Supported poly(allyl)amine and derivatives for CO
Supported amine polymer adsorbents based on polymers containing only or primarily primary amines sites are to be used as regenerable adsorbents for CO 2 capture from ultra-dilute gas streams, such as ambient air, or from mixtures of gases containing preferably at least 10% oxygen. and can also be useful for use at the moderate gas pressures found in typical post-combustion capture processes, such as flue gas from large point sources such as coal-fired power plants. Preferred supported solid amine adsorbents of this invention are based on poly(allylamine) (“PAA”) and poly(vinyl amine) (“PVAm”), both of which are linear polymers, and their derivatives, containing substantially all primary amine groups, supported on substrates. Preferred such substrates include silica mesocellular foam (MCF) and mesoporous-γ-alumina, as well on mesoporous-γ-alumina coated throughout the pores of MCF, most preferably of monolithic structure. Preferred derivatives include the guanidinylated and cross-linked poly(allylamine) materials.
1. A process for removing CO 2 from a gas mixture, the gas mixture being selected from the group consisting of ambient air and mixtures of ambient air with a minor proportion of an effluent gas, or a flue gas, wherein the mixture contains at least 15% oxygen, at ambient temperatures, the process comprising passing the gas mixture through a porous substrate, selected from the group consisting of granular and monolithic mesocellular foam silica, granular and monolithic mesoporous-γ-alumina, and, granular and monolithic mesoporous-γ-alumina coated on mesocellular foam silica, the porous substrate being impregnated with a sorbent for CO 2 , wherein the sorbent is selected from the group consisting of poly(allylamine), and cross-linked and branched derivatives of the poly(allylamine), the sorbent having an average molecular weight below about 5000 Daltons, to form a CO 2 -loaded substrate-supported sorbent, and treating the CO 2 -loaded sorbent-impregnated substrate in a closed container, with process heat steam at a temperature of not greater than 120° C., to remove and capture the CO 2 from the CO 2 -loaded, sorbent-impregnated substrate and regenerate the CO 2 -loaded sorbent-impregnated substrate for reuse in the process for removing CO 2 from the gas mixture.
2. The process of claim 1 , wherein the average molecular weight of the poly(allylamine) and the cross-linked and branched derivatives of the poly(allylamine), is in the range of from about 500 to about 2200 Daltons.
3. The process of claim 1 , wherein the porous substrate is mesoporous-γ-alumina coated on mesocellular foam silica.
4. The process of claim 1 , wherein the gas mixture is ambient air.
5. The process of claim 1 , wherein the sorbent is poly(allylamine) having an average molecular weight below about 3000 Daltons.
6. The process of claim 5 , wherein the sorbent is a cross-linked poly(allylamine) cross-linked with epichlorhydrin.
7. The process of claim 1 , wherein the porous substrate is selected from the group consisting of mesocellular foam silica and mesoporous-γ-alumina.
8. The process of claim 7 , wherein the mesoporous-γ-alumina substrate is a macro- and mesoporous alumina in monolithic shape.
9. The process of claim 7 , wherein the substrate is mesocellular foam silica in monolithic shape.