Separation and purification process and system of 1, 4-butanediol
A technology for separation and purification of butanediol, applied in the separation/purification of hydroxyl compounds, organic chemistry, production of bulk chemicals, etc., can solve the problem of low purity of 1,4-butanediol, and achieve simple equipment and separation efficiency High, high product purity effect
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Embodiment 1
[0043] The embodiment of the present invention provides a separation and purification process of 1,4-butanediol, and the process includes:
[0044] S101: Crude 1,4-butanediol is separated in a weight-removing column. Among them, the content of 1,4-butanediol is 80.1wt%, the content of 2-(4-hydroxybutoxy)tetrahydrofuran is 0.6wt%, the content of light components is 17.1wt%, and the content of other heavy components is 2.2 wt%. Light components such as γ-butyrolactone and unreacted dimethyl succinate are extracted from the top of the weight removal tower; 1,4-butanediol and 2-(4-hydroxybutoxy)tetrahydrofuran are extracted from the side line The mixture a; the bottom of the column produced 2-(4-hydroxybutoxy) tetrahydrofuran and other heavy components. The packing height of the weight-removing tower is 50 theoretical trays, the operating pressure is 10kPa, the reflux ratio is 8, the temperature at the top of the tower is 180°C, and the temperature at the bottom of the tower is ...
Embodiment 2
[0051] The embodiment of the present invention provides a separation and purification process of 1,4-butanediol, and the process includes:
[0052] S201: Crude 1,4-butanediol is separated in a weight removal tower. Among them, the content of 1,4-butanediol is 80.1wt%, the content of 2-(4-hydroxybutoxy)tetrahydrofuran is 0.6wt%, the content of light components is 17.1wt%, and the content of other heavy components is 2.2 wt%. Light components such as γ-butyrolactone and unreacted dimethyl succinate are extracted from the top of the weight removal tower; 1,4-butanediol and 2-(4-hydroxybutoxy)tetrahydrofuran are extracted from the side line The mixture a; the bottom of the column produced 2-(4-hydroxybutoxy) tetrahydrofuran and other heavy components. The packing height of the weight-removing tower is 10 theoretical trays, the operating pressure is 5kPa, the reflux ratio is 5, the temperature at the top of the tower is 160°C, and the temperature at the bottom of the tower is 180...
Embodiment 3
[0059] The embodiment of the present invention provides a separation and purification process of 1,4-butanediol, and the process includes:
[0060] S301: Crude 1,4-butanediol is separated in a weight removal tower. Among them, the content of 1,4-butanediol is 80.1wt%, the content of 2-(4-hydroxybutoxy)tetrahydrofuran is 0.6wt%, the content of light components is 17.1wt%, and the content of other heavy components is 2.2 wt%. Light components such as γ-butyrolactone and unreacted dimethyl succinate are extracted from the top of the weight removal tower; 1,4-butanediol and 2-(4-hydroxybutoxy)tetrahydrofuran are extracted from the side line The mixture a; the bottom of the column produced 2-(4-hydroxybutoxy) tetrahydrofuran and other heavy components. The packing height of the weight-removing tower is 50 theoretical trays, the operating pressure is 25kPa, the reflux ratio is 10, the temperature at the top of the tower is 200°C, and the temperature at the bottom of the tower is 2...
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