A kind of external presulfurization method of hydrogenation catalyst
A technology of hydrogenation catalyst and off-site pre-sulfurization, which is applied in chemical instruments and methods, catalyst activation/preparation, catalyst protection, etc., can solve the difficulty of recycling and sewage treatment, uneven distribution of active components, and flammable vulcanizing agent. Toxic and other problems, to achieve the effect of being beneficial to environmental protection, saving time and money, and shortening the start-up time
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Embodiment 1
[0033] Mix 1 kg of the oxidized hydrogenation catalyst and sulfur (140 g) in Comparative Example 1 into the first vulcanization unit, at P 1 =0.1MPa pressure, filled with nitrogen, and heated to a certain temperature T 1 =185°C, then stop filling nitrogen and switch to hydrogen and pressurize with hydrogen to pressure P 2 =0.3MPa, then stop filling hydrogen, then control the heating rate to 35°C / h, and raise the temperature to T 2 =250°C and continue vulcanization for a period of time t=2h, after the vulcanization is over, use nitrogen to blow the gas in the first vulcanization unit into the second vulcanization unit filled with oxidized hydrogenation catalyst and sulfur for recycling. A vulcanization device is filled with nitrogen and the temperature is adjusted to T after the replacement is completed. 3 =30°C, then add a passivating agent for passivation, and drop to 15°C in a nitrogen atmosphere after passivation. The presulfided catalyst was designated as Sample B.
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Embodiment 2
[0037] Mix 1 kg of oxidation state hydrogenation catalyst KC-103 (oxidation state) and sulfur (160 g) in Comparative Example 1 into the first sulfurization unit, 1 =0.1MPa pressure, filled with nitrogen, and heated to a certain temperature T 1 =200°C, then stop filling nitrogen and switch to hydrogen and pressurize with hydrogen to pressure P 2 =0.4MPa, then stop filling hydrogen, then control the heating rate to 35°C / h, and raise the temperature to T 2 =275°C and continue vulcanization for a period of time t=2h, after the vulcanization is completed, use nitrogen to blow the gas in the first vulcanization unit into the second vulcanization unit filled with oxidized hydrogenation catalyst and sulfur for recycling. A vulcanization device is filled with nitrogen and the temperature is adjusted to T after the replacement is completed. 3 =80°C, then add a passivating agent for passivation, and drop to 25°C in a nitrogen atmosphere after passivation. The presulfided catalyst was ...
Embodiment 3
[0041] Mix 1kg of hydrogenation catalyst in oxidized state and sulfur (180g) in comparative example 1 into the first vulcanization unit, at P 1 =0.1MPa pressure, filled with nitrogen, and heated to a certain temperature T 1 =205°C, then stop filling nitrogen and switch to hydrogen and pressurize with hydrogen to pressure P 2 =0.2MPa, then stop filling hydrogen, then control the heating rate to 35°C / h, and raise the temperature to T 2 =300°C and continue vulcanization for a period of time t=2h, after the vulcanization is over, use nitrogen to blow the gas in the first vulcanization unit into the second vulcanization unit filled with oxidized hydrogenation catalyst and sulfur for recycling. A vulcanization device is filled with nitrogen and the temperature is adjusted to T after the replacement is completed. 3 =110°C, then add a passivating agent for passivation, and drop to 25°C in a nitrogen atmosphere after passivation. The presulfided catalyst was designated as sample D. ...
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