CN103752288B - A kind of preparation method being applied to the adsorbent that rapamycin is separated - Google Patents

A kind of preparation method being applied to the adsorbent that rapamycin is separated Download PDF

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CN103752288B
CN103752288B CN201410035278.2A CN201410035278A CN103752288B CN 103752288 B CN103752288 B CN 103752288B CN 201410035278 A CN201410035278 A CN 201410035278A CN 103752288 B CN103752288 B CN 103752288B
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rapamycin
preparation
fluoro
adsorbent
pore
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CN103752288A (en
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王琪宇
张玲
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Jingjiang City Chengzhong Village Investment And Construction Co ltd
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Abstract

A kind of preparation method being applied to the adsorbent that rapamycin is separated.Invent a kind of preparation method being applied to the adsorbent that rapamycin is separated: in a kettle., squeeze into pure water, add a certain amount of dispersant, initator, methyl methacrylate/N, N-methylene-bisacrylamide/1, 1-bis-fluoro-2, 2-dichloroethylene/maleic acid, pore-foaming agent etc., be warming up to reaction temperature, question response terminates. dries, extracting pore-foaming agent, dry closing bag. the present invention introduces a small amount of 1 in polymerization, 1-bis-fluoro-2, 2-dichloroethylene, maleic acid is as comonomer, to improve the compatibility of resin and rapamycin, and resin matrix ground is high temperature resistant, the ability of acid and alkali corrosion, thus improve the intensity of polymer beads. to erythromycin good separating effect, by force selective.The introducing of fluoro-containing group, resin matrix corrosion resistance is strengthened, and spherome surface is protected, thus extends service life.

