CN114350647B - Application of UCST type nonionic water-soluble polymer in immobilized glucose isomerase - Google Patents

Application of UCST type nonionic water-soluble polymer in immobilized glucose isomerase Download PDF

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CN114350647B
CN114350647B CN202111593054.XA CN202111593054A CN114350647B CN 114350647 B CN114350647 B CN 114350647B CN 202111593054 A CN202111593054 A CN 202111593054A CN 114350647 B CN114350647 B CN 114350647B
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glucose isomerase
soluble polymer
type nonionic
aam
nonionic water
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CN114350647A (en
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王赟
韩娟
吴嘉聪
宋永庆
毛艳丽
仰榴青
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Jiangsu University
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Abstract

The invention provides an application of UCST type nonionic water-soluble polymer in immobilized glucose isomerase, belonging to the technical field of immobilized enzyme; in the invention, UCST type nonionic water-soluble polymer which is polymerized with VBA block after the reversible addition-fragmentation chain transfer polymerization of acrylamide AAM and acrylonitrile AN is adopted to fix glucose isomerase; the UCST type nonionic water-soluble polymer can be used under the condition of existence of salt and has low hysteresis, and has good application on glucose isomerase.

Description

Application of UCST type nonionic water-soluble polymer in immobilized glucose isomerase
Technical Field
The invention belongs to the technical field of immobilized enzymes, and particularly relates to application of UCST type nonionic water-soluble polymers in immobilized glucose isomerase.
Background
Glucose Isomerase (GI), also known as xylose isomerase, can isomerise glucose into fructose, and is one of the key enzymes for preparing fructose-glucose syrup from starch in the food industry. Large scale conversion and utilization of glucose is closely related to the healthy life of contemporary people. With the development of economy and the maturation of the market, the consumption of High Fructose Corn Syrup (HFCS) increases year by year, and the market competition is also becoming vigorous. Currently, HFCS may be produced using GI isomerization. However, the method is difficult to mass-produce due to factors such as poor separation technology, low enzyme yield of the strain, and the like, and has the problems of high production cost and the like. The liquid enzyme preparation has the defects of incapability of recycling and low use efficiency.
Immobilization refers to a technique of limiting enzyme molecules to a certain spatial range by using a physical or chemical method to perform catalytic reaction. On the basis of keeping the activity of the enzyme molecules, the tolerance of the enzyme molecules to external factors is enhanced through immobilization, so that the enzyme can be recycled, and the production cost is reduced. The immobilized enzyme has rapid development and various kinds, and can be divided into adsorption, embedding, chemical crosslinking and covalent bonding methods, and the different methods have different lengths, so that the immobilized enzyme can be screened by combining the characteristics and the use environment of the enzyme. However, the existing immobilization technology has the problems of poor biocompatibility, fewer surface functional groups, difficult degradation in a natural state and the like.
Disclosure of Invention
Aiming at the defects in the prior art, the invention provides the application of UCST type nonionic water-soluble polymer in immobilized glucose isomerase. In the invention, UCST type nonionic water-soluble polymer which is polymerized with VBA block after the reversible addition-fragmentation chain transfer polymerization of acrylamide AAM and acrylonitrile AN is adopted to fix glucose isomerase; the UCST type nonionic water-soluble polymer can be used under the condition of existence of salt and has low hysteresis, and has good application on glucose isomerase.
The invention provides an application of UCST type nonionic water-soluble polymer in immobilized glucose isomerase.
Further, the chemical formula of the UCST type nonionic water-soluble polymer is mVBA x-b-P(AAMk-co-ANn, wherein m and b represent VBA and two monomers are combined in a block polymerization mode, wherein x represents the polymerization degree of polyphenyl boric acid, k and n respectively represent the polymerization degree of acrylamide and acrylonitrile in the polymer, the range of x, k and n is between 1 and 100, and P represents polymerization; the structural formula of the polymer is as follows:
Further, the high critical dissolution temperature of the UCST type nonionic water-soluble polymer can be adjusted within 0-100 ℃, and the phase transition temperature hysteresis is within 2 ℃.
Further, the application is as follows:
mVBA x-b-P(AAMk-co-ANn) is dissolved in water, glutaraldehyde is added and stirred, the precipitate is removed by low-temperature centrifugation after stirring, the precipitate and glucose isomerase are dissolved in phosphate buffer solution, immobilization reaction is carried out, and immobilized glucose isomerase is obtained by low-temperature centrifugation and washing after the reaction is finished.
Further, the mVBA x-b-P(AAMk-co-ANn) water and glutaraldehyde in a ratio of 30mg to 1ml:30mg.
Further, the ratio of the amount of the precipitate, glucose isomerase and phosphate buffer was 20mg:1mg:1mL.
Further, the stirring condition is 50 ℃ stirring reaction for 4 hours.
Further, the immobilization reaction conditions were stirring at 50℃for 2 hours.
Further, both low temperature centrifuges were at 4 ℃.
Compared with the prior art, the invention has the beneficial effects that:
In the invention, amino and boric acid groups existing in UCST type nonionic water-based polymer structure are used for realizing double-step immobilization, and the immobilization capacity and the mechanical strength are improved. The finished product (Glase) fixed into the granule has the characteristics of high activity, continuous production, automation and controllability, and the product is easy to separate and refine, thereby improving the quality of the product, reducing the production cost and powerfully promoting the development of the production of the high fructose syrup.
