Selective sorption of dialkylated multinuclear aromatic compound

Chemistry of hydrocarbon compounds – Aromatic compound synthesis – By condensation of entire molecules or entire hydrocarbyl...

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585467, 585820, 585828, 585831, C07C 264, C07C 268, C07C 712

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052685233

DESCRIPTION:

BRIEF SUMMARY
FIELD OF THE INVENTION

The invention relates to a process for the separation of various dialkyl multinuclear aromatic compounds from a feed stream of mixed isomers of those compounds. A shape selective adsorbent is employed resulting in a process that is more efficient than processes based upon prior separation techniques. Of special interest are combination processes involving synthesis steps followed by sorption steps using the same shape selective materials.


BACKGROUND OF THE INVENTION

The present invention relates to a process for separating various dialkyl multinuclear aromatic compounds from streams containing their isomers. These isomers are of interest for the production of certain di-substituted aromatics which in turn are employed in the synthesis of liquid crystal polymers and specially polyesters.
The p,p'-dialkyl multinuclear aromatic products most suitable for this process, their respective stream, and shape selective catalysts are outlined in the table below:


______________________________________ Shape Selective Product Stream Material ______________________________________ 2,6-diisopropylbiphenyl Mixed DIPN's Mordenite (DIPN) 4,4'-diisopropylbiphenyl Mixed DIBP's ZSM-12, (DIPBP) mordenite 2,6-dimethylnaphthalene Mixed DMN's ZSM-5 (DMN) 4,4-diethylbiphenyl Mixed DEBP's ZSM-12 2-methyl-6-isopropyl Mixed MIPN's Mordenite naphthalene (MIPN) ______________________________________
Those liquid crystal polymers and specially polyesters would likely be commercially attractive if either dihydroxy or dicarboxy forms of the dialkyl multinuclear aromatic compounds were readily available. Unfortunately, they are not. Viable feedstocks which are convertible into either the dihydroxy or dicarboxy monomers based upon known technology are the compounds listed above.
In manufacturing these dialkyl multinuclear aromatics it is clear that some monoalkyl and trialkyl products and a mix of dialkyl isomers will also be produced. In any crude diethyl multinuclear aromatic product stream, separation of these isomers by thermal distillation is difficult because the boiling points of the respective isomers are very close. Similarly, isomer separation by fractional crystallization using melting points is inefficient and suffers from yield problems because of the loss of the desired product in the mother liquor and because of large recycle streams.
It is taught in U.K. Patent Application No. 2,199,590 filed Nov. 27, 1987, that a specific isomer of dimethylnaphthalene can be separated from other isomers when a zeolite Y containing specific metallic ions is used as an adsorbent in combination with a specific desorbent.
Similarly, the separation 4,4'-dialkylbiphenyls in using mordenites is suggested in Japanese Kokai 89/249,729 (assigned to Nippon Steel Chemical Co.).
The references do not suggest combination processes in which the shape selective material used to synthesize the desired p,p'-dialkyl multinuclear aromatic product in a first step is also -used to separate that product from its accompanying isomers.


BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 represents a simulated moving bed column which can be employed in practicing the separation step of the present invention.
FIG. 2 is a graph demonstrating the efficacy of the present invention by comparing ratios of 2,6-diisopropylnaphthalene adsorbed with the volume of desorbent employed.


SUMMARY OF THE INVENTION

This invention is to an adsorbent process for the separation of p,p'-dialkyl multinuclear aromatic compounds from their isomers and, optionally, containing a synthesis step for producing those compounds using materials comprising the same shape selective materials.
Generically, the combination process entails synthesizing the p,p'-dialkyl multinuclear aromatic product compounds using feedstocks and acidic shape selective materials listed in the table below and then adsorbing those product compounds using the same shape selective materials.


______________________________________ Shape Selective Products Alky

REFERENCES:
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patent: 5017735 (1991-05-01), Fellmann et al.
Broughton, D. B., "Bulk separations via absorption" CEP (Oct. 1977) pp. 49-51.
Meier et al., "Atlas of zeolite structure types" Second Edition, (1987) Butterworths Publishers, London, pp. 62-63.
Scherzer, J., "The Preparation and characterization of aluminum-deficient zeolites" Whyte et al., eds., Catalytic Materials: Relationship Between Structure and Reactivity, American Chemical Society, Washington, D.C., (1984) pp. 157-159.
Flanigen et al., "Aluminophosphate molecular sieves and the periodic table" Murakami et al., eds., New Developments in Zeolite Science and Technology, Elsevier, Amsterdam, (1986) pp. 103-112.
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Philippaerts et al., "The implantation of boron-nitrogen compounds in mordenite LP and their influence on the adsorption properties" Stud. Surf. Sci. Catal. (1986) 28:319-327.
Niwa et al., "Fine control of the pore-opening size of the zeolite mordenite by chemical vapor deposition of silicon alkoxide" J. Chem. Soc. Faraday Trans. (1984) 80:3135-3145.
Niwa et al., "Modification of H-mordenite by a vapour-phase deposition method" J. Chem. Soc., Chem., Commun. (1982) pp. 819-820.
Hidalgo et al., "Modification of mordenite by chemical vapour deposition of metal chloride" Zeolites (1984) 4:175-180.

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