Ion exchange material prepared from partially pyrolyzed macroporous polymer particles

Claim 2

Macroporous, carbonaceous particles having high resistance to crushing and particle sloughage and bearing functional groups selected from the group consisting of ion exchange functional groups and precursors thereof, the particles being derived from carbonaceous, macroporous polymer adsorbent particles which (a) comprise the product of controlled thermal degradation at a temperature of about 300° C. to about 800° C. of a macroporous synthetic polymer containing macropores ranging from about 5 to about 10,000 nanometers in average critical dimension and containing a carbon-fixing moiety, (b) are themselves derived from one or more ethylenically unsaturated monomers, or monomers which may be condensed to yield macroporous polymers, or mixtures thereof, one of the monomers being styrene, and (c) have at least 85% by weight of carbon, multimodal pore distribution with macropores ranging in size from about 5 to about 10,000 nanometers in average critical dimension, and a carbon-to-hydrogen atom ratio of between about 1.5:1 and about 20:1.

Claim 3

Carbonaceous particles according to claim 1 wherein the functional groups are precursors of ion exchange functional groups.

Claim 4

Carbonaceous particles according to claim 2 wherein the functional groups are present at a level of at least about 3% by weight of the particles.

Claim 5

Carbonaceous particles according to claim 2 wherein the functional groups are present at a level of at least about 5% by weight of the particles.

Claim 6

Carbonaceous particles according to claim 2 wherein the functional groups are present at a level of at least about 8% by weight of the particles.

Claim 7

Carbonaceous particles according to claim 2 wherein the functional groups are selected from the group consisting of covalent chlorine, covalent bromine, chloromethyl, bromomethyl, and amidomethyl.

Claim 8

Carbonaceous particles according to claim 1 wherein the functional groups are ion exchange functional groups.

Claim 9

Carbonaceous particles according to claim 7 wherein the functional groups are present at a level of at least about 0.2 milliequivalents per gram of the particles.

Claim 10

Carbonaceous particles according to claim 7 wherein the functional groups are present at a level of at least about 0.5 milliequivalents per gram of the particles.

Claim 11

Carbonaceous particles according to claim 7 wherein the functional groups are present at a level of at least about 1 milliequivalent per gram of the particles.

Claim 12

Carbonaceous particles according to claim 7 wherein the ion exchange functional groups are anion exchange groups.

Claim 13

Carbonaceous particles according to claim 11 wherein the anion exchange groups are selected from the group consisting of amino, alkyl monosubstituted amino wherein the alkyl group contains 1-6 carbon atoms, alkyl disubstituted amino wherein the alkyl groups are independently selected and contain 1-6 carbon atoms, polyamino alkyl, alkyl substituted polyaminoalkyl, quaternary amino and alkyl substituted quaternary amino wherein the alkyl groups are independently selected and contain 1-6 carbon atoms per amine nitrogen.

Claim 14

Carbonaceous particles according to claim 7 wherein the ion exchange functional groups are cation exchange groups.

Claim 15

Carbonaceous particles according to claim 13 wherein the cation exchange groups are selected from the group consisting of sulfonic acid and carboxylic acid.

Claim 16

A process for preparing functionalized carbonaceous particles useful as selective adsorbents, ion exchange materials or precursors thereof, which process comprises reacting, at a temperature from about room temperature to about 500° C., a reagent selected from the group consisting of halogen gas, sulfuryl halide, halosulfonic acid, sulfuric acid, nitric acid, bis-halomethylmethyl ether, and N-hydroxymethyl-N-alkylformamides, with carbonaceous, macroporous polymer adsorbent particles which (a) comprise the product of controlled thermal degradation at a temperature from about 300° C. to about 800° C., of a macroporous, synthetic polymer containing macropores ranging from about 5 to about 10,000 nanometers in average critical dimension and containing a carbon-fixing moiety, (b) are derived from one or more ethylenically unsaturated monomers, or monomers which may be condensed to yield macroporous polymers, or mixtures thereof, one of the monomers being styrene, and (c) have at least 85% by weight of carbon, multimodal pore distribution with macropores ranging in size from about 5 to about 10,000 nanometers in average critical dimension, and a carbon-to-hydrogen atom ratio of between about 1.5:1 and about 20:1.

Claim 17

A process for preparing functionalized carbonaceous particles useful as selective adsorbents, ion exchange materials or precursors thereof, which process comprises reacting, at a temperature from about room temperature to about 500° C., a reagent selected from the group consisting of halogen gas, sulfuryl halide, halosulfonic acid, sulfuric acid, nitric acid, bis-halomethylmethyl ether, and N-hydroxymethyl-N-alkylformamides, with carbonaceous, macroporous polymer adsorbent particles which (a) comprise the product of controlled thermal degradation at a temperature from about 300° C. to about 800° C., of a macroporous, synthetic polymer containing macropores ranging from about 5 to about 10,000 nanometers in average critical dimension and containing a carbon-fixing moiety, (b) are derived from one or more ethylenically unsaturated monomers, or monomers which may be condensed to yield macroporous polymers, or mixtures thereof, one of the monomers being styrene, and (c) have at least 85% by weight of carbon, multimodal pore distribution with macropores ranging in size from about 5 to about 10,000 nanometers in average critical dimension, and a carbon-to-hydrogen atom ratio of between about 1.5:1 and about 20:1.

