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CN110885408B - A method for controlling the mechanical properties of acrylonitrile-based binary copolymerized high-strength hydrogels by molecular weight of cross-linking agent - Google Patents

A method for controlling the mechanical properties of acrylonitrile-based binary copolymerized high-strength hydrogels by molecular weight of cross-linking agent Download PDF

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CN110885408B
CN110885408B CN201811052059.XA CN201811052059A CN110885408B CN 110885408 B CN110885408 B CN 110885408B CN 201811052059 A CN201811052059 A CN 201811052059A CN 110885408 B CN110885408 B CN 110885408B
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刘文广
刘博�
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Tianjin University
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Abstract

The invention provides a method for regulating and controlling mechanical properties of acrylonitrile-based binary copolymerization high-strength hydrogel by utilizing molecular weight of a cross-linking agent, which can obtain the acrylonitrile-based binary copolymerization high-strength hydrogel with controllable mechanical strength by initiating the cross-linking polymerization of acrylonitrile and polyethylene glycol dimethacrylate with different molecular weights in dimethyl sulfoxide through free radicals. The mechanical strength of the hydrogel is regulated and controlled by regulating the molecular weight of the cross-linking agent, so that the hydrogel has universality in practical application, the performance of the hydrogel can be regulated according to different environments, and meanwhile, the water content of the hydrogel is regulated and controlled by regulating the molecular weight of the cross-linking agent, so that the purposes of controlling the mechanical strength and the water content of the hydrogel are achieved.

Description

Method for regulating and controlling mechanical properties of acrylonitrile-based binary copolymerization high-strength hydrogel by using molecular weight of cross-linking agent
Technical Field
The invention relates to the technical field of mechanical strength controllable hydrogel, in particular to a method for regulating and controlling the mechanical property of acrylonitrile-based binary copolymerization high-strength hydrogel by utilizing the molecular weight of a cross-linking agent.
Background
The conventional artificial hydrogel usually has the microscopic defects of low molecular chain density, small acting force between molecular chains, arbitrary cross-linked network structure formed in the gelling process and the like of a molecular-level high-molecular polymer, so that the hydrogel macroscopically has the serious defects of poor mechanical property, poor stability, poor stimulus responsiveness and the like, and the practical application of the hydrogel is greatly hindered.
The traditional high-strength hydrogel is complex in preparation process and relates to multi-step polymerization, and the synthesized hydrogel is single and uncontrollable in mechanical property and even cannot stably exist in a water environment, so that the hydrogel does not have universality in practical application.
Disclosure of Invention
The invention overcomes the defects in the prior art, and provides a method for regulating and controlling the mechanical property of acrylonitrile-based binary copolymerization high-strength hydrogel by using the molecular weight of a cross-linking agent.
The purpose of the invention is realized by the following technical scheme.
The method for regulating and controlling the mechanical property of acrylonitrile-based binary copolymerization high-strength hydrogel by utilizing the molecular weight of a cross-linking agent comprises the following steps:
step 1, adding acrylonitrile and a cross-linking agent polyethylene glycol dimethacrylate (PEGDMA) into dimethyl sulfoxide (DMSO), placing the mixture in a centrifugal tube for dissolving, swirling the mixture in the centrifugal tube until a clear solution is obtained, carrying out nitrogen bubbling on the solution at the room temperature of 20-25 ℃ for 8-12min to remove oxygen, and simultaneously adding an initiator Benzoyl Peroxide (BPO) and a promoter N, N-Dimethylaniline (DMA) for initiating system polymerization, wherein the mass ratio of the acrylonitrile to the cross-linking agent (PEGDMA) is (0.5-1.5) to 1, the total solid content is 25-35 wt% (the total solid content is the ratio of the total mass of all reactants to the total mass of all solvents), the Benzoyl Peroxide (BPO) is 1-3 wt% of the total mass of monomers and the cross-linking agent, and the N, N-Dimethylaniline (DMA) is 40-60 wt% of the mass of the Benzoyl Peroxide (BPO), the molecular weight of polyethylene glycol dimethacrylate (PEGDMA) is 2000-8000;
and 2, placing the reaction solution prepared in the step 1 in a mold consisting of a polymethyl methacrylate (PMMA) plate and a silica gel gasket for polymerization, wherein the reaction temperature is 20-30 ℃, the reaction time is 20-30 hours, taking out the gel after the reaction is finished, and soaking the gel in Phosphate Buffer Solution (PBS) at the temperature of 20-30 ℃ to replace the organic solvent and remove residual monomers and initiators, so as to obtain the strength-controllable binary copolymerization high-strength hydrogel.