In the invention, UCST polymer is combined with glucose isomerase to construct immobilized enzyme, so that the immobilized enzyme can be separated, recovered and recycled under the regulation of external stimulus factors, and the stability of the enzyme is improved. The amino and boric acid groups in UCST-type nonionic water-soluble polymer can be activated by glutaraldehyde to realize double immobilization, so that the immobilization capacity and the mechanical strength are improved. The immobilized glucose isomerase prepared by the invention has better temperature stability than free enzyme, and the immobilized glucose isomerase still maintains more than seventy percent of activity after being circularly catalyzed for seven times.
Drawings
FIG. 1 is a schematic diagram of the synthesis of polymer mVBA x-b-P(AAMk-co-ANn); in the figure, step a is BTPA of the synthesis process, b is the synthesis process of the random monomer, and c is the synthesis process of the temperature-sensitive polymer mVBA x-b-P(AAMm-co-ANn).
FIG. 2 is a graph showing the immobilization of immobilized glucose isomerase prepared under different glutaraldehyde concentration (a), mVBA x-b-P(AAMk-co-ANn concentration (b), pH (c) and immobilization time (d).
FIG. 3 is a graph showing the effect of different conditions on immobilized glucose isomerase-catalyzed glucose isomerization; wherein a is a metal ion, b is a pH value, c is a temperature, and d is a time.
FIG. 4 is a graph showing the storage stability of immobilized glucose isomerase.
FIG. 5 is a graph showing the cycling stability of immobilized glucose isomerase.
Detailed Description
The invention will be further described with reference to the drawings and the specific embodiments, but the scope of the invention is not limited thereto.
Example 1: UCST-type polymer mVBA 6-b-P(AAM69-co-AN24)
Nonionic polymers mVBA 6-b-P(AAM69-co-AN24 with high critical solution temperatures are synthesized using a reversible addition-fragmentation chain transfer polymerization mechanism). Firstly, synthesizing a random monomer P (AAM 69-co-AN24), then, inserting a 4-vinyl phenylboronic acid block into the random monomer, wherein a detailed synthesis flow chart is shown in fig. 1, a is a BTPA synthesis process, b is a random monomer P (AAM 69-co-AN24), and c is a preparation process of a target polymer mVBA 6-b-P(AAM69-co-AN24). The method comprises the following specific steps:
(1) Preparation of Benzyl Trithiocarbonate (BTPA):
3.25g of potassium hydroxide is weighed and dissolved in 31.25ml of water and stirred, then 2.5ml of 3-mercaptopropionic acid and 4.5ml of carbon disulfide are dripped into the mixture, the mixture is reacted for 5 hours at room temperature in an oil bath, then 6g of benzyl bromide is dripped into the mixture within 1 hour, the temperature of the oil bath is raised to 85.0 ℃ and the mixture is refluxed for 12 hours. Naturally cooling the solution to room temperature after the reaction is finished, adding 70ml of chloroform and 6ml of concentrated hydrochloric acid into the reaction solution, and stirring while adding to obtain a mixed solution; the mixed solution was then rinsed with deionized water until the upper phase was clear, the upper phase was removed, the lower phase was concentrated to an orange oily liquid, 4ml of methylene chloride was added, the mixture was frozen in a refrigerator to reduce the temperature, the product was crystallized, and then filtered through a buchner funnel and the solids were washed with clear water to remove the solvent, finally obtaining a yellow powder sample.
(2) Preparation of initiator AIBN (azobisisobutyronitrile):
adding azobisisobutyronitrile into 50ml, heating to 50deg.C, stirring to dissolve AIBN (about 5 min), immediately filtering to remove insoluble substances, placing into refrigerator, crystallizing to obtain needle-like product, filtering, vacuum drying, drying at room temperature, and sealing and storing in refrigerator.
(3) Preparation of random monomer P (AAM 69-co-AN24):
BTPA 0.11g, AIBN 0.02g, acrylamide 2g and acrylonitrile 0.6g are weighed, put into a single-neck flask, added with 15ml DMF for ultrasonic treatment, discharged from air and reacted for 24 hours at 70 ℃ in an oil bath by a nitrogen protection device. After the reaction is finished, the mixture is placed into an ice water bath, cooled and poured into a beaker with the existing methanol, the dosage of the methanol is 10 times of that of DMF, the mixture is stirred and filtered to obtain solid, the solid is placed into a vacuum drying oven for drying, the solid is taken out, dissolved in a dialysis bag by adding water, dialyzed for 24 hours, and the yellow powdery solid, namely P (AAM 69-co-AN24) is obtained through freeze drying.
(4) MVBA 6-b-P(AAM69-co-AN24) preparation:
Weighing 0.38g of 4-vinylphenylboronic acid, putting the random monomer P (AAM 69-co-AN24) 0.75g,AIBN 0.1163g synthesized in the step (3) into a single-neck flask, adding 20ml of DMF (dimethyl formamide) into the flask, performing ultrasonic treatment, exhausting air, adding a nitrogen protection device, and reacting for 24 hours at 70 ℃. After the reaction is finished, the mixture is placed into an ice-water bath, cooled and poured into a beaker with the existing methanol, the dosage of the methanol is 10 times that of DMF, the mixture is centrifuged to obtain white solid, the white solid is placed for 8 hours, water is added for direct dialysis, and the white powdery solid is obtained through freeze drying, namely mVBA 6-b-P(AAM69-co-AN24.
Example 2: preparation of immobilized glucose isomerase
First, 0.3g mVBA 6-b-P(AAM69-co-AN24) was dissolved in 1mL of water, glutaraldehyde was added, and stirred at 45℃for 4 hours. Then, the precipitate was taken and washed with 1mL of deionized water at a low temperature of 4 ℃ for ten minutes, the operation was repeated twice to remove remaining glutaraldehyde, next, the precipitate and glucose isomerase were dissolved in 1mL of phosphate buffer solution at ph=8, the immobilization reaction was carried out at 50 ℃ for 2 hours, after that, the precipitate was taken and washed with 1mL of phosphate buffer solution at ph=8 at a low temperature of 4 ℃ for ten minutes, the operation was repeated twice to obtain immobilized glucose isomerase, and the cloud point after immobilization was 46.7 ℃.
