeds quality, and the heating-up temperature of the ethyl acetate is 90 DEG C, the temperature of the aerated reaction is 60 DEG C, and the air-flow velocity of the aerated reaction is 5mL/min.
Water-bath temperature in the step 5 is 75 DEG C, and the condensing mode of the distillation reaction uses air setting method.
The concentration of the sodium hydroxide lye in the step 7 is 8%, and the temperature of the constant temperature stirring is 90 DEG C, stirring speed It is 1200r/min to spend.
The addition of the sodium hydroxide lye in the step 7 is 14 times of peony seeds, and atlapulgite addition is tree peony The 14% of seed.
The temperature for doing deodorant in the step 8 is 150 DEG C, and pressure is 5MPa, and the deodorant reaction time is 6h.
The oil yield and nutrient composition content of embodiment 1-3
Embodiments of the invention are the foregoing is only, the present invention is not intended to limit, all use equivalents or equivalent transformation The technical scheme that mode is obtained, all falls within protection scope of the present invention.

Claims (9)

1. a kind of tree peony edible oil squeezes technique, and its step is as follows:
Step 1, peony seeds are dipped in water, carry out aeration flushing, are filtered using screen after being rinsed through 3-4h;
Peony seeds after cleaning are carried out low temperature compacting by step 2, and through constant temperature drying 6-8h, then secondary compacting, obtains peony seeds Powder;
Step 3, tree peony powder of seeds is put into reactor, adds ethanol to be stirred immersion 2-4h;
Step 4, gas is thermally formed by ethyl acetate, is passed through aerated reaction in reactor, until ethyl acetate all injects anti- In answering kettle;
Step 5, water-bath distillation reaction is carried out by reaction solution, until abjection ethyl acetate and ethanol, obtain crude oil;
Step 6, crude oil is put into after carrying out filter cleaner in filter, obtains crude oil;
Step 7, crude oil is put into sodium hydroxide lye, constant temperature stirring 2-3h, stands reaction 2-3h, is subsequently adding active white Soil, stirs 1-2h, and suction filtration obtains the edible crude oil of tree peony;
Step 8, carries out batch deodorization method deodorant, you can obtain tree peony edible oil by the edible crude oil of tree peony.
2. a kind of tree peony edible oil according to claim 1 squeezes technique, it is characterised in that the exposure in the step 1 Gas gas uses air, and aerated reaction air velocity is 10-15mL/min.
3. a kind of tree peony edible oil according to claim 1 squeezes technique, it is characterised in that low in the step 2 The temperature of temperature and pressure is 30-40 DEG C, and the temperature of the constant temperature drying is 60-70 DEG C.
4. a kind of tree peony edible oil according to claim 1 squeezes technique, it is characterised in that the second in the step 3 Alcohol addition is 2-4 times of peony seeds quality, and the mixing speed of the stirring immersion is 400-600r/min.
5. a kind of tree peony edible oil according to claim 1 squeezes technique, it is characterised in that the second in the step 4 Acetoacetic ester amount is 0.3-1.1 times of peony seeds quality, and the heating-up temperature of the ethyl acetate is 80-100 DEG C, the aerated reaction Temperature be 50-65 DEG C, the air-flow velocity of the aerated reaction is 3-7mL/min.
6. a kind of tree peony edible oil according to claim 1 squeezes technique, it is characterised in that the water in the step 5 Bath reaction temperature is 70-80 DEG C, and the condensing mode of the distillation reaction uses air setting method.
7. a kind of tree peony edible oil according to claim 1 squeezes technique, it is characterised in that the hydrogen in the step 7 The concentration for aoxidizing soda lye is 3-13%, and the temperature of the constant temperature stirring is 70-100 DEG C, and mixing speed is 800-1400r/ min。
8. a kind of tree peony edible oil according to claim 1 squeezes technique, it is characterised in that the hydrogen in the step 7 The addition for aoxidizing soda lye is 11-17 times of peony seeds, and atlapulgite addition is the 10-17% of peony seeds.
9. a kind of tree peony edible oil according to claim 1 squeezes technique, it is characterised in that done in the step 8 Deodorant temperature is 130-160 DEG C, and pressure is 2-8MPa, and the deodorant reaction time is 4-8h.
CN201710143290.9A 2017-03-11 2017-03-11 A kind of tree peony edible oil squeezes technique Pending CN106833874A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710143290.9A CN106833874A (en) 2017-03-11 2017-03-11 A kind of tree peony edible oil squeezes technique

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710143290.9A CN106833874A (en) 2017-03-11 2017-03-11 A kind of tree peony edible oil squeezes technique

Publications (1)

Publication Number Publication Date
CN106833874A true CN106833874A (en) 2017-06-13

Family

ID=59144735

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710143290.9A Pending CN106833874A (en) 2017-03-11 2017-03-11 A kind of tree peony edible oil squeezes technique

Country Status (1)

Country Link
CN (1) CN106833874A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113150872A (en) * 2021-05-07 2021-07-23 四川省运好农业开发有限公司 Comprehensive-nutrition peony essential oil refining method