Description

A kind of preparation method being applied to the adsorbent that rapamycin is separated
Technical field
The present invention relates to a kind of preparation method of resin sorbent, particularly a kind of preparation method being applied to the adsorbent that rapamycin is separated.
Background technology
Rapamycin (Rapamycin, RAPA), has another name called sirolimus (Sirolimus), is a kind of Novel macrocyclic lactone immunodepressant.The molecular formula of RAPA is C51H79NO13, and molecular weight 991 is white crystalline solid, and fusing point is 183-185 DEG C, and lipophilicity is dissolved in the organic solvents such as methyl alcohol, ethanol, acetone, chloroform, atomic water-soluble, is dissolved in ether hardly.RAPA, by different cytokine receptor disabling signal conduction, blocks T lymphocyte and other cells process by G1 phase to the S phase, thus plays immunosuppressive effect.Along with the increase of organ transplant quantity, immunodepressant class medicine for reducing rejection after organ transplant also presents quick growth trend, the product that particularly rapamycin etc. are new is becoming organ transplant immunodepressant main product gradually, and as a kind of novel anti-rejection medicine, be that the preparation of raw material just goes on the market at home with rapamycin.Domesticly to start late due to drug level, this type of product technology construction cycle is longer, particularly the factor such as perfect not to the utmost of existing production technology, and the technology and the level of production that have had a strong impact on rapamycin improve, because production capacity is less, existing output still can not meet domestic demand.Current China rapamycin formulation relies on import to be main, and import volume presents the trend increased year by year.The preparation made for raw material with this product is after Chinese market listing, and produce market capacity is huge, and market prospects are noticeable.
CN102433364 provides a kind of technique of preparing rapamycin by using microbial fermentation method, wherein, comprises the following steps: first in slant medium, cultivate water suction strepto-, then transfers to cultivate in fresh seeds culture medium; By the bacterial strain cultivated through described seed culture medium according to 2% inoculum concentration be seeded in fresh fermentation medium and carry out fermented and cultured, obtain the zymotic fluid containing rapamycin, utilize the dissolubility difference of rapamycin in water and organic solvent, abstraction and purification is carried out to the zymotic fluid containing rapamycin.After rapamycin dissolving crude product, upper silicagel column carries out chromatographic purifying, wash-out is carried out with the hexane solution (acetone 30%) of acetone, collect the eluent containing rapamycin, rapamycin crystal is added as seed after concentrate eluant, concentrate is cooled to 0-5 DEG C, stir after 1 hour and leave standstill crystallization, the rapamycin product obtained that is recrystallized filters rear dry acquisition rapamycin finished product.
CN101133065 describes the rapamycin of purifying and the method for obtaining purified rapamycin, it comprises: (a) is having under suitable alkali existent condition, with trim,ethylchlorosilane process rapamycin in atent solvent, thus provide rapamycin 31,42-two-0-trimethyl silyl ether; B () filters the two-0-trimethyl silyl ether of rapamycin 31,42-; C () extracts the two-0-trimethyl silyl ether of rapamycin 31,42-in heptane; D () washs the two-0-trimethyl silyl ether of stripped rapamycin 31,42-; And (e) makes the two-0-trimethyl silyl ether deprotection of stripped thunder handkerchief mould 31,42-with acid, thus produce rapamycin.
The fermentation yield of rapamycin is low, and from zymotic fluid, the difficulty of separation and Extraction rapamycin is larger.The greatest drawback of existing technique is exactly that separative efficiency is lower, energy consumption is higher, contaminated wastewater is serious.Adopt resin absorption technique to be then expected to overcome these defects, but require the adsorption capacity of resin and relatively high to the selection removal ability of pigment, common polymeric adsorbent is difficult to reach this requirement.Usually, the polarity etc. of the specific area of resin, resin pore structure and resin is larger to organic Adsorption Effect.Rapamycin is low pole material, according to the principle of " analog absorption analog ", and should be better with macroporous resin adsorption effect that is nonpolar or low pole.Meanwhile, when polymeric adsorbent has under suitable aperture can guarantee the condition of solute molecule good diffusion, resin specific area is larger, and adsorbance is also larger.Have higher compared with the adsorbance of low pole macroporous absorbent resin to rapamycin of bigger serface.
Summary of the invention
Object be for from rapamycin separation of fermentative broth rapamycin to the basic demand of adsorption and separation material, provide a kind of preparation method of adsorbent being applied to rapamycin and being separated, simultaneously openly its preparation method.
In a kettle., squeeze into pure water, add a certain amount of dispersant, initator, methyl methacrylate/N, N-methylene-bisacrylamide/1, the monomers such as 1-bis-fluoro-2,2-dichloroethylene/maleic acid, pore-foaming agent etc., be warming up to reaction temperature, question response terminates. and to dry, extracting pore-foaming agent, dry closing bag. the present invention introduces a small amount of 1 in polymerization, 1-bis-fluoro-2,2-dichloroethylene, maleic acid as comonomer, to improve the compatibility of resin and rapamycin, and resin matrix ground is high temperature resistant, the ability of acid and alkali corrosion.
The invention provides a kind of preparation method being applied to the adsorbent that rapamycin is separated, realized by following steps: the preparation of step 1. aqueous phase
By weight, add 100 parts of pure water 0.5-2 part organic chemistry dispersant (preferably 0.5 part) in pressure reaction still, stir;
Described chemical dispersant is selected from polyvinyl alcohol, gelatin or CMC etc.
The preparation of step 2. oil phase
