CN114591537B - Bio-based solvent-resistant plasticizer and preparation method thereof - Google Patents
Bio-based solvent-resistant plasticizer and preparation method thereof Download PDFInfo
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- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
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- C08K5/3467—Heterocyclic compounds having nitrogen in the ring having more than two nitrogen atoms in the ring
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Abstract
The invention discloses a bio-based solvent-resistant plasticizer and a preparation method thereof. The components of the bio-based solvent-resistant plasticizer prepared by the invention are matched with each other, so that the plasticizer has good plasticizing effect, and can improve the flexibility, tensile strength, extraction resistance and degradability of polyethylene resin, so that the polyethylene is endowed with good flame retardant property, and meanwhile, the prepared raw materials are environment-friendly and have good biocompatibility.
Description
Technical Field
The invention relates to the technical field of plastic product additives, in particular to a bio-based solvent-resistant plasticizer and a preparation method thereof.
Background
Over the past sixty years, plastics have become an indispensable novel material in the world and have wide application, and are widely applied to the fields of food packaging, medical supplies, electronic products, building materials and the like. The selection of the plasticizer plays a vital role in the performance and safety of the plastic articles. The plasticizing effect of several traditional plasticizers on different polymers is different, and besides good biocompatibility with polymer materials, other characteristics such as leaching resistance, flexibility and thermal stability and resistance to factors such as moisture and light are required to be considered when the plasticizers are selected. Different types of plasticizers are known, of which more than 300 are known, of which more than 50 are used for commercial purposes. The most commonly used plasticizers are generally esters of organic compounds. Solvent resistance is not ideal, and this performance disadvantage severely limits the use of bio-based plasticizer materials
Patent CN111087572a discloses a bio-based aqueous polyurethane resin with wear resistance, solvent resistance and water resistance and a preparation method thereof, wherein the bio-based aqueous polyurethane resin comprises: active hydrogen-containing polyols, long chain compounds having a dimerized fatty acid backbone, and the like. The bio-based aqueous polyurethane resin prepared by the invention has excellent performances of wear resistance, solvent resistance, water resistance and the like. The defects are that the mechanical property is poor, and the quality stability of the product is not guaranteed.
Patent CN113549199A relates to a bio-based solvent-resistant polyester polyol, polyurethane resin and a preparation process thereof, and belongs to the technical field of polyurethane polyols and preparation methods thereof. A bio-based solvent-resistant polyester polyol is characterized by comprising bio-based dihydric alcohol and bio-based dibasic acid, wherein the molar ratio of the bio-based dihydric alcohol to the bio-based dibasic acid is (1.05-1.2): 1. the invention provides a method for synthesizing bio-based solvent-resistant polyurethane polyol, which adopts a special production process of step polymerization to produce polyurethane resin, and the prepared polyurethane resin has excellent solvent resistance and high temperature resistance. However, the polyurethane resin has the defects of poor processability and high volatility in the preparation process.
Disclosure of Invention
Aiming at the problems of poor mechanical property and processability, large pollution and solvent intolerance in the prior art, the invention aims to provide a preparation method of a bio-based solvent-resistant plasticizer with simple method, environment-friendly raw materials and low dissolution rate.
In order to achieve the above object, the present invention is realized by the following technical scheme:
the bio-based solvent-resistant plasticizer is modified isosorbide dioleate, tri (ethyl butyrate) isocyanurate and tetrabutylammonium chloride, wherein the mass ratio of the bio-based solvent-resistant plasticizer to the tetrabutylammonium chloride is 1:2 to 4:0.1 to 0.3.
The addition of tetrabutylammonium chloride endows more branched structures in the plasticizer molecules, a large number of polar acid ester structures improve the compatibility with a resin matrix, and the plasticizer with more branched structures has good compatibility with the resin, so that the plasticizer is not easy to diffuse into the medium, and has better extraction resistance in the polar solvent. The water is a polar solvent, the solubility of the bio-based solvent-resistant plasticizer in water is high, the mass loss rate of the plasticizer in water is high, the sample can be used as an auxiliary agent in lipophilic packaging materials and other non-hydrophilic resin products, and the good hydrophilicity is easy to degrade in the natural environment where the plasticizer product exists in a large amount of water.
The preparation method of the isosorbide dioxilate comprises the following steps:
s1, mixing and heating oleic acid and isosorbide, adding a catalyst, heating and reacting, cooling after the reaction is finished, adding a sodium hydroxide aqueous solution, continuously heating and reacting, collecting a supernatant after the reaction is finished, washing with water, and drying to obtain the isosorbide dioleate;
s2, mixing and heating the isosorbide dioleate with a catalyst, adding formic acid and hydrogen peroxide aqueous solution, heating for reaction, collecting an organic phase after the reaction is finished, washing with water, and drying to obtain the isosorbide dioxilate.
Preferably, the preparation method of the isosorbide diepoxide comprises the following steps:
s1, mixing 50-100 g of oleic acid with 10-30 g of isosorbide, heating to 120-150 ℃ under the atmosphere of nitrogen after uniformly mixing, adding 0.1-1 g of catalyst, continuously heating to 130-160 ℃ for reacting for 7-10 h, cooling to 20-30 ℃ after the reaction is finished, adding 5-10 mL of 10-20 wt% sodium hydroxide aqueous solution, heating to 40-70 ℃ for reacting for 30-60 min, centrifuging for 10-20 min after the reaction is finished, collecting supernatant, washing the supernatant with water for 2-3 times, and carrying out vacuum distillation on the supernatant at 60-80 ℃ for 10-30 min after the washing is finished to obtain the isosorbide dioleate;
s2, mixing 50-100 g of isosorbide dioleate with 5-10 g of catalyst, heating to 50-70 ℃ after uniformly mixing, adding 10-20 g of formic acid and 40-70 g of 20-50wt% hydrogen peroxide aqueous solution, stirring and reacting for 5-10 h at 50-70 ℃, standing and separating to collect an organic phase, washing with water for 2-3 times, and carrying out vacuum distillation on the organic phase at 60-80 ℃ for 10-30 min after washing is completed, thus obtaining the isosorbide dioxilate.
