Step-by-step sulfuration method of sulfur tolerant shift catalyst
A sulfur-resistant conversion and catalyst technology, which is applied in the direction of catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of high cost and long vulcanization time, so as to reduce the total time, improve the vulcanization effect, Effect of reducing vulcanization cost
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Embodiment 1
[0024] 50,000m 3 / h Hydrogen production capacity Coal gasification unit A, the conversion system cobalt-molybdenum series sulfur-resistant shift catalyst loading capacity 128m 3 . After replacing the sulfur-resistant shift catalyst in 2011, due to the failure of the heating furnace, the method of the present invention was used for vulcanization. The temperature of the catalyst bed is raised. After the temperature reaches 215°C, the temperature is kept constant for 3 hours, and the medium and low temperature pre-sulfurization is carried out; before the vulcanization starts, the internal vulcanization pressure of the controller is 1.0MPa, and the air velocity of the circulating gas is 600h.-1 , add hydrogen to nitrogen (volume ratio: hydrogen: nitrogen = 1:9) together with nitrogen into the start-up furnace for heating; using CS 2 As a vulcanization medium for vulcanization, the vulcanizing agent is slowly added in a small amount and multiple times; and the temperature rise rat...
Embodiment 2
[0027] 450ktNH 3 / a device B, the shift system cobalt-molybdenum series sulfur-tolerant shift catalyst has a total loading capacity of 158m 3 . After replacing the sulfur-tolerant shift catalyst at the beginning of 2012, when there was a shortage of high-pressure steam and it was impossible to heat-exchange and raise the temperature, vulcanization was carried out according to the method of the present invention. During medium and low temperature pre-sulfurization, the temperature of the catalyst bed is raised. After the temperature reaches 200°C, keep the temperature constant for 5 hours to perform medium-low temperature pre-sulfurization; -1 , add hydrogen to nitrogen (volume ratio: hydrogen: nitrogen = 1:4) together with nitrogen into the start-up furnace for heating; using CS 2 As a vulcanization medium for vulcanization, the vulcanizing agent is slowly added in a small amount and multiple times; and the temperature rise rate of the catalyst bed is controlled at 40~50°C / h...
Embodiment 3
[0030] 300ktNH 3 / a device C, the shift system cobalt-molybdenum series sulfur-tolerant shift catalyst has a total loading capacity of 88m 3 . After replacing the sulfur-resistant conversion catalyst in 2011, due to the failure of the electric heater, the heating power decreased, and the vulcanization was carried out according to the method of the present invention. During medium and low temperature vulcanization, the temperature of the catalyst bed is raised. After the temperature reaches 220°C, keep the temperature constant for 2 hours to perform medium and low temperature pre-sulfurization; -1 , add hydrogen to nitrogen (volume ratio: hydrogen: nitrogen = 1:99) together with nitrogen into the start-up furnace for heating; using CS 2 As a vulcanization medium for vulcanization, the vulcanizing agent is slowly added in a small amount and multiple times; and the temperature rise rate of the catalyst bed is controlled at 95~100°C / h by controlling the amount of vulcanizing age...
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