By weight, by 100 parts of methyl methacrylates, 30-100 part (preferably 70 parts) N, N-methylene-bisacrylamide, 3-10 part (preferably 6 parts) 1,1-bis-fluoro-2,2-dichloroethylene, 3-10 part (preferably 5 parts) maleic acid mixes, then adds 0.5-3 part peroxide initiator (preferably 2 parts), 10-40 part pore-foaming agent, stirs;
Step 3. suspension polymerization
Being added in step 1 to be equipped with by the oil-phase solution prepared in step 2 beaker prepares in the pressure reaction still of aqueous phase, and at 60-95 DEG C of reaction 7-20h, reaction terminates rear blowing, and washing microballoon is limpid to water, after oven dry, pore-foaming agent extracting is clean, obtains product.
Fluoro-2, the 2-dichloroethylene structural formulas of described in step 21,1-bis-are shown in formula (1), are commercially available prod, as 1,1-bis-fluoro-2, the 2-dichloroethylene products that Hangzhou Bao Kai biochemicals Co., Ltd produces.
CF 2=CCl 2(1)
Maleic acid structural formula described in step 2 is shown in formula (2), is commercially available prod, as the maleic acid product that Zhengzhou Tian Yao Science and Technology Ltd. produces.
HO 2CCH=CHCO 2H(2)
The preferred benzoyl peroxide of peroxide initiator described in step 2.
Pore-foaming agent described in step 2 is good solvent or poor solvent or mixed solvent, as white oil, and solvent naphtha, toluene etc., preferred toluene.
Beneficial effect of the present invention:
1): by the inventive method obtain a kind of be applied to rapamycin be separated adsorbent good to rapamycin compatibility, to rapamycin good separating effect, by force selective.
2) introducing of fluoro-containing group, resin matrix corrosion resistance is strengthened, and spherome surface is protected, thus extends service life.
Detailed description of the invention
Following examples are only further illustrate the present invention, are not restriction the scope of protection of the invention.
Embodiment 1
The preparation of step 1. aqueous phase
By weight, add 100 parts of pure water in pressure reaction still, 0.5 part of gelatin, stirs.
The preparation of step 2. oil phase
The oil phase component of following ratio is mixed in beaker, stirs;
Step 3. suspension polymerization
Being added in step 1 to be equipped with by the oil-phase solution prepared in step 2 prepares in the pressure reaction still of aqueous phase, and at 80 DEG C of reaction 14h, reaction terminates rear blowing, reaction terminates rear blowing, washing microballoon is limpid to water, after oven dry, pore-foaming agent extracting is clean, obtains product. be numbered W-1
Embodiment 2
The preparation of step 1. aqueous phase
By weight, add 100 parts of pure water in pressure reaction still, 1.5 parts of polyvinyl alcohol, stir.
The preparation of step 2. oil phase
The oil phase component of following ratio is mixed in beaker, stirs;
Step 3. suspension polymerization
Being added in step 1 to be equipped with by the oil-phase solution prepared in step 2 prepares in the pressure reaction still of aqueous phase, and at 60 DEG C of reaction 20h, reaction terminates rear blowing, reaction terminates rear blowing, washing microballoon is limpid to water, after oven dry, pore-foaming agent extracting is clean, obtains product. be numbered W-2
Embodiment 3
The preparation of step 1. aqueous phase
By weight, add 100 parts of pure water in pressure reaction still, 2 parts of CMCs, stir.
The preparation of step 2. oil phase
The oil phase component of following ratio is mixed in beaker, stirs;
Step 3. suspension polymerization
Being added in step 1 to be equipped with by the oil-phase solution prepared in step 2 beaker prepares in the pressure reaction still of aqueous phase, and at 95 DEG C of reaction 10h, reaction terminates rear blowing, reaction terminates rear blowing, washing microballoon is limpid to water, after oven dry, pore-foaming agent extracting is clean, obtains product. be numbered W-3
Embodiment 4
In step 2,1,1-bis-fluoro-2,2-dichloroethylene weight portions are 10, the other the same as in Example 1.Products obtained therefrom is numbered W-4.
Embodiment 5
In step 2,1,1-bis-fluoro-2,2-dichloroethylene weight portions are 3, the other the same as in Example 1.Products obtained therefrom is numbered W-5.
Embodiment 6
In step 2, maleic acid weight portion is 10, the other the same as in Example 1.Products obtained therefrom is numbered W-6.
Embodiment 7
In step 2, maleic acid weight portion is 3, the other the same as in Example 2.Products obtained therefrom is numbered W-7.
Comparative example 1
In step 2,1,1-bis-fluoro-2,2-dichloroethylene weight portions are 0, the other the same as in Example 1.Products obtained therefrom is numbered W-8
Comparative example 2
In step 2, maleic acid weight portion is 0, the other the same as in Example 1.Products obtained therefrom is numbered W-9
Comparative example 3
In step 2, maleic acid weight portion is 0, and other is with embodiment 8.Products obtained therefrom is numbered W-10
With FTIS, pressing potassium bromide troche does infrared spectrum analysis to synthesized each resin.Infrared spectrum from product: W1-W10 is at 1725cm -1near there is the carbonyl peak of ester group, at 3305cm -1near there is N-H stretching vibration peak, illustrate and introduce acrylamide group in the skeleton of resin; At 1250cm in the collection of illustrative plates of W1-W7, W9 sample -1near have CF 2, CF 3stretching vibration peak, 665cm -1near have CF 2cF 3absworption peak, illustrated 1,1-bis-fluoro-2,2-dichloroethylene exist; 720cm -1near there is cis C-H architectural feature peak, the existence of maleic acid (maleic acid) is described; So can determine that this patent product generates by methyl methacrylate cross-linking system and fluoro-2, the 2-dichloroethylene of 1,1-bis-, the polymer of maleic acid monomer copolymerization.
Embodiment 8
Accurately take each 5g of wet resin that pretreated embodiment 1-7 and comparative example 8-10 is obtained, be placed in 250mL tool plug ground triangular flask, precision adds people 100mL and extracts stoste, at room temperature vibrate triangular flask 5h, fully after absorption, filters, getting filtrate uses LC-10AD high performance liquid chromatograph to measure the concentration of rapamycin, compare with the measurement result extracting stoste, be calculated as follows adsorption capacity, in table 1:
Adsorbance (w/%)=[(extracting original liquid concentration-filter liquor concentration) x liquor capacity)/dried resin quality] x100%
Table 1: the polymeric adsorbent adsorption capacity list that this patent is obtained

