CN106964324B - A kind of isoflavones isolates and purifies the preparation method with macroporous absorbent resin - Google Patents

A kind of isoflavones isolates and purifies the preparation method with macroporous absorbent resin Download PDF

Info

Publication number
CN106964324B
CN106964324B CN201710216749.3A CN201710216749A CN106964324B CN 106964324 B CN106964324 B CN 106964324B CN 201710216749 A CN201710216749 A CN 201710216749A CN 106964324 B CN106964324 B CN 106964324B
Authority
CN
China
Prior art keywords
absorbent resin
macroporous absorbent
parts
preparation
added
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.)
Active
Application number
CN201710216749.3A
Other languages
Chinese (zh)
Other versions
CN106964324A (en
Inventor
闫磊
蔡克瑞
孙凯
梁军
桂金秋
王妍
刘春玲
张丽荣
宋铁军
晁岳刚
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.)
Mudanjiang Medical University
Original Assignee
Mudanjiang Medical University
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 Mudanjiang Medical University filed Critical Mudanjiang Medical University
Priority to CN201710216749.3A priority Critical patent/CN106964324B/en
Publication of CN106964324A publication Critical patent/CN106964324A/en
Application granted granted Critical
Publication of CN106964324B publication Critical patent/CN106964324B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D311/00Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings
    • C07D311/02Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings ortho- or peri-condensed with carbocyclic rings or ring systems
    • C07D311/04Benzo[b]pyrans, not hydrogenated in the carbocyclic ring
    • C07D311/22Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 4
    • C07D311/26Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 4 with aromatic rings attached in position 2 or 3
    • C07D311/34Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 4 with aromatic rings attached in position 2 or 3 with aromatic rings attached in position 3 only
    • C07D311/36Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 4 with aromatic rings attached in position 2 or 3 with aromatic rings attached in position 3 only not hydrogenated in the hetero ring, e.g. isoflavones
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D311/00Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings
    • C07D311/02Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings ortho- or peri-condensed with carbocyclic rings or ring systems
    • C07D311/04Benzo[b]pyrans, not hydrogenated in the carbocyclic ring
    • C07D311/22Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 4
    • C07D311/26Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 4 with aromatic rings attached in position 2 or 3
    • C07D311/40Separation, e.g. from natural material; Purification
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F212/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F212/02Monomers containing only one unsaturated aliphatic radical
    • C08F212/04Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F212/06Hydrocarbons
    • C08F212/08Styrene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/30Introducing nitrogen atoms or nitrogen-containing groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/26Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by elimination of a solid phase from a macromolecular composition or article, e.g. leaching out
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2201/00Foams characterised by the foaming process
    • C08J2201/04Foams characterised by the foaming process characterised by the elimination of a liquid or solid component, e.g. precipitation, leaching out, evaporation
    • C08J2201/042Elimination of an organic solid phase
    • C08J2201/0422Elimination of an organic solid phase containing oxygen atoms, e.g. saccharose
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2201/00Foams characterised by the foaming process
    • C08J2201/04Foams characterised by the foaming process characterised by the elimination of a liquid or solid component, e.g. precipitation, leaching out, evaporation
    • C08J2201/042Elimination of an organic solid phase
    • C08J2201/0424Elimination of an organic solid phase containing halogen, nitrogen, sulphur or phosphorus atoms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2325/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Derivatives of such polymers
    • C08J2325/02Homopolymers or copolymers of hydrocarbons
    • C08J2325/04Homopolymers or copolymers of styrene
    • C08J2325/08Copolymers of styrene
    • C08J2325/14Copolymers of styrene with unsaturated esters

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Analytical Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

The invention discloses a kind of isoflavones to isolate and purify the preparation method with macroporous absorbent resin, it is related to biological medicine technical field of purification, preparation method includes the following steps: the preparation of (1) macroporous absorbent resin, (2) pretreatment of macroporous absorbent resin, the modification of (3) macroporous absorbent resin.The made macroporous absorbent resin of the present invention reaches 17mg/g or more to the adsorbance of isoflavones, the efficient desorption of isoflavones is able to achieve after the flushing of 60% methanol solution, desorption efficiency reaches 98.5% or more, the purity of made isoflavones reaches 60% or more, therefore the macroporous absorbent resin is suitable for efficiently separating for isoflavones.

