CN104311530A - Method for extracting high-purity piperine with low pollution - Google Patents

Method for extracting high-purity piperine with low pollution Download PDF

Info

Publication number
CN104311530A
CN104311530A CN201410553065.9A CN201410553065A CN104311530A CN 104311530 A CN104311530 A CN 104311530A CN 201410553065 A CN201410553065 A CN 201410553065A CN 104311530 A CN104311530 A CN 104311530A
Authority
CN
China
Prior art keywords
piperine
filtrate
acid
solid
low
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
CN201410553065.9A
Other languages
Chinese (zh)
Inventor
李鑫
曹华茹
陈亮
鲁燚
羊梦诗
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.)
Zhejiang A&F University ZAFU
Original Assignee
Zhejiang A&F University ZAFU
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 Zhejiang A&F University ZAFU filed Critical Zhejiang A&F University ZAFU
Priority to CN201410553065.9A priority Critical patent/CN104311530A/en
Publication of CN104311530A publication Critical patent/CN104311530A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D317/00Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms
    • C07D317/08Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3
    • C07D317/44Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 ortho- or peri-condensed with carbocyclic rings or ring systems
    • C07D317/46Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 ortho- or peri-condensed with carbocyclic rings or ring systems condensed with one six-membered ring
    • C07D317/48Methylenedioxybenzenes or hydrogenated methylenedioxybenzenes, unsubstituted on the hetero ring
    • C07D317/50Methylenedioxybenzenes or hydrogenated methylenedioxybenzenes, unsubstituted on the hetero ring with only hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached to atoms of the carbocyclic ring
    • C07D317/60Radicals substituted by carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Medicines Containing Plant Substances (AREA)

Abstract

The invention discloses a method for extracting piperine with low pollution, and in particular relates to a method for extracting and purifying piperine by using low-toxic organic solvents including ethanol and acetone. The method comprises the steps of extracting piperine by adopting a reflux method and using nontoxic ethanol as a solvent, adjusting the pH value through hydrochloric acid, removing piperic acid, neutralizing redundant acid by using sodium hydroxide, adding distilled water, sufficiently cooling to obtain crude piperine, performing re-crystallization purification by using low-toxic acetone as a solvent, and performing vacuum drying to obtain high-purity piperine. The method overcomes the defects of common toxic solvents such as methanol and chloroform in traditional extraction methods and the defect of pollution to a water environment in an acid extraction method. Moreover, the method has the advantages of high extraction rate, high purity, low production cost, low pollution, simple production process and the like, and the obtained piperine product is high in activity, purely natural and high in medical value.

