Abstract A solid adsorbent useful for the separation of para-xylene from a mixture of C8 aromatic hydrocarbons. The adsorbent is prepared by the steps of: ion-exchanging a precursor mass containing type X or type Y zeolite and amorphous material with an aqueous sodium hydroxide solution to effect the addition of sodium cations to the zeolite structure, ionexchanging the sodium-exchanged mass to effect the essentially complete exchange of sodium cations, and drying the resulting material at conditions to reduce the LOI at 900 DEG C. to less than about 10 wt. %. The sodium cations can be essentially completely exchanged with barium and potassium cations in a weight ratio of from about 1.5 to 200 or with barium alone. I have found that the sodium hydroxide exchange step produces an adsorbent that has faster adsorption-desorption rates for the desired para-xylene isomer and permits a suitable adsorbent to be produced which contains barium cations alone.
A solid adsorbent produced by the steps of: a. contacting a precursor mass comprising a X or Y structured zeolite having a Na 2 O/Al 2 O 3 ratio less than about 0.7 with an aqueous sodium hydroxide solution at first ion-exchange conditions to increase the sodium cations content to a Na 2 O/Al 2 O 3 ratio of greater than about 0.7; b. treating the sodium-exchanged mass at second ionexchange conditions to effect the essentially complete exchange of sodium cations; and, c. drying the resulting exchanged mass at conditions sufficient to reduce the LOI at 900° C. to less than about 10 wt. %.
Claim 2
Dependent Claim
105 words
A solid adsorbent produced by the steps of: a. contacting a precursor mass comprising a X or Y structured zeolite having a Na 2 O/Al 2 O 3 ratio less than about 0.7 with an aqueous sodium hydroxide solution at first ion-exchange conditions to increase the sodium cations content to a Na 2 O/Al 2 O 3 ratio of greater than about 0.7; b. treating the sodium-exchanged mass at second ionexchange conditions to effect the essentially complete exchange of sodium cations; and, c. drying the resulting exchanged mass at conditions sufficient to reduce the LOI at 900° C. to less than about 10 wt. %.
Claim 3
Dependent Claim
43 words
The adsorbent of claim 1 further characterized in that said first ion-exchange conditions include a temperature within the range of from about 50° F. to about 250° F. and a sodium hydroxide solution concentration of from about 0.5 to about 10 wt. %.
Claim 4
Dependent Claim
42 words
The adsorbent of claim 1 further characterized in that said second ion-exchange conditions include a pH sufficient to preclude formation of the hydrogen form of the zeolite, and a temperature within the range of from about 50° F. to about 250° F.
Claim 5
Dependent Claim
31 words
The adsorbent of claim 1 further characterized in that the sodium cations are essentially completely exchanged with barium and potassium cations in a weight ratio of from about 1.5 to 200.
Claim 6
Dependent Claim
17 words
The adsorbent of claim 1 further characterized in that cations are essentially completely exchanged with barium cations.
Claim 7
Dependent Claim
24 words
The adsorbent of claim 1 further characterized in that it is in a particle size range of about 16 to 40 U.S. Standard Mesh.