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US3962362A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for preparing polyphenyls

Assignee: Texaco Development Corp
•
Filing: 1975-03-31
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Granted: 1976-06-08
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Expires: 1995-03-31
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Abstract

Abstract Polyphenyls including biphenyl and terphenyl, are prepared by hydroalkylation of a charge benzene, dehydrogenation of hydroalkylate, and separation of desired product polyphenyls.

Inventors

  • 👤 Robert M. Suggitt

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 08:24
CPC Classifications
C; C07; C07C; C07C15/00; C07C15/12; C07C15/14; C07C2/00; C07C2/74; C07C5/00; C07C5/32; C07C5/367

Claims Analysis

Total Claims: 19
Claim 1
Independent Claim 112 words
The method which comprises hydroalkylating a charge monocyclic aromatic hydrocarbon stream with a hydroalkylating quantity of hydrogen in the presence of hydroalkylation catalyst at hydroalkylation conditions thereby forming a hydroalkylate product stream containing naphthenyl benzenes; dehydrogenating, in the presence of dehydrogenating catalyst at dehydrogenation conditions, a dehydrogenation charge stream containing at least a portion of the naphthenyl benzenes in said hydroalkylate product and at least one diluent-carrier selected from the group consisting of benzene, cyclohexylbenzenes, methylcyclopentane, cyclohexane, toluene, xylene, and mixtures thereof, thereby forming a dehydrogenated product stream containing polyphenyls in diluent-carrier, said diluent-carrier being of lower molecular weight than said product polyphenyls; and recovering said polyphenyls from said dehydrogenated product stream.
Claim 2
Independent Claim 112 words
The method which comprises hydroalkylating a charge monocyclic aromatic hydrocarbon stream with a hydroalkylating quantity of hydrogen in the presence of hydroalkylation catalyst at hydroalkylation conditions thereby forming a hydroalkylate product stream containing naphthenyl benzenes; dehydrogenating, in the presence of dehydrogenating catalyst at dehydrogenation conditions, a dehydrogenation charge stream containing at least a portion of the naphthenyl benzenes in said hydroalkylate product and at least one diluent-carrier selected from the group consisting of benzene, cyclohexylbenzenes, methylcyclopentane, cyclohexane, toluene, xylene, and mixtures thereof, thereby forming a dehydrogenated product stream containing polyphenyls in diluent-carrier, said diluent-carrier being of lower molecular weight than said product polyphenyls; and recovering said polyphenyls from said dehydrogenated product stream.
Claim 3
Dependent Claim 15 words
The method as claimed in claim 1 wherein said charge monocyclic aromatic hydrocarbon is benzene.
Claim 4
Dependent Claim 12 words
The method as claimed in claim 1 wherein said diluent-carrier is benzene.
Claim 5
Dependent Claim 23 words
The method as claimed in claim 1 wherein said diluent-carrier includes at least one component of the hydroalkylate in addition to naphthenyl benzene.
Claim 6
Dependent Claim 23 words
The method as claimed in claim 1 wherein said hydroalkylate product stream is passed directly to the dehydrogenating operation as dehydrogenation charge stream.
Claim 7
Dependent Claim 35 words
The method as claimed in claim 1 wherein said hydroalkylate product stream is fractionated to yield (i) a fraction containing increased proportions of mononaphthenyl benzenes and (ii) a fraction containing increased proportions of dinaphthenyl benzenes.
Claim 8
Dependent Claim 33 words
The method as claimed in claim 6 wherein said fraction containing increased proportions of mononaphthenyl benzenes is passed to said dehydrogenating operation thereby forming a dehydrogenated product stream containing increased proportions of biphenyl.
Claim 9
Dependent Claim 33 words
The method as claimed in claim 6 wherein said fraction containing increased proportions of dinaphthenyl benzenes is passed to said dehydrogenating operation thereby forming a dehydrogenated product stream containing increased proportions of terphenyls.
Claim 10
Independent Claim 86 words
The method which comprises hydroalkylating a charge benzene stream with a hydroalkylating quantity of hydrogen in the presence of hydroalkylation catalyst at hydroalkylation conditions thereby forming a hydroalkylate product stream containing unconverted benzene and naphthenyl benzenes; dehydrogenating, in the presence of dehydrogenating catalyst at dehydrogenation conditions, a dehydrogenation charge stream containing at least the naphthenyl benzenes in said hydroalkylate product and a dehydrogenated product-solubilizing amount of benzene, thereby forming a dehydrogenated product stream containing polyphenyls in benzene; and recovering said polyphenyls from said dehydrogenated product stream.
Claim 11
Independent Claim 86 words
The method which comprises hydroalkylating a charge benzene stream with a hydroalkylating quantity of hydrogen in the presence of hydroalkylation catalyst at hydroalkylation conditions thereby forming a hydroalkylate product stream containing unconverted benzene and naphthenyl benzenes; dehydrogenating, in the presence of dehydrogenating catalyst at dehydrogenation conditions, a dehydrogenation charge stream containing at least the naphthenyl benzenes in said hydroalkylate product and a dehydrogenated product-solubilizing amount of benzene, thereby forming a dehydrogenated product stream containing polyphenyls in benzene; and recovering said polyphenyls from said dehydrogenated product stream.
