CN104845731A - Cucumber seed oil extraction method - Google Patents

Cucumber seed oil extraction method Download PDF

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Publication number
CN104845731A
CN104845731A CN201510215267.7A CN201510215267A CN104845731A CN 104845731 A CN104845731 A CN 104845731A CN 201510215267 A CN201510215267 A CN 201510215267A CN 104845731 A CN104845731 A CN 104845731A
Authority
CN
China
Prior art keywords
seed oil
oil
cucumidis sativi
cucumber seed
semen cucumidis
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
CN201510215267.7A
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Chinese (zh)
Inventor
刘亮
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.)
Anqing Docile Citizens Under A New Regime Or Alien Rulerss' Grain And Oil Trade Co Ltd
Original Assignee
Anqing Docile Citizens Under A New Regime Or Alien Rulerss' Grain And Oil Trade Co 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 Anqing Docile Citizens Under A New Regime Or Alien Rulerss' Grain And Oil Trade Co Ltd filed Critical Anqing Docile Citizens Under A New Regime Or Alien Rulerss' Grain And Oil Trade Co Ltd
Priority to CN201510215267.7A priority Critical patent/CN104845731A/en
Publication of CN104845731A publication Critical patent/CN104845731A/en
Pending legal-status Critical Current

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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
    • 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
    • C11B1/06Production of fats or fatty oils from raw materials by pressing

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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)
  • Coloring Foods And Improving Nutritive Qualities (AREA)

Abstract

The invention relates to a cucumber seed oil extraction method. Cucumber seed oil is obtained through processes of immersion, enzymolysis, baking, reflux extraction and the like. Cucumber seed oil is compound extracted through a pressing and extracting technology, so that natural nutritional ingredients in cucumber seeds are maintained to the largest extent, the extracted cucumber seed oil solvent residual amount is zero, volatile oil in cucumber seeds can be retained through a low-temperature processing technology, fresh smell is provided, the acid value, the luster and the phospholipid content of cucumber seed oil reach the national secondary extracted oil standard basically, and after refinement, the saturated fatty acid content is increased, the oil yield reaches 45.32%, the linoleic acid content is as high as 78%, the acid value is low, and the unsaturated fatty acid content is 86%. The method has the advantages that extraction time is short, the efficiency is high, energy is saved, the product quality is good, pollution is prevented, and the content of linoleic acid components in the cucumber seed oil is increased apparently.

Description

A kind of Semen Cucumidis sativi oil extracting method
Technical field
The present invention relates to a kind of extracting method of Vegetable oil lipoprotein, particularly relate to a kind of Semen Cucumidis sativi oil extracting method.
Background technology
Cucumber is Curcurbitaceae annual herb plant, originate in India, China generally cultivates various places, grab fruit clavate, blackish green, green or Huang Zise, seed white, Long Circle, tender fruit makes fresh Lay or is processed into pickles, when cultivating the cucumber of excellent crystal seed, the cucumber that a large amount of grain is large and full can be left: seed, Semen Cucumidis sativi is the best secret recipe that synthetism among the people is strengthened bone and replenished the calcium, to osteoporosis, legs and feet knot, rheumatosis, sacroiliitis, the disease of the internal organs such as cervical spondylosis and liver stomach spleen lung has the function resuming treatment and keep healthy, current Semen Cucumidis sativi oil is commercially not general, it is low that extracting method also exists extraction efficiency, the non-oil substances contained is there is more in leaching oil, dissolvent residual is had in grease, the shortcoming that security is not high.
Summary of the invention
The object of the present invention is to provide a kind of Semen Cucumidis sativi oil extracting method.
The technical solution used in the present invention is, a kind of Semen Cucumidis sativi oil extracting method, and it comprises following steps:
1) Semen Cucumidis sativi is put into after water soaks 24-26 hour by the weight ratio of 1:3 squeeze the juice, obtain Semen Cucumidis sativi juice, in Semen Cucumidis sativi juice, add cellulase by the weight ratio of 0.005-0.008 and proteolytic enzyme carries out enzymolysis, obtain enzymolysis solution and Production With Residue of Enzymatic Hydrolysis, enzymolysis solution is separated with Production With Residue of Enzymatic Hydrolysis;
2) by Production With Residue of Enzymatic Hydrolysis roasting twice, first time cures and cure 8-10 second under the stoving temperature of 189-192 DEG C, and second time is cured and cure 15-18 minute under the stoving temperature of 65-70 DEG C, obtains curing material;
3) squeezing curing material at the pressure of 500bar-550bar, obtaining squeezing fluid and press residue;
4) food grade potassium hydroxide and ethanol are mixed to get parting liquid by the weight ratio of 1:50, parting liquid is heated to 50-55 DEG C, mix with enzymolysis solution and press residue, frequency be 150-165khz, after power processes 15-18 minute under being the ultrasonic wave of 210-220W, refluxing extraction 2-2.5 hour in the water-bath of 58-60 DEG C, and filtered while hot, obtain filtered liquid;
5) filtered liquid is put into distiller to boil under the pressure of 1937pa-2600pa, after reclaiming distillate, namely obtain Semen Cucumidis sativi oil.
The present invention adopts squeezing and extracting technology compound collecting Semen Cucumidis sativi oil, remain the natural nutrient component in Semen Cucumidis sativi to greatest extent, in the Semen Cucumidis sativi oil extracted, solvent residual amount is zero, Low temperature processing techniques can make ethereal oil in Semen Cucumidis sativi remain, there is fresh scent, the acid number of Semen Cucumidis sativi oil, peroxide value, color and luster and phospholipids content reach the standard that national secondary leaches oil substantially, after refining, saturated fatty acid content raises, oil yield reaches 45.32%, linoleic acid content is up to 78%, acid number is lower, unsaturated fatty acid content is 86%, extraction time is short, efficiency is high, save energy, good product quality, pollution-free, and significantly improve the content of Semen Cucumidis sativi oil Linoleic acid component.
Embodiment
1) Semen Cucumidis sativi is put into after water soaks 24-26 hour by the weight ratio of 1:3 squeeze the juice, obtain Semen Cucumidis sativi juice, in Semen Cucumidis sativi juice, add cellulase by the weight ratio of 0.005-0.008 and proteolytic enzyme carries out enzymolysis, obtain enzymolysis solution and Production With Residue of Enzymatic Hydrolysis, enzymolysis solution is separated with Production With Residue of Enzymatic Hydrolysis;
2) by Production With Residue of Enzymatic Hydrolysis roasting twice, first time cures and cure 8-10 second under the stoving temperature of 189-192 DEG C, and second time is cured and cure 15-18 minute under the stoving temperature of 65-70 DEG C, obtains curing material;
3) squeezing curing material at the pressure of 500bar-550bar, obtaining squeezing fluid and press residue;
4) food grade potassium hydroxide and ethanol are mixed to get parting liquid by the weight ratio of 1:50, parting liquid is heated to 50-55 DEG C, mix with enzymolysis solution and press residue, frequency be 150-165khz, after power processes 15-18 minute under being the ultrasonic wave of 210-220W, refluxing extraction 2-2.5 hour in the water-bath of 58-60 DEG C, and filtered while hot, obtain filtered liquid;
5) filtered liquid is put into distiller to boil under the pressure of 1937pa-2600pa, after reclaiming distillate, namely obtain Semen Cucumidis sativi oil.

