Method for refining and separating dimethyl nylon acid
A technology of dimethyl mixed diacid and dimethyl succinate, which is applied to the preparation of carboxylic acid esters, chemical instruments and methods, and the preparation of organic compounds, and can solve complex production processes, high production costs, and large investment in equipment and other issues, to achieve the effects of simplified production process, environmentally friendly production process and high purity
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Embodiment 1
[0020] The raw material dimethyl mixed diacid is pumped into the first rectification tower with 100 trays connected in series at the head end, the vacuum degree in the tower is -0.07MPa, the gas phase temperature at the top of the tower is 90°C, and the temperature at the bottom of the tower is At 110°C, light components are separated from the top of the first rectification tower. After being condensed by the condenser, the liquid reflux ratio is 20:1. After the light components at the bottom of the tower cannot be detected, the bottom materials enter the towers connected in series The second rectification tower with 100 plates; the vacuum degree in the second rectification tower is -0.075MPa, the gas phase temperature at the top of the tower is 95°C, and the temperature at the bottom of the tower is 115°C. The top of the second rectification tower is separated, and after being condensed by the condenser, the liquid reflux ratio is 8:1, and the bottom material enters the third ...
Embodiment 2
[0022] The raw material dimethyl mixed diacid is pumped into the first rectification tower with 100 trays connected in series at the head end, the vacuum degree in the tower is -0.065MPa, the gas phase temperature at the top of the tower is 92°C, and the temperature at the bottom of the tower is At 113°C, the light components are separated from the top of the first rectification tower. After being condensed by the condenser, the liquid reflux ratio is 19:1. After the light components at the bottom of the tower cannot be detected, the bottom materials enter the towers connected in series The second rectification tower with 100 plates; the vacuum degree in the second rectification tower is -0.07MPa, the gas phase temperature at the top of the tower is 98°C, and the temperature at the bottom of the tower is 117°C. The top of the second rectification tower is separated, and after being condensed by the condenser, the liquid reflux ratio is 7:1, and the bottom material enters the th...
Embodiment 3
[0024] The raw material dimethyl mixed diacid is pumped into the first rectification tower with 100 trays connected in series at the head end, the vacuum degree in the tower is -0.06MPa, the gas phase temperature at the top of the tower is 95°C, and the temperature at the bottom of the tower is At 115°C, the light component is separated from the top of the first rectification tower. After being condensed by the condenser, the liquid reflux ratio is 18:1. After the light component at the bottom of the tower cannot be detected, the bottom material enters the columns connected in series The second rectification tower with 100 plates; the vacuum in the second rectification tower is -0.065MPa, the gas phase temperature at the top of the tower is 100°C, and the temperature at the bottom of the tower is 122°C. The top of the second rectification tower is separated, and after being condensed by the condenser, the liquid reflux ratio is 6.5:1, and the bottom material enters the third re...
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