Adsorption desulphurization catalyst and preparation method thereof
An adsorption desulfurization and catalyst technology, applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of low sulfur capacity, poor regeneration stability, loss of octane number, etc., and reduce residence time. , Improve the regeneration stability performance, the effect of basically no loss of octane number
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Embodiment 1
[0054] (1) The ZSM-5 / MCM-41 composite molecular sieve is subjected to hydrothermal dealumination for standby, and the specific treatment conditions are as follows: (a) ZSM-5 / MCM-41 composite molecular sieve is self-made, and its silicon-aluminum ratio is 32.1; (b) 100g molecular sieves were treated continuously for 5 hours under the conditions of 480°C and 90g / h water vapor; (c) drying the obtained molecular sieves under the conditions of 300°C for use.
[0055] (2) Add 500ml of deionized water into the neutralization kettle, heat to 50°C, add 36g of ZSM-5 / MCM-41 composite molecular sieve and stir well.
[0056] (3) 15.7g of zirconium oxychloride was dissolved in nitric acid for subsequent use.
[0057] (4) 35.0g of nickel nitrate and 875.9g of zinc nitrate were added into 1500ml of water and dissolved completely, and zirconium oxychloride prepared in step (3) was added into the nickel-zinc solution to obtain an acid solution.
Embodiment 2
[0067] The catalyst preparation steps and conditions were carried out according to Example 1.
[0068] Nickel nitrate 17.5g, zinc nitrate 656.9g, ZSM-5 / MCM-41 composite molecular sieve 90.0g, zirconium oxychloride 39.3g, silica gel 17.5g. Catalyst A-2 was obtained.
Embodiment 3
[0070] The catalyst preparation steps and conditions were carried out according to Example 1.
[0071] Nickel nitrate 58.4g, zinc nitrate 766.4g, ZSM-5 / MCM-41 composite molecular sieve 60.0g, zirconium oxychloride 31.4g, silica gel 5.0g. Catalyst A-3 was obtained.
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