Comprehensive utilization method of low-concentration 1,4-butanediol
A butanediol and low-concentration technology, applied in the field of chemical rectification, can solve the problem of low concentration of 1,4-butanediol, and achieve the effects of creating economic value, increasing concentration and avoiding pollution
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Embodiment 1
[0018] A kind of low-concentration 1, the comprehensive utilization method of 4-butanediol comprises the following processing steps: (1) crude distillation: the material collection containing low-concentration 1,4-butanediol is put into the reactor, in the reactor Add alkaline auxiliary agent sodium carbonate in the middle, the consumption of described sodium carbonate is 0.6wt% of still raffinate. , the reaction kettle is heated, the temperature at the bottom of the kettle is controlled at 105°C, the temperature at the top of the kettle is controlled at 50°C, the reflux ratio is controlled at 0.1, and methanol, tetrahydrofuran, and water are separated from the top of the kettle; (2) the intermediate glycol component Separation: continue heating the still liquid after step (1), so that the temperature at the bottom of the still is raised to 115°C, the temperature at the top of the still is controlled at 90°C, the reflux ratio is controlled at 0.3, and the glycol component is se...
Embodiment 2
[0021] A kind of low-concentration 1, the comprehensive utilization method of 4-butanediol comprises the following processing steps: (1) crude distillation: the material collection containing low-concentration 1,4-butanediol is put into the reactor, in the reactor Add alkaline auxiliary agent sodium carbonate, the consumption of described sodium carbonate is 0.8wt% of still raffinate, the reaction kettle is heated, and the temperature at the bottom of the still is controlled at 107 ℃, and the temperature at the top of the still is controlled at 60 ℃, and the reflux ratio is controlled at 0.13, methanol, tetrahydrofuran, and water are separated from the top of the kettle; (2) Separation of the diol component of the intermediate: continue heating the still liquid after the treatment in step (1), so that the temperature at the bottom of the kettle rises to 130°C, The temperature is controlled at 100°C, the reflux ratio is controlled at 0.35, and the glycol component is separated f...
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