A kind of production process of epoxy fatty acid methyl ester plasticizer and the plasticizer obtained
An epoxy fatty acid methyl ester and production process technology, which is applied in the field of plasticizer preparation, can solve the problems of lack of controllability of different raw materials and uncontrollable product quality, and achieve the effect of reducing raw material costs and ensuring product quality
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Embodiment 1
[0024] Taking the daily processing capacity of 60 tons as an example, the waste oil methyl ester of Zhejiang Dongjiang Energy Technology Co., Ltd. was used as raw material for epoxidation. After the material is dehydrated in the post-treatment tank, it is kept at 110°C and 1 kPa for 2 hours, and then pumped into the stripping tower with a feed rate of 2 tons per hour. The feed rate depends on the processing capacity and product flash. Point requirement adjustment is mainly to ensure that the liquid level of the tray is below 35 cm, control the surface area to volume ratio of the liquid, and ensure the final product result, thereby controlling the effect of stripping. The pressure of the stripper is controlled at about 1 kPa, which is also to ensure the stripping effect, and the vacuum condition can improve the light removal capacity. The temperature is controlled by the outer wall coil at 110°C-115°C (the temperature of the inner tray of the lifting tower) to ensure the moistu...
Embodiment 2
[0026] Taking the daily processing capacity of 60 tons as an example, the fatty acid methyl ester of Jiangsu Jiemei Bioenergy Recovery Co., Ltd. was used as the raw material for epoxidation. The raw materials are dehydrated in the post-treatment kettle, kept at 110°C and 1 kPa for 2 hours, and then pumped into the stripping tower with a feed rate of 3 tons per hour. The feed rate depends on the processing capacity and product The flash point requires adjustment, mainly to ensure that the liquid level of the tray is below 35 cm, to control the surface area to volume ratio of the liquid, to ensure the final product result, and to control the stripping effect. The pressure of the stripper is controlled at about 1 kPa, which is also to ensure the stripping effect, and the vacuum condition can improve the light removal capacity. The temperature is controlled by the outer wall coil at 115°C-120°C (the temperature of the inner tray of the lifting tower) to ensure the moisture content...
Embodiment 3
[0028]Taking the daily processing capacity of 60 tons as an example, the refined fatty acid methyl ester of Tangshan Jinlihai Biodiesel Co., Ltd. was used as raw material for epoxidation. The final material is dehydrated in the post-treatment kettle, kept at 110°C and 1 kPa for 2 hours, and then pumped into the stripping tower with a feed rate of 2.5 tons per hour. The feed rate depends on the processing capacity and The flash point of the product needs to be adjusted, mainly to ensure that the liquid level of the tray is below 35 cm, to control the surface area to volume ratio of the liquid, to ensure the final product result, and to control the stripping effect. The pressure of the stripper is controlled at about 1 kPa, which is also to ensure the stripping effect, and the vacuum condition can improve the light removal capacity. The temperature is controlled by the outer wall coil at 115°C-120°C (the temperature of the tray inside the tower), which ensures the moisture conte...
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