Example 3: optimized condition exploration of immobilized glucose isomerase
In this example, different immobilized glucose isomerase was prepared by changing glutaraldehyde concentration, polymer concentration, pH and immobilization time, and optimizing conditions of immobilized glucose isomerase were explored by examining the properties.
(1) Optimization of glutaraldehyde concentration:
The preparation of immobilized glucose isomerase was as shown in example 2, with the following differences: the concentration of glutaraldehyde was modified to 10, 20, 30, 40, 50, 60mg, respectively, and then the immobilization amount of immobilized glucose isomerase prepared under the condition of adding glutaraldehyde of different concentrations was examined.
As shown in fig. 2a, continued increase of glutaraldehyde as glutaraldehyde concentration increases to saturation at glutaraldehyde concentration 30mg results in reduced affinity for the carrier substrate, and it can be seen that the immobilization is optimal at glutaraldehyde concentration 30 mg/mL.
(2) MVBA x-b-P(AAMk-co-ANn) optimization of concentration:
The preparation of immobilized glucose isomerase was as shown in example 2, with the following differences: mVBA x-b-P(AAMk-co-ANn) were modified to 10, 20, 30, 40, 50, 60mg, respectively, and then the immobilized glucose isomerase prepared under the condition of adding mVBA x-b-P(AAMk-co-ANn) at different concentrations was examined.
As shown in fig. 2b, with mVBA x-b-P(AAMk-co-ANn) concentration increase, the solids loading was first rising and then falling, with the maximum solids loading at 30mg/mL polymer. This is because mVBA x-b-P(AAMk-co-ANn) the limited enzyme-accessible site at 30mg/mL has reached saturation and cannot access more enzyme.
(3) Optimization of pH value:
The preparation of immobilized glucose isomerase was as shown in example 2, with the following differences: the pH values were modified to 5.0, 5.5, 6.0, 6.5, 7.0, 7.5, 8.0, 8.5, 9.0, 9.5, 10.0, respectively, and then the immobilization amounts of immobilized glucose isomerase prepared under the conditions of different pH values were examined.
As shown in fig. 2c, the pH change has little effect on the immobilized enzyme, but the immobilization is significantly higher than other pH values at ph=8, so we choose ph=8 as the optimal pH value.
(4) Optimization of immobilization time:
The preparation of immobilized glucose isomerase was as shown in example 2, with the following differences: the immobilization time was modified to 0.5, 1,2, 3, 4h, respectively, and then the immobilization amounts of immobilized glucose isomerase prepared under the conditions of different immobilization times were examined.
As shown in FIG. 2d, the immobilization time is 2h, and the immobilization amount is reduced after saturation, so that the immobilization time is preferably 2 h.
In summary, the optimal conditions for immobilized glucose isomerase are: glutaraldehyde concentration 30mg/mL, polymer concentration 30mg/mL, pH=8, time 2h.
Example 4: immobilized glucose isomerase catalyzed glucose isomerization
In this example, glucose (1.44 g) was used as an isomerization target, and the catalytic activity of immobilized glucose isomerase was evaluated. 200mg of the sample was dispersed in 10mL of glucose solution. Samples of 500. Mu.L were taken at set time intervals (10 min). The sample was subjected to high-phase liquid phase measurement for fructose content.
Fig. 3 is a graph showing the effect of different conditions on immobilized glucose isomerase to catalyze glucose isomerization, and fig. 3a shows that different metal ions have different catalytic effects on immobilized glucose isomerase, but Co 2+ ions can effectively promote glucose isomerization effect. Fig. 3b is the effect of PH on glucose isomerization, and it can be seen that fructose yields can be maximized at ph=7. FIG. 3c is the effect of temperature on isomerised fructose, it being seen that the fructose yield is highest at a temperature of 85 ℃. FIG. 3d shows the effect of time on fructose yield, and it was found that with increasing time, fructose yield increased, preferably 3h time was chosen in view of efficiency.
Fig. 4 shows the search of optimized conditions of the catalytic glucose isomerization experiment, and the research on metal ions, PH, temperature and catalytic time is used to obtain the optimized immobilization conditions, namely, the metal ions are Co 2+, ph=7 and the catalytic time is 3 hours at 85 ℃.
Example 5: storage stability and recycling stability of immobilized glucose isomerase
To investigate the storage stability of the synthesized UCST-GI and the free GI, the samples were stored at constant temperature in a refrigerator at 4℃and the enzyme activities were taken out and measured at fixed intervals, and a relative enzyme activity data map was obtained based on the optimal enzyme activities.
As shown in fig. 4, the immobilized GI was relatively more active than the free GI. These results clearly demonstrate that UCST-GI has good storage stability and great potential for industrial application.
Recycling stability is an important reference standard for measuring the success of enzyme immobilization. As shown in FIG. 5, the immobilized enzyme still has 76.53% relative enzyme activity after catalyzing glucose to repeat 10 times. In some cases, the enzyme activity is inevitably lost in the separation process, and the hydrogen bonding effect becomes weak with the increase of the cycle times, so that the immobilized enzyme is difficult to completely separate. Therefore, the immobilized glucose isomerase which is recycled for a plurality of times in the experiment can reduce the cost of industrial application.
The examples are preferred embodiments of the present invention, but the present invention is not limited to the above-described embodiments, and any obvious modifications, substitutions or variations that can be made by one skilled in the art without departing from the spirit of the present invention are within the scope of the present invention.