Description

A kind of isoflavones isolates and purifies the preparation method with macroporous absorbent resin
Technical field:
The present invention relates to biological medicine technical field of purification, and in particular to a kind of isoflavones is isolated and purified to be inhaled with macropore The preparation method of attached resin.
Background technique:
Naturally occurring isoflavones shares 12 kinds, is divided into 3 major class of daidzin, genistin and C22H22O10.Greatly Beans isoflavones has the function of anti-oxidant, pre- anti-cancer, strengthen immunity and improvement breeding performonce fo animals etc., has been widely used in In the fields such as biology, feed, medicine and health care of food.The study found that the aglycon of only sequestered just has biological activity, need The aglycon for being converted to sequestered through enzymatic hydrolysis or sour water solution glucosides could be absorbed by animal or human body.Currently, improving the different Huang of soybean The method of Aglycones content mainly has extraction, physics auxiliary law, High Pressure Wet and ultrafiltration etc. in ketone, but there are works for these methods The disadvantages of skill is more complex, higher cost and Determination of Residual Organic Solvents are high is unsuitable for mass preparation.
Flavonoids by Macroporous Adsorption Resin is in recent years using a kind of extensive purification process, other opposite purification process have selection Property it is good, nontoxic and pollution-free the advantages that, but the adsorbance of macroporous absorbent resin used at present is lower, and while desorbing need it is a large amount of Organic solvent rinses, even if these organic solvents can be recycled, it is also desirable to consume big energy to realize.
Summary of the invention:
Technical problem to be solved by the present invention lies in provide that a kind of adsorbance is high, desorption is easy and that Aglycones content is high is big Beans isoflavones isolates and purifies the preparation method with macroporous absorbent resin.
The following technical solution is employed for the technical problems to be solved by the invention to realize:
A kind of isoflavones isolates and purifies the preparation method with macroporous absorbent resin, and preparation method includes following step It is rapid:
(1) preparation of macroporous absorbent resin: Xiang Shuizhong be proportionally added into styrene, hydrogenated rosin acrylic acid glycerine ester, Hydroxyethyl methacrylate, nanometer pore-foaming agent and initiator, after being sufficiently mixed under supersonic frequency 40kHz, output power 200W It is ultrasonically treated 15min, the microwave treatment 10min under microwave frequency 2450MHz, output power 700W, and in 0-5 DEG C of environment 30min is stood, continues microwave treatment 10min after mixing, 15min is then stood in -5-0 DEG C of environment, after mixing Microwave treatment 10min again, gained mixed liquor are cooled to 0-5 DEG C of heat preservation mixing 1h with the cooling rate of 5 DEG C/min, will then mix Liquid is closed to be separated by solid-liquid separation, gained solid phase obtains Archon with the washing of 35-40 DEG C of warm water three times, finally by Archon at 60-65 DEG C vacuum Drying is to get macroporous absorbent resin;
(2) poloxamer, N- methylol the pretreatment of macroporous absorbent resin: are added into above-mentioned made macroporous absorbent resin Acrylamide and hydrolysis of polymaleic anhydride, and 65-70 DEG C of heat preservation mixing 30min is warming up to the heating rate of 5 DEG C/min, then to 30-35 DEG C of water of 3 times of weight is added in gained mixture, continuation is warming up to reflux state heat preservation with the heating rate of 5 DEG C/min and mixes 15min is closed, then cooled to room temperature, filtering, gained resin sphere is washed three times, is finally dried in vacuo at 60-65 DEG C;
(3) nano-titanium dioxide and clothing health the modification of macroporous absorbent resin: are added into isocyanuric acid three-glycidyl ester Acid anhydrides is warming up to 115-120 DEG C of heat preservation mixing 15min with the heating rate of 5 DEG C/min, adds macropore after pretreatment and inhale Attached resin continues to mix 30min in 115-120 DEG C of heat preservation, after naturally cool to washing after room temperature three times, most afterwards through gained resin Sphere is dried in vacuo at 60-65 DEG C.
Water, styrene, hydrogenated rosin acrylic acid glycerine ester, hydroxyethyl methacrylate, nanometer cause in the step (1) The mass ratio of hole agent and initiator is 300-400:45-50:30-35:15-20:40-45:0.5-1.
Macroporous absorbent resin in the step (2), poloxamer, N hydroxymethyl acrylamide and hydrolysis of polymaleic anhydride Mass ratio is 60-65:1-2:0.5-1:0.5-1.
Macroporous absorbent resin, isocyanuric acid three-glycidyl ester, nano-titanium dioxide and itaconic anhydride in the step (3) Mass ratio be 60-65:5-10:3-5:0.1-0.2.