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1858171A (en) * 2006-06-06 2006-11-08 薛二娜 Solvent method for extracting peony matrix oil
CN101549932A (en) * 2009-05-14 2009-10-07 蔡志武 Integrated production method of organic sewage/waste residue treatment, microalgae culturing and oil refining
CN102071096A (en) * 2009-11-20 2011-05-25 菏泽瑞璞牡丹产业科技发展有限公司 Preparation method of peony seed oil
CN102071097A (en) * 2009-11-20 2011-05-25 菏泽瑞璞牡丹产业科技发展有限公司 Cold-pressing method of peony seed oil
CN202173938U (en) * 2011-07-19 2012-03-28 南昌洋浦天然香料香精有限公司 Neutralization reaction kettle with blast aeration agitation used in spice purifying process
CN102851112A (en) * 2012-09-07 2013-01-02 乔新光 Preparation method for selenium-rich peony seed essential oil
CN103173275A (en) * 2013-03-06 2013-06-26 曹庸 Pressing-low-temperature continuous phase-change castor oil extraction method
CN103992872A (en) * 2013-10-31 2014-08-20 菏泽中禾健元生物科技有限公司 Production method of peony seed oil
CN104277908A (en) * 2014-09-25 2015-01-14 齐鲁工业大学 Preparation method of peony seed oil
CN104629902A (en) * 2015-02-12 2015-05-20 江南大学 Method for extracting maize germ oil assisted by ethyl alcohol and steam explosion
CN105567416A (en) * 2016-02-18 2016-05-11 南宁市品迪生物工程有限公司 Technology for producing peony seed oil
CN105567415A (en) * 2016-02-18 2016-05-11 南宁市品迪生物工程有限公司 Method for preparing peony seed oil
CN105602708A (en) * 2016-02-18 2016-05-25 南宁市品迪生物工程有限公司 Method for producing peony seed oil
CN106010782A (en) * 2016-07-11 2016-10-12 铜陵亚通牡丹产业发展有限公司 Preparation technology of peony seed oil

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1858171A (en) * 2006-06-06 2006-11-08 薛二娜 Solvent method for extracting peony matrix oil
CN101549932A (en) * 2009-05-14 2009-10-07 蔡志武 Integrated production method of organic sewage/waste residue treatment, microalgae culturing and oil refining
CN102071096A (en) * 2009-11-20 2011-05-25 菏泽瑞璞牡丹产业科技发展有限公司 Preparation method of peony seed oil
CN102071097A (en) * 2009-11-20 2011-05-25 菏泽瑞璞牡丹产业科技发展有限公司 Cold-pressing method of peony seed oil
CN202173938U (en) * 2011-07-19 2012-03-28 南昌洋浦天然香料香精有限公司 Neutralization reaction kettle with blast aeration agitation used in spice purifying process
CN102851112A (en) * 2012-09-07 2013-01-02 乔新光 Preparation method for selenium-rich peony seed essential oil
CN103173275A (en) * 2013-03-06 2013-06-26 曹庸 Pressing-low-temperature continuous phase-change castor oil extraction method
CN103992872A (en) * 2013-10-31 2014-08-20 菏泽中禾健元生物科技有限公司 Production method of peony seed oil
CN104277908A (en) * 2014-09-25 2015-01-14 齐鲁工业大学 Preparation method of peony seed oil
CN104629902A (en) * 2015-02-12 2015-05-20 江南大学 Method for extracting maize germ oil assisted by ethyl alcohol and steam explosion
CN105567416A (en) * 2016-02-18 2016-05-11 南宁市品迪生物工程有限公司 Technology for producing peony seed oil
CN105567415A (en) * 2016-02-18 2016-05-11 南宁市品迪生物工程有限公司 Method for preparing peony seed oil
CN105602708A (en) * 2016-02-18 2016-05-25 南宁市品迪生物工程有限公司 Method for producing peony seed oil
CN106010782A (en) * 2016-07-11 2016-10-12 铜陵亚通牡丹产业发展有限公司 Preparation technology of peony seed oil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113150872A (en) * 2021-05-07 2021-07-23 四川省运好农业开发有限公司 Comprehensive-nutrition peony essential oil refining method

Similar Documents

Publication Publication Date Title
CN105495553A (en) Rich-selenium black fungus fermentation slurry and preparation method and application thereof
CN107400610A (en) A kind of selenium-rich highland barley Lycium chinense wine production technology
CN101215515B (en) Method for preparing cordyceps sinensis vinegar
CN103564406B (en) Method for brewing black millet iron-rich nutritional soy
CN101396110B (en) Preparation method of flavor sauce
CN105441271A (en) Brewing method of similar soybean-flavor baijiu
CN104522612B (en) A kind of production method brewageing mushroom soy sauce
CN103865712B (en) Taishan radix cynanchi bungei health-care yellow wine and preparation method thereof
CN105875196B (en) A kind of cultural method of phellinus igniarius mycelium culture culture medium and phellinus igniarius mycelium
CN106754404A (en) A kind of Chinese caterpillar fungus culture medium for improving cordycepin content
CN105567416A (en) Technology for producing peony seed oil
CN109479622A (en) A kind of tea tree mushroom strains industrial production method
CN106833874A (en) A kind of tree peony edible oil squeezes technique
CN109006179A (en) A kind of production method of mushroom cultivation substrate
CN105039132A (en) Sea-buckthorn vinegar preparing method
CN105273919B (en) A kind of preparation method of bamboo wine
CN103431067A (en) Method for producing rose fermented bean curd
CN105166673A (en) Rice bran processing method and rice bran cake production method
CN105110960A (en) Efficient bamboo fungus culture medium with vinasse as main materials and preparation method thereof
CN105638368B (en) A kind of oil introduction method of tree peony
CN109022501A (en) A method of ferulic acid is obtained using waste
CN104082580A (en) Good-palatability compound goose feed and preparing method of good-palatability compound goose feed
CN109674000B (en) Method for preparing pure fermented soybean sour soup
CN103911265B (en) A kind of universal health promoting wine base wine and preparation method thereof
CN110063490A (en) A kind of Cortex Eucommiae bean sheet jelly and preparation method thereof

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