Claims (1)

1. a Semen Cucumidis sativi oil extracting method, it is characterized in that, it comprises following steps:
1) Semen Cucumidis sativi is put into after water soaks 24-26 hour by the weight ratio of 1:3 squeeze the juice, obtain Semen Cucumidis sativi juice, in Semen Cucumidis sativi juice, add cellulase by the weight ratio of 0.005-0.008 and proteolytic enzyme carries out enzymolysis, obtain enzymolysis solution and Production With Residue of Enzymatic Hydrolysis, enzymolysis solution is separated with Production With Residue of Enzymatic Hydrolysis;
2) by Production With Residue of Enzymatic Hydrolysis roasting twice, first time cures and cure 8-10 second under the stoving temperature of 189-192 DEG C, and second time is cured and cure 15-18 minute under the stoving temperature of 65-70 DEG C, obtains curing material;
3) squeezing curing material at the pressure of 500bar-550bar, obtaining squeezing fluid and press residue;
4) food grade potassium hydroxide and ethanol are mixed to get parting liquid by the weight ratio of 1:50, parting liquid is heated to 50-55 DEG C, mix with enzymolysis solution and press residue, frequency be 150-165khz, after power processes 15-18 minute under being the ultrasonic wave of 210-220W, refluxing extraction 2-2.5 hour in the water-bath of 58-60 DEG C, and filtered while hot, obtain filtered liquid
5) filtered liquid is put into distiller to boil under the pressure of 1937pa-2600pa, after reclaiming distillate, namely obtain Semen Cucumidis sativi oil.
CN201510215267.7A 2015-04-30 2015-04-30 Cucumber seed oil extraction method Pending CN104845731A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510215267.7A CN104845731A (en) 2015-04-30 2015-04-30 Cucumber seed oil extraction method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510215267.7A CN104845731A (en) 2015-04-30 2015-04-30 Cucumber seed oil extraction method

Publications (1)

Publication Number Publication Date
CN104845731A true CN104845731A (en) 2015-08-19

Family

ID=53845723

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510215267.7A Pending CN104845731A (en) 2015-04-30 2015-04-30 Cucumber seed oil extraction method

Country Status (1)

Country Link
CN (1) CN104845731A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1051057A (en) * 1990-12-10 1991-05-01 王绍璋 Preparation and processing method of abelmoschus manihot oil
CN101385485A (en) * 2007-09-11 2009-03-18 北京健健康康生物技术有限公司 Preparation method of watermelon seeds oil
CN101690525A (en) * 2009-10-27 2010-04-07 浙江大学 Method for extracting myrica seed oil
CN101779705A (en) * 2010-02-22 2010-07-21 北京市科威华食品工程技术有限公司 Production method of grape seed oil
CN103589505A (en) * 2013-11-29 2014-02-19 东北农业大学 Evening primrose oil extraction method
CN104531338A (en) * 2015-01-05 2015-04-22 湖南紫苏科研有限公司 Method for comprehensively extracting and refining perilla oil

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1051057A (en) * 1990-12-10 1991-05-01 王绍璋 Preparation and processing method of abelmoschus manihot oil
CN101385485A (en) * 2007-09-11 2009-03-18 北京健健康康生物技术有限公司 Preparation method of watermelon seeds oil
CN101690525A (en) * 2009-10-27 2010-04-07 浙江大学 Method for extracting myrica seed oil
CN101779705A (en) * 2010-02-22 2010-07-21 北京市科威华食品工程技术有限公司 Production method of grape seed oil
CN103589505A (en) * 2013-11-29 2014-02-19 东北农业大学 Evening primrose oil extraction method
CN104531338A (en) * 2015-01-05 2015-04-22 湖南紫苏科研有限公司 Method for comprehensively extracting and refining perilla oil

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Application publication date: 20150819

RJ01 Rejection of invention patent application after publication