Method for Improving the Product Quality of Ethylene Glycol Produced from Syngas
A product quality, ethylene glycol technology, applied in chemical instruments and methods, preparation of hydroxyl compounds, preparation of organic compounds, etc., can solve problems such as reducing product purity, industrialization restrictions, and inability to process routes.
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Embodiment 1
[0050] Stream 1 contains 97% ethylene glycol, 350ppm of C=O impurities, and enters the rectifying tower 2 with an overhead pressure of 0.1kpa. The rising gas at the top of the column of 2 contains 99.2% of ethylene glycol and 188ppm of C=O impurities. The ascending gas is completely condensed by the condenser 4 and then divided into two parts, a stream 5 and a stream 7, and the mass ratio of the two streams is 0.01. The cooling medium of the condenser 4 is cooling water at 10°C. Stream 5 is extracted as first-class product of ethylene glycol. Stream 7 is cooled to 80 DEG C through cooler 6, and after entering refiner 8 for refining, C=O impurity stream 10 containing ethylene glycol 99.7% and 15 ppm enters heater 9 and is heated to bubble point temperature and returns to tower 2 as reflux. The polyester grade ethylene glycol extracted from the side line of the second tower contains 99.94% ethylene glycol and 6ppm of C=O impurity.
[0051] Table 1 shows the UV values of the ...
Embodiment 2
[0055] Stream 1 contains 85% ethylene glycol, 500ppm of C=O impurities, and enters the rectifying tower 2 with an overhead pressure of 30kpa. The rising gas at the top of tower 2 contains 99.99% of ethylene glycol and 327ppm of C=O impurities. The ascending gas is completely condensed by the condenser 4 and then divided into two parts, a stream 5 and a stream 7, and the mass ratio of the two streams is 0.5. The cooling medium of the condenser 4 is saturated water at 130°C. The cooling medium outlet of the condenser 4 is saturated steam at 130°C. Stream 5 is extracted as first-class product of ethylene glycol. Stream 7 is cooled to 130 DEG C through cooler 6, enters refiner 8 after refining, stream 10 containing the C=O impurity of ethylene glycol 99.3% and 8ppm enters heater 9 and is heated to bubble point temperature and returns 2 towers as reflux. The polyester-grade ethylene glycol extracted from the 2-tower measuring line contains 99.8% ethylene glycol and 8ppm of C=O im...
Embodiment 3
[0060] Stream 1 contains 99% ethylene glycol and 130ppm of C=O impurities, and enters the rectifying tower 2 with an overhead pressure of 3kpa. The rising gas at the top of the tower contains 99.93% of ethylene glycol and 35ppm of C=O impurities. The ascending gas is completely condensed by the condenser 4 and then divided into two parts, a stream 5 and a stream 7, and the mass ratio of the two streams is 0.06. The cooling medium of the condenser 4 is saturated water at 120°C. The cooling medium outlet of the condenser 4 is saturated steam at 120°C. Stream 5 is extracted as first-class product of ethylene glycol. Stream 7 is cooled to 90 DEG C through cooler 6, and after entering refiner 8 for refining, stream 10 containing ethylene glycol 99.94% and 2ppm C=O impurities enters heater 9 and is heated to the bubble point temperature and returns to tower 2 as reflux. The polyester-grade ethylene glycol extracted from the 2-tower measuring line contains 99.95% ethylene glycol an...
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