A method for measuring the activity of desulfurization adsorbent
A measurement method and adsorbent technology, applied in the separation method, measurement device, fluorescence/phosphorescence, etc., can solve the problems of long cycle, slow speed, long evaluation cycle, etc., and achieve the effect of simple operation
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Embodiment 1
[0060] Put 16 grams of fresh desulfurization adsorbent FCAS in a small fixed-bed reactor, first reduce the adsorbent for 2 hours under the conditions of pressure 2.5 MPa, hydrogen 16 liters / hour, and temperature 400 ° C, and then use sulfur weight Fraction is 0.2% thiophene+n-octane (analytically pure, 99%) solution as hydrocarbon oil feedstock, at pressure is 2.5 MPa, hydrogen 16 liters / hour, weight hourly space velocity 5 hours -1 , the temperature is 400°C, and the desulfurization adsorption reaction is carried out under the reaction conditions of a hydrogen-oil molar ratio of 1. The sulfur content of the product is analyzed by a SINDIE online total sulfur analyzer. When the sulfur weight fraction of the desulfurization product is greater than 0.001%, the feed is stopped. The weight of the raw material entering into the reactor to contact and react with the adsorbent is measured by the feed weight flow meter as the weight of the desulfurization product. And the relative des...
Embodiment 2
[0062] Put 16 grams of the desulfurization adsorbent S1 to be tested in a small fixed-bed reactor, and first regenerate the adsorbent. The regeneration conditions are: regeneration stage 1, the regeneration temperature is 430°C, the pressure is normal pressure, and the regeneration gas is air and Mixed gas of nitrogen (8 liters / hour air + 8 liters / hour nitrogen), regeneration for 2 hours; regeneration stage 2, regeneration temperature is 480 ° C, pressure is 0.1 MPa, regeneration gas is a mixed gas of air and nitrogen (12 liters / hour air + 4 liters / hour nitrogen), regeneration for 2 hours; regeneration stage 3, regeneration temperature is 530°C, pressure is 0.1 MPa, regeneration gas is 16 liters / hour air, regeneration is 2 hours. Then at a pressure of 2.5 MPa, a hydrogen gas of 16 liters / hour, and a temperature of 400° C., the adsorbent was reduced for 0.5 hour, and then the sulfur weight fraction was 0.2% thiophene+n-octane (analytically pure, 99%) The solution is used as th...
Embodiment 3
[0064]Put 16 grams of the desulfurization adsorbent S2 to be tested in a small fluidized bed reactor, and first regenerate the adsorbent. The regeneration conditions are: regeneration stage 1, the regeneration temperature is 430 ° C, the pressure is 0.5 MPa, and the regeneration gas is Mixed gas of air and nitrogen (8 liters / hour of air + 8 liters / hour of nitrogen), regeneration for 2 hours; regeneration stage 2, regeneration temperature is 480 ° C, pressure is 0.5 MPa, regeneration gas is a mixture of air and nitrogen ( 12 liters / hour air + 4 liters / hour nitrogen); regeneration for 2 hours, regeneration stage 3, regeneration temperature 530°C, pressure 0.5 MPa, regeneration gas 16 liters / hour air, regeneration 2 hours. Then at a pressure of 1.5 MPa, a hydrogen gas of 32 liters per hour, and a temperature of 400° C., the adsorbent was reduced for 2 hours, and then the sulfur weight fraction was 0.2% thiophene+n-octane (analytically pure, 99%) The solution is used as the hydroc...
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