CN1416710A - Fast barbasco extracting and purifying process - Google Patents

Fast barbasco extracting and purifying process Download PDF

Info

Publication number
CN1416710A
CN1416710A CN 02153008 CN02153008A CN1416710A CN 1416710 A CN1416710 A CN 1416710A CN 02153008 CN02153008 CN 02153008 CN 02153008 A CN02153008 A CN 02153008A CN 1416710 A CN1416710 A CN 1416710A
Authority
CN
China
Prior art keywords
rotenone
extraction
former medicine
solvent
dimethyl formamide
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.)
Granted
Application number
CN 02153008
Other languages
Chinese (zh)
Other versions
CN1202727C (en
Inventor
郑树芹
寇进年
兰俊贞
刘钧平
寇保祥
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN 02153008 priority Critical patent/CN1202727C/en
Publication of CN1416710A publication Critical patent/CN1416710A/en
Application granted granted Critical
Publication of CN1202727C publication Critical patent/CN1202727C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Extraction Or Liquid Replacement (AREA)

Abstract

The fast barbasco extracting and purifying process mainly includes crushing derris root, leaching in leaching solvent benzene or vinyl trichloride with water-displacing agent N, N-dimethyl formamide in 2.5-10 times the derris root volume, filtering, submicron suction filtering, depression concentration, washing in methanol, and ethanol, mixture, discharging, crystallization and stoving. The said process features fast extracting speed, high production efficiency, low cost, high barbasco yield and less environmental pollution and can be used in industrial production.

Description

The former medicine fast purification of rotenone extraction method
Technical field
The present invention relates to the insecticide technical field.
Technical background
A large amount of uses of chemical pesticide for a long time, human Pest Control has been played important function, but the residue of pesticide on crop, the vegetables Lay mankind itself's health has also been constituted the serious danger side of body, so the exploitation of biological source insecticide become an important channel of environmental protection type agricultural.The application of rotenone in insecticide can effectively address the above problem, and is characterized in not having poisoning, is difficult for residually, do not influence food quality, and insect is difficult for producing resistance and wildness again.The applicant had once applied for " process for extracting raw rotenone " patent, efficiently solve the industrial production problem of rotenone, but its extraction rate is still slower, production efficiency need improve, owing to used the carbon tetrachloride toxic solvent in the technology, had problem of environmental pollution and former medicine loss waste problem.
Summary of the invention
The purpose of this invention is to provide the former medicine fast purification of a kind of rotenone extraction method, not only extraction rate is fast for it, can improve its production efficiency greatly, reduces cost, and can effectively reduce the loss waste of environmental pollution and active ingredient, be particularly suitable for commercial Application.
One of technical scheme of the present invention is:, the former medicine fast purification of a kind of rotenone extraction method, comprise derris root is pulverized, stirring and leaching in the lixiviate still, with the leaching liquor coarse filtration, after handling, the sub-micron suction strainer enters concentrating under reduced pressure in the anti-still, air-dry or chemical method shrink, the weight proportion that it is characterized in that derris root and extraction solvent is 10-40: 100, extraction solvent is for being purified petroleum benzin, and aqua NN dimethyl formamide is caught up with in adding, its weight proportion is NN dimethyl formamide: purified petroleum benzin=2-40: 98-60, and extraction temperature is 70-80 ℃; Coarse filtration, fine filtering enter in the washer after concentrating, and wash under high pressure blowback condition, wash qualified post crystallization, release liquid, and it is qualified that clout enters the dried bath of drier, gets product; The paste rotenone after it concentrates and the weight ratio of cleaning solvent are 10-50: 90-50, and cleaning solvent is an alcohols material.
Be good with NN dimethyl formamide: purified petroleum benzin=4-20: 96-80 in the above-mentioned extraction solvent.
For making effect better, above-mentioned derris root preferably is crushed to 2.0-2.5mm sawdust shape.
Above-mentioned the most handy ethanol of cleaning solvent and methyl alcohol mixed liquor, its weight proportion are ethanol: methyl alcohol=1: 2-25.
Two of technical scheme of the present invention is: the former medicine fast purification of a kind of rotenone extraction method, comprise derris root is pulverized, stirring and leaching in the lixiviate still, with the leaching liquor coarse filtration, after handling, the sub-micron suction strainer enters concentrating under reduced pressure in the anti-still, air-dry or chemical method shrink, the weight proportion that it is characterized in that derris root and extraction solvent is 10-40: 100, extraction solvent is a trichloro-ethylene, and aqua NN dimethyl formamide is caught up with in adding, its weight proportion is NN dimethyl formamide: trichloro-ethylene=8-30: 92-70, and extraction temperature is 70-85 ℃; Coarse filtration, fine filtering enter in the washer after concentrating, and wash under high pressure blowback condition, wash qualified post crystallization, release liquid, and clout enters that to do bath in the drier qualified, gets product; The paste rotenone after it concentrates and the weight ratio of cleaning solvent are 10-50: 90-50, and cleaning solvent is an alcohols material.
Be good with NN dimethyl formamide: trichloro-ethylene=10-20: 90-80 in the above-mentioned extraction solvent.
For making effect better, above-mentioned derris root preferably is crushed to the sawdust shape of 2.0-2.5mm.
Above-mentioned alcohols cleaning solvent can be used ethanol and methyl alcohol mixed liquor, and its weight proportion is an ethanol: methyl alcohol=1: 2-25.
Good effect of the present invention is as follows: extraction rate is fast, the production efficiency height, and cost reduces greatly, and because without carbon tetrachloride Xian Di agent, so rotenone loss less wastage, the output capacity height, the availability height can effectively reduce environmental pollution, is particularly suitable for industry and applies.Be described further below in conjunction with embodiment, but not as a limitation of the invention.
Embodiment
Scheme one embodiment: get derris root and pulverize, extract, shrink gained rotenone cream is put into washer pressurization blowback Xian Di by scheme one described technology, qualified back blowing, drying is up to the standards, and gets product.Extract proportioning and temperature in the kettle such as following table 1:
Figure A0215300800041
Rotenone cream and washing agent proportioning such as following table 2:
Figure A0215300800042
Pure proportioning such as following table 3 in the washing agent:
Figure A0215300800051
Annotate: 10-15 ℃ commonly used of wash temperature, under crystallization temperature, to be advisable.
Scheme two embodiment: get derris root and pulverize, extract by scheme two technologies.
Extract solvent burden ratio and temperature in the kettle such as following table 4:
Figure A0215300800052
Annotate: rotenone cream and washing agent proportioning are with table 2, table 3.Rotenone cream water content generally is not more than 5 ‰ herein.
The rotenone that the foregoing description can make is former in index parameter such as following table 5:
Project Index
The top grade product Primes Qualified
The rotenone mass fraction 〉= ????75.0 ????50.0 ????35.0
The water quality mark, acid (with sulfuric acid) mass fraction, ????1.5 ????0.3
Its extraction time, comparable above-mentioned prior art shortened 1/2 to more than 2/3, as being 3h originally, now can reach 1h, so improved productivity ratio greatly, cost can reduce more than 1/3, and pollutes and lack, and because of make the Xian Di solvent without carbon tetrachloride, the rotenone dissolving is run off and reduced.

