Patent ID: 6864399
Filing Date: 2005-03-08
Classification: B01J,C07C,Y02P

Abstract:
1. In the production of ethylbenzene the method comprising: (a) supplying a feed stock containing benzene into a reaction zone and into contact with a molecular sieve catalyst comprising a zeolite beta alkylation catalyst formulated with a silica binder; (b) supplying ethylene to said reaction zone; (c) operating said reaction zone at temperature and pressure conditions in which benzene is in the liquid phase or in the supercritical phase to cause ethylation of said benzene in the presence of said alkylation catalyst at a primary activity; (d) recovering an alkylation product containing ethylbenzene from said reaction zone; (e) continuing the operation of said reaction zone until the activity of said catalyst for the ethylation of benzene decreases by a value of at least 0.1% from the primary activity of said catalyst for the ethylation of benzene; (f) terminating the operation of said reaction zone for the alkylation of benzene and instituting a regeneration procedure in which said catalyst is regenerated in an oxidizing environment at a average temperature in the course of said regeneration procedure of less than 500° C., (g) subsequent to said regeneration procedure, reinstituting the operation of said alkylation reaction zone by supplying benzene to said alkylation reaction zone containing said regenerated catalyst (h) operating said reaction zone at temperature arid pressure conditions effective to cause the ethylation of said benzene in the liquid phase or in the supercritical phase to cause ethylation of said benzene in the presence of said regenerated catalyst to produce ethylbenzene at a secondary activity of at least 95% of the primary activity, (i) continuing the operation of said alkylation reaction zone until the activity of said catalyst for the ethylation of benzene declines by an amount of at least 0.1% of the secondary activity; (j) terminating the operation of the alkylation reaction zone and secondly regenerating said catalyst in an oxidizing environment and at an average temperature of less than 500° C. to effect a regeneration of said catalyst, (k) supplying benzene and ethylene to said alkylation reaction zone containing said secondly regenerated catalyst; (l) operating said reaction zone at temperature and pressure conditions effective to cause the ethylation of benzene in liquid phase or in the supercritical phase to cause ethylation of said benzene in the presence of said regenerated catalyst to provide an initial tertiary activity for the ethylation of benzene of at least 95% of the secondary activity; (m) continuing the operation of said alkylation reaction zone until the activity of said regenerated catalyst for the ethylation of benzene declines by an amount of at least 0.1% of the tertiary activity; (n) terminating the operation of said alkylation reaction zone and thirdly regenerating said catalyst in an oxidizing environment and at an average temperature of less than 500° C. to effect a third regeneration of said catalyst; (o) supplying benzene and ethylene to said alkylation reaction zone containing said thirdly regenerated catalyst; and (p) operating said reaction zone at temperature and pressure conditions effective to cause the ethylation of benzene in liquid phase or in the supercritical phase to cause ethylation of said benzene in the presence of said regenerated catalyst to provide a quaternary activity for the ethylation of benzene of at least 95% of the tertiary activity wherein said zeolite beta exhibits a regeneration coefficient at the conclusion of at least three regenerations which is at least 105% of the value of the regeneration coefficient of the zeolite beta catalyst formulated with an aluminum binder in the same amount as the silica binder employed with the zeolite beta, wherein the zeolite beta alkylation catalyst formulated with a silica binder comprises a lanthanum-modified zeolite beta in which lanthanum ions are incorporated by ion exchange into the zeolite beta.