Purifying method for 1,4-cyclohexanedimethanol
A technology of cyclohexanedimethanol and purification method, which is applied in the field of reducing saponification value during rectification, can solve the problems of reducing product yield, affecting economic benefits, restricting the development of downstream products, etc., and achieve the effect of improving product quality
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example 1
[0016] Put 1t of crude product of 1,4-cyclohexanedimethanol in the distillation tower kettle, adopt a rectification tower with a tower height of 15m and a tower diameter of 0.8m, raise the temperature of the rectification tower, and turn on the vacuum pump to make the vacuum degree of the tower reach -0.095~ -1MPa, the temperature at the bottom of the tower is 230°C, when the temperature at the top of the tower reaches 200°C, start to collect 1,4-cyclohexanedimethanol into the finished product tank, when the temperature at the top of the tower exceeds 205°C, stop the rectification, and get the product 0.945t , The yield is 94.5%. After testing, the product has a purity of 99.8%, a saponification value of 0.38 mgKOH / g, and a moisture content of 0.06%.
example 2
[0018] Put 1t of crude product of 1,4-cyclohexanedimethanol into the distillation tower kettle, adopt a rectification tower with a tower height of 22m and a tower diameter of 0.8m, raise the temperature of the rectification tower, and turn on the vacuum pump to make the vacuum degree of the tower reach -0.095~ -1MPa, the temperature at the bottom of the tower is 230°C, when the temperature at the top of the tower reaches 200°C, start to collect 1,4-cyclohexanedimethanol into the finished product tank, when the temperature at the top of the tower exceeds 205°C, stop the rectification to obtain the product 0.805t , The yield is 80.5%. After testing, the product has a purity of 99.9%, a saponification value of 0.19 mgKOH / g, and a moisture content of 0.06%.
example 3
[0020] Put 1t of crude product 1,4-cyclohexanedimethanol into the distillation column kettle, add 0.96kg of NaOH solid (the molar ratio of alkali to ester impurities = 1:1), and use a rectification system with a tower height of 15m and a tower diameter of 0.8m Tower, heat up the rectification tower, turn on the vacuum pump to make the vacuum degree of the tower reach -0.095~-1MPa, the temperature at the bottom of the tower is 240°C, when the temperature at the top of the tower reaches 195°C, start to collect 1,4-cyclohexanedimethanol into the finished product tank, when the tower top temperature exceeds 205°C, the rectification is stopped to obtain a product of 0.938t with a yield of 93.8%. After testing, the product has a purity of 99.8%, a saponification value of 0.37mgKOH / g, and a moisture content of 0.05%.
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Abstract
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