In step 1, the mass ratio of acrylonitrile to the crosslinking agent is 1:1, and the total solid content is 28 to 32 wt%.
In step 1, Benzoyl Peroxide (BPO) accounts for 1-2 wt% of the total mass of the monomer and the cross-linking agent, and N, N-Dimethylaniline (DMA) accounts for 48-52 wt% of the mass of the Benzoyl Peroxide (BPO).
In the step 2, the temperature of the polymerization reaction is 24-28 ℃, and the time of the polymerization reaction is 22-26 h.
In the step 2, the length and width of the polymethyl methacrylate (PMMA) plate are 8-12cm, the thickness is 1-3mm, the thickness of the silica gel gasket is 0.5-2.5mm, and the soaking process is to replace Phosphate Buffer Solution (PBS) every 10-12h for 5-10 days.
As shown in FIG. 1, after cutting the gel into dumbbell type test pieces (effective length 10mm, width 2mm, thickness 0.5mm), the gel was stretched using a strain rate of 100mm/min to obtain a hydrogel having Young's modulus of 0.5 to 2.1MPa and tensile strength of 1.7 to 3.0MPa, indicating that the tensile properties of the hydrogel can be changed according to the change in molecular weight of the crosslinking agent.
As shown in FIG. 2, after the gel was prepared into a cylindrical sample (effective diameter 4.7mm, height 4mm), it was compressed at a strain rate of 10mm/min to obtain a hydrogel having a compression modulus of 1.4-3.5MPa and a compressive strength of 9.0-14.5MPa, indicating that the compression properties of the hydrogel could be changed according to the change in molecular weight of the crosslinking agent.
As shown in FIG. 3, the prepared columnar gel was soaked in PBS, and the water content of the hydrogel after equilibration was 65-85%, indicating that the water content of the hydrogel can be changed according to the change of the molecular weight of the cross-linking agent.
The invention has the beneficial effects that: the preparation method is simple, the mechanical property of the hydrogel can be changed by the simple method, and the controllability of the performance is realized; the hydrogel has high modulus and strength, and can stably exist in a water environment.
Drawings
FIG. 1 is a tensile stress-strain test chart of the hydrogel prepared by the present invention, wherein a is the molecular weight of the cross-linking agent 2000, b is the molecular weight of the cross-linking agent 4000, c is the molecular weight of the cross-linking agent 6000, and d is the molecular weight of the cross-linking agent 8000;
FIG. 2 is a graph of the compressive stress-strain test of the hydrogel prepared by the present invention, wherein a is the molecular weight of the cross-linking agent 2000, b is the molecular weight of the cross-linking agent 4000, c is the molecular weight of the cross-linking agent 6000, and d is the molecular weight of the cross-linking agent 8000;
FIG. 3 is a graph showing the equilibrium water content of the hydrogel prepared according to the present invention.
Detailed Description
The technical solution of the present invention is further illustrated by the following specific examples.
Example 1
Step 1, weighing 0.15g of polyethylene glycol dimethacrylate (PEGDMA, molecular weight 2000) by using an analytical balance, putting the weighed polyethylene glycol dimethacrylate into a 5ml centrifuge tube, measuring 0.7ml of DMSO by using a pipette gun to completely dissolve the polyethylene glycol dimethacrylate, adding 0.15ml of acrylonitrile, adding 0.006g of BPO, uniformly mixing the mixture again, and introducing nitrogen for 10min to remove oxygen.
And 2, adding 3 mu L of DMA (direct memory access) into the mixture, uniformly mixing, immediately adding the solution in the centrifugal tube into a mold consisting of a PMMA (polymethyl methacrylate) plate and a silica gel gasket by using a plastic dropper, sealing the opening by using a preservative film, placing the opening in a thermostat at 25 ℃ for 24 hours, and taking out the opening.
And 3, uncovering the mold, taking out the gel sheet, and soaking the gel sheet in Phosphate Buffered Saline (PBS) at 25 ℃. In the soaking process, PBS is replaced every 12h, and the soaking is carried out for 7 days so as to replace the organic solvent and remove residual monomers and the initiator.
