Functionalised alumina adsorbent materials for removal of contaminants from water
A composition is provided for removal of a target substance from a fluid stream. The composition may be used to remove polyfluorinated alkyl substances (PFAS) from water. The composition comprises a support material comprising an alumina; and a sorbent molecule that comprises a core polymer; wherein the core polymer is covalently linked to the support material; and wherein the sorbent molecule further comprises one or more covalently linked sorbent groups. Processes for removal of target substances such as PFAS are also provided.
1. A composition for removal of a poly- and perfluorinated alkyl substance (PFAS) from an aqueous liquid, the composition comprising:
a particulate support material comprising a bimodal alumina having pores within a mesoporous range and pores within a macroporous range;
(i) wherein a majority of the pores within the mesoporous range have an average pore size of between 2 nm and 50 nm; and
(ii) wherein the bimodal alumina has a BET pore volume within the mesoporous range of not less than around 0.20 cm 3 /g; and
a sorbent molecule that comprises a linear or branched core polymer selected from one or more of: poly(ethylenimine); poly(allylamine); poly(methylmethacrylate); poly(vinylalcohol); poly(vinylamine); poly(vinylchloride); poly(2-vinylpyridine); poly(3-vinylpyridine); or poly(4-vinylpyridine);
wherein the linear or branched core polymer is covalently linked to the particulate support material; and
wherein the sorbent molecule further comprises one or more covalently linked sorbent groups.
2. The composition of claim 1 , wherein the alumina has an average pore size within the mesoporous range of between about 2 about 20 nm.
3. The composition of claim 1 , wherein a majority of the pores within the macroporous range have an average pore size of between 1 μm and 10 μm.
4. The composition of claim 1 , wherein the core polymer comprises a linear or branched poly(ethylenimine) having a weight average molecular weight of not less thanaround 25 kDa.
5. The composition of claim 1 , wherein the covalently linked sorbent groups comprise one or more groups selected from:
a substituted or unsubstituted C1-C12 alkyl group; a substituted or unsubstituted C2-C12 alkenyl group; a substituted or unsubstituted C2-C12 alkynyl group; a substituted or unsubstituted C1-C12 alkoxy group; a substituted or unsubstituted C1-C12 acyl group; a substituted or unsubstituted aromatic hydrocarbon group; a substituted or unsubstituted aromatic group; a heterocyclic group; and a hydrogen atom.
6. The composition of claim 1 , wherein the core polymer comprises at least one tertiary amino group and wherein the at least one tertiary amino group is converted to a quaternary nitrogen.
7. The composition of claim 1 , wherein the core polymer comprises C1-C10 alkyl substituted linear poly(ethylenimine).
8. The composition of claim 1 , wherein the core polymer comprises C1-C6 alkyl substituted branched poly(ethylenimine).
9. The composition of claim 1 , wherein support material is in a form selected from: granular; powder; and spheroidal particles.
10. A process for removal of a target substance from a fluid stream that comprises water, the process comprising contacting the fluid stream with a composition as defined in claim 1 , and wherein the target substance comprises one or more poly- and perfluorinated alkyl substances (PFAS).
11. The process of claim 10 , wherein the PFAS is selected from a perfluorinated anionic surfactant compound, including one or more selected from the group consisting of:
perfluorobutane sulfonate (PFBS); perfluorobutanoic acid (PFBA); perfluoropentanoic acid (PFPeA); perfluorohexanesulfonate (PFHS); perfluorohexanoic acid (PFHA); perfluorooctanoic acid (PFOA); perfluorooctane sulfonate (PFOS); perfluorononanoic acid (PFNA); and perfluorodecanoic acid (PFDA); 6:2 fluorotelomer sulfonic acid (6:2 FTSA); and hexafluoropropylene oxide dimer acid (HFPO-DA).
12. The process of claim 10 , wherein the linear or branched PEI has weight average molecular weight of not less than around 25 kDa.
13. The process of claim 10 , wherein the particulate alumina is in a form selected from: granular; powder; and spheroidal particles.
14. The process of claim 10 , wherein the support material is comprised within a packed bed.
15. The process of claim 14 , wherein the support material is comprised within a filter unit.
16. A filter for the adsorption of one or more PFAS from a contaminated water source, wherein the filter comprises a composition as described in claim 1 .
17. The filter of claim 16 , wherein the filter is configured as a point-of-use (POU) filter.
18. The filter of claim 17 , wherein the filter is comprised within a replaceable cartridge.
19. The filter of claim 16 , wherein the filter is configured to be incorporated into a point-of-entry (POE) system.
20. The filter of claim 16 , wherein the composition is comprised within a packed bed that is configured to permit a minimum water flow rate there-through of at least 2 litres/min.