Method for generating polyvalent alcohol and formiate by extractive crystallization separating cannizzaro process
A technology for extracting crystallization and polyols, applied in chemical instruments and methods, preparation of carboxylate salts, preparation of organic compounds, etc., can solve problems such as increased equipment investment and operating costs, long production process cycle, and decreased product yield. Achieve the effects of saving equipment investment and dynamic costs, reducing three waste pollution, and shortening the crystallization cycle
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Embodiment 1
[0043] Example 1: The mixed solution obtained in the above reaction 1 was separated from trimethylolethane and sodium formate in the following steps.
[0044] Step 1. Add n-butanol to the mixed solution of trimethylolethane and sodium formate, and the volume ratio of the added n-butanol to the mixed solution of trimethylolethane and sodium formate is 5:1. Make trimethylolethane into n-butanol to form the oil phase of the extract, sodium formate and the raffinate together form the water phase of the extract,
[0045] Step 2, separating the oil phase and the water phase of the extract,
[0046] Step 3, the water phase of the extract is crystallized by evaporation to obtain 1430kg of sodium formate crystals,
[0047] Step 4: Add ethyl acetate to the oil phase of the extract in step 2, and the volume ratio of the added ethyl acetate to the oil phase of the extract in step 2 is 8:1. Utilize ethyl acetate to extract n-butanol in the oil phase, trimethylolethane is separated out wi...
Embodiment 2
[0051] Embodiment 2: The mixed solution obtained in the above reaction 1 is separated from trimethylolethane and sodium formate in the following steps.
[0052] Step 1, the mixture of trimethylolethane and sodium formate is concentrated to make a concentrated solution, the concentration temperature is controlled at 90-100°C, the pressure is controlled at 40-45Kpa, and the concentration of trimethylolethane in the concentrated solution is controlled at 45% by weight, then add n-octanol to the concentrated solution, and the volume ratio of the added n-octanol to the concentrated solution is 3:1. Make trimethylolethane into n-octanol to form the oil phase of the extract, sodium formate and the raffinate together form the water phase of the extract,
[0053] Step 2, separating the oil phase and the water phase of the extract,
[0054] Step 3, the water phase of the extract is crystallized by evaporation to obtain 1445kg of sodium formate crystals,
[0055] Step 4, adding acetone...
Embodiment 3
[0059] Embodiment 3: The mixed solution obtained in the above reaction 2 is separated from trimethylolpropane and sodium formate in the following steps.
[0060] Step 1, add 2-ethylhexanol in the mixed solution of trimethylolpropane and sodium formate,
[0061] The volume ratio of the mixed solution of the added 2-ethylhexanol to trimethylolpropane and sodium formate is 6:1. Make trimethylolpropane into 2-ethylhexanol to form the oil phase of the extract, sodium formate and the raffinate together form the water phase of the extract,
[0062] Step 2, separating the oil phase and the water phase of the extract,
[0063] Step 3, the water phase of the extract is crystallized by evaporation to obtain 1138kg of sodium formate crystals,
[0064] Step 4. Concentrate the oil phase of the extract in step 2. The concentration temperature is controlled at 100-110°C, the pressure is controlled at 1-5Kpa, and the concentration of trimethylolpropane in the concentrated solution is control...
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