Isosorbide is a bio-based diol with an aromatic-like structure, and can be esterified with carboxylic acid to obtain isosorbide, which has a chemical structure similar to that of phthalate plasticizers and good biodegradability. According to the invention, the isosorbide dioleate is obtained by carrying out esterification reaction on the isosorbide dioleate and oleic acid obtained by hydrolysis in vegetable oil, and because unsaturated double bonds are contained in an alkyl long chain of the oleic acid, and because the double bonds have high chemical activity, oxidation reaction is easy to occur in the processing and using processes, if the isosorbide dioleate is directly used as a plasticizer, the heat resistance and ageing resistance are poor, so that the epoxy isosorbide dioleate is obtained by carrying out epoxidation modification on the double bonds on the oleic acid, and has the functions of the plasticizer and the heat stabilizer.
The preparation method of the modified isosorbide dioleate comprises the following steps:
s1, mixing and heating oleic acid and isosorbide, adding a catalyst, heating and reacting, cooling after the reaction is finished, adding a sodium hydroxide aqueous solution, continuously heating and reacting, collecting a supernatant after the reaction is finished, washing with water, and drying to obtain the isosorbide dioleate;
s2, mixing and heating the isosorbide dioleate with a catalyst, adding formic acid and hydrogen peroxide aqueous solution, heating for reaction, collecting an organic phase after the reaction is finished, washing with water, and drying to obtain the isosorbide dioxilate;
s3, mixing and heating the di-epoxy isosorbide oleate and toluene, adding diethyl phosphate, toluene and a catalyst, stirring, heating for reaction, cooling after the reaction is finished, washing with water, and distilling to obtain diethyl phosphate di-oleic isosorbide;
and S4, mixing diethyl phosphate dioleate isosorbide, acetic anhydride and strong acid cation exchange resin, heating for reaction after uniform mixing, distilling after the reaction is finished, washing with saturated sodium bicarbonate aqueous solution, washing with water, and distilling after the washing is finished to obtain modified dioleate isosorbide.
Preferably, the preparation method of the modified isosorbide dioleate comprises the following steps:
s1, mixing 50-100 g of oleic acid with 10-30 g of isosorbide, heating to 120-150 ℃ under the atmosphere of nitrogen after uniformly mixing, adding 0.1-1 g of catalyst, continuously heating to 130-160 ℃ for reacting for 7-10 h, cooling to 20-30 ℃ after the reaction is finished, adding 5-10 mL of 10-20 wt% sodium hydroxide aqueous solution, heating to 40-70 ℃ for reacting for 30-60 min, centrifuging for 10-20 min after the reaction is finished, collecting supernatant, washing the supernatant with water for 2-3 times, and carrying out vacuum distillation on the supernatant at 60-80 ℃ for 10-30 min after the washing is finished to obtain the isosorbide dioleate;
s2, mixing 50-100 g of isosorbide dioleate with 5-10 g of catalyst, heating to 50-70 ℃ after uniformly mixing, adding 10-20 g of formic acid and 40-70 g of 20-50wt% hydrogen peroxide aqueous solution, stirring and reacting for 5-10 hours at 50-70 ℃, standing and separating to collect an organic phase, washing with water for 2-3 times, and carrying out vacuum distillation on the organic phase at 60-80 ℃ for 10-30 min after washing is completed to obtain the isosorbide dioxilate;
s3, mixing 50-100 g of diepoxy isosorbide oleate with 25-75 g of toluene, heating to 30-50 ℃ after uniformly mixing, adding 25-50 g of diethyl phosphate, 25-75 g of toluene and 0.5-1 g of catalyst, stirring for 20-30 min, heating to 70-80 ℃ for stirring and reacting for 4-8 h, cooling to 20-30 ℃ after the reaction is finished, washing with water for 2-3 times, and removing the solvent by vacuum distillation at 60-80 ℃ after the washing is finished to obtain diethyl phosphate diisosorbitol oleate;
s4, mixing 20-50 g of diethyl phosphate dioleate isosorbide, 10-40 g of acetic anhydride and 2-5 g of strong acid cation exchange resin, heating to 100-120 ℃ for reaction for 4-6 h after uniform mixing, distilling for 10-30 min at 80-100 ℃ after reaction, washing for 2-3 times by using saturated sodium bicarbonate aqueous solution, washing for 2-3 times by using water, and vacuum distilling for 20-40 min at 60-80 ℃ after washing is completed to obtain modified dioleate isosorbide.
Preferably, the catalyst in the step S1 is tetrabutyl titanate.
Preferably, the catalyst in the step S2 is a strong acid cation exchange resin.
Preferably, the catalyst in the step S3 is triphenylphosphine.
In order to further improve the functional characteristics of the di-epoxy isosorbide oleate, the epoxy group of the di-epoxy isosorbide oleate is further modified to increase the flame retardant property, and after the epoxy group of the di-epoxy isosorbide oleate is subjected to the epoxidation addition of the phosphate, a hydrophilic hydroxyl group is generated on an alkyl long chain of the oleic acid, and in order to reduce the hydrophilicity of the di-epoxy isosorbide oleate and improve the hydrolysis resistance, the heat resistance and the solvent extraction resistance of the di-epoxy isosorbide oleate, acetic anhydride and the hydroxyl group in the structure of the di-ethyl oleate are adopted to react to convert the hydroxyl group into an ester group, and the modified di-oleic acid isosorbide has better performance and better biosafety than the di-ethyl oleate due to the end capping effect of an acetyl group.
Meanwhile, the phosphate group in the modified isosorbide dioleate has excellent flame retardant property, and the phosphate group is mainly decomposed into a non-flammable liquid film of phosphoric acid through the phosphorus compound during combustion, the phosphoric acid can be further dehydrated to generate metaphosphoric acid, the metaphosphoric acid is further polymerized to generate polymetaphosphoric acid, in the process, a covering layer generated by the phosphoric acid plays a covering effect, the polymetaphosphoric acid is a very strong dehydrating agent, so that the polymer is dehydrated and carbonized, the mode of the combustion process of the polymer is changed, a carbon film is formed on the surface of the polymer to isolate air, and the stronger flame retardant effect is exerted; meanwhile, the phosphorus-containing flame retardant is also a free radical scavenger, and phosphorus-containing free radicals are formed when the polymer burns and can be combined with hydrogen atoms in a flame area to play a role in inhibiting flame, so that the aim of flame retardance is fulfilled.
