Continuous production process for dimethyl fumarate
A technology of dimethyl fumarate and production process, which is applied in the preparation of carboxylate, the preparation of organic compounds, chemical instruments and methods, etc., can solve problems such as low yield and complicated operation, and achieve non-corrosion reaction equipment. , the reaction conditions are simple, the effect of not polluting the environment
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Embodiment 1
[0018] A kind of continuous production process of dimethyl fumarate, such as figure 1 As shown, the 732-type polystyrene sulfonic acid cation exchange resin (purchased from Shanghai Yige Industrial Co., Ltd.) was evenly filled into the reaction column 4 and heated to 70-75 °C; Raw material fumaric acid and methanol solution, the molar ratio is: 1:5, through the feed pump 2, from the feed port 3 of the fixed reaction column into the reaction column 4, adjust the flow rate of the flow pump, control the feed rate of raw materials, Make the residence time of raw material in reaction column be 4h, discharge port 6 collects reaction product; Pass reaction product into cold water, stir, have a large amount of white crystals to separate out; Filter, filter cake with 8%Na 2 CO 3 The solution was washed; filtered again, the filter cake was washed with distilled water until neutral, and then dried at room temperature to obtain the product. The yield was 89.6%.
Embodiment 2
[0020] A kind of continuous production process of dimethyl fumarate, such as figure 1 As shown, the D-61 polystyrene sulfonic acid cation exchange resin (purchased from Shanghai Yige Industrial Co., Ltd.) was evenly filled into the reaction column 4 and heated to 75-80 °C; The reaction raw materials fumaric acid and methanol solution, molar ratio is: 1:8, join in the reaction column 4 from the inlet 3 of fixed reaction column, adjust the flow rate of flow pump, control the addition speed of raw material, make raw material in reaction The residence time in the column is 8h, and the reaction product is collected at 6 outlets; the reaction product is passed into cold water, stirred, and a large amount of white crystals are precipitated; filtered, and the filter cake is washed with 9%Na 2 CO 3 The solution was washed; filtered again, the filter cake was washed with distilled water until neutral, and then dried at room temperature to obtain the product. The yield was 94.3%.
Embodiment 3
[0022] A continuous production process for dimethyl fumarate, D-72 type polystyrene sulfonic acid type cation exchange resin (purchased from Shanghai Yige Industrial Co., Ltd.), is evenly filled in the reaction column 4, heated to 82- 88°C; put the reaction raw material fumaric acid and methanol solution in the raw material cylinder 1, the molar ratio is: 1:6, add it to the reaction column from the feed port 3 of the fixed reaction column, adjust the flow rate of the flow pump, and control The adding speed of raw material makes the residence time of raw material in reaction column be 6h, and the reaction product is collected at 6 places of outlet; Pass reaction product into cold water, stir, have a large amount of white crystals to separate out; Filter, filter cake with 10% Na 2 CO 3 The solution was washed; filtered again, the filter cake was washed with distilled water until neutral, and then dried at room temperature to obtain the product. The yield was 95.7%.
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