Claims (8)

1, the former medicine fast purification of a kind of rotenone extraction method, comprise derris root is pulverized, stirring and leaching in the lixiviate still, with the leaching liquor coarse filtration, enter concentrating under reduced pressure in the anti-still, air-dry or chemical method shrink after the sub-micron suction strainer is handled, the weight proportion that it is characterized in that derris root and extraction solvent is 10-40: 100; Extraction solvent is a purified petroleum benzin, and adds and to catch up with aqua NN dimethyl formamide, and its weight proportion is NN dimethyl formamide: purified petroleum benzin=2-40: 98-60, and extraction temperature is 70-85 ℃; Coarse filtration, fine filtering enter in the washer after concentrating again, wash under high pressure blowback condition, wash qualified post crystallization, release liquid, and clout enters that to do bath in the drier qualified, gets product; The paste rotenone after it concentrates and the weight ratio of cleaning solvent are 10-50: 90-50, and cleaning solvent is an alcohols material.
2, the former medicine fast purification of rotenone according to claim 1 extraction method is characterized in that N.N dimethyl formamide in the extraction solvent: purified petroleum benzin=4-20: 96-80.
3, the former medicine fast purification of rotenone according to claim 1 extraction method is characterized in that derris root is crushed to the sawdust shape of 2.0-2.5mm.
4, according to claim 1, the former medicine fast purification of 2 or 3 described rotenone extraction method, it is characterized in that cleaning solvent ethanol and methyl alcohol mixed liquor, its weight proportion is an ethanol: methyl alcohol=1: 2-25.
5, the former medicine fast purification of a kind of rotenone extraction method, comprise derris root is pulverized, stirring and leaching in the lixiviate still, with the leaching liquor coarse filtration, enter concentrating under reduced pressure in the anti-still, air-dry or chemical method shrink after the sub-micron suction strainer is handled, the weight proportion that it is characterized in that derris root and extraction solvent is 10-40: 100; Extraction solvent is a trichloro-ethylene, and adds and to catch up with aqua NN dimethyl formamide, and its weight proportion is NN dimethyl formamide: trichloro-ethylene=8-30: 92-70, and extraction temperature is 70-85 ℃; Coarse filtration, fine filtering enter in the washer after concentrating, and wash under high pressure blowback condition, wash qualified post crystallization, release liquid, and it is qualified that clout enters the dried bath of drier, gets product; The paste rotenone after it concentrates and the weight ratio of cleaning solvent are 10-50: 90-50, and cleaning solvent is an alcohols material.
6, the former medicine fast purification of rotenone according to claim 5 extraction method is characterized in that in the extraction solvent, N.N dimethyl formamide: trichloro-ethylene=10-20: 90-80.
7, the former medicine fast purification of rotenone according to claim 5 extraction method is characterized in that derris root is crushed to the sawdust shape of 2.0-2.5mm.
8, according to claim 5, the former medicine fast purification of 6 or 7 described rotenone extraction method, it is characterized in that cleaning solution ethanol and methyl alcohol mixed liquor, its weight proportion is an ethanol: methyl alcohol=1: 2-25.
CN 02153008 2002-11-25 2002-11-25 Fast barbasco extracting and purifying process Expired - Fee Related CN1202727C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 02153008 CN1202727C (en) 2002-11-25 2002-11-25 Fast barbasco extracting and purifying process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 02153008 CN1202727C (en) 2002-11-25 2002-11-25 Fast barbasco extracting and purifying process