The preparation method of the tri (ethyl butyrate) isocyanurate comprises the following steps: mixing tri (2-hydroxyethyl) isocyanurate, methylene dichloride and triethylamine, stirring and dissolving under nitrogen atmosphere, adding n-butyryl chloride for reaction, heating for reaction, washing an organic phase with water after the reaction is finished, drying after the washing is finished, and distilling to obtain the tri (ethyl butyrate) isocyanurate.
Preferably, the preparation method of the tri (ethyl butyrate) isocyanurate comprises the following steps: 10-20 g of tri (2-hydroxyethyl) isocyanurate, 100-150 mL of dichloromethane and 30-40 mL of triethylamine are mixed, stirred under nitrogen atmosphere for 10-20 min to be fully dissolved, 10-20 mL of n-butyryl chloride is added at 0-4 ℃ to react for 2-4 h, the temperature is heated to 40-50 ℃ to react for 30-60 min, after the reaction is finished, the organic phase is washed with water for 2-3 times, the washing is finished, anhydrous magnesium sulfate is used for drying to remove water, and vacuum distillation is carried out for 20-40 min at 40-60 ℃ to obtain the tri (ethyl butyrate-based) isocyanurate.
The tri (2-hydroxyethyl) isocyanurate has excellent chemical stability and flame retardance, and the structure of the tri (2-hydroxyethyl) isocyanurate contains a multifunctional triazine ring structure, wherein the active hydroxyethyl group connected with a nitrogen atom has strong reactivity, so that the tri (2-hydroxyethyl) isocyanurate is widely used as an auxiliary agent such as a plasticizer, an adhesive, a flame retardant and the like. Similar to pentaerythritol, all have a polyol structure, but have 3 more nitrogen atoms and have the functions of a carbon source and a gas source. The flame-retardant plasticizer tri (ethyl butyrate) isocyanurate with ester groups is prepared by reacting the flame-retardant plasticizer tri (ethyl butyrate) isocyanurate with n-butyryl chloride with tri (2-hydroxyethyl) isocyanurate through ester groups, the advantages of the flame-retardant plasticizer and the lipid plasticizer are combined, the structural symmetry is good, the polyethylene resin can be endowed with better plasticity and flame retardant performance, and meanwhile, the flame-retardant plasticizer has good environmental benefits.
The inventor finds that the shorter alkyl side chain of the tri (ethyl butyrate) isocyanurate has a plurality of advantages compared with the longer alkyl side chain through a large number of experiments, for example, under the condition of adding the plasticizer with the same mass, the carbon group content is more, the shorter alkyl side chain and the more carbonyl content can enhance the polarization interaction with the resin, and the plasticizing efficiency is improved. However, the disadvantage is that short alkyl side chains and lower molecular weights result in poor solvent extraction resistance.
Preferably, the bio-based environment-friendly plasticizer is prepared from the following components in percentage by mass: 1 to 5 of modified isosorbide dioleate and tris (ethyl butyrate) isocyanurate.
In the invention, the modified isosorbide dioleate has better compatibility with resin, can be used as a primary plasticizer, can enter an amorphous region of a molecular chain of the resin, can also enter a crystallization region of the molecular chain, has stronger plasticizing effect, and has insufficient lubrication degree; the tri (ethyl butyrate) isocyanurate has the advantages of high polarity, poor compatibility with resin and easy extraction, so that a certain problem exists in single use, and the modified isosorbide dioleate and the tri (ethyl butyrate) isocyanurate are matched for use, so that the plasticizing and lubricating balance effect is achieved, and particularly when the resin is added with various functional auxiliary agents, the tri (ethyl butyrate) isocyanurate has a good dispersing effect.
In addition to the synergistic plasticizing effect, the modified isosorbide dioleate and the tri (ethyl butyrate) isocyanurate have flame retardant groups, namely phosphorus-containing flame retardant groups and nitrogen-containing flame retardant groups. The phosphide, the nitride and the resin can form an expansion type flame-retardant system, wherein the phosphide can generate metaphosphoric acid with stronger acidity to provide an acid source in the combustion process, the nitride can generate a large amount of nitric oxide and ammonia gas to provide an air source in the combustion process, and the carbon skeleton of the modified isosorbide dioleate and the tri (ethyl butyrate) isocyanurate and the resin can provide a carbon source. When the intumescent flame retardant system is heated, the charring agent is dehydrated into charcoal under the action of the charring catalyst, the carbide forms a charcoal layer with a fluffy porous closed structure under the action of gas decomposed by the charring agent, once the charcoal layer is formed, the charcoal layer is incombustible, heat conduction between the polymer and a heat source can be weakened, gas diffusion is organized, and once the charcoal layer is burnt, enough fuel and oxygen are not obtained, and the burnt polymer can self-extinguish.
The invention also provides an application method of the bio-based solvent-resistant plasticizer, wherein any bio-based environment-friendly plasticizer is added into polyethylene.
Preferably, the weight of the bio-based solvent-resistant plasticizer is 10-50% of the weight of the polyethylene.
The invention also provides a preparation method of the polyethylene resin containing the bio-based solvent-resistant plasticizer, which comprises the following steps: firstly, 50-90 parts by mass of polyethylene and 10-50 parts by mass of bio-based solvent-resistant plasticizer are mixed, and then the mixture is poured into a double screw extruder to be melted for 2-3 times to prepare a blend; the blend is then crushed into pellets, which are then injection molded by an injection molding machine.
Preferably, the temperature of each zone of the twin-screw extruder is set to 140 to 150 ℃, 175 to 185 ℃, 190 to 200 ℃.
Preferably, the temperature of the charging barrel of the injection molding machine is 165-175 ℃ and the melting time is 5-10 min.
