Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
138 words
A method for the production of improved adsorbent particles having increased capacity for olefins and decreased catalytic activity from a precursor mass comprising sodium Y zeolite having a Na 2 O/Al 2 O 3 ratio less than about 0.7 and amorphous material selected from the group consisting of silica, alumina and slica-alumina mixtures and silica-alumina compounds which method comprises the steps of: a. contacting said precursor mass with an aqueous sodium hydroxide solution at ion exchange conditions to increase the sodium cation content to a Na 2 O/Al 2 O 3 ratio of greater than about 0.7 and to remove from about 1 to about 15 wt. % silica and alumina from the precursor mass; b. washing said mass with water to remove therefrom excess sodium hydroxide; and, c. at least partially dehydrating said mass at dehydrating conditions.
Claim 2
Independent Claim
138 words
A method for the production of improved adsorbent particles having increased capacity for olefins and decreased catalytic activity from a precursor mass comprising sodium Y zeolite having a Na 2 O/Al 2 O 3 ratio less than about 0.7 and amorphous material selected from the group consisting of silica, alumina and slica-alumina mixtures and silica-alumina compounds which method comprises the steps of: a. contacting said precursor mass with an aqueous sodium hydroxide solution at ion exchange conditions to increase the sodium cation content to a Na 2 O/Al 2 O 3 ratio of greater than about 0.7 and to remove from about 1 to about 15 wt. % silica and alumina from the precursor mass; b. washing said mass with water to remove therefrom excess sodium hydroxide; and, c. at least partially dehydrating said mass at dehydrating conditions.
Claim 3
Dependent Claim
44 words
The method of claim 1 further characterized in that said ion exchange conditions include a temperature within the range of from about 50° F. to about 300° F. and a sodium hydroxide solution concentration of from about 0.05 to about 10 wt. % NaOH.
Claim 4
Dependent Claim
43 words
The method of claim 2 further characterized in that said ion exchange conditions include a temperature within the range of the from about 150° F. to about 250° F. and a sodium hydroxide solution concentration of from about 0.5 to 5 wt. %.
Claim 5
Dependent Claim
27 words
The method of claim 1 further characterized in that said dehydration conditions include a temperature within the range of from about 100° F. to about 1000° F.
Claim 6
Dependent Claim
27 words
The method of claim 1 further characterized in that the wash water in step (b) is maintained at a pH within the range of 7 to 10.
Claim 7
Dependent Claim
126 words
An improved adsorbent having increased capacity for olefins and decreased catalytic activity produced by the steps of: a. contacting a precursor mass comprising sodium Y zeolite having a Na 2 O/Al 2 O 3 ratio less than about 0.7 and amorphous material selected from the group consisting of silica and alumina and silica-alumina mixtures and compounds with an aqueous sodium hydroxide solution at ion exchange conditions to increase the sodium cation content to a Na 2 O/Al 2 O 3 greater than about 0.7 and to remove from about 1 to about 15 wt. % of silica and alumina from the precursor mass; b. washing said mass with water to remove therefrom excess sodium hydroxide; and, c. at least partially dehydrating said mass at dehydrating conditions.
Claim 8
Dependent Claim
126 words
An improved adsorbent having increased capacity for olefins and decreased catalytic activity produced by the steps of: a. contacting a precursor mass comprising sodium Y zeolite having a Na 2 O/Al 2 O 3 ratio less than about 0.7 and amorphous material selected from the group consisting of silica and alumina and silica-alumina mixtures and compounds with an aqueous sodium hydroxide solution at ion exchange conditions to increase the sodium cation content to a Na 2 O/Al 2 O 3 greater than about 0.7 and to remove from about 1 to about 15 wt. % of silica and alumina from the precursor mass; b. washing said mass with water to remove therefrom excess sodium hydroxide; and, c. at least partially dehydrating said mass at dehydrating conditions.
Claim 9
Dependent Claim
26 words
The adsorbent of claim 6 further characterized in that the volatile content of said adsorbent is less than about 10 wt. % LOI at 900° C.
Claim 10
Dependent Claim
25 words
The adsorbent of claim 6 further characterized in that it is in a particle size range of about 16 to about 40 U.S. Standard mesh.