Highly selective alkylation process with low zeolite catalyst composition
A catalyst and composition technology, applied in the direction of catalysts, hydrocarbons, hydrocarbons, etc., can solve the problems of expensive, reduced effective use of zeolite, high cost of zeolite, etc.
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Embodiment 1
[0068] Example 1 is a comparative example made of 70 wt% UZM-8 and 30 wt% alumina. When preparing the catalyst, the synthesized UZM-8 and HNO 3 Peptized Catapal C alumina (prepared using a HNO3 / alumina weight ratio of 0.17) was mixed and ground so that the consistency of the dough was easily extruded into cylindrical pellets with a 1 / 16" diameter. Extrusion The material was calcined in flowing air at 600° C. for 1 hour. The calcined catalyst was then subjected to ammonium ion exchange at 60° C. using a 10 wt.
Embodiment 2
[0069] Example 2 is also a comparative example prepared in the same manner as Example 1 except that it contains 50 wt% alumina and 50 wt% UZM-8 in a trilobal shape with a 1 / 16" circumference.
[0070] Examples 3 and 4 represent those used in the present invention and contained 30 and 12 wt. % UZM-8 zeolite, respectively, with the balance being alumina, in a trilobal shape with a 1 / 16" circumference.
[0071] To test catalyst performance, 25 grams of catalyst was mixed with quartz sand to fill the gaps to ensure proper flow distribution before loading into a 7 / 8" ID standard steel reactor. The catalyst was preconditioned with a 3A dryer at 200°C 12 hours of flowing benzene drying. After drying, recycle benzene was introduced followed by propylene. The benzene to propylene molar ratio used for this test was 2.0, and the product effluent to combined fresh feed ratio was 7.4 (by weight), Propylene weight hourly space velocity is 1.04 hours -1 , the inlet temperature is 115°C, and...
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