A catalyst for non-hydrogenation deolefination of aromatic hydrocarbons and its preparation method
A catalyst and non-hydrogen-facing technology, applied in the direction of molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of wastewater discharge, waste gas, complex catalyst preparation process, high cost, etc., and achieve low loss of aromatics and low cost low cost, simple preparation
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Embodiment 1
[0020] The metal content is weighed to 4600μg / g, the composition of the waste catalytic cracking catalyst is 80g of 60% USY molecular sieve and kaolin, and 20g of alumina dry rubber powder is mixed and extruded to have a diameter of 2*4mm, and then calcined at 540℃. Hours, catalyst A was obtained.
Embodiment 2
[0022] The metal content is weighed to 3800μg / g, the composition of the waste catalytic cracking catalyst is 80g of the composition of 65% ReY molecular sieve and kaolin, and 20g of alumina dry rubber powder is mixed and kneaded with a diameter of 2*4mm, and then calcined at 540℃. Hours, catalyst B was obtained.
Embodiment 3
[0024] The metal content is weighed to 4600μg / g, the composition of the waste catalytic cracking catalyst is 70g of a composition of 60% USY molecular sieve and kaolin, and 30g of alumina dry rubber powder is mixed and kneaded with a diameter of 2*4mm, and then calcined at 540℃. Hours, catalyst C was obtained.
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Abstract
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