Coal-based ethylene glycol refining process and system
A technology for producing ethylene glycol and ethylene glycol from coal is applied in the preparation of hydroxyl compounds, the preparation of organic compounds, and the separation/purification of hydroxyl compounds, which can solve the problems of low yield, substandard product purity, and high energy consumption of the device , to achieve the effect of high product quality, improved production yield and reasonable process
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Embodiment 1
[0031] A coal-to-ethylene glycol refining process, such as figure 1 As shown, the process includes the following steps:
[0032] Step 1: The crude ethylene glycol passes through the precision filter 1 to remove mechanical impurities, and the crude ethylene glycol contains 65% methanol and 30% ethylene glycol;
[0033] Step 2: The raw material that removes mechanical impurities enters from the middle of the pre-stripping tower 2, and the methanol in the raw material liquid is removed from the top of the pre-stripping tower and sent to the intermediate tank area, which is transported to the synthesis system as a raw material, and the methanol is recycled to reduce material consumption. The crude ethylene glycol after removing most of the methanol is discharged from the tower kettle, the operating pressure is slightly positive pressure, the temperature at the top of the tower is 64.5-65.5°C, the temperature at the bottom of the tower is 99-103°C, and the reflux ratio is between 1...
Embodiment 2
[0044] A coal-to-ethylene glycol refining system, such as figure 2 As shown, it includes precision filter 1, pre-stripping tower 2, main stripping tower 3, light removal tower 4, degreasing tower 5, product rectification tower 6, recovery tower 7, weight removal tower 8, liquid phase hydrogenation reactor 9 and dealdehyde device 10; the outlet of the precision filter is connected to the middle inlet of the pre-stripping tower through a pipeline, and the outlet of the pre-stripping tower is connected to the middle entrance of the main stripping tower through a pipeline, and the outlet of the main stripping tower is connected to the stripping tower through a pipeline. The inlet of the middle part of the light tower, the outlet of the tower kettle of the light removal tower are connected to the upper inlet of the skimming tower through pipelines, the outlet of the tower kettle of the skimming tower is connected to the inlet of the middle and lower part of the product distillation...
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