The nanometer pore-foaming agent is made of the raw material of following parts by weight: 5-10 parts of microcrystalline cellulose, polyglutamic acid 3-5 Part, 1-2 parts of rilanit special, 0.5-1 parts of polydimethyl diallyl ammonium chloride, 0.5-1 parts of sodium gluconate, ferrocene 0.05-0.1 parts, 30-50 parts of water, preparation method are as follows: microcrystalline cellulose and rilanit special are added into water, and is warming up to back Stream mode heat preservation mixing 15min, after naturally cool to addition polyglutamic acid and poly dimethyl allyl chlorination after 40-45 DEG C Ammonium, stirring 30min form lotion, sodium gluconate and ferrocene are then added, be sent into gained mixture spray after mixing In mist drying machine, particle is ground obtained by drying is made nanometer powder, finally adds water that solid content 30- is made nanometer powder The lotion of 35wt% is to get nanometer pore-foaming agent.
The nano-titanium dioxide is the nano-powder made of after the modified processing of titanium dioxide, preparation method are as follows: Crospovidone and hexamethylolmelamine pregnancy ether are added into titanium dioxide, is first heated up with the heating rate of 5 DEG C/min 30min is mixed to 120-125 DEG C of heat preservation, anionic polyacrylamide and epoxidized soybean oil is added, continues at 120-125 DEG C Heat preservation mixing 30min, gained mixture is cooled to 40-50 DEG C with the cooling rate of 10 DEG C/min, and 40-50 DEG C of water is added, with The heating rate of 10 DEG C/min is warming up to reflux state heat preservation mixing 10min, and 1h is stood after cooled to room temperature, is filtered, Obtained solid is dried at 75-80 DEG C, is finally sent into nano-level grinder, ground to obtain nano-titanium dioxide.
The titanium dioxide, crospovidone, hexamethylolmelamine pregnancy ether, anionic polyacrylamide, epoxy The mass ratio of soybean oil and water is 30-40:3-5:0.5-1:2-3:0.1-0.3:100-150.
The beneficial effects of the present invention are:
(1) it uses three step microwave treatment methods association with the operation that cools down in the preparatory phase of macroporous absorbent resin, is prepared shortening The resistant of high or low temperature of macroporous absorbent resin is improved while time;
(2) it by the pretreatment of water-soluble poloxamer, N hydroxymethyl acrylamide and hydrolysis of polymaleic anhydride, reduces The surface tension of macroporous absorbent resin increases the surface-active of macroporous absorbent resin, in favor of the modification of lower step;
(3) macroporous absorbent resin is carried out using isocyanuric acid three-glycidyl ester, nano-titanium dioxide and itaconic anhydride Modification increases its specific surface area, enhances its adsorption activity;
(4) made macroporous absorbent resin reaches 17mg/g or more to the adsorbance of isoflavones, through 60% methanol solution The efficient desorption of isoflavones is able to achieve after flushing, desorption efficiency reaches 98.5% or more, and the purity of made isoflavones reaches To 60% or more, therefore the macroporous absorbent resin is suitable for efficiently separating for isoflavones.
Specific embodiment:
In order to be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, tie below Specific embodiment is closed, the present invention is further explained.
Embodiment 1
(1) 45 parts of styrene, 30 parts of hydrogenated rosins third preparation of macroporous absorbent resin: are proportionally added into 350 parts of water Olefin(e) acid glycerine ester, 15 parts of hydroxyethyl methacrylates, 40 parts of nanometer pore-foaming agents and 0.5 part of initiator, are sufficiently mixed rear Yu Chao It is ultrasonically treated 15min under acoustic frequency 40kHz, output power 200W, it is micro- under microwave frequency 2450MHz, output power 700W Wave handles 10min, and 30min is stood in 0-5 DEG C of environment, continues microwave treatment 10min after mixing, then in -5-0 DEG C 15min is stood in environment, microwave treatment 10min, gained mixed liquor are cooled down again with the cooling rate of 5 DEG C/min after mixing 1h is mixed to 0-5 DEG C of heat preservation, is then separated by solid-liquid separation mixed liquor, gained solid phase obtains Archon with 35-40 DEG C of warm water washing three times, Finally Archon is dried in vacuo at 60-65 DEG C to get macroporous absorbent resin;
(2) pretreatment of macroporous absorbent resin: into above-mentioned made 60 parts of macroporous absorbent resins be added 2 parts of poloxamers, 0.5 part of N hydroxymethyl acrylamide and 1 part of hydrolysis of polymaleic anhydride, and 65-70 DEG C of guarantor is warming up to the heating rate of 5 DEG C/min Temperature mixing 30min, then 30-35 DEG C of water of 3 times of weight is added into gained mixture, continue to heat up with the heating rate of 5 DEG C/min Keep the temperature mixing 15min to reflux state, then cooled to room temperature, filtering, gained resin sphere washes three times, finally in It is dried in vacuo at 60-65 DEG C;
(3) 3 parts of nano-titanium dioxides the modification of macroporous absorbent resin: are added into 10 parts of isocyanuric acid three-glycidyl esters With 0.15 part of itaconic anhydride, 115-120 DEG C of heat preservation mixing 15min is warming up to the heating rate of 5 DEG C/min, adds and is located in advance 60 parts of macroporous absorbent resins after reason, continue in 115-120 DEG C of heat preservation mixing 30min, after naturally cool to washing three after room temperature It is secondary, most it is dried in vacuo at 60-65 DEG C through gained resin sphere afterwards.
