Catalyst for dehydrogenation and purification of bimetallic synthesis gas and preparation method thereof
A technology for purifying catalyst and synthesis gas, which is applied in the field of bimetallic synthesis gas dehydrogenation purification catalyst and its preparation, and achieves the effects of low equipment requirements, superior catalytic performance and simple preparation method
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example 1
[0027] Put 15 g of activated alumina particles with a diameter of 2 to 3 mm into a pre-cleaned and dried corundum crucible, place them in a muffle furnace for roasting, and slowly raise the temperature from room temperature to 500 °C through a program, keep the temperature at a constant temperature for 6 h, and then cool it down. The final alumina carrier was soaked in dilute nitric acid with a concentration of 2% at 60 °C for 10 h, washed with deionized water until neutral, dried in an oven, and stored in a desiccator; weighed 0.101 g CuCl 2 2H 2 O Pour 15 ml of dilute nitric acid solution with a concentration of 1.0%, and stir until it is completely dissolved to obtain an aqueous solution of copper ions. Add 15 g of pre-treated alumina carrier to the above aqueous solution, immerse for 8 hours, and filter out the solution. The impregnated catalyst samples were dried in an oven at 160 °C, cooled to room temperature, then placed in a muffle furnace, heated to 450 °C by program...
example 2
[0030] In Example 1, CuCl was weighed in the catalyst preparation step 2 2H 2 O weight changed to 0.202g, PdCl 2 Change the weight to 0.125g, which is the cost example. At an airspeed of 1333 h -1 , the pressure is 0.25 MPa, the reaction temperature is 130-153 ℃, the H in the raw material reaction tail gas 2 The content is lower than 1711 ppm, and the minimum H 2 The content was removed to 93 ppm, and the specific results are as follows:
[0031] Mixed gas flow (ml / min) 333 333 333 333 o 2 Flow (ml / min) 6.9 4.5 4.0 3.6 Reaction temperature (°C) 134.5 136.5 137.8 152.6 After reaction H 2 content (ppm) 93 267 384 1711
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