Claim 18

The process of claim 15 wherein the reagent is selected from the group consisting of halogen gas, sulfuryl halide, halosulfonic acid and bi-halomethylmethyl ether, and the particles are subsequently reacted with a reagent selected from the group consisting of primary amines having 1-6 carbon atoms, secodary amines having 1-6 carbon atoms, and polyalkylene polyamines having 1-6 carbon atoms per amine nitrogen.

Claim 19

The process of claim 15 wherein the reagent is an N-hydroxymethyl-N-alkyl formamide, and the resulting amidomethyl groups are subsequently hydrolyzed with acid.

Claim 20

A process for removing ions from solution which comprises contacting the solution, for sufficient time to permit ion exchange, with macroporous, carbonaceous, particles bearing ion exchange functional groups, the particles being derived from carbonaceous, macroporous polymer adsorbent particles which (a) comprise the product of controlled thermal degradation, at a temperature of about 300° C. to about 800° C., of a macroporous, synthetic polymer containing macropores ranging from about 5 to about 10,000 nanometers in average critical dimension and containing a carbon-fixing moiety, (b) are themselves derived from one or more ethylenically unsaturated monomers, or monomers which may be condensed to yield macroporous polymers, or mixtures thereof, one of the monomers being styrene, and (c) have at least 85% by weight of carbon, multimodal pore distribution with macropores ranging in size from about 5 to about 10,000 nanometers in average critical dimension, and a carbon-to-hydrogen atom ratio of between about 1.5:1 and about 20:1.

Claim 21

A process for removing ions from solution which comprises contacting the solution, for sufficient time to permit ion exchange, with macroporous, carbonaceous, particles bearing ion exchange functional groups, the particles being derived from carbonaceous, macroporous polymer adsorbent particles which (a) comprise the product of controlled thermal degradation, at a temperature of about 300° C. to about 800° C., of a macroporous, synthetic polymer containing macropores ranging from about 5 to about 10,000 nanometers in average critical dimension and containing a carbon-fixing moiety, (b) are themselves derived from one or more ethylenically unsaturated monomers, or monomers which may be condensed to yield macroporous polymers, or mixtures thereof, one of the monomers being styrene, and (c) have at least 85% by weight of carbon, multimodal pore distribution with macropores ranging in size from about 5 to about 10,000 nanometers in average critical dimension, and a carbon-to-hydrogen atom ratio of between about 1.5:1 and about 20:1.

Claim 22

The process according to claim 18 wherein the solution has a density of from about 1.03 to about 1.2 grams per cubic centimeter, and the particles bearing ion exchange functional groups are separated from the solution by gravity subsequent to ion exchange.

Claim 23

The process according to claim 19 wherein the ions are uranyl ions and the functional groups are anion exchange groups.

Claim 24

The process according to claim 20 wherein the anion exchange groups are strongly basic.

Claim 25

A process for removing organic vapors from air which comprises contacting the air containing organic vapors with macroporous, carbonaceous particles bearing ion exchange functional groups, the particles being derived from carbonaceous, macroporous polymer adsorbent particles which (a) comprise the product of controlled thermal degradation at a temperature of about 300° C. to about 800° C. of a macroporous synthetic polymer containing macropores ranging from about 5 to about 10,000 nanometers in average critical dimension and containing a carbon-fixing moiety, (b) are themselves derived from one or more ethylenically unsaturated monomers, or monomers which may be condensed to yield macroporous polymers, or mixtures thereof, one of the monomers being styrene, and (c) have at least 85% by weight of carbon, multimodal pore distribution with macropores ranging in size from about 5 to about 10,000 nanometers in average critical dimension, and a carbon-to-hydrogen atom ratio of between about 1.5:1 and about 20:1.

Claim 26

A process for removing organic vapors from air which comprises contacting the air containing organic vapors with macroporous, carbonaceous particles bearing ion exchange functional groups, the particles being derived from carbonaceous, macroporous polymer adsorbent particles which (a) comprise the product of controlled thermal degradation at a temperature of about 300° C. to about 800° C. of a macroporous synthetic polymer containing macropores ranging from about 5 to about 10,000 nanometers in average critical dimension and containing a carbon-fixing moiety, (b) are themselves derived from one or more ethylenically unsaturated monomers, or monomers which may be condensed to yield macroporous polymers, or mixtures thereof, one of the monomers being styrene, and (c) have at least 85% by weight of carbon, multimodal pore distribution with macropores ranging in size from about 5 to about 10,000 nanometers in average critical dimension, and a carbon-to-hydrogen atom ratio of between about 1.5:1 and about 20:1.