High epoxide number environment-friendly plasticizer production process
A production process and environment-friendly technology, applied in the direction of fatty acid esterification, sulfonate ester preparation, organic chemistry, etc., can solve the problems of high price, unfavorable market expansion, unstable product quality, etc., and achieve easy access to process raw materials, The effect of simple equipment
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Embodiment 1
[0019] The method for preparing high epoxy value environment-friendly plasticizer of the present invention,
[0020] (1) Continuously enter 78.6% of refined cottonseed oil, 21% methanol (content 99.5%) and 0.4% sodium methoxide into the transesterification reactor for transesterification reaction. The reaction temperature is controlled at 85°C and the reaction time is 30 minutes. Mix fatty acid methyl ester and glycerin. The glycerol is separated by standing precipitation. Esterification rate is 99.2%, fatty acid methyl ester iodine value≤0.1, acid value≤0.5, moisture content≤0.1%, free oil≤2%.
[0021] (2) The mixed fatty acid methyl ester enters the packed rectification tower for rectification and separation. The top temperature of the tower is 190°C, the bottom temperature of the tower is 240°C, the vacuum degree is 0.09Mpa, and the reflux ratio is 2.
[0022] (3) Methyl oleate from the bottom of the rectification tower enters the epoxidation reactor, adding 001×7 type acid ion ...
Embodiment 2
[0028] Method for preparing environment-friendly plasticizer with high epoxy value in the present invention
[0029] (1) 80% refined cottonseed oil, 19.7% methanol (content 99.5%) and 0.3% sodium methoxide are continuously fed into the transesterification reactor for transesterification reaction. The reaction temperature is controlled at 80°C and the reaction time is 30 minutes. Mix fatty acid methyl ester and glycerin, stand still and precipitate to separate glycerin. Esterification rate is 99.5%, fatty acid methyl ester iodine value≤0.1, acid value≤0.5, moisture content≤0.1%, free oil≤2%.
[0030] (2) The mixed fatty acid methyl ester enters the packed rectification tower for rectification and separation. The top temperature of the tower is 195°C, the bottom temperature of the tower is 245°C, the vacuum degree is 0.09Mpa, and the reflux ratio is 4.
[0031] (3) Methyl oleate from the bottom of the rectification tower enters the epoxidation reactor, adding 001×7 type acid ion excha...
Embodiment 3
[0037] Method for preparing environment-friendly plasticizer with high epoxy value in the present invention
[0038] (1) Continuously enter 84.5% of refined cottonseed oil, 15.2% methanol (content 99.5%) and 0.3% sodium methoxide into the transesterification reactor for transesterification reaction. The reaction temperature is controlled at 90°C and the reaction time is 30 minutes. Mix fatty acid methyl ester and glycerin. The glycerol is separated by standing precipitation. Esterification rate is 99.3%, fatty acid methyl ester iodine value≤0.1, acid value≤0.5, moisture content≤0.1%, free oil≤2%.
[0039] (2) The mixed fatty acid methyl esters enter the packed rectification tower for rectification and separation. The top temperature of the tower is 175°C, the bottom temperature of the tower is 225°C, the vacuum degree is 0.09Mpa, and the reflux ratio is 5.
[0040] (3) Methyl oleate from the bottom of the rectification tower enters the epoxidation reactor, adding 001×7 acidic ion e...
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