Publications (2)

Publication Number Publication Date
CN1416710A true CN1416710A (en) 2003-05-14
CN1202727C CN1202727C (en) 2005-05-25

Family

ID=4752187

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 02153008 Expired - Fee Related CN1202727C (en) 2002-11-25 2002-11-25 Fast barbasco extracting and purifying process

Country Status (1)

Country Link
CN (1) CN1202727C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103044440A (en) * 2012-12-31 2013-04-17 深圳市华农生物工程有限公司 Critical extraction method for rotenone

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103044440A (en) * 2012-12-31 2013-04-17 深圳市华农生物工程有限公司 Critical extraction method for rotenone
CN103044440B (en) * 2012-12-31 2015-11-18 深圳市华农生物工程有限公司 A kind of Critical extraction method for rotenone

Also Published As

Publication number Publication date
CN1202727C (en) 2005-05-25

Similar Documents

Publication Publication Date Title
CN104059947A (en) Method for preparing high-purity sulforaphane
CN105396163A (en) Air smell removing liquid containing bamboo vinegar and preparing method of air smell removing liquid
CN108176361A (en) Sulfhydryl modified charcoal based on agricultural wastes and its preparation method and application
CN107653055B (en) Method for extracting tea seed oil by ultrasonic-assisted aqueous enzymatic method
CN106833895A (en) A kind of extracting method of volatile argyi leaf oil
CN104998616A (en) Method for producing biological carbon from corn straws
CN107737579A (en) A kind of biomass carbon buffer and preparation method thereof
WO2023232087A1 (en) Clean product set prepared by using energy grass as raw material, and preparation method therefor
Devadharshini et al. Green synthesis of silver nanoparticles
CN1416710A (en) Fast barbasco extracting and purifying process
CN113633589A (en) Extraction process of cherry blossom extract for cherry blossom moisturizing hair conditioner
CN105968080A (en) Method for extracting anthocyanidin from black chokeberries
CN105381485A (en) Herb vinegar-containing air deodorizing liquid and manufacturing method thereof
CN107987862A (en) The method that a kind of Asia/supercritical methanol liquified cellulosic prepares primary biomass platform chemicals
JP2010024197A (en) Aqueous solution of saponin originating from strained lees of camellia seeds, and method of preparing the same
CN115594794B (en) PH responsive porous polymer microsphere, preparation method thereof and method for treating waste tobacco leaves by using same
CN110615857A (en) Method for recycling waste in orange can processing production
CN114192107B (en) Preparation method of corn stalk charcoal with high adsorptivity and application of corn stalk charcoal in preparation of drug sustained release preparation
CN113292628B (en) Extraction and decoloration method of saponin extraction liquid
CN109852469A (en) A kind of preparation method of coconut nutrition peanut oil
CN108166098A (en) Preparation method of banana nanofiber
CN107488413A (en) The extracting method of tannin extract in a kind of granatum
CN1508139A (en) Process for extracting rubusoside of fruit of Gorsvenor Momordica
CN105537248B (en) The method of comprehensive utilization of banana stem leaves
CN110078782B (en) Tea saponin extraction and refining process

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20050525