Claims (1)

1. be applied to a preparation method for the adsorbent that rapamycin is separated, it is characterized in that comprising the following steps:
The preparation of step 1. aqueous phase
By weight, add 100 parts of pure water in a kettle., 0.5-2 part organic chemistry dispersant, stirs;
Described chemical dispersant is selected from polyvinyl alcohol, gelatin or CMC;
The preparation of step 2. oil phase
By weight, by 100 parts of methyl methacrylates, 30-100 part N, N-methylene-bisacrylamide, 3-10 part 1, fluoro-2, the 2-dichloroethylene of 1-bis-, 3-10 part maleic acid mixes, add 0.5-3 part peroxide initiator, 10-40 part pore-foaming agent again, stir;
Step 3. suspension polymerization
Being added to be equipped with by the oil-phase solution prepared in step 2 prepares in the reactor of aqueous phase, and at 70-100 DEG C of reaction 10-20h, reaction terminates rear blowing, and washing microballoon is limpid to water, after oven dry, pore-foaming agent extracting is clean, obtains product.
CN201410035278.2A 2014-01-22 2014-01-22 A kind of preparation method being applied to the adsorbent that rapamycin is separated Active CN103752288B (en)

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Publication number Priority date Publication date Assignee Title
CN104262358B (en) * 2014-09-29 2016-02-17 常州兰陵制药有限公司 Extract the method for rapamycin
CN105289545B (en) * 2015-11-30 2017-12-01 王琪宇 A kind of preparation of rapamycin separation adsorbent
CN105582901B (en) * 2015-12-21 2018-03-02 王金明 A kind of preparation of the adsorbent of long carbochain biatomic acid zymotic fluid
CN105597711B (en) * 2016-03-09 2018-11-23 徐州鸿丰高分子材料有限公司 A kind of preparation method of the adsorbent material of binary acid treating
CN105646801A (en) * 2016-03-09 2016-06-08 张玲 Preparation of octylphenol ethoxylate adsorbing material
CN105833854A (en) * 2016-06-13 2016-08-10 王金明 Preparation method of purified vanadium adsorption material
CN106268688A (en) * 2016-08-21 2017-01-04 王琪宇 A kind of preparation method of expoxy propane purification adsorbent

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