초록 ▼

This invention relates to the use of pore mouth control of zeolite NaA for developing a novel molecular sieve adsorbents and their potential in the separation and purification of gaseous mixtures by the size/shape selective adsorption. More specifically,the invention relates to the manufacture and u

This invention relates to the use of pore mouth control of zeolite NaA for developing a novel molecular sieve adsorbents and their potential in the separation and purification of gaseous mixtures by the size/shape selective adsorption. More specifically,the invention relates to the manufacture and use of a molecular sieve adsorbent, which is selective towards oxygen from its gaseous mixture with nitrogen and argon by pore mouth control of zeolite NaA with liquid phase alkoxide deposition on the external surface 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 ▼

1. A process for the preparation of a molecular sieve adsorbent for the size/shape selective separation of air, which comprises (1) activating a commercially available zeolite A at a temperature in the range of from 350 to 450° C. to eliminate physically adsorbed water, for a period of time ranging

1. A process for the preparation of a molecular sieve adsorbent for the size/shape selective separation of air, which comprises (1) activating a commercially available zeolite A at a temperature in the range of from 350 to 450° C. to eliminate physically adsorbed water, for a period of time ranging from 3 to 6 hours; (2) cooling the activated zeolite in a desiccator under vacuum in the range of from 1×10?2 to 1×10?4 mm Hg; (3) treating the cooled zeolite with tetra alkyl ortho silicate dissolved in a dry solvent at a concentration ranging from 0.1 to 1.0 wt. %/volume for a specified period of time in the range of from 4 to 8 hours under continuous stirring; (4) recovering the solvent by conventional techniques for re-use; (5) drying the treated zeolite in air in static condition at an ambient temperature in the range of from 20 to 35° Celsius to provide a modified zeolite; (6) heating the modified zeolite to a temperature in the range of from 450 to 600° Celsius for a period of time ranging from 3 to 8 hours; and (7) cooling the zeolite at ambient temperature in static conditions to provide the molecular sieve adsorbent having a preferential oxygen adsorption selectivity over nitrogen and argon.2. The process as claimed in claim 1, wherein from 0.10 to 1.00 weight percent of tetra alkyl ortho silicate was deposited uniformly on the zeolite surface from its dry solution in the dry solvent.3. The process as claimed in claim 2, wherein the said tetra alkyl ortho silicate deposition on the zeolite surface was carried out in a simple liquid phase reaction at ambient temperature and pressure conditions.4. The process as claimed in claim 3 wherein the tetra alkyl ortho silicate deposited on the zeolite surface was converted into silica by calcination in air at 500 to 650° C. for 3 to 6 hours.5. The process as claimed in claim 4 wherein the adsorbent as prepared is useful for the separation and purification of nitrogen and argon from its mixture with oxygen.6. The process as claimed in claim 5 wherein the adsorbent as prepared is useful for the chromatographic separation of oxygen, nitrogen and argon from its mixture.7. The process as claimed in claim 3 wherein the adsorbent as prepared is useful for the separation and purification of nitrogen and argon from its mixture with oxygen.8. The process as claimed in claim 3 wherein the adsorbent as prepared is useful for the chromatographic separation of oxygen, nitrogen and argon from its mixture.9. The process as claimed in claim 2 wherein the tetra alkyl ortho silicate deposited on the zeolite surface was converted into silica by calcination in air at 500 to 650° C. for 3 to 6 hours.10. The process as claimed in claim 1, wherein the said tetra alkyl ortho silicate deposition on the zeolite surface was carried out in a simple liquid phase reaction at ambient temperature and pressure conditions.11. The process as claimed in claim 1 wherein the tetra alkyl ortho silicate deposited on the zeolite surface was converted into silica by calcination in air at 500 to 650° C. for 3 to 6 hours.12. The process as claimed in claim 1 wherein the adsorbent as prepared is useful for the separation and purification of nitrogen and argon from its mixture with oxygen.13. The process as claimed in claim 1 wherein the adsorbent as prepared is useful for the chromatographic separation of oxygen, nitrogen and argon from its mixture.14. The process as claimed in claim 1 wherein the tetra alkyl ortho silicate deposited on the zeolite surface was converted into silica by calcination in air at 550° C. for 4 hours.15. The process as claimed in claim 1 wherein the commercially available zeolite A comprises a sodium zeolite A having the general formula, (Na2O)6.(Al2O3)6.(SiO2)12+x.wH2On where the value of x varies from 0.001 to 0.1, and w is the number of moles of water.