The preparation of nanometer pore-foaming agent: 5 parts of microcrystalline celluloses and 1 part of rilanit special are added into 50 parts of water, and is warming up to Reflux state heat preservation mixing 15min, after naturally cool to 5 parts of polyglutamic acids of addition and 0.5 part of poly dimethyl two after 40-45 DEG C Allyl ammonium chloride, stirring 30min form lotion, 0.5 part of sodium gluconate and 0.05 part of ferrocene are then added, be uniformly mixed Gained mixture is sent into spray dryer afterwards, particle is ground obtained by drying is made nanometer powder, finally by nanometer powder Add water that the lotion of solid content 30-35wt% is made to get nanometer pore-foaming agent.
The preparation of nano-titanium dioxide: 3 parts of crospovidone and 0.5 part of hexamethylol three are added into 40 parts of titanium dioxide Poly cyanamid pregnancy ether is first warming up to 120-125 DEG C of heat preservation with the heating rate of 5 DEG C/min and mixes 30min, add 3 parts of yin from Sub- polyacrylamide and 0.2 part of epoxidized soybean oil continue the heat preservation mixing 30min at 120-125 DEG C, and gained mixture is with 10 DEG C/cooling rate of min is cooled to 40-50 DEG C, and 40-50 DEG C of 150 parts of water is added, it is warming up to the heating rate of 10 DEG C/min Reflux state heat preservation mixing 10min, 1h is stood after cooled to room temperature, is filtered, and obtained solid is dried at 75-80 DEG C, Finally it is sent into nano-level grinder, it is ground to obtain nano-titanium dioxide.
Embodiment 2
(1) 50 parts of styrene, 35 parts of hydrogenated rosins third preparation of macroporous absorbent resin: are proportionally added into 350 parts of water Olefin(e) acid glycerine ester, 15 parts of hydroxyethyl methacrylates, 40 parts of nanometer pore-foaming agents and 0.5 part of initiator, are sufficiently mixed rear Yu Chao It is ultrasonically treated 15min under acoustic frequency 40kHz, output power 200W, it is micro- under microwave frequency 2450MHz, output power 700W Wave handles 10min, and 30min is stood in 0-5 DEG C of environment, continues microwave treatment 10min after mixing, then in -5-0 DEG C 15min is stood in environment, microwave treatment 10min, gained mixed liquor are cooled down again with the cooling rate of 5 DEG C/min after mixing 1h is mixed to 0-5 DEG C of heat preservation, is then separated by solid-liquid separation mixed liquor, gained solid phase obtains Archon with 35-40 DEG C of warm water washing three times, Finally Archon is dried in vacuo at 60-65 DEG C to get macroporous absorbent resin;
(2) 2 parts of poloxamers, 1 pretreatment of macroporous absorbent resin: are added into above-mentioned made 65 parts of macroporous absorbent resins Part N hydroxymethyl acrylamide and 0.5 part of hydrolysis of polymaleic anhydride, and 65-70 DEG C of guarantor is warming up to the heating rate of 5 DEG C/min Temperature mixing 30min, then 30-35 DEG C of water of 3 times of weight is added into gained mixture, continue to heat up with the heating rate of 5 DEG C/min Keep the temperature mixing 15min to reflux state, then cooled to room temperature, filtering, gained resin sphere washes three times, finally in It is dried in vacuo at 60-65 DEG C
(3) 5 parts of nano-titanium dioxides the modification of macroporous absorbent resin: are added into 10 parts of isocyanuric acid three-glycidyl esters With 0.15 part of itaconic anhydride, 115-120 DEG C of heat preservation mixing 15min is warming up to the heating rate of 5 DEG C/min, adds and is located in advance 65 parts of macroporous absorbent resins after reason, continue in 115-120 DEG C of heat preservation mixing 30min, after naturally cool to washing three after room temperature It is secondary, most it is dried in vacuo at 60-65 DEG C through gained resin sphere afterwards.
The preparation of nanometer pore-foaming agent: 10 parts of microcrystalline celluloses and 2 parts of rilanit specials are added into 50 parts of water, and are warming up to Reflux state heat preservation mixing 15min, after naturally cool to 5 parts of polyglutamic acids of addition and 0.5 part of poly dimethyl two after 40-45 DEG C Allyl ammonium chloride, stirring 30min form lotion, 0.5 part of sodium gluconate and 0.05 part of ferrocene are then added, be uniformly mixed Gained mixture is sent into spray dryer afterwards, particle is ground obtained by drying is made nanometer powder, finally by nanometer powder Add water that the lotion of solid content 30-35wt% is made to get nanometer pore-foaming agent.
The preparation of nano-titanium dioxide: 5 parts of crospovidone and 0.5 part of hexamethylol three are added into 40 parts of titanium dioxide Poly cyanamid pregnancy ether is first warming up to 120-125 DEG C of heat preservation with the heating rate of 5 DEG C/min and mixes 30min, add 2 parts of yin from Sub- polyacrylamide and 0.2 part of epoxidized soybean oil continue the heat preservation mixing 30min at 120-125 DEG C, and gained mixture is with 10 DEG C/cooling rate of min is cooled to 40-50 DEG C, and 40-50 DEG C of 150 parts of water is added, it is warming up to the heating rate of 10 DEG C/min Reflux state heat preservation mixing 10min, 1h is stood after cooled to room temperature, is filtered, and obtained solid is dried at 75-80 DEG C, Finally it is sent into nano-level grinder, it is ground to obtain nano-titanium dioxide.
