Method for improving quality of ethylene glycol product
A product quality, ethylene glycol technology, applied in chemical instruments and methods, bulk chemical production, preparation of organic compounds, etc.
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Embodiment 1
[0014] Adopt nickel solid oxide as catalyzer, take the ethylene glycol product that dimethyl oxalate hydrogenation prepares as raw material, with ethylene glycol raw material, purity is 99.8% (the ultraviolet transmittance of raw material is 2,275nm place at 220nm place 91, 95 at 350nm), at a temperature of 60°C, a pressure of 1.0MPa, and a space velocity of 20 hours -1 , the hydrogen / alcohol ratio (hereinafter referred to as molar ratio) is 3: 1 under the condition of passing through the rotating packed bed reactor, contacting with the catalyst, and obtaining the effluent of ethylene glycol after the reaction; Wherein, the rotating speed of the rotating packed bed reactor is 500 rpm. The ethylene glycol product obtained after hydrogenation has an ultraviolet absorption rate of 78 at 220nm, 95 at 275nm, and 100 at 350nm after separation.
Embodiment 2
[0016] Adopt nickel solid oxide as catalyzer, take the ethylene glycol product that dimethyl oxalate hydrogenation prepares as raw material, with ethylene glycol raw material, purity is 99.8% (the ultraviolet transmittance of raw material is 2,275nm place at 220nm place 91, 95 at 350nm), at a temperature of 90°C, a pressure of 3.0MPa, and a space velocity of 50 hours -1 , under the condition that hydrogen / alcohol ratio is 10:1, pass through the rotating packed bed reactor, contact with the catalyst, and obtain the effluent of ethylene glycol after the reaction; wherein, the rotating speed of the rotating packed bed reactor is 800 rpm. The ethylene glycol product obtained after hydrogenation has an ultraviolet absorption rate of 77 at 220nm, 96 at 275nm and 100 at 350nm after separation.
Embodiment 3
[0018] Nickel solid oxide is adopted as catalyst, and the ethylene glycol product obtained by hydrogenation of dimethyl oxalate is used as raw material, and the ethylene glycol raw material has a purity of 99.9% (the ultraviolet transmittance of the raw material is 0 at 220nm, and 275nm) 90, 95 at 350nm), at a temperature of 40°C, a pressure of 1.0MPa, and a space velocity of 10 hours -1 , under the condition that the ratio of hydrogen / alcohol is 2:1, pass through the rotating packed bed reactor, contact with the catalyst, and obtain the effluent of ethylene glycol after the reaction; wherein, the rotating speed of the rotating packed bed reactor is 1000 rpm. The ethylene glycol product obtained after hydrogenation has an ultraviolet absorption rate of 79 at 220nm, 97 at 275nm, and 99 at 350nm after separation.
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