Description

A kind of low stain extracts the method for high-purity piperine
Technical field
The invention discloses a kind of low stain and extract the method for high-purity piperine, particularly relate to and a kind ofly utilize low toxicity organic solvent ethanol, the method for extraction purification piperine that acetone is solvent.
Background technology
Piperine is owing to having antibacterial desinsection, anti-oxidant, diarrhoea, depression, enhancing immunity and the unique effects such as anticancer, and active strong, and pharmaceutical use is large.And the main component in pepper fruit is alkaloid, volatility grease, protein-based, sylvic oil lipid, mineralogical composition and starch, so the method for extracting and developing high-content, high reactivity piperine composition is studied widely from pepper.The method of current extraction piperine has solvent-extraction process, acid extraction method, ultrasonic extraction, microwave loss mechanisms, supercritical fluid carbon dioxide extraction method and ultrasonic wave ionic liquid extract method etc.Wherein solvent-extraction process and acid extraction method simple, easy to operate due to principle, be the method for the extraction piperine of main flow always.But the organic solvent that the methyl alcohol that solvent-extraction process in the past uses solvability strong, chloroform etc. are poisonous, to the injury of human body and the pollution of environment very serious.A kind of method that low stain extracts high purity piperine uses ethanol to extract for solvent, acetone is that solvent carries out recrystallization purifying, instead of the weak point of conventional organic solvent (as methyl alcohol, chloroform etc. are toxic) in traditional extraction process, also overcome the pollution of acid extraction method to water surrounding.And there is the advantages such as the little and production technique of high extraction, high purity, lower production cost, pollution is simple.
Summary of the invention
The object of the present invention is to provide a kind of high extraction, high purity, the method for green oligosaprobic extraction piperine.
The technical scheme solving the problems of the technologies described above employing is: adopt nontoxic ethanol to extract piperine as the circumfluence method of solvent, by salt acid for adjusting pH value removing piperinic acid, and with in sodium hydroxide and unnecessary acid, adding distil water and fully cooling obtain thick piperine, carry out recrystallization purifying with low toxicity acetone as solvent again, obtain highly purified piperine through vacuum-drying.
The further processing step of the present invention: pepper fruit is ground to form 60 order pepper powder by (1), and join 95% ethanolic soln, solid-to-liquid ratio is 1: 4, it is the 2h that refluxes at 80 DEG C that immersion 0.5h is placed on bath temperature, carries out collected by suction filtrate, filter residue;
(2) carry out underpressure distillation to the filtrate obtained to concentrate, filtrate is concentrated into the 1/5-1/4 of original solution volume;
(3) to the filter residue obtained 95% alcohol immersion 0.5h, solid-to-liquid ratio is 1: 3, and refluxes again and collected by suction filtrate, and reflux conditions is identical with step (1);
(4) merging of two parts of filtrates is carried out underpressure distillation to concentrate, the 1/5-1/4 that filtrate is concentrated into original solution volume obtains enriched material;
(5) in enriched material, add the hydrochloric acid of appropriate 6.0mol/L, regulate pH=4, leave standstill 4h, leave standstill under 1200r/min after centrifugal 10min, removing insolubles (being insoluble to the piperinic acid of acid), obtains filtrate;
(6) filtrate regulates pH=11 with 10% sodium hydroxide solution, the acid that object removing is residual;
(7) in hot water bath, slowly add distilled water until have yellow mercury oxide to separate out in filtrate, then continue adding distil water and separate out to no longer including yellow mercury oxide, the distilled water added is about 2 times of filtrate, then solution one is placed in frozen water fully cools 4h;
(8) gained mixed solution centrifugal 10min under 1200r/min obtains yellow powder solid, i.e. thick piperine;
(9) in thick piperine, add acetone and make saturated solution under low-grade fever condition, then filtered while hot cannot be dissolved if any solid, if thick piperine all dissolves, add the distilled water with acetone equivalent, treat that a large amount of solid is separated out, carry out centrifugal, filter and obtain solid, then in filtrate, add the distilled water with acetone equivalent, treat that solid is separated out, centrifugal, filtration obtains solid again, repeats this step 2-3 time;
(10) the solid equal-volume washed with diethylether twice will obtained, remove lipid-soluble substance, vacuum-drying obtains the pale yellow powder piperine of higher degree.
The invention has the beneficial effects as follows: a kind of low stain extracts high-purity piperine method and adopts ethanol to be that solvent extracts, acetone is that solvent carries out recrystallization purifying, overcome the weak point of conventional organic solvent (as methyl alcohol, chloroform etc. are toxic) in traditional extraction process, also overcome the pollution of acid extraction method to water surrounding.And there is the advantages such as the little and production technique of high extraction, high purity, lower production cost, pollution is simple, the piperine Product Activity obtained is high, pure natural, medical value high.
Embodiment
Below in conjunction with case study on implementation, the present invention is described in more detail.
(1) pepper fruit is ground to form 60 order pepper powder, join 95% ethanolic soln, solid-to-liquid ratio is 1: 4, and it is the 2h that refluxes at 80 DEG C that immersion 0.5h is placed on bath temperature, carries out collected by suction filtrate, filter residue;
(2) carry out underpressure distillation to the filtrate obtained to concentrate, filtrate is concentrated into the 1/5-1/4 of original solution volume;
(3) to the filter residue obtained 95% alcohol immersion 0.5h, solid-to-liquid ratio is 1: 3, and refluxes again and collected by suction filtrate, and reflux conditions is identical with step (1);
(4) merging of two parts of filtrates is carried out underpressure distillation to concentrate, the 1/5-1/4 that filtrate is concentrated into original solution volume obtains enriched material;
(5) in enriched material, add the hydrochloric acid of appropriate 6.0mol/L, regulate pH=4, leave standstill 4h, leave standstill under 1200r/min after centrifugal 10min, removing insolubles (being insoluble to the piperinic acid of acid), obtains filtrate;
(6) filtrate regulates pH=11 with 10% sodium hydroxide solution, the acid that object removing is residual;
(7) in hot water bath, slowly add distilled water until have yellow mercury oxide to separate out in filtrate, then continue adding distil water and separate out to no longer including yellow mercury oxide, the distilled water added is about 2 times of filtrate, then solution is placed in frozen water fully cools 4h;
(8) gained mixed solution centrifugal 10min under 1200r/min obtains yellow powder solid, i.e. thick piperine;
(9) in thick piperine, add acetone and make saturated solution under low-grade fever condition, then filtered while hot cannot be dissolved if any solid, if thick piperine all dissolves, add the distilled water with acetone equivalent, treat that a large amount of solid is separated out, carry out centrifugal, filter and obtain solid, then in filtrate, add the distilled water with acetone equivalent, treat that solid is separated out, centrifugal, filtration obtains solid again, repeats this step 2-3 time;
(10) the solid equal-volume washed with diethylether twice will obtained, remove lipid-soluble substance, vacuum-drying obtains the pale yellow powder piperine of higher degree, and content is 98.9%, and purity is 99.96%.

