Synthesis of liquid end hydroxy styrene-butadiene rubber
A hydroxy-terminated styrene-butadiene and liquid rubber technology, applied in the field of free radical polymerization, can solve the problems of low styrene content, severe reaction, difficult control, etc., and achieve the effects of less residual monomers, good color and low cost of raw materials
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Embodiment 1
[0015] Add 20% butadiene, styrene (butadiene / styrene is 75 / 25) 2.8Kg of monomer total amount in 50L stainless steel pressure-resistant polymerization kettle, industrial ethanol 2.635Kg, hydrogen peroxide (50%) 0.28Kg, ethanolamine 0.14Kg, dodecyl mercaptan 0.112Kg, start the reaction polymerization tank to stir, when the temperature rises to 125°C, turn on the high-precision metering pumps for butadiene, styrene and organic peroxide to reduce the remaining 80% The monomer, initiator, and solvent were divided into three parts on average, and the addition was completed within the first hour, the second hour, and the third hour respectively. After the addition was completed, the reaction was continued for 1 hour to end. Add 0.65Kg of the terminator sodium methylenediphthalene disulfonate to the crude polymer glue, and continue to stir and react. After the reaction is completed, wash with water and let it stand. After entering the desiccator for drying, add anti-aging agent and ant...
Embodiment 2
[0017] Add 20% butadiene, styrene (butadiene / styrene is 75 / 25) 2.8Kg of monomer total amount in 50L stainless steel pressure-resistant polymerization kettle, industrial ethanol 2.635Kg, hydrogen peroxide (50%) 0.28Kg, dodecyl mercaptan 0.112Kg, start the reaction polymerization tank to stir, when the temperature rises to 125°C, add the remaining 80% butadiene, styrene and initiator to the reaction tank continuously within 4 hours In the process, the addition was completed, and the reaction was continued for 1 hour until the end of the polymerization reaction. Process operation and aftertreatment method are with embodiment 1. The main physical properties of the polymer are: number average molecular weight 2626, hydroxyl value 0.756mmol / g, viscosity 15.6Pa.s, benzene knot 22.65%, dispersion index 2.89, average functionality 1.99.
Embodiment 3
[0019] Add 25% (butadiene / styrene is 75 / 25) 3.50Kg of total monomer in 50L stainless steel pressure-resistant polymerization kettle, industrial acetone 3.15Kg, hydrogen peroxide (23%) 0.76Kg, triethanolamine 0.018Kg , N-mercaptan 0.16Kg. Start the reaction polymerization tank to stir, heat up to 128°C, and the remaining 75% monomer, initiator, and solvent are fed in the same manner as in Example 1. After the addition was complete, the reaction was continued for 1 hour to end. The reaction was continued for 1 hour until the end of the polymerization reaction. Add 0.65Kg of terminator sodium methylenediphthalene disulfonate to the crude polymer glue, react at 100°C for half an hour, then wash with water, let it stand, and send it to a desiccator for drying, add anti-aging agent, anti-oxidant Additives such as additives are filtered through a filter to obtain a hydroxyl-terminated polybutadiene-styrene liquid polymer. Its main physical property indicators are: number average m...
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