Claim 12
Independent Claim 131 words
The method which comprises hydroalkylating a charge benzene stream with a hydrogen partial pressure of 50 to 1500 psig in the presence of hydroalkylating catalyst at temperature of 80°-200°C and pressure of 50-1500 psig thereby forming a hydroalkylate product stream containing (i) unconverted benzene and (ii) cyclohexyl benzene; flashing at least a portion of said unconverted benzene from said hydroalkylate product stream in a first flashing operation thereby forming a first flashed hydroalkylate product stream containing a dehydrogenated product-solubilizing amount of benzene; dehydrogenating said first flashed hydroalkylate product stream containing said dehydrogenated product-solubilizing amount of benzene at 700°-1100°F and total pressure of 0-1000 psig thereby forming a fluid dehydrogenated product stream containing polyphenyls in benzene; separating said benzene from said dehydrogenated product stream; and recovering said polyphenyls from said product stream.
Claim 13
Independent Claim 131 words
The method which comprises hydroalkylating a charge benzene stream with a hydrogen partial pressure of 50 to 1500 psig in the presence of hydroalkylating catalyst at temperature of 80°-200°C and pressure of 50-1500 psig thereby forming a hydroalkylate product stream containing (i) unconverted benzene and (ii) cyclohexyl benzene; flashing at least a portion of said unconverted benzene from said hydroalkylate product stream in a first flashing operation thereby forming a first flashed hydroalkylate product stream containing a dehydrogenated product-solubilizing amount of benzene; dehydrogenating said first flashed hydroalkylate product stream containing said dehydrogenated product-solubilizing amount of benzene at 700°-1100°F and total pressure of 0-1000 psig thereby forming a fluid dehydrogenated product stream containing polyphenyls in benzene; separating said benzene from said dehydrogenated product stream; and recovering said polyphenyls from said product stream.
Claim 14
Independent Claim 69 words
The method which comprises dehydrogenating, in the presence of dehydrogenating catalyst at dehydrogenation conditions, a dehydrogenation charge stream containing a naphthenyl benzene and at least one diluent-carrier selected from the group consisting of benzene, cyclohexyl benzene, methyl cyclopentane, cyclohexane, toluene, xylene, and mixtures thereof thereby forming a dehydrogenated product stream containing polyphenyls in diluent-carrier, said diluent-carrier being of lower molecular weight than said polyphenyls; and recovering said product stream.
Claim 15
Independent Claim 69 words
The method which comprises dehydrogenating, in the presence of dehydrogenating catalyst at dehydrogenation conditions, a dehydrogenation charge stream containing a naphthenyl benzene and at least one diluent-carrier selected from the group consisting of benzene, cyclohexyl benzene, methyl cyclopentane, cyclohexane, toluene, xylene, and mixtures thereof thereby forming a dehydrogenated product stream containing polyphenyls in diluent-carrier, said diluent-carrier being of lower molecular weight than said polyphenyls; and recovering said product stream.
Claim 16
Independent Claim 51 words
The method which comprises dehydrogenating, in the presence of dehydrogenating catalyst at dehydrogenation conditions, a dehydrogenation charge stream containing a cyclohexyl benzene and, as a diluent-carrier, benzene thereby forming a dehydrogenated product stream containing biphenyl and benzene; separating said benzene from said product stream; and recovering said product stream containing biphenyl.
Claim 17
Independent Claim 51 words
The method which comprises dehydrogenating, in the presence of dehydrogenating catalyst at dehydrogenation conditions, a dehydrogenation charge stream containing a cyclohexyl benzene and, as a diluent-carrier, benzene thereby forming a dehydrogenated product stream containing biphenyl and benzene; separating said benzene from said product stream; and recovering said product stream containing biphenyl.
Claim 18
Independent Claim 55 words
The method which comprises dehydrogenating, in the presence of dehydrogenating catalyst at dehydrogenation conditions, a dehydrogenation charge stream containing a dicyclohexyl benzene and, as a diluent-carrier, benzene or a cyclohexyl benzene thereby forming a dehydrogenated product stream containing terphenyl and diluent-carrier; separating said diluent-carrier from said product stream; and recovering said product stream containing terphenyl.
Claim 19
Independent Claim 55 words
The method which comprises dehydrogenating, in the presence of dehydrogenating catalyst at dehydrogenation conditions, a dehydrogenation charge stream containing a dicyclohexyl benzene and, as a diluent-carrier, benzene or a cyclohexyl benzene thereby forming a dehydrogenated product stream containing terphenyl and diluent-carrier; separating said diluent-carrier from said product stream; and recovering said product stream containing terphenyl.

References Cited (Backward Citations)

US3784618A Cited
US3784619A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-06-08 1979-12-08 1980-06-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-06-08 1983-12-08 1984-06-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-06-08 1987-12-08 1988-06-08 $7700.00 Window Closed / Lapsed

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