Compared with the prior art, the invention has the beneficial effects that:
1. the raw materials selected by the invention are green and environment-friendly, and meet the requirements of green chemistry, and the prepared bio-based solvent-resistant plasticizer has the advantages of high efficiency and low toxicity.
2. Compared with the isosorbide in the prior art, the modified isosorbide dioleate prepared by the invention has better plasticity, heat resistance and flame retardance.
3. The tri (ethyl butyrate) isocyanurate prepared by the method has good plasticity and flame retardance, and can improve the flexibility and strength of polyethylene.
4. The invention combines the modified isosorbide dioleate and the tri (ethyl butyrate) isocyanurate to achieve the balance effect of plasticization and lubrication, and simultaneously the modified isosorbide dioleate and the tri (ethyl butyrate) isocyanurate can form an expansion type flame-retardant system to improve the flame retardant property of the polyethylene.
5. The addition of tetrabutylammonium chloride improves the compatibility with the resin matrix, and endows the bio-based solvent-resistant plasticizer with excellent extraction resistance and degradability in polar solvents.
Detailed Description
The experimental methods used in the following examples are conventional methods unless otherwise specified.
Materials, reagents and the like used in the examples described below are commercially available unless otherwise specified.
The specific parameters of part of substances and instruments in the embodiment of the invention are as follows:
polyethylene, technical grade, available from south Beijing bermuda Biotechnology Co.
Oleic acid, analytically pure, purchased from Shanghai source leaf Biotechnology Co.
Isosorbide, 98% pure, was purchased from national pharmaceutical group chemical company, inc.
Strong acid cation exchange resin, model Dowex 50WX8, available from national pharmaceutical chemicals limited.
Tris (2-hydroxyethyl) isocyanurate, 98% pure, available from Sandeli chemical Co., ltd.
Tetrabutylammonium chloride, nantong Runfeng petrochemical Co., ltd., molecular weight: 277.92, cas No.: 1112-67-0.
Example 1
A method for preparing polyethylene resin containing bio-based solvent-resistant plasticizer, comprising the following steps:
respectively accurately weighing 70g of polyethylene and 30g of bio-based solvent-resistant plasticizer, uniformly mixing, pouring the mixture into a double-screw extruder, and melting for 2 times to prepare a blend, wherein the temperature of each region of the double-screw extruder is set to 140 ℃, 175 ℃, 190 ℃; the blend was then crushed into pellets by a powerful crusher, and the pellets were injection molded into polyethylene resin plastic sheets by a mini injection molding machine at a cylinder temperature of 165℃for a melting time of 5 minutes.
The bio-based solvent-resistant plasticizer is prepared from the following components in percentage by mass: 3 a mixture of modified isosorbide dioleate and tris (ethyl butyrate) isocyanurate.
The preparation method of the modified isosorbide dioleate comprises the following steps:
s1, mixing 100g of oleic acid with 30g of isosorbide, heating to 130 ℃ under the atmosphere of nitrogen after uniformly mixing, adding 0.5g of tetrabutyl titanate, continuously heating to 150 ℃ for reaction for 7 hours, cooling to 25 ℃ after the reaction is finished, adding 10mL of 15wt% sodium hydroxide aqueous solution, heating to 60 ℃ for reaction for 30 minutes, centrifuging for 15 minutes after the reaction is finished, collecting supernatant, washing the supernatant with water for 3 times, and carrying out vacuum distillation on the supernatant at 80 ℃ for 20 minutes after the washing is finished to obtain the isosorbide dioleate;
s2, mixing 100g of isosorbide dioleate with 10g of strong acid cation exchange resin, heating to 60 ℃ after uniform mixing, adding 15g of formic acid and 65g of 35wt% hydrogen peroxide aqueous solution, stirring at 60 ℃ for reaction for 6 hours, standing, separating and collecting an organic phase, washing with water for 3 times, and carrying out vacuum distillation on the organic phase at 80 ℃ for 20min after washing is completed to obtain the isosorbide dioxilate;
s3, mixing 100g of isosorbide dioxilate with 75g of toluene, heating to 40 ℃ after uniform mixing, adding 40g of diethyl phosphate, 75g of toluene and 0.5g of triphenylphosphine, stirring for 30min, heating to 75 ℃ and stirring for reaction for 4h, cooling to 25 ℃ after the reaction is finished, washing with water for 3 times, vacuum distilling at 80 ℃ after the washing is finished to remove the solvent to obtain diethyl phosphate isosorbide dioxilate,
s4, mixing 50g of diethyl phosphate dioleate isosorbide, 40g of acetic anhydride and 5g of strong acid cation exchange resin, heating to 120 ℃ for reaction for 4 hours after uniform mixing, distilling at 100 ℃ for 15 minutes after the reaction is finished, washing 3 times by using saturated sodium bicarbonate aqueous solution, washing 3 times by using water, and vacuum distilling at 80 ℃ for 30 minutes after the washing is finished to obtain modified dioleate isosorbide.
The preparation method of the tri (ethyl butyrate) isocyanurate comprises the following steps: mixing 20g of tris (2-hydroxyethyl) isocyanurate, 150mL of dichloromethane and 35mL of triethylamine, stirring under nitrogen atmosphere for 15min to fully dissolve, adding 20mL of n-butyryl chloride at 0 ℃, reacting for 2h, heating to 45 ℃ for 30min, washing an organic phase with water for 3 times after the reaction is finished, drying the washed organic phase with anhydrous magnesium sulfate to remove water, and carrying out vacuum distillation at 60 ℃ for 30min to obtain the tris (ethyl butyrate-based) isocyanurate.
Example 2
A method for preparing polyethylene resin containing bio-based solvent-resistant plasticizer, comprising the following steps:
respectively accurately weighing 70g of polyethylene and 30g of bio-based solvent-resistant plasticizer, uniformly mixing, pouring the mixture into a double-screw extruder, and melting for 2 times to prepare a blend, wherein the temperature of each region of the double-screw extruder is set to 140 ℃, 175 ℃, 190 ℃; the blend was then crushed into pellets by a powerful crusher, and the pellets were injection molded into polyethylene resin plastic sheets by a mini injection molding machine at a cylinder temperature of 165℃for a melting time of 5 minutes.
