Aldossary, Mohammed R.

Almulla, Faisal M.

Garforth, Arthur A.

Jumah, Abdulrahman Bin

Tedstone, Aleksander A.

Zholobenko, Vladimir I.

Catalyst deactivation remains a main challenge in the transalkylation process. To develop a cost-eﬀective catalyst,improvingtheregenerationcharacteristicsofBetaandPt-Betacatalystswasinvestigated.BothBetaandPtBeta catalysts were studied in transalkylation in the presence of hydrogen. The regeneration process was carried out using hydrogen for four cycles of operation (30h on stream per cycle). A Pt-Beta catalyst with enhanced regeneration and activity characteristic relative to the parent materials is presented, and found to be stable, with the activity fully restored by regeneration with hydrogen at 500°C. The activity of the parent Beta dropped gradually after each cycle suggesting that the hydrogen alone at 500°C was insuﬃcient in removing the coke formed during the reaction. The drop in activity was attributed to the disappearance of Brønsted acid sites over the spent Beta catalyst due to the growth of coke molecules trapped in the zeolite micropores leading to the formation of highly polyaromatic molecules blocking those active sites. This limitation can be eﬀectively overcome by platinum addition which enhanced the removal of coke during the regeneration via hydrocracking.<br/

Effect of hydrogenative regeneration on the activity of beta and Pt-Beta zeolites during the transalkylation of toluene with 1,2,4-trimethylbenzene

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