Preparation method of colorless pentalyn
A technology for rosin pentaerythritol ester and refined rosin is applied in the field of deep processing of rosin, which can solve the problems of high equipment and cost, and achieve the effects of improving the quality and yield of rosin, saving equipment and cost, and saving energy consumption.
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example 1
[0021] Example 1, take 1000kg of rosin in a dissolving tank, add 60kg of turpentine oil, heat up, stir, and fully dissolve. Filter the dissolved pine resin to remove mechanical impurities. The turpentine liquid is put into a distillation kettle for steam distillation at a distillation temperature of 140°C to separate high-grade turpentine. Raise the temperature to 170° C., carry out steam distillation under reduced pressure with a vacuum degree of 20 mmHg, and separate middle oil and heavy oil from turpentine. When the temperature is raised to 270°C and the vacuum degree is 5mmHg, refined rosin is produced by rectification under reduced pressure. The obtained refined rosin was directly put into the esterification reaction kettle, 1.1kg of catalyst and 93kg of pentaerythritol were added, and the esterification reaction was carried out at 270°C with a stirring speed of 50r / min and a reaction time of 8h. After the esterification reaction, vacuum distillation was carried out at ...
example 2
[0022] Example 2, take by weighing 1300kg of pine resin in a dissolving tank, add 120kg of turpentine medium oil, heat up, stir, and fully dissolve. Filter the dissolved pine resin to remove mechanical impurities. The turpentine liquid is put into a distillation kettle for steam distillation at a distillation temperature of 150°C to separate high-grade turpentine. Raise the temperature to 180° C., carry out steam distillation under reduced pressure with a vacuum degree of 15 mmHg, and separate middle oil and heavy oil from turpentine. When the temperature is raised to 250°C and the vacuum degree is 5mmHg, refined rosin is produced by rectification under reduced pressure. The obtained refined rosin was directly put into the esterification reaction kettle, 1.5kg of catalyst and 120kg of pentaerythritol were added, at 270°C, the stirring speed was 80r / min, the reaction time was 8h, and the esterification reaction was carried out. After the esterification reaction, vacuum distil...
example 3
[0023] Example 3, take by weighing 1300kg of turpentine in a dissolving tank, add 100kg of turpentine medium oil, heat up, stir, and fully dissolve. Filter the dissolved pine resin to remove mechanical impurities. The turpentine liquid is put into a distillation kettle for steam distillation at a distillation temperature of 150°C to separate high-grade turpentine. Raise the temperature to 180° C., carry out steam distillation under reduced pressure with a vacuum degree of 30 mmHg, and separate middle oil and heavy oil from turpentine. When the temperature is raised to 270°C and the vacuum degree is 5mmHg, refined rosin is produced by rectification under reduced pressure. The obtained refined rosin was directly put into the esterification reaction kettle, 1.6kg of catalyst and 120kg of pentaerythritol were added, at 270°C, the stirring speed was 70r / min, the reaction time was 8h, and the esterification reaction was carried out. After the esterification reaction, vacuum distil...
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