The bio-based solvent-resistant plasticizer is isosorbide diepoxide.
The preparation method of the isosorbide dioxilate comprises the following steps:
s1, mixing 100g of oleic acid with 30g of isosorbide, heating to 130 ℃ under the atmosphere of nitrogen after uniformly mixing, adding 0.5g of tetrabutyl titanate, continuously heating to 150 ℃ for reaction for 7 hours, cooling to 25 ℃ after the reaction is finished, adding 10mL of 15wt% sodium hydroxide aqueous solution, heating to 60 ℃ for reaction for 30 minutes, centrifuging for 15 minutes after the reaction is finished, collecting supernatant, washing the supernatant with water for 3 times, and carrying out vacuum distillation on the supernatant at 80 ℃ for 20 minutes after the washing is finished to obtain the isosorbide dioleate;
s2, mixing 100g of isosorbide dioleate with 10g of strong acid cation exchange resin, heating to 60 ℃ after uniform mixing, adding 15g of formic acid and 65g of 35wt% hydrogen peroxide aqueous solution, stirring at 60 ℃ for reaction for 6 hours, standing, separating and collecting an organic phase, washing with water for 3 times, and carrying out vacuum distillation on the organic phase at 80 ℃ for 20min after washing is completed, thus obtaining the isosorbide dioxilate.
Example 3
A method for preparing polyethylene resin containing bio-based solvent-resistant plasticizer, comprising the following steps:
respectively accurately weighing 70g of polyethylene and 30g of bio-based solvent-resistant plasticizer, uniformly mixing, pouring the mixture into a double-screw extruder, and melting for 2 times to prepare a blend, wherein the temperature of each region of the double-screw extruder is set to 140 ℃, 175 ℃, 190 ℃; the blend was then crushed into pellets by a powerful crusher, and the pellets were injection molded into polyethylene resin plastic sheets by a mini injection molding machine at a cylinder temperature of 165℃for a melting time of 5 minutes.
The bio-based solvent-resistant plasticizer is modified isosorbide dioleate.
The preparation method of the modified isosorbide dioleate comprises the following steps:
s1, mixing 100g of oleic acid with 30g of isosorbide, heating to 130 ℃ under the atmosphere of nitrogen after uniformly mixing, adding 0.5g of tetrabutyl titanate, continuously heating to 150 ℃ for reaction for 7 hours, cooling to 25 ℃ after the reaction is finished, adding 10mL of 15wt% sodium hydroxide aqueous solution, heating to 60 ℃ for reaction for 30 minutes, centrifuging for 15 minutes after the reaction is finished, collecting supernatant, washing the supernatant with water for 3 times, and carrying out vacuum distillation on the supernatant at 80 ℃ for 20 minutes after the washing is finished to obtain the isosorbide dioleate;
s2, mixing 100g of isosorbide dioleate with 10g of strong acid cation exchange resin, heating to 60 ℃ after uniform mixing, adding 15g of formic acid and 65g of 35wt% hydrogen peroxide aqueous solution, stirring at 60 ℃ for reaction for 6 hours, standing, separating and collecting an organic phase, washing with water for 3 times, and carrying out vacuum distillation on the organic phase at 80 ℃ for 20min after washing is completed to obtain the isosorbide dioxilate;
s3, mixing 100g of isosorbide dioxilate with 75g of toluene, heating to 40 ℃ after uniform mixing, adding 40g of diethyl phosphate, 75g of toluene and 0.5g of triphenylphosphine, stirring for 30min, heating to 75 ℃ and stirring for reaction for 4h, cooling to 25 ℃ after the reaction is finished, washing with water for 3 times, vacuum distilling at 80 ℃ after the washing is finished to remove the solvent to obtain diethyl phosphate isosorbide dioxilate,
s4, mixing 50g of diethyl phosphate dioleate isosorbide, 40g of acetic anhydride and 5g of strong acid cation exchange resin, heating to 120 ℃ for reaction for 4 hours after uniform mixing, distilling at 100 ℃ for 15 minutes after the reaction is finished, washing 3 times by using saturated sodium bicarbonate aqueous solution, washing 3 times by using water, and vacuum distilling at 80 ℃ for 30 minutes after the washing is finished to obtain modified dioleate isosorbide.
Example 4
A method for preparing polyethylene resin containing bio-based solvent-resistant plasticizer, comprising the following steps:
respectively accurately weighing 70g of polyethylene and 30g of bio-based solvent-resistant plasticizer, uniformly mixing, pouring the mixture into a double-screw extruder, and melting for 2 times to prepare a blend, wherein the temperature of each region of the double-screw extruder is set to 140 ℃, 175 ℃, 190 ℃; the blend was then crushed into pellets by a powerful crusher, and the pellets were injection molded into polyethylene resin plastic sheets by a mini injection molding machine at a cylinder temperature of 165℃for a melting time of 5 minutes.
The bio-based solvent resistant plasticizer is tris (ethyl butyrate) isocyanurate.
The preparation method of the tri (ethyl butyrate) isocyanurate comprises the following steps: mixing 20g of tris (2-hydroxyethyl) isocyanurate, 150mL of dichloromethane and 35mL of triethylamine, stirring under nitrogen atmosphere for 15min to fully dissolve, adding 20mL of n-butyryl chloride at 0 ℃, reacting for 2h, heating to 45 ℃ for 30min, washing an organic phase with water for 3 times after the reaction is finished, drying the washed organic phase with anhydrous magnesium sulfate to remove water, and carrying out vacuum distillation at 60 ℃ for 30min to obtain the tris (ethyl butyrate-based) isocyanurate.
Example 5
A method for preparing polyethylene resin containing bio-based solvent-resistant plasticizer, comprising the following steps:
respectively accurately weighing 70g of polyethylene and 30g of bio-based solvent-resistant plasticizer, uniformly mixing, pouring the mixture into a double-screw extruder, and melting for 2 times to prepare a blend, wherein the temperature of each region of the double-screw extruder is set to 140 ℃, 175 ℃, 190 ℃; the blend was then crushed into pellets by a powerful crusher, and the pellets were injection molded into polyethylene resin plastic sheets by a mini injection molding machine at a cylinder temperature of 165℃for a melting time of 5 minutes.
