Abstract
Phragmites australis (an invasive plant in North America) was used as feedstock for ABE (acetone-butanol-ethanol) fermentation by Clostridium saccharobutylicum. Sulphuric acid pretreated phragmites hydrolysate (SAEH) without detoxification inhibited butanol production (0.73 g/L butanol from 30 g/L sugars). The treatment of SAEH with resin L-493 prior the fermentation resulted in no inhibitory effects and an ABE titer of 14.44 g/L, including 5.49 g/L butanol was obtained, corresponding to an ABE yield and productivity of 0.49 g/g and 0.60 g/L/h, respectively. Dual functionality of the resin was realized by also using it as an in-situ product removal agent. Integrating in-situ product removal allowed for the use of high substrate concentrations without the typical product inhibition. Resin-detoxified SAEH was supplemented with neat glucose and an effective ABE titer of 33 g/L (including 13.7 g/L acetone, 16.4 g/L butanol and 1.9 g/L ethanol) was achieved with resin-based in-situ product removal, corresponding to an ABE yield and productivity of 0.41 g/g and 0.69 g/L/h, respectively. Both detoxification of the substrate and the products was achieved by the same resin, which was added prior the fermentation. Integrating hydrolysate detoxification and in-situ butanol removal in a batch process through single resin can potentially simplify cellulosic butanol production.
Highlights
Another major problem associated with ABE fermentation is end-product inhibition
Phragmites australis was treated with dilute sulphuric acid to generate sulfuric acid pretreated hydrolysates (SAH), which was further hydrolyzed enzymatically (CellicCTec 2, Novozyme, Denmark) to obtain fermentable sugars (SAEH)
The effect of inhibitor removal was investigated by fermenting the Sulphuric acid pretreated phragmites hydrolysate (SAEH) directly and after equilibrating with resin L-493 (Dow Canada, Calgary, AB), which was removed prior to fermentation
Summary
Butanol titers in a batch fermentation by C. acetobutylicum ATCC 824 (most commonly studied butanol producing strain) rarely exceed 13 g/L1. Such dilute product streams will cause high energy costs during downstream processing[15]. The overall goal is the utilization of phragmites with dilute sulphuric acid pretreatment as substrate for ABE fermentation, where detoxification of the feedstock (removal of phenolix, furans, etc.) and detoxification of the fermentation broth (in-situ product removal of butanol) are realized with a single sorption resin
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