Example 2
Step 1, weighing 0.2g of polyethylene glycol dimethacrylate (PEGDMA, molecular weight 4000) by using an analytical balance, putting the weighed polyethylene glycol dimethacrylate into a 5ml centrifuge tube, measuring 0.7ml of DMSO by using a pipette gun to completely dissolve the polyethylene glycol dimethacrylate, adding 0.1ml of acrylonitrile, adding 0.006g of BPO, uniformly mixing the mixture again, and introducing nitrogen for 12min to remove oxygen.
And 2, adding 3 mu L of DMA (direct memory access) into the mixture, uniformly mixing, immediately adding the solution in the centrifugal tube into a mold consisting of a PMMA (polymethyl methacrylate) plate and a silica gel gasket by using a plastic dropper, sealing the opening by using a preservative film, placing the opening in a thermostat at 20 ℃ for 30 hours, and taking out the opening.
And 3, uncovering the mold, taking out the gel sheet, and soaking the gel sheet in Phosphate Buffer Solution (PBS) at the temperature of 20 ℃. In the soaking process, PBS is required to be replaced every 11 hours, and the soaking is carried out for 5 days so as to replace the organic solvent and remove residual monomers and initiators.
Example 3
Step 1, weighing 0.13g of polyethylene glycol dimethacrylate (PEGDMA, molecular weight of 6000) by using an analytical balance, putting the weighed polyethylene glycol dimethacrylate into a 5ml centrifuge tube, measuring 0.7ml of DMSO by using a pipette gun to completely dissolve the polyethylene glycol dimethacrylate, adding 0.17ml of acrylonitrile, adding 0.006g of BPO, uniformly mixing the mixture again, and introducing nitrogen for 11min to remove oxygen.
And 2, adding 3 mu L of DMA (direct memory access) into the mixture, uniformly mixing, immediately adding the solution in the centrifugal tube into a mold consisting of a PMMA (polymethyl methacrylate) plate and a silica gel gasket by using a plastic dropper, sealing the opening by using a preservative film, placing the preservative film in a thermostat at 28 ℃ for 24 hours, and taking out the preservative film.
And 3, uncovering the mold, taking out the gel sheet, and soaking the gel sheet in Phosphate Buffered Saline (PBS) at 28 ℃. In the soaking process, PBS is replaced every 12h, and the soaking is carried out for 10 days so as to replace the organic solvent and remove residual monomers and the initiator.
Example 4
Step 1, weighing 0.15g of polyethylene glycol dimethacrylate (PEGDMA, molecular weight of 8000) by using an analytical balance, putting the weighed polyethylene glycol dimethacrylate into a 5ml centrifuge tube, measuring 0.7ml of DMSO by using a pipette gun to completely dissolve the polyethylene glycol dimethacrylate, adding 0.15ml of acrylonitrile, adding 0.006g of BPO, uniformly mixing the mixture again, and introducing nitrogen for 8min to remove oxygen.
And 2, adding 3 mu L of DMA (direct memory access) into the mixture, uniformly mixing, immediately adding the solution in the centrifugal tube into a mold consisting of a PMMA (polymethyl methacrylate) plate and a silica gel gasket by using a plastic dropper, sealing the opening by using a preservative film, placing the opening in a 30-DEG C incubator for 30 hours, and taking out.
And 3, uncovering the mold, taking out the gel sheet, and soaking the gel sheet in Phosphate Buffer Solution (PBS) at the temperature of 30 ℃. In the soaking process, PBS is required to be replaced every 11 hours, and the soaking is carried out for 6 days so as to replace the organic solvent and remove residual monomers and initiators.
The invention has been described in an illustrative manner, and it is to be understood that any simple variations, modifications or other equivalent changes which can be made by one skilled in the art without departing from the spirit of the invention fall within the scope of the invention.