Claims (2)

1. the method for a low stain extraction high-purity piperine, it is characterized in that: adopt nontoxic ethanol to extract piperine as the circumfluence method of solvent, by salt acid for adjusting pH value removing piperinic acid, and with in sodium hydroxide and unnecessary acid, adding distil water and fully cool and obtain thick piperine.Carry out recrystallization purifying with low toxicity acetone as solvent again, obtain highly purified piperine through vacuum-drying.
2. low stain as claimed in claim 1 extracts the method for high-purity piperine, it is characterized in that comprising the steps:
(1) pepper fruit is ground to form 60 order pepper powder, join 95% ethanolic soln, solid-to-liquid ratio is 1: 4, and it is the 2h that refluxes at 80 DEG C that immersion 0.5h is placed on bath temperature, carries out collected by suction filtrate, filter residue;
(2) carry out underpressure distillation to the filtrate obtained to concentrate, filtrate is concentrated into the 1/5-1/4 of original solution volume;
(3) to the filter residue obtained 95% alcohol immersion 0.5h, solid-to-liquid ratio is 1: 3, and refluxes again and collected by suction filtrate, and reflux conditions is identical with step (1);
(4) merging of two parts of filtrates is carried out underpressure distillation to concentrate, the 1/5-1/4 that filtrate is concentrated into original solution volume obtains enriched material;
(5) in enriched material, add the hydrochloric acid of appropriate 6.0mol/L, regulate pH=4, leave standstill 4h, leave standstill under 1200r/min after centrifugal 10min, removing insolubles (being insoluble to the piperinic acid of acid), obtains filtrate;
(6) filtrate regulates pH=11 with 10% sodium hydroxide solution, the acid that object removing is residual;
(7) in hot water bath, slowly add distilled water until have yellow mercury oxide to separate out in filtrate, then continue adding distil water and separate out to no longer including yellow mercury oxide, the distilled water added is about 2 times of filtrate, then solution is placed in frozen water fully cools 4h;
(8) gained mixed solution centrifugal 10min under 1200r/min obtains yellow powder solid, i.e. thick piperine;
(9) in thick piperine, add acetone and make saturated solution under low-grade fever condition, then filtered while hot cannot be dissolved if any solid, if thick piperine all dissolves, add the distilled water with acetone equivalent, treat that a large amount of solid is separated out, carry out centrifugal, filter and obtain solid, then in filtrate, add the distilled water with acetone equivalent, treat that solid is separated out, centrifugal, filtration obtains solid again, repeats this step 2-3 time;
(10) the solid equal-volume washed with diethylether twice will obtained, remove lipid-soluble substance, vacuum-drying obtains the pale yellow powder piperine of higher degree.
CN201410553065.9A 2014-10-09 2014-10-09 Method for extracting high-purity piperine with low pollution Pending CN104311530A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410553065.9A CN104311530A (en) 2014-10-09 2014-10-09 Method for extracting high-purity piperine with low pollution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410553065.9A CN104311530A (en) 2014-10-09 2014-10-09 Method for extracting high-purity piperine with low pollution

Publications (1)

