Abstract A type A zeolite corresponding to the formula x Me II O · n ME I 2 O · Al 2 O 3 · (1.85 ± 0.5) SiO 2 in which Me I is a monovalent metal; Me II is a divalent metal; x has a value of at least 0.80; and n has a value of (1.0 ± 0.2) - x Is produced by treating a type Na-A zeolite with a solution of a divalent metal salt to replace sodium and introduce x moles of the divalent metal. This introduces far more divalent metal than is needed for adsorption but the resulting zeolite does not undergo the loss in adsorptive capacity upon regeneration in the presence of water vapor which is exhibited by those of a lower degree of exchange. The new zeolites are particularly suitable for treatment of a mixture of substances comprising a polar or polarizable substances and less polar or less polarizable substances, a mixture of nitrogen and oxygen and a mixture of CO 2 with other gases.
A process for separating a mixture of substances, comprising treating a type Na-A zeolite with a solution of a calcium salt to replace sodium and introduce x moles of calcium, the zeolite then having the formula xCaO . nNa.sub.2 O . Al.sub.2 O.sub.3 . (1.85 ± 0.5) SiO.sub.2 in which x has a value of at least 0.80; and n has a value of (1.0 ± 0.2) - x, and contacting the modified zeolite with the mixture of substances selectively to adsorb on the zeolite predetermined ones of said substances, desorbing said substances, regenerating the zeolite in the presence of water vapor, the adsorptive capacity following regeneration remaining substantially as high as at the outset, and repeating the adsorption, desorption and regeneration.
Claim 2
Dependent Claim
122 words
A process for separating a mixture of substances, comprising treating a type Na-A zeolite with a solution of a calcium salt to replace sodium and introduce x moles of calcium, the zeolite then having the formula xCaO . nNa.sub.2 O . Al.sub.2 O.sub.3 . (1.85 ± 0.5) SiO.sub.2 in which x has a value of at least 0.80; and n has a value of (1.0 ± 0.2) - x, and contacting the modified zeolite with the mixture of substances selectively to adsorb on the zeolite predetermined ones of said substances, desorbing said substances, regenerating the zeolite in the presence of water vapor, the adsorptive capacity following regeneration remaining substantially as high as at the outset, and repeating the adsorption, desorption and regeneration.
Claim 3
Dependent Claim
27 words
A process as claimed in claim 1 wherein the mixture of substances comprises a mixture of polar or polarizable substances and less polar or less polarizable substances.
Claim 4
Dependent Claim
19 words
A process as claimed in claim 1 wherein the mixture of substances comprises a mixture of nitrogen and oxygen.
Claim 5
Dependent Claim
21 words
A process as claimed in claim 1 wherein the mixture of substances comprises a mixture of CO 2 with other gases.