The bio-based solvent-resistant plasticizer is prepared from the following components in percentage by mass: 3:0.2 mixing of modified isosorbide dioleate, tris (ethyl butyrate) isocyanurate and tetrabutylammonium chloride.
The preparation method of the modified isosorbide dioleate comprises the following steps:
s1, mixing 100g of oleic acid with 30g of isosorbide, heating to 130 ℃ under the atmosphere of nitrogen after uniformly mixing, adding 0.5g of tetrabutyl titanate, continuously heating to 150 ℃ for reaction for 7 hours, cooling to 25 ℃ after the reaction is finished, adding 10mL of 15wt% sodium hydroxide aqueous solution, heating to 60 ℃ for reaction for 30 minutes, centrifuging for 15 minutes after the reaction is finished, collecting supernatant, washing the supernatant with water for 3 times, and carrying out vacuum distillation on the supernatant at 80 ℃ for 20 minutes after the washing is finished to obtain the isosorbide dioleate;
s2, mixing 100g of isosorbide dioleate with 10g of strong acid cation exchange resin, heating to 60 ℃ after uniform mixing, adding 15g of formic acid and 65g of 35wt% hydrogen peroxide aqueous solution, stirring at 60 ℃ for reaction for 6 hours, standing, separating and collecting an organic phase, washing with water for 3 times, and carrying out vacuum distillation on the organic phase at 80 ℃ for 20min after washing is completed to obtain the isosorbide dioxilate;
s3, mixing 100g of isosorbide dioxilate with 75g of toluene, heating to 40 ℃ after uniform mixing, adding 40g of diethyl phosphate, 75g of toluene and 0.5g of triphenylphosphine, stirring for 30min, heating to 75 ℃ and stirring for reaction for 4h, cooling to 25 ℃ after the reaction is finished, washing with water for 3 times, vacuum distilling at 80 ℃ after the washing is finished to remove the solvent to obtain diethyl phosphate isosorbide dioxilate,
s4, mixing 50g of diethyl phosphate dioleate isosorbide, 40g of acetic anhydride and 5g of strong acid cation exchange resin, heating to 120 ℃ for reaction for 4 hours after uniform mixing, distilling at 100 ℃ for 15 minutes after the reaction is finished, washing 3 times by using saturated sodium bicarbonate aqueous solution, washing 3 times by using water, and vacuum distilling at 80 ℃ for 30 minutes after the washing is finished to obtain modified dioleate isosorbide.
The preparation method of the tri (ethyl butyrate) isocyanurate comprises the following steps: mixing 20g of tris (2-hydroxyethyl) isocyanurate, 150mL of dichloromethane and 35mL of triethylamine, stirring under nitrogen atmosphere for 15min to fully dissolve, adding 20mL of n-butyryl chloride at 0 ℃, reacting for 2h, heating to 45 ℃ for 30min, washing an organic phase with water for 3 times after the reaction is finished, drying the washed organic phase with anhydrous magnesium sulfate to remove water, and carrying out vacuum distillation at 60 ℃ for 30min to obtain the tris (ethyl butyrate-based) isocyanurate.
Test example 1
Testing the plastic performance: the samples obtained in examples 1 to 5 and polyethylene as a control group to which no plasticizer was added were subjected to the following GB/T1040.3-2006 "determination of Plastic tensile Property 3: the tensile strength and the elongation at break of the thin plastic and the thin sheet are detected by a method of test conditions of the thin plastic and the thin sheet, and the tensile speed is 50mm/min; determination of deformation temperature under Plastic load according to GB/T1634.2-2019 part 1: the method in the general test method detects the load deformation temperature of the steel sheet, and uses a method A of bending stress of 1.8 MPa; the sample size was
120 mm. Times.10 mm. Times.3 mm. The same sample was repeated for 5 samples and the average was taken. The results are shown in Table 1:
table 1 plastics property test
| Tensile Strength (MPa) | Elongation at break (%) | |
| Example 1 | 36.7 | 140.3 |
| Example 2 | 30.1 | 109.4 |
| Example 3 | 32.7 | 122.4 |
| Example 4 | 33.6 | 124.7 |
| Example 5 | 36.2 | 138.9 |
| Control group | 27.6 | 90.5 |
The plastic performance can be obviously improved by adding the plasticizer into the plastic, and the performance of the plasticizer added in each embodiment can be judged through testing, so that the larger the tensile strength and the elongation at break are, the better the plasticizing performance of the plasticizer is.
From the results in table 1, it is known that the bio-based environment-friendly plasticizer prepared in the present invention can significantly improve the performance of polyethylene, wherein the tensile strength and elongation at break of example 1 are the highest, and the possible reason is that bio-based environment-friendly plasticizer molecules can be inserted between polyethylene resin molecular chains, thereby weakening the attraction between the molecular chains, preventing aggregation of the polyethylene molecular chains, and as a result, increasing the mobility of the polyethylene molecular chains, reducing the crystallinity of the polymer molecular chains, thereby significantly improving the tensile strength and elongation at break of the polyethylene resin; compared with the mechanical property of the embodiment 2, the mechanical property of the embodiment 3 is slightly improved, because the phosphate group is introduced to carry out acetyl encapsulation, the polarization interaction between the phosphate group and the polyethylene resin can be enhanced, and the plasticizing efficiency is improved, so that the mechanical property is improved; in the embodiment 4, the tri (ethyl butyrate) isocyanurate has smaller molecular weight, is easier to be inserted between polyethylene molecular chains, and can increase the intermolecular distance of the polymers, thereby playing a good plasticizing effect; in the embodiment 1, the modified isosorbide dioleate and the tri (ethyl butyrate) isocyanurate are compounded for use, and under the lubrication action of the tri (ethyl butyrate) isocyanurate, the macromolecule modified isosorbide dioleate is easier to penetrate between polyethylene molecular chains, so that the plasticization action of the modified isosorbide dioleate is better exerted, and the synergistic effect of the modified isosorbide dioleate and the tri (ethyl butyrate) isocyanurate is better.