Embodiment 3
(1) 50 parts of styrene, 35 parts of hydrogenated rosins third preparation of macroporous absorbent resin: are proportionally added into 350 parts of water Olefin(e) acid glycerine ester, 15 parts of hydroxyethyl methacrylates, 40 parts of nanometer pore-foaming agents and 0.5 part of initiator, are sufficiently mixed rear Yu Chao It is ultrasonically treated 15min under acoustic frequency 40kHz, output power 200W, it is micro- under microwave frequency 2450MHz, output power 700W Wave handles 10min, and 30min is stood in 0-5 DEG C of environment, continues microwave treatment 10min after mixing, then in -5-0 DEG C 15min is stood in environment, microwave treatment 10min, gained mixed liquor are cooled down again with the cooling rate of 5 DEG C/min after mixing 1h is mixed to 0-5 DEG C of heat preservation, is then separated by solid-liquid separation mixed liquor, gained solid phase obtains Archon with 35-40 DEG C of warm water washing three times, Finally Archon is dried in vacuo at 60-65 DEG C to get macroporous absorbent resin;
(4) 2 parts of poloxamers, 1 pretreatment of macroporous absorbent resin: are added into above-mentioned made 65 parts of macroporous absorbent resins Part N hydroxymethyl acrylamide and 0.5 part of hydrolysis of polymaleic anhydride, and 65-70 DEG C of guarantor is warming up to the heating rate of 5 DEG C/min Temperature mixing 30min, then 30-35 DEG C of water of 3 times of weight is added into gained mixture, continue to heat up with the heating rate of 5 DEG C/min Keep the temperature mixing 15min to reflux state, then cooled to room temperature, filtering, gained resin sphere washes three times, finally in It is dried in vacuo at 60-65 DEG C
(5) 5 parts of nano-titanium dioxides the modification of macroporous absorbent resin: are added into 10 parts of isocyanuric acid three-glycidyl esters With 0.15 part of itaconic anhydride, 115-120 DEG C of heat preservation mixing 15min is warming up to the heating rate of 5 DEG C/min, adds and is located in advance 65 parts of macroporous absorbent resins after reason, continue in 115-120 DEG C of heat preservation mixing 30min, after naturally cool to washing three after room temperature It is secondary, most it is dried in vacuo at 60-65 DEG C through gained resin sphere afterwards.
The preparation of nanometer pore-foaming agent: 10 parts of microcrystalline celluloses and 2 parts of rilanit specials are added into 50 parts of water, and are warming up to Reflux state heat preservation mixing 15min, after naturally cool to 5 parts of polyglutamic acids of addition and 0.5 part of poly dimethyl two after 40-45 DEG C Allyl ammonium chloride, stirring 30min form lotion, 0.5 part of sodium gluconate and 0.05 part of ferrocene are then added, be uniformly mixed Gained mixture is sent into spray dryer afterwards, particle is ground obtained by drying is made nanometer powder, finally by nanometer powder Add water that the lotion of solid content 30-35wt% is made to get nanometer pore-foaming agent.
Reference examples 1
(1) 50 parts of styrene, 35 parts of hydrogenated rosins third preparation of macroporous absorbent resin: are proportionally added into 350 parts of water Olefin(e) acid glycerine ester, 15 parts of hydroxyethyl methacrylates, 40 parts of isooctane and 0.5 part of initiator, in supersonic frequency after being sufficiently mixed It is ultrasonically treated 15min under rate 40kHz, output power 200W, at microwave under microwave frequency 2450MHz, output power 700W 10min is managed, and stands 30min in 0-5 DEG C of environment, continues microwave treatment 10min after mixing, then in -5-0 DEG C of environment Middle standing 15min, microwave treatment 10min, gained mixed liquor are cooled to 0- with the cooling rate of 5 DEG C/min again after mixing 5 DEG C of heat preservations mix 1h, are then separated by solid-liquid separation mixed liquor, and gained solid phase obtains Archon with 35-40 DEG C of warm water washing three times, finally Archon is dried in vacuo at 60-65 DEG C to get macroporous absorbent resin;
(2) 2 parts of poloxamers, 1 pretreatment of macroporous absorbent resin: are added into above-mentioned made 65 parts of macroporous absorbent resins Part N hydroxymethyl acrylamide and 0.5 part of hydrolysis of polymaleic anhydride, and 65-70 DEG C of guarantor is warming up to the heating rate of 5 DEG C/min Temperature mixing 30min, then 30-35 DEG C of water of 3 times of weight is added into gained mixture, continue to heat up with the heating rate of 5 DEG C/min Keep the temperature mixing 15min to reflux state, then cooled to room temperature, filtering, gained resin sphere washes three times, finally in It is dried in vacuo at 60-65 DEG C