Publication Number Publication Date
CN104311530A true CN104311530A (en) 2015-01-28

Family

ID=52366872

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410553065.9A Pending CN104311530A (en) 2014-10-09 2014-10-09 Method for extracting high-purity piperine with low pollution

Country Status (1)

Country Link
CN (1) CN104311530A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019073491A1 (en) 2017-10-14 2019-04-18 Cipla Limited Process for the preparation of piperine
CN113372322A (en) * 2021-05-28 2021-09-10 海南省农垦科学院集团有限公司 Preparation method of high-purity piperine
CN115052592A (en) * 2019-12-10 2022-09-13 布莱特西德公司 Composition and method for producing deodorized peppers

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1294127A (en) * 2000-11-03 2001-05-09 海南绿田园高新技术发展有限公司 Process for preparing piperine
CN101985440A (en) * 2010-10-30 2011-03-16 暨南大学 Method for producing piperine
CN102503928A (en) * 2011-12-01 2012-06-20 晨光生物科技集团股份有限公司 Production method of high-purity piperine

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1294127A (en) * 2000-11-03 2001-05-09 海南绿田园高新技术发展有限公司 Process for preparing piperine
CN101985440A (en) * 2010-10-30 2011-03-16 暨南大学 Method for producing piperine
CN102503928A (en) * 2011-12-01 2012-06-20 晨光生物科技集团股份有限公司 Production method of high-purity piperine

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
侯文洁等: "胡椒中胡椒碱的提取工艺研究", 《中国调味品》 *
朱静平: "《化学材料合成与制备技术实训》", 31 July 2014, 北京理工大学出版社 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019073491A1 (en) 2017-10-14 2019-04-18 Cipla Limited Process for the preparation of piperine
CN111615511A (en) * 2017-10-14 2020-09-01 西普拉有限公司 Process for preparing piperine
US11267798B2 (en) 2017-10-14 2022-03-08 Cipla Limited Process for the preparation of piperine
CN115052592A (en) * 2019-12-10 2022-09-13 布莱特西德公司 Composition and method for producing deodorized peppers
CN113372322A (en) * 2021-05-28 2021-09-10 海南省农垦科学院集团有限公司 Preparation method of high-purity piperine

Similar Documents

Publication Publication Date Title
CN106860492B (en) Preparation method of cannabinol compound
CN103349110B (en) Active tea cream high in extraction rate and complete in beneficial component preservation and preparation method thereof
CN104530173B (en) A kind of extract the technique of tea saponin in cake of camellia oleifera seeds
CN104997817A (en) Extraction method of moringa oleifera leaf extractive
CN104311530A (en) Method for extracting high-purity piperine with low pollution
CN103193832B (en) Method for extracting and separating high-purity tea polyphenol from tea leaves
CN105342892A (en) Pyracantha fortuneana fruit procyanidine cream and preparing method thereof
CN104095889B (en) A kind of preparation method of ginkgo biloba p.e
CN104710393A (en) Pretreatment ethanol extraction method of dihydroquercetin in larix gmelini wood powder
WO2016082059A1 (en) Method for extracting artemisinin by aqueous solution ultrasound
CN106083834B (en) A kind of silibinin isolation and purification method
CN102718738A (en) Method for extracting, separating and purifying anthocyanin from blueberry peel and residues
CN103819572A (en) Extraction technology for production of polysaccharide from mulberry leaf
CN102935091A (en) Propolis flavonoid extracting method
CN104561220A (en) Method for preparing tomatidine through cellulose hydrolysis of tomato branches and leaves
CN102285976A (en) Method for extracting isoorientin from bamboo leaf flavones
CN103058858A (en) Method for extracting high-purity carnosic acid from rosemary
CN104530749A (en) Method for extracting natural pigment from bark
WO2008124857A3 (en) Plant extract, and use thereof
CN103613575A (en) Method for purifying high-content epigallocatechin gallate (EGCG)
CN104356171A (en) Preparation method of tea polyphenol
CN104004049A (en) Method for extracting holotoxin
CN104987954B (en) Method for extracting volatile oil and magnolol from magnolia officinalis leaves
CN104497622B (en) A kind of Camellia sinensis arnotto brown pigment extracting method
JP2014118370A (en) Method of manufacturing polymethoxyflavones

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into 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: 20150128