title: Process evaluation of enzymatic hydrolysis with filtrate recycle for the production of high concentration sugars.
abstract: Process simulation and lab trials were carried out to demonstrate and confirm the efficiency of the concept that recycling hydrolysate at low total solid enzymatic hydrolysis is one of the options to increase the sugar concentration without mixing problems. Higher sugar concentration can reduce the capital cost for fermentation and distillation because of smaller retention volume. Meanwhile, operation cost will also decrease for less operating volume and less energy required for distillation. With the computer simulation, time and efforts can be saved to achieve the steady state of recycling process, which is the scenario for industrial production. This paper, to the best of our knowledge, is the first paper discussing steady-state saccharification with recycling of the filtrate form enzymatic hydrolysis to increase sugar concentration. Recycled enzymes in the filtrate (15-30% of the original enzyme loading) resulted in 5-10% higher carbohydrate conversion compared to the case in which recycled enzymes were denatured. The recycled hydrolysate yielded 10% higher carbohydrate conversion compared to pure sugar simulated hydrolysate at the same enzyme loading, which indicated hydrolysis by-products could boost enzymatic hydrolysis. The high sugar concentration (pure sugar simulated) showed inhibition effect, since about 15% decrease in carbohydrate conversion was observed compared with the case with no sugar added. The overall effect of hydrolysate recycling at WinGEMS simulated steady-state conditions with 5% total solids was increasing the sugar concentration from 35 to 141 g/l, while the carbohydrate conversion was 2% higher for recycling at steady state (87%) compared with no recycling strategy (85%). Ten percent and 15% total solid processes were also evaluated in this study.
authors.affiliation: Department of Forest Biomaterials, North Carolina State University, Raleigh, NC 27695, USA.
authors.forename: Ying
authors.initials: Y
authors.lastname: Xue
authors.forename: Jannov
authors.initials: J
authors.lastname: Rusli
authors.forename: Hou-Min
authors.initials: HM
authors.lastname: Chang
authors.forename: Richard
authors.initials: R
authors.lastname: Phillips
authors.forename: Hasan
authors.initials: H
authors.lastname: Jameel
mesh_terms: D018533:Biomass; D002241:Carbohydrates / Q000737:chemistry*; D002254:Carbonates / Q000737:chemistry; D002480:