Separation and recovery of xylose using weakly basic anion exchange resins
US-9777342-B2 · Oct 3, 2017 · US
US9945000B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9945000-B2 |
| Application number | US-201615133529-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 20, 2016 |
| Priority date | Apr 21, 2015 |
| Publication date | Apr 17, 2018 |
| Grant date | Apr 17, 2018 |
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Acid hydrolysis of biomass is an important step for releasing the component sugars before converting them to fuels and/or biochemicals. During such a process, a significant amount of mineral acid, such as sulfuric acid, is used. In most cases, the residual acid is neutralized with lime before the sugar conversion step. By doing so, a waste calcium sulphate stream is generated and sent to disposal. The efficient separation of acid from the sugars would allow the recycle of the acid and make the entire process more economically viable. We found that a resin bed packed with an acid retardation resin can be used to achieve an efficient separation (i.e. 98.5% recovery of the acid) of the sulfuric acid from the sugars. The resin bed can be simply regenerated with water.
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The invention claimed is: 1. A method for treating a biomass hydrolysate solution containing an acid and non-ionic organic compound, the method comprising: feeding the hydrolysate solution to a fixed-resin bed of an acid retardation unit, the acid retardation unit comprising a base and a top opposite the base, and the fixed-resin incorporating a particulate quaternary ammonium resin retaining the acid and rejecting the non-ionic organic compound; and eluting the acid retained in the fixed-resin with water to recover a purified acid, wherein more than 90% by weight of the acid in the biomass hydrolysate solution is recovered. 2. The method of claim 1 wherein more than 75% by weight of the non-ionic organic compound in the biomass hydrolysate is recovered. 3. The method of claim 1 wherein the hydrolysate is fed into a base of the acid retardation unit up through the fixed-resin bed. 4. The method claim 1 wherein the water eluting the acid is into the top of the acid retardation unit down through the fixed-resin bed. 5. The method of claim 1 wherein the acid is at least one of sulfuric acid, phosphoric acid, nitric acid, hydrochloric acid, formic acid, lactic acid and succinic acid. 6. The method of claim 5 wherein the acid is sulfuric acid from 1 to 98% H2SO4. 7. The method of claim 1 wherein the non-ionic organic compound is at least one of a soluble sugar and soluble alcohol. 8. The method of claim 1 wherein the non-ionic organic compound is a sugar. 9. The method of claim 1 wherein the particulate quaternary ammonium resin is under compression within the fixed-resin bed. 10. The method of claim 1 , wherein the particulate quaternary ammonium resin has a constant average particle size of 50 μm. 11. The method of claim 1 , wherein the feeding of the hydrolysate has a duration of 2 to 5 minutes. 12. The method of claim 1 , wherein the eluting the acid has a duration of 2 to 5 minutes.
using only anionic ion-exchange material (C13B20/148 takes precedence) · CPC title
Removal of organic impurities · CPC title
Xylose · CPC title
obtained otherwise than by reactions only involving unsaturated carbon-to-carbon bonds · CPC title
obtained by saccharification of cellulosic materials (manufacture of fodder A23K10/32) · CPC title
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