초록 ▼

The invention relates to the manufacture of molecular sieve adsorbents, which are selective towards oxygen from its gaseous mixture with argon and/or nitrogen. More particularly, this invention relates to the manufacture of molecular sieve adsorbents useful for the separation of oxygen-argon gaseous

The invention relates to the manufacture of molecular sieve adsorbents, which are selective towards oxygen from its gaseous mixture with argon and/or nitrogen. More particularly, this invention relates to the manufacture of molecular sieve adsorbents useful for the separation of oxygen-argon gaseous mixture. More specifically, the invention relates to the manufacture and use of a molecular sieve adsorbent by cation exchange in zeolites by rare earth cations to obtain oxygen selective adsorbent from its gaseous mixture with nitrogen and argon at ambient conditions of temperature and pressure. Thus prepared adsorbent is useful for the separation and purification of nitrogen and argon from its mixture with oxygen.

대표청구항 ▼

We claim: 1. A process for preparing a molecular sieve adsorbent for selective adsorption of oxygen from air, the process consisting essentially of: (i) exchanging zeolite X with water-soluble salt of a rare earth metal selected from the group consisting of cerium, europium, gadolinium and any mixt

We claim: 1. A process for preparing a molecular sieve adsorbent for selective adsorption of oxygen from air, the process consisting essentially of: (i) exchanging zeolite X with water-soluble salt of a rare earth metal selected from the group consisting of cerium, europium, gadolinium and any mixture thereof; (ii) filtering the mixture, washing the powder or pellet with heated distilled water until it is free from anions to obtain an exchanged zeolite; (iii) drying the exchanged zeolite; (iv) and activating the exchanged zeolite at the temperature range of 350 to 450�� C. for a period in the range of 3-6 hours followed by cooling under inert or vacuum, wherein Na cations of zeolite are exchanged with salts of the rare earth metals selected from chloride, nitrate and acetate, wherein the cation exchange is carried out at a temperature in the range of 30�� C. to 90�� C. for a period in the range of 4 to 8 hours, and wherein the adsorbent has adsorbence up to 850 mm Hg. 2. A process as claimed in claim 1 wherein the zeolite X is used in powder form has 100% crystallinity or pellet form. 3. A process as claimed in claim 1 wherein the cation exchange is carried out at a cation concentration in the range of 0.01 to 0.1 M solution. 4. A process as claimed in claim 1 wherein the exchanged zeolite is dried in a temperature range of 20�� C. to 80�� C. in air or under vacuum. 5. A process for preparing a molecular sieve adsorbent for selective adsorption of oxygen from air, the process consisting essentially of: (i) exchanging zeolite X with water-soluble salt of a rare earth metal selected from the group consisting of cerium, europium, gadolinium and any mixture thereof; (ii) filtering the mixture, washing the powder or pellet with heated distilled water until it is free from anions to obtain an exchanged zeolite; (iii) drying the exchanged zeolite; (iv) and activating the exchanged zeolite at the temperature range of 350 to 450�� C. for a period in the range of 3-6 hours followed by cooling under inert or vacuum, wherein Na cations of zeolite are exchanged with salts of the rare earth metals selected from chloride, nitrate and acetate, and wherein the cation exchange is carried out at a temperature in the range of 30�� C. to 90�� C. for a period in the range of 4 to 8 hours. 6. A process as claimed in claim 5 wherein the zeolite X is used in powder form has 100% crystallinity or pellet form. 7. A process as claimed in claim 5 wherein the cation exchange is carried out at a cation concentration in the range of 0.01 to 0.1 M solution. 8. A process as claimed in claim 5 wherein the exchanged zeolite is dried in a temperature range of 20�� C. to 80�� C. in air or under vacuum.