(3) 5 parts of nano-titanium dioxides the modification of macroporous absorbent resin: are added into 10 parts of isocyanuric acid three-glycidyl esters With 0.15 part of itaconic anhydride, 115-120 DEG C of heat preservation mixing 15min is warming up to the heating rate of 5 DEG C/min, adds and is located in advance 65 parts of macroporous absorbent resins after reason, continue in 115-120 DEG C of heat preservation mixing 30min, after naturally cool to washing three after room temperature It is secondary, most it is dried in vacuo at 60-65 DEG C through gained resin sphere afterwards.
The preparation of nano-titanium dioxide: 5 parts of crospovidone and 0.5 part of hexamethylol three are added into 40 parts of titanium dioxide Poly cyanamid pregnancy ether is first warming up to 120-125 DEG C of heat preservation with the heating rate of 5 DEG C/min and mixes 30min, add 2 parts of yin from Sub- polyacrylamide and 0.2 part of epoxidized soybean oil continue the heat preservation mixing 30min at 120-125 DEG C, and gained mixture is with 10 DEG C/cooling rate of min is cooled to 40-50 DEG C, and 40-50 DEG C of 150 parts of water is added, it is warming up to the heating rate of 10 DEG C/min Reflux state heat preservation mixing 10min, 1h is stood after cooled to room temperature, is filtered, and obtained solid is dried at 75-80 DEG C, Finally it is sent into nano-level grinder, it is ground to obtain nano-titanium dioxide.
Reference examples 2
(1) 50 parts of styrene, 35 parts of hydrogenated rosins third preparation of macroporous absorbent resin: are proportionally added into 350 parts of water Olefin(e) acid glycerine ester, 15 parts of hydroxyethyl methacrylates, 40 parts of isooctane and 0.5 part of initiator, in supersonic frequency after being sufficiently mixed It is ultrasonically treated 15min under rate 40kHz, output power 200W, at microwave under microwave frequency 2450MHz, output power 700W 10min is managed, and stands 30min in 0-5 DEG C of environment, continues microwave treatment 10min after mixing, then in -5-0 DEG C of environment Middle standing 15min, microwave treatment 10min, gained mixed liquor are cooled to 0- with the cooling rate of 5 DEG C/min again after mixing 5 DEG C of heat preservations mix 1h, are then separated by solid-liquid separation mixed liquor, and gained solid phase obtains Archon with 35-40 DEG C of warm water washing three times, finally Archon is dried in vacuo at 60-65 DEG C to get macroporous absorbent resin;
(2) 2 parts of poloxamers, 1 pretreatment of macroporous absorbent resin: are added into above-mentioned made 65 parts of macroporous absorbent resins Part N hydroxymethyl acrylamide and 0.5 part of hydrolysis of polymaleic anhydride, and 65-70 DEG C of guarantor is warming up to the heating rate of 5 DEG C/min Temperature mixing 30min, then 30-35 DEG C of water of 3 times of weight is added into gained mixture, continue to heat up with the heating rate of 5 DEG C/min Keep the temperature mixing 15min to reflux state, then cooled to room temperature, filtering, gained resin sphere washes three times, finally in It is dried in vacuo at 60-65 DEG C
(3) 5 parts of nano-titanium dioxides the modification of macroporous absorbent resin: are added into 10 parts of isocyanuric acid three-glycidyl esters With 0.15 part of itaconic anhydride, 115-120 DEG C of heat preservation mixing 15min is warming up to the heating rate of 5 DEG C/min, adds and is located in advance 65 parts of macroporous absorbent resins after reason, continue in 115-120 DEG C of heat preservation mixing 30min, after naturally cool to washing three after room temperature It is secondary, most it is dried in vacuo at 60-65 DEG C through gained resin sphere afterwards.
Embodiment 4
Equivalent embodiment 1, embodiment 2, embodiment 3, reference examples 1 and the made macroporous absorbent resin of reference examples 2 are used for Amount and isolating and purifying with batch isoflavones extracting solution, and the commercially available macroporous absorbent resin HP-20 of equivalent is set as reference examples 3。
The preparation of refined solution to be separated: being centrifuged after isoflavones ethanol extract is refrigerated 48h, and take supernatant, on Then clear liquid concentration, then the degreasing after refrigerating for 24 hours adjust pH value to neutrality to get purifying to be separated with 5mol/L hydrochloric acid solution Liquid;
Isoflavones isolates and purifies: glass adsorption column is packed into after macroporous absorbent resin plus equivalent amount of water are sufficiently soaked In, then pass through adsorption column by equivalent and with batch refined solution to be separated, rinses macropore using 60% methanol solution after the completion of absorption Resin is adsorbed, until the mass percent of isoflavones is lower than 0.5% in outflow solution, and after drying by gained eluent The powder rich in isoflavones is made, measures macroporous absorbent resin in the adsorbance of isoflavones, desorption efficiency and powder The purity of isoflavones, measurement result are as shown in table 1.
The treatment effect of the made macroporous absorbent resin of table 1
Figure BDA0001262451170000091
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention.The technology of the industry Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this The principle of invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these changes Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its Equivalent thereof.