Test example 2
Flame retardant performance test: the flame retardant properties of the plastics were characterized by the oxygen index of the plastics, and the oxygen index of the samples prepared in examples 1 to 5 and the polyethylene without plasticizer as a control group were measured according to the method of GB/T2406.2-2009, and the results are shown in Table 2.
TABLE 2 flame retardant Performance test
The flame retardant property of the independent polyethylene resin is poor, and the flame retardant property of the independent polyethylene resin can be improved by adding a plasticizer, so that the higher the oxygen index in the test is, the better the corresponding flame retardant property is.
As is clear from the results of table 2, the oxygen index of example 1 was the highest, indicating that the flame retardant effect was the best, and that example 2 did not significantly improve the flame retardant performance as compared to the control group, and that example 3 and example 4 significantly improved the flame retardant performance as compared to the control group. The possible reason for this is that the plasticizer prepared in example 2 does not introduce a flame retardant group and thus does not have a flame retardant effect; in the process, the coating layer formed by the phosphoric acid plays a covering role, and the polymetaphosphoric acid enables a strong dehydrating agent to dehydrate and carbonize the polymer, changes the mode of the combustion process of the polymer and forms a carbon film on the surface to isolate air, thereby exerting a stronger flame retardant effect; meanwhile, the phosphorus-containing flame retardant is also a free radical scavenger, phosphorus-containing free radicals are formed when the polymer burns and can be combined with hydrogen atoms in a flame area to play a role in inhibiting flame, so that the aim of flame retardance is fulfilled; the tris (ethyl butyrate) isocyanurate used in example 4 is a nitrogen flame retardant except for having plasticizing effect, and can undergo decomposition reaction when heated, and the decomposition products comprise nitrogen monoxide, nitrogen dioxide, ammonia and other nonflammable gases, wherein the ammonia is a main component, has the functions of cooling, absorbing heat, diluting oxygen and the like, plays the roles of absorbing heat and isolating oxygen, and can absorb a large amount of heat in the decomposition process, so that the temperature of the combustion surface of the flame retardant material is obviously reduced, and the flame retardant purpose is achieved; the two are matched to form an intumescent flame-retardant system in embodiment 1, when the system is heated, the charring agent is dehydrated into charcoal under the action of the charring catalyst, carbide forms a charcoal layer with a fluffy porous closed structure under the action of gas decomposed by the charring agent, once the carbide is formed, the carbide is incombustible, heat conduction between the polymer and a heat source can be weakened, gas diffusion is organized, and once the carbide is combusted, enough fuel and oxygen can not be obtained, the combusted polymer can be self-quenched, so that the flame-retardant system has a good flame-retardant effect.
Test example 3
Volatility test: the samples prepared in examples 1 to 5 and polyethylene as a control group to which no plasticizer was added were placed in a convection oven at 70℃for 24 hours and 72 hours, respectively, and their volatility was evaluated, and the sizes of the samples and control group were 120 mm. Times.10 mm. Times.3 mm, respectively. Then cooled to room temperature in a desiccator for 2 hours. Recording the weight change before and after the treatment, and recording the initial mass of the sample as m 0 The quality of the control group is m 1 The mass of the treated sample is m 2 The quality of the treated control group is m 3 The plasticizer volatility is calculated as follows:
volatility (%) = [ (m) 2 -m 0 )-(m 3 -m 1 )]/m 0 ×100％
The results are shown in Table 3.
Table 3 volatility test
| 24h volatility (%) | Volatility for 72h (%) | |
| Example 1 | 3.1 | 5.3 |
| Example 2 | 2.3 | 3.5 |
| Example 3 | 2.2 | 3.2 |
| Example 4 | 6.8 | 10.6 |
| Example 5 | 2.8 | 4.2 |
The plastic added with the plasticizer can leak in the use process, so that the plastic performance is poor, and the lower the volatilization rate is, the better the stability of the plasticizer is, and the lower the solubility is.
As can be seen from the results of table 3, the volatilization rate of example 4 was highest, the volatilization rate of example 1 was significantly lower than that of example 4, and the volatilization rates of examples 2 and 3 were lower. The possible reasons for this are that the volatility of the plasticizer is closely related to its molecular weight, solubility, compatibility and chemical structure, and that the tris (ethylbutyrate-based) isocyanurate used in example 4 is more volatile in the heat convection environment because of its lower molecular weight, and the relatively more polar bonds therein, and the worse modified isosorbide dioleate than polyethylene compatibility; in the embodiment 1, the modified isosorbide dioleate is used together with the tri (ethyl butyrate) isocyanurate, the modified isosorbide dioleate is inserted between polyethylene molecular chains, the tri (ethyl butyrate) isocyanurate plays a role in lubrication, and meanwhile, strong intermolecular forces and hydrogen bonds exist between the modified isosorbide dioleate and the tri (ethyl butyrate) isocyanurate, so that volatilization of the tri (ethyl butyrate) isocyanurate can be prevented to a certain extent, and the volatilization rate is remarkably reduced compared with that of the embodiment 4; examples 2 and 3 have long nonpolar alkyl chains, have good compatibility with polyethylene resins, and have large molecular weights and are not easily volatilized, so that the volatilization rates of both examples are low.
In conclusion, the components of the bio-based solvent-resistant plasticizer of the polyethylene resin prepared by the invention are matched with each other, so that the plasticizer has good plasticizing effect, and can improve the flexibility and tensile strength of the polyethylene resin, so that the polyethylene resin has good flame retardant property, and meanwhile, the preparation raw material is green and environment-friendly, has good biocompatibility, and can replace the traditional phthalate plasticizer.
