Method for producing triacrylic ester of alkoxylating trimethylolpropane
A technology of alkoxylated trimethylolpropane triacrylate and alkoxylated trimethylolpropane, which is applied in the field of alkoxylated trimethylolpropane triacrylate and can solve the problem of low color number, Problems such as low yield, to achieve the effect of reducing production cost, improving yield and preventing polymerization
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Embodiment 1
[0020] Take by weighing 600kg color number and be No. 60 EO3-TMP (addition degree is the ethoxylated trimethylolpropane of 3), slowly dissolve in 500kg toluene under the situation of stirring, then pump into 5000 liters of in the reactor. Turn on the steam switch slightly, and heat the reactor to 70-80°C. With stirring, 35 kg of benzenesulfonic acid, 15 kg of p-hydroxyanisole, 15 kg of activated carbon, and then a total of 500 kg of acrylic acid were added slowly. During the period, closely observe the situation of the reaction system to prevent the reaction system from performing violent reactions in advance.
[0021] Control the amount of steam used, and carefully raise the temperature of the reactor to 105-115°C, while feeding 1.2L / min of air. According to the situation of the esterification reaction, gradually add the toluene at the remaining 400kg normal temperature, so that the reaction will not be too violent. The water generated by the esterification reaction is tak...
Embodiment 2
[0027] Weigh 500kg of PO3-TMP (propoxylated trimethylolpropane with an addition degree of 3) whose color number is No. 20, slowly dissolve in 540kg toluene while stirring, and heat to the The trimethylolpropane is completely dissolved, and then pumped into a 5000-liter reactor. Turn on the steam switch slightly, and heat the reactor to 70-80°C. With stirring, 24 kg of p-toluenesulfonic acid, 8 kg of hydroquinone, 8 kg of copper sulphate, and then slowly a total of 360 kg of acrylic acid were added. During the period, closely observe the situation of the reaction system to prevent the reaction from proceeding prematurely and excessively.
[0028] Control the amount of steam used, and carefully raise the temperature of the reactor to 90-110°C, while feeding 0.6L / min of oxygen. According to the situation of the esterification reaction, gradually add the toluene at the remaining 600kg normal temperature, so that the reaction will not be too violent. The water generated by the e...
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