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US 8,076,527 B2Granted
Process for production of ethylbenzene from toluene and methane
AssigneeFina Technology, Inc.
InventorsJames R. Butler, Joseph E. Pelati
Life of this patent
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Abstract
A process for making ethylbenzene and/or styrene by reacting toluene with methane is disclosed. In one embodiment the process can include reacting toluene with methane to form a product stream comprising ethylbenzene and further processing the ethylbenzene to form styrene in an existing styrene production facility.
Claims13
A process for making ethylbenzene and styrene comprising:
- reacting toluene and methane in one or more reactors to form a first product stream comprising ethylbenzene and styrene;
- further processing at least a portion of the components of the first product stream in at least a portion of an existing styrene production facility;
- wherein the one or more reactors comprises a reaction zone and wherein the one or more reactors are capable of dissipating heat to maintain the reaction zone within a desired temperature range for reacting toluene and methane to form ethylbenzene and styrene;
- wherein the reaction zone comprises one or more catalyst sites comprising a catalyst selected from the group consisting of X zeolite, Y zeolite, mordenite, silicalite, and combinations thereof;
- wherein the catalyst is modified with molybdenum, sodium or other basic ion.
2 more elements
A process for making ethylbenzene and styrene comprising:
- reacting toluene and methane in one or more reactors to form a first product stream comprising ethylbenzene and styrene and one or more of benzene, toluene, and methane;
- sending the first product stream to a first separation apparatus that separates the stream into at least benzene;
- removing at least a portion of the benzene from the first separation apparatus;
- reacting the benzene with ethylene in an alkylation reactor to form ethylbenzene;
- and
- dehydrogenating the ethylbenzene to thereby form styrene;
- wherein at least a portion of one or more of the separation, alkylation, and dehydrogenation processes are performed utilizing the facilities of an existing styrene production facility;
- wherein the one or more reactors comprise a reaction zone capable of dissipating heat to maintain the reaction zone within a desired temperature range for reacting toluene and methane to form ethylbenzene and styrene;
- wherein the reaction zone comprises one or more catalyst sites comprising a catalyst selected from the group consisting of X zeolite, Y zeolite, mordenite, silicalite, and combinations thereof;
- wherein the catalyst is modified with molybdenum, sodium or other basic ion.
7 more elements
Dependencies are inferred from the claim text.