Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
170 words
A process for producing aromatic compounds containing a high proportion of benzene which comprises passing a feed containing at least 50 weight percent of C 2 to C 10 aliphatic hydrocarbons to a first stage reaction zone where it is contacted under conversion conditions with a catalyst comprising an aluminosilicate zeolite characterized by a Constraint Index within the approximate range of 1 to 12 and a degree of acidity indicated by an alpha value of at least 3, and passing the effluent from the first stage reaction zone directly to a second stage reaction zone where it is contacted under conversion conditions with a catalyst comprising platinum and either a zeolite having a Constraint Index in the approximate range of 1 to 12, or a potassium form of zeolite L in which the number of protonic acid sites have been reduced by exchange with barium, strontium or calcium, said second stage catalyst having a low degree of acidity as indicated by an alpha value of no higher than about 1.
Claim 2
Dependent Claim
170 words
A process for producing aromatic compounds containing a high proportion of benzene which comprises passing a feed containing at least 50 weight percent of C 2 to C 10 aliphatic hydrocarbons to a first stage reaction zone where it is contacted under conversion conditions with a catalyst comprising an aluminosilicate zeolite characterized by a Constraint Index within the approximate range of 1 to 12 and a degree of acidity indicated by an alpha value of at least 3, and passing the effluent from the first stage reaction zone directly to a second stage reaction zone where it is contacted under conversion conditions with a catalyst comprising platinum and either a zeolite having a Constraint Index in the approximate range of 1 to 12, or a potassium form of zeolite L in which the number of protonic acid sites have been reduced by exchange with barium, strontium or calcium, said second stage catalyst having a low degree of acidity as indicated by an alpha value of no higher than about 1.
Claim 3
Dependent Claim
16 words
The process of claim 1 wherein the zeolite of said first stage catalyst is a ZSM-5.
Claim 4
Dependent Claim
19 words
The process of claim 2 wherein said ZSM-5 has an as synthesized silica/alumina ratio of about 25 to 1000.
Claim 5
Dependent Claim
27 words
The process of claim 3 wherein said ZSM-5 has gallium loaded therein in an amount of about 0.5 to 5% based on the weight of the catalyst.
Claim 6
Dependent Claim
21 words
The process of claim 4 wherein said gallium loaded ZSM-5 is calcined at a temperature of at least about 700° C.
Claim 7
Dependent Claim
29 words
The process of claim 5 wherein said calcining is carried out at a temperature of about 800° to 825° C. for a period of about 1 to 1.5 hours.
Claim 8
Dependent Claim
51 words
The process of claim 1 wherein said second stage catalyst comprises a zeolite having a Constraint Index in the approximate range of about 1 to 12, and an as synthesized silica/alumina ratio of at least about 25, and about 0.1 to 1.0% of platinum, based on the weight of the catalyst.
Claim 9
Dependent Claim
47 words
The process of claim 1 wherein said second stage catalyst comprises a potassium form of zeolite L in which the number of protonic acid sites has been reduced by exchange with barium ions, and about 0.1 to 1.0% of platinum based on the weight of the catalyst.
Claim 10
Dependent Claim
83 words
The process of claim 1 wherein the conversion conditions of said first stage reaction zone include a temperature of from about 450° C. to about 700° C., a pressure of from about one atmosphere to about 1000 psig, and a EHSV of from about 0.1 to about 50, and the conversion conditions of said second stage reaction zone include a temperature of about 450° to 595° C., a pressure of about one to 30 atmospheres, and a WHSV of about 1 to 50.