Core-in-shell composite adsorbent for use in PSA prepurifiers
The present invention relates generally to an attrition resistant core-in-shell composite adsorbent comprising at least a zeolite-containing CO 2 removal adsorbent and a binder on an inert dense core. The attrition resistant core-in-shell composite adsorbent has an attrition loss of less than about 2 wt %. The core-in-shell composite adsorbent is preferably used in a multi-layered adsorption system in a cyclic adsorption process, preferably used in a PSA prepurification process prior to cryogenic air separation.
1. A multi-layered PSA adsorption system for purifying a gaseous feed containing less than about 5% CO 2 in a cyclic adsorption process, wherein said system comprises two or more adsorbent layers wherein the first layer comprises a water and/or water vapor removing adsorbent and the second layer comprises a CO 2 removing adsorbent, wherein said CO 2 removing adsorbent is a core-in-shell composite adsorbent comprising an inert dense core, and an adsorptive shell, wherein said adsorptive shell comprises at least one zeolite-containing CO 2 removal adsorbent and a binder, wherein the core to bead diameter ratio of said composite adsorbent ranges from about 50% to about 90% and wherein said binding agent comprises greater than about 10 wt % of the adsorptive shell material, wherein the attrition loss of said core-in-shell composite adsorbent is less than about 2 wt %, and wherein volumetric performance of said adsorbent is greater than or equal to 0.70 BSF (m3/s.m2).
2. The adsorption system of claim 1 wherein said binder is a clay selected from a group comprising attapulgite, sepiolite, kaolin, haloysite and mixtures thereof.
3. The adsorption system of claim 1 wherein the volumetric performance of core-in-shell adsorbent is greater than or equal to 0.76 BSF (m3/s.m2).
4. The adsorption system of claim 1 wherein the zeolite is type X and has a SiO 2 /Al 2 O 3 ratio of about less than or equal to 2.5.
5. The adsorption system of claim 1 wherein the first layer is activated alumina and the inert dense core in the core-in-shell adsorbent of the second layer is sand.
6. A cyclic adsorption process for removing at least water and CO 2 from a gaseous water and CO 2 containing feed stream comprising contacting the feed stream with the adsorption system of claim 1 .
7. A core-in-shell composite adsorbent for use in purifying a process gas stream containing less than about 5% CO 2 in an adsorption process, said composite comprising an adsorptive shell on an inert dense core, wherein said adsorptive shell comprises a zeolite-containing CO 2 removal adsorbent and a clay binding agent wherein the clay binder constitutes greater than about 10 wt % of the adsorptive shell and the core to bead diameter ratio ranges from about 50% to about 90%, wherein the attrition loss of said core-in-shell composite adsorbent is less than about 2 wt %, and wherein volumetric performance of said adsorbent is greater than or equal to 0.70 BSF (m3/s.m2).
8. The adsorbent of claim 7 wherein the inert dense core is naturally occurring sand.
9. The adsorbent of claim 7 wherein the zeolite is type X and has a SiO 2 /Al 2 O 3 ratio of about 2.0.
10. A cyclic adsorption process for removing CO 2 from a gaseous feed stream containing at least water and CO 2 comprising contacting the feed stream with the adsorbent of claim 7 and recovering the CO 2 depleted stream.
11. The adsorbent of claim 7 used for removing CO 2 from air in a PSA adsorption process.
12. A cyclic gas adsorption process for removing at least CO 2 from a gas stream having less than 5% CO 2 , the process comprising contacting the gas stream with a multilayer adsorption system comprising two or more adsorbent layers wherein the first adsorbent layer comprises at least a water and/or water vapor removing adsorbent and the second adsorbent layer comprises a core-in-shell composite adsorbent comprising at least a zeolite-containing CO 2 removal adsorbent shell on an inert dense core, wherein the core to bead diameter ratio ranges from about 50% to about 90%, wherein the attrition loss of said core-in-shell composite adsorbent is less than 2 wt %, wherein volumetric performance of said adsorbent is greater than or equal to 0.70 BSF (m3/s.m2), and recovering the CO 2 depleted gas stream.
13. The process of claim 12 wherein the CO 2 removal adsorbent also removes nitrogen oxides, hydrocarbons or both.
14. The process of claim 12 wherein the zeolite is type X and has a SiO 2 /Al 2 O 3 ratio of about less than or equal to 2.5.
15. The process of claim 12 wherein the zeolite is type X and has a SiO 2 /Al 2 O 3 ratio of about 2.0.
16. The process of claim 12 wherein the adsorption process is selected from PSA, TSA and VPSA processes.
17. The process of claim 12 wherein the process is a PSA prepurification process for the removal of at least water and CO 2 in air prior to a cryogenic air separation process.
18. The composite adsorbent of claim 7 wherein the core to bead diameter ratio ranges from about 60 to 80%.