Method for preparing glycol by using oxalic ester
A technology for ethylene glycol and oxalate, which is applied in the field of ethylene glycol production by hydrogenation of dimethyl oxalate or hydrogenation of diethyl oxalate, and can solve the problems of low selectivity of target products and low utilization rate of hydrogen.
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Embodiment 1
[0021] Weigh 200 grams of a silicon oxide carrier with a specific surface area of 300 square meters per gram, and configure the catalyst according to the content of 35 parts of active metal copper. After soaking in the solution for 24 hours, vacuum-dry at room temperature for 12 hours to obtain a solid. The solid was then dried at 120°C for 12 hours and calcined at 450°C for 4 hours to obtain the desired CuO / SiO 2 catalyst precursor.
[0022] Weigh the CuO / SiO to be prepared 230 grams of catalyst precursors are loaded into a tube reactor with a diameter of 18 mm. The pre-reaction catalyst is at 200 ml / min, hydrogen molar content is 20%, and nitrogen molar content is 80% from room temperature to 3°C / min. 450° C. and constant temperature for 6 hours to activate to obtain the desired catalyst.
[0023] Using dimethyl oxalate as raw material, fresh hydrogen, recycle gas I, recycle gas II are mixed with dimethyl oxalate raw materials, and then first enter the reactor to contac...
Embodiment 2
[0025] 48%Cu+8%Zn+0.2%K / SiO obtained according to the various steps and conditions of Example 1 2 catalyst.
[0026] Taking by weighing 30 grams of the prepared catalyst and packing it into a tube reactor with a diameter of 18 millimeters, the pre-reaction catalyst is at 200 ml / min, hydrogen molar content 20%, nitrogen molar content 80% conditions, from room temperature to 3 ℃ / Minutes to 450 ° C, constant temperature for 6 hours to activate the reaction.
[0027] Using dimethyl oxalate as raw material, fresh hydrogen, recycle gas I, recycle gas II are mixed with dimethyl oxalate raw materials, and then first enter the reactor to contact with copper-containing catalyst to generate reaction effluent I containing ethylene glycol; After the reaction effluent I of glycol is separated by gas and liquid, the liquid phase effluent enters the separation system and is separated to obtain ethylene glycol products. The gas phase effluent is divided into gas phase effluent I and gas pha...
Embodiment 3
[0029] 25%Cu+5%Zn+1%Fe / SiO obtained according to the various steps and conditions of Example 1 2 catalyst.
[0030] Take by weighing 30 grams of the prepared catalyst and pack it into a tube reactor with a diameter of 18 millimeters. The pre-reaction catalyst is at 200 ml / min, hydrogen molar content 20%, nitrogen molar content 80% conditions, from room temperature to 3 ℃ Rise to 450°C per minute, keep the temperature for 6 hours for activation and then react.
[0031] Diethyl oxalate is used as raw material, fresh hydrogen, cycle gas I, cycle gas II are mixed with diethyl oxalate raw material, and firstly enter the reactor to contact with copper-containing catalyst to generate reaction effluent I containing ethylene glycol; After the reaction effluent I of glycol is separated by gas and liquid, the liquid phase effluent enters the separation system and is separated to obtain ethylene glycol products. The gas phase effluent is divided into gas phase effluent I and gas phase ef...
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