Claims (10)

1.利用交联剂分子量调控丙烯腈基二元共聚高强度水凝胶力学性能的方法,其特征在于:按照下述步骤进行:1. utilize the method for crosslinking agent molecular weight regulation and control acrylonitrile-based binary copolymer high-strength hydrogel mechanical properties, it is characterized in that: carry out according to the following steps: 步骤1,将丙烯腈和交联剂聚乙二醇二甲基丙烯酸酯(PEGDMA)加入到二甲基亚砜(DMSO)中,置于离心管内溶解,涡旋离心管内混合物直至得到澄清溶液,通过在室温20-25℃下对上述溶液进行氮气鼓泡8-12min,除去氧气,同时加入引发剂过氧化苯甲酰(BPO)和促引发剂N,N-二甲基苯胺(DMA),用于引发体系聚合,其中,丙烯腈与交联剂(PEGDMA)的质量比为(0.5-1.5):1,总体固含量为25-35wt%,过氧化苯甲酰(BPO)为单体和交联剂总质量的1-3wt%,N,N-二甲基苯胺(DMA)为过氧化苯甲酰(BPO)质量的40-60wt%,聚乙二醇二甲基丙烯酸酯(PEGDMA)的分子量为2000-8000;Step 1, add acrylonitrile and cross-linking agent polyethylene glycol dimethacrylate (PEGDMA) into dimethyl sulfoxide (DMSO), dissolve in a centrifuge tube, vortex the mixture in the centrifuge tube until a clear solution is obtained, By bubbling the above solution with nitrogen at room temperature 20-25°C for 8-12min, the oxygen was removed, and the initiator benzoyl peroxide (BPO) and the pro-initiator N,N-dimethylaniline (DMA) were added simultaneously, It is used to initiate system polymerization, wherein the mass ratio of acrylonitrile to cross-linking agent (PEGDMA) is (0.5-1.5): 1, the overall solid content is 25-35wt%, and benzoyl peroxide (BPO) is the monomer and 1-3wt% of the total mass of the crosslinking agent, N,N-dimethylaniline (DMA) is 40-60wt% of the mass of benzoyl peroxide (BPO), polyethylene glycol dimethacrylate (PEGDMA) The molecular weight is 2000-8000; 步骤2,将步骤1制备得到的反应液置于由聚甲基丙烯酸甲酯(PMMA)板及硅胶垫片组成的模具内进行聚合,反应温度为20-30℃,反应时间为20-30h,反应结束后,取出凝胶,将其浸泡在20-30℃磷酸盐缓冲液(PBS)中,以置换出有机溶剂、除去残余单体和引发剂,得到强度可控二元共聚高强度水凝胶。In step 2, the reaction solution prepared in step 1 is placed in a mold composed of a polymethyl methacrylate (PMMA) plate and a silica gel gasket for polymerization, the reaction temperature is 20-30 ° C, and the reaction time is 20-30 h, After the reaction, take out the gel and soak it in phosphate buffered saline (PBS) at 20-30°C to replace the organic solvent, remove residual monomers and initiators, and obtain a high-strength hydrogel of binary copolymerization with controllable strength. glue. 2.根据权利要求1所述的利用交联剂分子量调控丙烯腈基二元共聚高强度水凝胶力学性能的方法,其特征在于:在步骤1中,丙烯腈与交联剂的质量比为1:1,总体固含量为28-32wt%。2. the method for utilizing the molecular weight of cross-linking agent to regulate and control the mechanical properties of acrylonitrile-based binary copolymerization high-strength hydrogel according to claim 1, is characterized in that: in step 1, the mass ratio of acrylonitrile and cross-linking agent is 1:1 with an overall solids content of 28-32 wt%. 3.根据权利要求1所述的利用交联剂分子量调控丙烯腈基二元共聚高强度水凝胶力学性能的方法,其特征在于:在步骤1中,过氧化苯甲酰(BPO)为单体和交联剂总质量的1-2wt%, N,N-二甲基苯胺(DMA)为过氧化苯甲酰(BPO)质量的48-52wt%。3. the method for utilizing crosslinking agent molecular weight to regulate and control the mechanical properties of acrylonitrile-based binary copolymer high-strength hydrogel according to claim 1, is characterized in that: in step 1, benzoyl peroxide (BPO) is a single 1-2 wt % of the total mass of the body and cross-linking agent, N,N-dimethylaniline (DMA) is 48-52 wt % of the mass of benzoyl peroxide (BPO). 4.根据权利要求1所述的利用交联剂分子量调控丙烯腈基二元共聚高强度水凝胶力学性能的方法,其特征在于:在步骤1中,N,N-二甲基苯胺(DMA)为过氧化苯甲酰(BPO)质量的48-52wt%。