%���� 8 0 obj <> /Filter /LZWDecode In this process, benzene is alkylated with CG propylene using a zeolite catalyst, yielding Cumene. Discusses about cumene production from benzene and propylene reaction. In addition, the zeolite-based process offers higher product purities and uses a regenerable catalyst, eliminating the waste disposal problems associated with the SPA and AlCl3 catalysts. Unknown The production rate of cumene is 92.86 kmol/h in the Turton et al. %���� << %PDF-1.6 ¥æ€»åŽ‚, ASSIGNMENT OF ASSIGNORS INTEREST. /Length 9 0 R stream �Ũ5ւ���¶Hd��?pd@�Ɣ�IKC���.�{2d��-�D�ȓ��>cPuZȣ�fA��{����6^x ��E�d�� �X�i�65��~K��/S*��YڢUaꈸ�r�'y�k�����3�I��p*O��M�)k��w� { ��zJy��"uA�&�7�v!�VE*:2� ��Q8I]�����X �����&SW�R$��#��A�a֢�SN��Fr���e� �$�&@��M�Y S�� <. SetaPDF-Merger Component v2.32.0.1371 ©Setasign 2005-2020 (www.setasign.com) design. stream Benzene and propylene are fed from separate storage tanks (TK-201 and TK-202, not shown on the PFD (Figure 1)), through �@h�A��� h���"%C04Z0㑼��Fr��@(#�� ��e1�&�I��,��H�C9���*AP�S6�̇�q��E9�bF� �n.H��!��! 2020-05-30T13:35:39-05:00 Ɠ.�̀���h����b� �(r�����5��j�5C�� ��k�ӷ�rG#�7����4�cDh4P�����#�A�c�[��)ck��J��h�H.ܾ��������L;Pq�ͅ���O�!�q,���UM�z�Hr�l�7\����,�F�['����`V����8qnI!D��8 ���Q����9���Jӵ3bz7� ;ASSIGNOR:KATALISTIKS INTERNATIONAL, INC., A CORP. OF MD;REEL/FRAME:005006/0782, UOP, A GENERAL PARTNERSHIP OF NY, ILLINOIS, ASSIGNMENT OF ASSIGNORS INTEREST. 17 0 obj ;ASSIGNOR:UOP INC.;REEL/FRAME:005077/0005, Process for continuous production of cumene and/or diisopropylbenzene, Process for the production of alkylbenzene using a mordenite modified based catalyst, Alkylation process with reactor effluent heat recovery, Process for the production of tertiary butylethylbenzene, Method for minimizing diarylalkane formation in alkylation of aromatics by olefins by zeolite beta, Integrated cracking and olefins derivative process utilizing dilute olefins, Method for minimizing diarylalkane formation in alkylation-transalkylation process using zeolite beta, Production of alkyl aromatics by passing transalkylation effluent to alkylation zone, Recovery process for wet aromatic alkylation and dry aromatic transalkylation, Production of ethyl aromatics by passing portions of transalkylation effluent to a multi-bed alkylation zone, Production of isopropyl aromatics by passing portions of transalkylation effluent to a multi-bed alkylation zone, Production of alkyl aromatics by passing transalkylation effluent to alkylation zone and to product recovery zone, Attrition resistant zeolitic layered catalyst composition and aromatics alkylation process for using the composition, Alkylation process operating at low olefin ratios, Carbon dioxide recovery in an ethylene to ethylene oxide production process, Olefin recovery in a polyolefin production process, Process for the production of alkylbenzene, Process for the production of alkylaromatics, Process for the production of alkylbenzene with ethane stripping, Aromatic alkylation process with direct recycle, Processes for the production of cumene, polyetherimides, and polycarbonates, Energy efficient method and apparatus for exothermic reactions, Selective preparation method for 1, 3 ,5-tricumene, Process for benzene removal from gasoline, Integrated methods of preparing renewable chemicals, Manufacture of isopropyl benzene by alkylation, Preparation of m-and p-diisopropylbenzene, Process for alkylation of aromatic compounds, Alkylation/transalkylation process for selective production of monoalkylated aromatics, Alkylation process operating at high recycle ratios, Method of controlling monoalkyl aromatic process, Process for preparing attrition resistant zeolitic layered catalyst composition, Energy efficient method for exothermic reactions, Selective production and reaction of p-Disubstituted aromatics over zeolite ZSM-48, Conversion of methanol to products comprising gasoline boiling components, Alkylation of aromatics with ethylene and propylene: recent developments in commercial processes.

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