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Alkylation and dealkylation of aromatics in the presence of crystalline aluminosilicates

E Bowes
TLDR
In this article, a process for alkylating or dealkylating a compound capable of alkylation or denoising a compound by contacting it in a reaction zone maintained under conditions effective for accomplishing said alkylation with a catalyst comprising a crystalline zeolite characterized by a unique X-ray diffraction pattern or products of thermal treatment of the zeolate.
Abstract
A process for alkylating or dealkylating a compound capable of alkylation or dealkylation by contacting it in a reaction zone maintained under conditions effective for accomplishing said alkylation or dealkylation with a catalyst comprising a crystalline zeolite characterized by a unique X-ray diffraction pattern or products of thermal treatment of the zeolite. The zeolite can be further defined by reference to the following formula expressed in terms of mole ratios of oxides: WHEREIN M is a cation, J is aluminum or gallium and Z is silicon or germanium and n is the valence of M.

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Use of diazobicyclooctane (DABCO) as a template in zeolite synthesis

TL;DR: In this article, a process for preparing a ZSM-4 type crystalline zeolite material wherein 1,4-diazobicyclo (2.2) octane (DABCO), triethylenediamine (TED) is used as the source of an organic cation is presented.
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Naphthalene alkylation process

TL;DR: In this paper, an alkylation of naphthalene with an olefin or other alkylating agent possessing at least 6 carbon atoms, usually 12 to 20 carbon atoms in the presence of a zeolite which contains cations having a radius of at least 2.5 A.
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Converting hydrocarbons with zeolite ZSM-4

TL;DR: In this paper, a process of converting a hydrocarbon charge by passing it over a new family of crystalline zeolites characterized by a distinctive X-ray powder diffraction pattern was described.
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Aromatic alkylation processes

TL;DR: In this article, a C 2 -C 4 alkylating agent over an alkylation catalyst comprising zeolite omega at moderate temperature conditions and under pressure to provide liquid phase conditions is used.
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Reduction of benzene content of reformate in a catalytic cracking unit

TL;DR: In this paper, a process for reducing the benzene content of a reformate stream in a conventional catalytic cracking reactor wherein a heavy hydrocarbon feed is cracked to lighter products by contact with a supply of hot regenerated cracking catalyst is disclosed.
References
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Alkylation of aromatic compounds in the presence of an alumino-silicate catalyst

TL;DR: In this paper, a process for producing alkylated organic compounds comprises effecting reaction of an alkylating agent and an aromatic hydrocarbon, or aromatic hydrocarbons containing a nonpolar substituent, at a temperature not in excess of 600 DEG F, in the presence of a superactive catalyst comprising a base-exchanged crystalline aluminosilicate having a residual sodium content not greater than 6% by weight of the dry aluminosa and a pore size of 6 to 15 Angstrom units; said catalyst having an activity constant above 10.