Claims (5)

1. a kind of isoflavones isolates and purifies the preparation method with macroporous absorbent resin, it is characterised in that: preparation method packet Include following steps:
(1) preparation of macroporous absorbent resin: Xiang Shuizhong is proportionally added into styrene, hydrogenated rosin acrylic acid glycerine ester, methyl Hydroxy-ethyl acrylate, nanometer pore-foaming agent and initiator, it is ultrasonic under supersonic frequency 40kHz, output power 200W after being sufficiently mixed 15min, the microwave treatment 10min under microwave frequency 2450MHz, output power 700W are handled, and is stood in 0-5 DEG C of environment 30min continues microwave treatment 10min after mixing, 15min is then stood in -5-0 DEG C of environment, after mixing again Microwave treatment 10min, gained mixed liquor is cooled to 0-5 DEG C of heat preservation mixing 1h with the cooling rate of 5 DEG C/min, then by mixed liquor It being separated by solid-liquid separation, gained solid phase obtains Archon with 35-40 DEG C of warm water washing three times, finally Archon is dried in vacuo at 60-65 DEG C, Up to macroporous absorbent resin;
(2) poloxamer, N- methylol propylene the pretreatment of macroporous absorbent resin: are added into above-mentioned made macroporous absorbent resin Amide and hydrolysis of polymaleic anhydride, and 65-70 DEG C of heat preservation mixing 30min is warming up to the heating rate of 5 DEG C/min, then to gained 30-35 DEG C of water of 3 times of weight is added in mixture, continues to be warming up to reflux state heat preservation mixing with the heating rate of 5 DEG C/min 15min, then cooled to room temperature, filtering, gained resin sphere are washed three times, are finally dried in vacuo at 60-65 DEG C;
(3) modification of macroporous absorbent resin: nano-titanium dioxide and itaconic anhydride being added into isocyanuric acid three-glycidyl ester, It is warming up to 115-120 DEG C of heat preservation mixing 15min with the heating rate of 5 DEG C/min, adds macroporous absorption tree after pretreatment Rouge continues to mix 30min in 115-120 DEG C of heat preservation, after naturally cool to washing after room temperature three times, most afterwards through gained resin sphere It is dried in vacuo at 60-65 DEG C;
The nanometer pore-foaming agent is made of the raw material of following parts by weight: 5-10 parts of microcrystalline cellulose, 3-5 parts of polyglutamic acid, 1-2 parts of rilanit special, 0.5-1 parts of polydimethyl diallyl ammonium chloride, 0.5-1 parts of sodium gluconate, ferrocene 0.05- 0.1 part, 30-50 parts of water, preparation method are as follows: microcrystalline cellulose and rilanit special are added into water, and is warming up to reflux shape State heat preservation mixing 15min, after naturally cool to polyglutamic acid and polydimethyl diallyl ammonium chloride are added after 40-45 DEG C, It stirs 30min and forms lotion, sodium gluconate and ferrocene is then added, be after mixing sent into gained mixture spraying dry In dry machine, particle is ground obtained by drying is made nanometer powder, finally adds water to be made solid content 30-35wt%'s nanometer powder Lotion is to get nanometer pore-foaming agent;
The nano-titanium dioxide is the nano-powder made of after the modified processing of titanium dioxide, preparation method are as follows: to two Crospovidone and hexamethylolmelamine pregnancy ether are added in titanium oxide, is first warming up to the heating rate of 5 DEG C/min 120-125 DEG C of heat preservation mixes 30min, adds anionic polyacrylamide and epoxidized soybean oil, and continuation is protected at 120-125 DEG C Temperature mixing 30min, gained mixture is cooled to 40-50 DEG C with the cooling rate of 10 DEG C/min, and 40-50 DEG C of water is added, with 10 DEG C/heating rate of min is warming up to reflux state heat preservation mixing 10min, 1h is stood after cooled to room temperature, is filtered, institute It obtains solid to dry at 75-80 DEG C, finally be sent into nano-level grinder, it is ground to obtain nano-titanium dioxide.
2. isoflavones according to claim 1 isolates and purifies the preparation method with macroporous absorbent resin, feature exists In: water, styrene, hydrogenated rosin acrylic acid glycerine ester, hydroxyethyl methacrylate, nanometer pore-foaming agent in the step (1) Mass ratio with initiator is 300-400:45-50:30-35:15-20:40-45:0.5-1.
3. isoflavones according to claim 1 isolates and purifies the preparation method with macroporous absorbent resin, feature exists In: the quality of macroporous absorbent resin, poloxamer, N hydroxymethyl acrylamide and hydrolysis of polymaleic anhydride in the step (2) Than for 60-65:1-2:0.5-1:0.5-1.
4. isoflavones according to claim 1 isolates and purifies the preparation method with macroporous absorbent resin, feature exists In: the matter of macroporous absorbent resin, isocyanuric acid three-glycidyl ester, nano-titanium dioxide and itaconic anhydride in the step (3) Amount is than being 60-65:5-10:3-5:0.1-0.2.
5. isoflavones according to claim 1 isolates and purifies the preparation method with macroporous absorbent resin, feature exists In: the titanium dioxide, crospovidone, hexamethylolmelamine pregnancy ether, anionic polyacrylamide, epoxidized soybean oil Mass ratio with water is 30-40:3-5:0.5-1:2-3:0.1-0.3:100-150.
CN201710216749.3A 2017-04-05 2017-04-05 A kind of isoflavones isolates and purifies the preparation method with macroporous absorbent resin Active CN106964324B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710216749.3A CN106964324B (en) 2017-04-05 2017-04-05 A kind of isoflavones isolates and purifies the preparation method with macroporous absorbent resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710216749.3A CN106964324B (en) 2017-04-05 2017-04-05 A kind of isoflavones isolates and purifies the preparation method with macroporous absorbent resin