4. the method for utilizing the molecular weight of crosslinking agent to regulate and control the mechanical properties of acrylonitrile-based binary copolymerization high-strength hydrogel according to claim 1, is characterized in that: in step 1, N,N-dimethylaniline (DMA) ) is 48-52 wt% of the mass of benzoyl peroxide (BPO). 5.根据权利要求1所述的利用交联剂分子量调控丙烯腈基二元共聚高强度水凝胶力学性能的方法,其特征在于:在步骤2中,聚合反应的温度为24-28℃,聚合反应的时间为22-26h。5. the method for utilizing crosslinking agent molecular weight to regulate and control the mechanical properties of acrylonitrile-based binary copolymerization high-strength hydrogel according to claim 1, is characterized in that: in step 2, the temperature of polymerization is 24-28 ℃, The polymerization time is 22-26h. 6.根据权利要求1所述的利用交联剂分子量调控丙烯腈基二元共聚高强度水凝胶力学性能的方法,其特征在于:在步骤2中,聚甲基丙烯酸甲酯(PMMA)板的长度与宽度为8-12cm,厚度为1-3mm,硅胶垫片厚度0.5-2.5mm。6. the method for utilizing crosslinking agent molecular weight to regulate and control the mechanical properties of acrylonitrile-based binary copolymer high-strength hydrogel according to claim 1, is characterized in that: in step 2, polymethyl methacrylate (PMMA) plate The length and width are 8-12cm, the thickness is 1-3mm, and the thickness of the silicone gasket is 0.5-2.5mm. 7.根据权利要求1所述的利用交联剂分子量调控丙烯腈基二元共聚高强度水凝胶力学性能的方法,其特征在于:在步骤2中,浸泡过程为每隔10-12h更换一次磷酸盐缓冲液(PBS),共浸泡5-10天。7. the method for adjusting the mechanical properties of acrylonitrile-based binary copolymerization high-strength hydrogel according to claim 1, is characterized in that: in step 2, the soaking process is to replace once every 10-12h Phosphate buffered saline (PBS) for 5-10 days. 8.如权利要求1-7任一所述的利用交联剂分子量调控丙烯腈基二元共聚高强度水凝胶力学性能的方法制备得到的丙烯腈基二元共聚高强度水凝胶,其特征在于:丙烯腈基二元共聚高强度水凝胶杨氏模量为0.5-2.1MPa,拉伸强度为1.7-3.0MPa。8. the acrylonitrile-based binary copolymerization high-strength hydrogel prepared by the method for adjusting the mechanical properties of acrylonitrile-based binary copolymerization high-strength hydrogels using the molecular weight of the crosslinking agent as described in any of claims 1-7, which It is characterized in that the Young's modulus of acrylonitrile-based binary copolymer high-strength hydrogel is 0.5-2.1 MPa, and the tensile strength is 1.7-3.0 MPa. 9.如权利要求1-7任一所述的利用交联剂分子量调控丙烯腈基二元共聚高强度水凝胶力学性能的方法制备得到的丙烯腈基二元共聚高强度水凝胶,其特征在于:丙烯腈基二元共聚高强度水凝胶压缩模量为1.4-3.5MPa,压缩强度为9.0-14.5MPa。9. the acrylonitrile-based binary copolymerization high-strength hydrogel prepared by the method for controlling the mechanical properties of the acrylonitrile-based binary copolymerization high-strength hydrogel using the molecular weight of the cross-linking agent as described in any one of claims 1-7, its It is characterized in that the compressive modulus of the high-strength hydrogel of acrylonitrile-based binary copolymerization is 1.4-3.5MPa, and the compressive strength is 9.0-14.5MPa. 10.如权利要求1-7任一所述的利用交联剂分子量调控丙烯腈基二元共聚高强度水凝胶力学性能的方法制备得到的丙烯腈基二元共聚高强度水凝胶,其特征在于:丙烯腈基二元共聚高强度水凝胶含水量为65-85%。10. The acrylonitrile-based binary copolymerization high-strength hydrogel prepared by the method for adjusting the mechanical properties of acrylonitrile-based binary copolymerization high-strength hydrogels by the molecular weight of the crosslinking agent according to any one of claims 1-7, which It is characterized in that the water content of the high-strength hydrogel of acrylonitrile-based binary copolymerization is 65-85%.
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