Test example 4
Extraction resistance test
The determination of the immersion effect of plastics-liquid chemicals is carried out by the method of the reference standard ISO 175-2011. Selecting the uniform parts of the samples of the example 1 and the example 5, cutting the sample 9 sheets of 50mm multiplied by 100mm respectively, marking the cut sample, drying the sample at normal temperature for 6 hours, taking out the sample, placing the sample on an analytical balance, weighing the sample, and marking the mass of the sample as m 0 (accurate to 0.0001 g). Soaking the test sample in a grinding conical flask containing the same volume of solvent, wherein the solvent is cyclohexane, petroleum ether and distilled water respectively, placing the test sample on a test stand horizontally at room temperature, taking out the test sample after 24 hours, wiping the residual solvent on the surface of the test sample with filter paper, placing the test sample horizontally in a blast drying oven at 30 ℃ for full drying, weighing the test sample after drying and cooling, and recording the mass as m. Each solvent was tested three times and the average of the mass loss rates of the final results was sampled and the test results are shown in table 4. The calculation method of the mass loss rate of the PVC test piece refers to the following formula.
N＝(m 0 -m)/m 0 ×100％
N: mass loss rate of sample,%;
m 0 : the mass of the sample before volatilization, g;
m: and g, the mass of the sample after volatilization.
TABLE 4 extraction resistance test results
As can be seen from the test results in Table 4, the mass loss rate (%) of example 5 was lower in cyclohexane and petroleum ether, and higher in distilled water, probably because the addition of tetrabutylammonium chloride imparted more branched structures in the plasticizer molecule, a large amount of polar acid ester structures improved the compatibility with the resin matrix, and the plasticizer having more branched structures had good compatibility with the resin, so that the plasticizer was not easily diffused into the medium, and had better extraction resistance in the polar solvent. The water is a polar solvent, the solubility of the bio-based solvent-resistant plasticizer in water is high, the mass loss rate of the plasticizer in water is high, the sample can be used as an auxiliary agent in lipophilic packaging materials and other non-hydrophilic resin products, and the good hydrophilicity is easy to degrade in the natural environment where the plasticizer product exists in a large amount of water.
Claims (5)
1. A preparation method of a bio-based solvent-resistant plasticizer is characterized by comprising the following steps: the bio-based solvent-resistant plasticizer is modified isosorbide dioleate, tri (ethyl butyrate) isocyanurate and tetrabutylammonium chloride, wherein the mass ratio is 1:2 to 4:0.1 to 0.3;
the preparation method of the modified isosorbide dioleate comprises the following steps:
s1, mixing 50-100 g of oleic acid with 10-30 g of isosorbide, heating to 120-150 ℃ under the atmosphere of nitrogen after uniformly mixing, adding 0.1-1 g of catalyst, continuously heating to 130-160 ℃ for reacting for 7-10 h, cooling to 20-30 ℃ after the reaction is finished, adding 5-10 mL of 10-20 wt% sodium hydroxide aqueous solution, heating to 40-70 ℃ for reacting for 30-60 min, centrifuging for 10-20 min after the reaction is finished, collecting supernatant, washing the supernatant with water for 2-3 times, and carrying out vacuum distillation on the supernatant at 60-80 ℃ for 10-30 min after the washing is finished to obtain the isosorbide dioleate;
s2, mixing 50-100 g of isosorbide dioleate with 5-10 g of catalyst, heating to 50-70 ℃ after uniformly mixing, adding 10-20 g of formic acid and 40-70 g of 20-50wt% hydrogen peroxide aqueous solution, stirring and reacting for 5-10 hours at 50-70 ℃, standing and separating to collect an organic phase, washing with water for 2-3 times, and carrying out vacuum distillation on the organic phase at 60-80 ℃ for 10-30 min after washing is completed to obtain the isosorbide dioxilate;
s3, mixing 50-100 g of diepoxy isosorbide oleate with 25-75 g of toluene, heating to 30-50 ℃ after uniformly mixing, adding 25-50 g of diethyl phosphate, 25-75 g of toluene and 0.5-1 g of catalyst, stirring for 20-30 min, heating to 70-80 ℃ for stirring and reacting for 4-8 h, cooling to 20-30 ℃ after the reaction is finished, washing with water for 2-3 times, and removing the solvent by vacuum distillation at 60-80 ℃ after the washing is finished to obtain diethyl phosphate diisosorbitol oleate;
s4, mixing 20-50 g of diethyl phosphate dioleate isosorbide, 10-40 g of acetic anhydride and 2-5 g of strong acid cation exchange resin, heating to 100-120 ℃ for reaction for 4-6 h after uniform mixing, distilling for 10-30 min at 80-100 ℃ after reaction, washing for 2-3 times by using saturated sodium bicarbonate aqueous solution, washing for 2-3 times by using water, and vacuum distilling for 20-40 min at 60-80 ℃ after washing is completed to obtain modified dioleate isosorbide.
2. The method of preparing a bio-based solvent resistant plasticizer according to claim 1, wherein: the catalyst in the step S1 is tetrabutyl titanate; the catalyst in the step S2 is a strong acid cation exchange resin.
3. The method for preparing a bio-based solvent resistant plasticizer according to claim 1, wherein the catalyst in the step S3 is triphenylphosphine.
4. The method for preparing the bio-based solvent resistant plasticizer according to claim 1, wherein the method for preparing tris (ethylbutyrate) -isocyanurate comprises the following steps: 10-20 g of tri (2-hydroxyethyl) isocyanurate, 100-150 mL of dichloromethane and 30-40 mL of triethylamine are mixed, stirred under nitrogen atmosphere for 10-20 min to be fully dissolved, 10-20 mL of n-butyryl chloride is added at 0-4 ℃ to react for 2-4 h, the temperature is heated to 40-50 ℃ to react for 30-60 min, after the reaction is finished, the organic phase is washed with water for 2-3 times, the washing is finished, anhydrous magnesium sulfate is used for drying to remove water, and vacuum distillation is carried out for 20-40 min at 40-60 ℃ to obtain the tri (ethyl butyrate-based) isocyanurate.
5. A bio-based solvent resistant plasticizer prepared by the method of any one of claims 1 to 4.
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| CN105153462A (en) * | 2014-10-16 | 2015-12-16 | 中国林业科学研究院林产化学工业研究所 | Soybean-oil-based flame-retardant plasticizer, and preparation method and application thereof |
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