Publications (2)

Publication Number Publication Date
CN106964324A CN106964324A (en) 2017-07-21
CN106964324B true CN106964324B (en) 2019-10-15

Family

ID=59337062

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710216749.3A Active CN106964324B (en) 2017-04-05 2017-04-05 A kind of isoflavones isolates and purifies the preparation method with macroporous absorbent resin

Country Status (1)

Country Link
CN (1) CN106964324B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108847487A (en) * 2018-06-11 2018-11-20 四会市恒星智能科技有限公司 A kind of micropore anticreep agent for preventing chloride plate active material from falling off
CN108808012A (en) * 2018-06-11 2018-11-13 四会市恒星智能科技有限公司 A method of prevent lead-acid battery electrode plate active material from falling off
CN113145088B (en) * 2020-01-22 2023-03-28 中国科学院大连化学物理研究所 Hydrophilic integral material and preparation and application thereof
CN113244899A (en) * 2021-05-28 2021-08-13 重庆智伦电镀有限公司 Adsorption resin recycling process for industrial wastewater treatment

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1349987A (en) * 2000-10-20 2002-05-22 中国食品发酵工业研究所 Soybean isoflavone and its prepn process with macroporous adsorption resin
CN101525324A (en) * 2009-04-03 2009-09-09 上海师范大学 Method for separating genistein monomer from daidzein monomer
CN103585254A (en) * 2013-11-22 2014-02-19 东北农业大学 Method for synchronously extracting soy isoflavone and soy saponine from hydrolysate of aqueous enzymatic method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1349987A (en) * 2000-10-20 2002-05-22 中国食品发酵工业研究所 Soybean isoflavone and its prepn process with macroporous adsorption resin
CN101525324A (en) * 2009-04-03 2009-09-09 上海师范大学 Method for separating genistein monomer from daidzein monomer
CN103585254A (en) * 2013-11-22 2014-02-19 东北农业大学 Method for synchronously extracting soy isoflavone and soy saponine from hydrolysate of aqueous enzymatic method

Also Published As

Publication number Publication date
CN106964324A (en) 2017-07-21

Similar Documents

Publication Publication Date Title
CN106964324B (en) A kind of isoflavones isolates and purifies the preparation method with macroporous absorbent resin
CN107029679B (en) For isolating and purifying vitamin B from fermentation liquid12Polymer adsorbing material
CN105949163A (en) Method for extracting and purifying anthocyanin in pomace of aronia melanocarpa
CN106008253B (en) A method of extracting high-purity ceramide from rice bran
CN103113195A (en) Novel method for rapidly preparing hydroxytyrosol
CN104817527A (en) Method for extracting anthocyanidin from pitaya peel
CN103467617A (en) Method for continuous counter-current ultrasonic extraction of high-purity astragalus polysaccharide
CN104926778A (en) Purple sweet potato anthocyanin extraction process
CN103535507A (en) Method for extracting soybean protein and purifying and recovering surface active agent
CN106866605A (en) A kind of highly effective extraction method of purple sweet potato anthocyanin
CN106220747A (en) Ultrasonic assistant Vacuum cavitation extracts Dendrobium officinale polysaccharide and the preparation technology of instant powder thereof
CN103012612A (en) Extraction method of wolfberry polysaccharide
CN107812121A (en) A kind of method that Polyphenols polyphenoils is extracted from rice bran
CN108014169A (en) A kind of preparation method and applications of kudzu root extract and/or kudzu root flavone
CN108578293A (en) A kind of environment-friendly type has the shampoo and preparation method thereof of anti-dandruff and itching-relieving efficacies
CN104068357B (en) A kind of preparation method of capsicum dietary fiber
CN105192604A (en) Full nutritional Chinese wolfberry juice containing superfine ground wolfberry seed powder and preparation method thereof
CN102302539A (en) Method for producing trifolium pratense L. isoflavones
CN108947988A (en) A method of extracting high purity puerarin from pueraria lobata
CN101983969B (en) Method of preparing ginkgo protein superfine powders
CN106176890A (en) A kind of method extracting triterpene saponin from Fructus Trichosanthis seed
CN108835635A (en) A method of antioxidant is extracted by grape pip
CN108782942A (en) A kind of production method of Instant soyabean protein powder
CN103585421A (en) Liver-nourishing and kidney-tonifying eucommia and preparation method thereof
CN104356249B (en) The preparation technology of a kind of high-purity Carnis Haliotidis polysaccharide and application thereof

Legal Events

Date Code Title Description
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant