초록 ▼

The present invention relates generally to a composite adsorbent comprising at least a zeolite-containing CO2 removal adsorbent and 10% or more of a metal oxide having a heat capacity of at least 20 cal/mol-° K (83.7 J/(mol·K). The composite is preferably used in a multi-layered adsorption system in

The present invention relates generally to a composite adsorbent comprising at least a zeolite-containing CO2 removal adsorbent and 10% or more of a metal oxide having a heat capacity of at least 20 cal/mol-° K (83.7 J/(mol·K). The composite is preferably used in a multi-layered adsorption system in a cyclic adsorption process. The adsorption system comprises two or more layers wherein the first layer is at least a water vapor removal adsorbent, such as activated alumina, and the second layer is the novel composite adsorbent. The adsorption system is preferably used in a PSA prepurification process prior to cryogenic air separation.

대표청구항 ▼

1. A multi-layered adsorption system for use in separating gases in a PSA or VPSA cyclic adsorption process comprising two or more adsorbent layers wherein the first layer is at least a water vapor removal adsorbent and the second layer is a composite adsorbent comprising agglomerated particles of 1

1. A multi-layered adsorption system for use in separating gases in a PSA or VPSA cyclic adsorption process comprising two or more adsorbent layers wherein the first layer is at least a water vapor removal adsorbent and the second layer is a composite adsorbent comprising agglomerated particles of 10-50% of a zeolite; 5-45% of activated alumina; and 10-50% of a metal oxide having a heat capacity of at least 20 cal/mol-° K (83.7 J/(mol·K)) in substantially uniform distribution and wherein the total of the zeolite, activated alumina and metal oxide equals 100 weight % as measured on a dry weight basis and the crush strength is more than about 4.5 Newtons (N) for particles in the 7×14 US mesh size range. 2. The adsorption system of claim 1 wherein the metal oxide selected from oxides of iron, cobalt, and lead. 3. The adsorption system of claim 2 wherein the metal oxide is one or more oxides of iron. 4. The adsorption system of claim 3 wherein the metal oxide is a naturally occurring iron ore rich in iron oxides. 5. The adsorption system of claim 3 wherein Fe3O4 is the predominant oxide species present. 6. The adsorption system of claim 3 wherein the zeolite is type X and has a SiO2/Al2O3 ratio of about less than or equal to 2.5. 7. The adsorption system of claim 1 wherein the composite has 40% of an X zeolite, 20% of activated alumina and 40% of a metal oxide selected from oxides of iron. 8. A cyclic adsorption process for removing at least water and CO2 from a gaseous water and CO2 containing feed stream comprising contacting the feed stream with the adsorption system of claim 1. 9. A composite adsorbent for use in removing at least CO2 from a process gas stream in a PSA or VPSA adsorption process comprising a zeolite-containing CO2 removal adsorbent comprising agglomerated particles of 10-50% of a zeolite; 5-45% of activated alumina; and 10-50% of a metal oxide having a heat capacity of at least 20 cal/mol-° K (83.7 J/(mol·K)) in substantially uniform distribution and wherein the total of the zeolite, activated alumina and metal oxide equals 100 weight % as measured on a dry weight basis and the crush strength is more than about 4.5 Newtons (N) for particles in the 7×14 US mesh size range. 10. The adsorbent of claim 9 wherein the composite contains a metal oxide selected from oxides of iron, cobalt, and lead. 11. The adsorbent of claim 10 wherein the metal oxide is a naturally occurring iron ore rich in iron oxides. 12. The adsorbent of claim 10 wherein the composite is one or more oxides of iron and Fe3O4 is the predominant oxide species present. 13. The adsorbent of claim 9 wherein the composite contains 40% of a zeolite, 20% of activated alumina and 40% of a metal oxide. 14. The adsorbent of claim 9 wherein the zeolite is type X and has a SiO2/Al2O3 ratio of about 2.0. 15. A cyclic adsorption process for removing CO2 from a gaseous feed stream containing at least water and not more than 5% CO2 comprising contacting the feed stream with the adsorption system of claim 9 and recovering the CO2 depleted stream. 16. A cyclic PSA or VPSA process for removing at least CO2 from a gas stream having less than 5% CO2, the process comprising contacting the gas stream with a multilayer adsorption system comprising two or more layers wherein the first layer is at least a water vapor removal adsorbent and the second layer is a composite comprising at least a zeolite-containing CO2 removal adsorbent and 10-50% of a zeolite; 5-45% of activated alumina; and 10-50% of metal oxide having a heat capacity of at least 20 cal/mol-° K (83.7 J/(mol·K)) and wherein the total of zeolite, activated alumina and metal oxide equals 100 weight % as measured on a dry weight basis and recovering the CO2 depleted gas stream. 17. The process of claim 16 wherein the adsorbent also removes nitrogen oxides, hydrocarbons or both. 18. The process of claim 16 wherein the metal oxide is selected from oxides of iron, cobalt, and lead. 19. The process of claim 18 wherein the metal oxide is one or more oxides of iron. 20. The system of claim 19 wherein the metal oxide is a naturally occurring iron ore rich in iron oxides. 21. The process of claim 19 wherein the Fe3O4 is the predominant oxide species present. 22. The process of claim 18 wherein the zeolite is type X and has a SiO2/Al2O3 ratio of about less than or equal to 2.5. 23. The process of claim 18 wherein the zeolite is type X and has a SiO2/Al2O3 ratio of about 2.0. 24. The process of claim 16 wherein the process is conducted at or near ambient temperature. 25. The process of claim 24 wherein the process is a PSA prepurification process for the removal of at least water and CO2 in air prior to a cryogenic air separation process.