Refining and purifying unit for continuous production of battery grade dimethyl carbonate
A technology of dimethyl carbonate and battery grade is applied in the field of refining and purification devices for continuous production of battery grade dimethyl carbonate, which can solve the problems of generating solid waste, high energy consumption, low yield and the like, and achieve higher sales prices and higher Economic benefits and the effect of solving cumbersome operations
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Embodiment 1
[0034] The device uses industrial-grade dimethyl carbonate as a raw material, and adopts a continuous method to refine and purify battery-grade dimethyl carbonate products, including the following steps:
[0035] A) Raw material feed: The raw material feed dimethyl carbonate extracted from the DMC refining tower tank of the industrial-grade dimethyl carbonate unit is pumped to the light removal tower 1 through the conveying pump, and the material is fed from the middle and upper part of the light removal tower 1. Material, control feed rate 1500Kg / h;
[0036] B) Light removal tower operation: control the top operating temperature of light removal tower 1 to 50°C, the operating temperature of the tower bottom of the light removal tower to 60°C, the top operating pressure of the light removal tower: 60KPa, the reflux ratio control: 20, and light removal The dimethyl carbonate material containing light component impurities obtained at the top of the tower, when the analytical pur...
Embodiment 2
[0039] The device uses industrial-grade dimethyl carbonate as a raw material, and adopts a continuous method to refine and purify battery-grade dimethyl carbonate products, including the following steps:
[0040] A) Raw material feed: The raw material feed dimethyl carbonate extracted from the DMC refining tower tank of the industrial-grade dimethyl carbonate unit is pumped to the light removal tower 1 through the conveying pump, and the material is fed from the middle and upper part of the light removal tower 1. Material, control feed rate 1500Kg / h;
[0041] B) Light removal tower operation: control the top operating temperature of light removal tower 1 to 75°C, the operating temperature of the light removal tower bottom to 85°C, the top operating pressure of the light removal tower: 105KPa, the reflux ratio control: 30, and light removal The dimethyl carbonate material containing light component impurities obtained at the top of the tower, when the analytical purity is great...
Embodiment 3
[0044] The device uses industrial-grade dimethyl carbonate as a raw material, and adopts a continuous method to refine and purify battery-grade dimethyl carbonate products, including the following steps:
[0045] A) Raw material feed: The raw material feed dimethyl carbonate extracted from the DMC refining tower tank of the industrial-grade dimethyl carbonate unit is pumped to the light removal tower 1 through the conveying pump, and the material is fed from the middle and upper part of the light removal tower 1. Material, control feed rate 1500Kg / h;
[0046] B) Light removal tower operation: control the operating temperature of the top of the light removal tower 1 to 100°C, the operating temperature of the bottom of the light removal tower to 110°C, the operating pressure of the top of the light removal tower: 150KPa, the reflux ratio control: 40, and light removal The dimethyl carbonate material containing light component impurities obtained at the top of the tower, when the...
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