Claims (6)

1. The application of UCST type nonionic water-soluble polymer in immobilized glucose isomerase;
The chemical formula of the UCST type nonionic water-soluble polymer is mVBA x-b-P(AAMk-co-ANn), wherein m and b represent VBA and two monomers are combined in a block polymerization mode, wherein x represents the polymerization degree of polyphenyl boric acid, k and n respectively represent the polymerization degree of acrylamide and acrylonitrile in the polymer, the ranges of x, k and n are all 1-100, and P represents polymerization; the structural formula of the polymer is as follows:
The high critical dissolution temperature of the UCST type nonionic water-soluble polymer can be adjusted within 0-100 ℃, and the phase transition temperature hysteresis is within 2 ℃;
The application is as follows:
mVBA x-b-P(AAMk-co-ANn) is dissolved in water, glutaraldehyde is added and stirred, the precipitate is obtained by low-temperature centrifugation after stirring, the precipitate and glucose isomerase are dissolved in phosphate buffer solution and are subjected to immobilization reaction, and immobilized glucose isomerase is obtained by low-temperature centrifugation and washing after the reaction.
2. The use according to claim 1, wherein the dosage ratio of mVBA x-b-P(AAMk-co-ANn), water and glutaraldehyde is 30mg:1ml:30mg.
3. The use according to claim 1, characterized in that the ratio of the amount of precipitate, glucose isomerase and phosphate buffer is 20mg:1mg:1mL.
4. The use according to claim 1, wherein the stirring conditions are 50 ℃ stirring for 4 hours.
5. The use according to claim 1, wherein the immobilization reaction conditions are 50 ℃ stirring reaction for 2 hours.
6. Use according to claim 1, characterized in that both low-temperature centrifuges are centrifuges at 4 ℃.
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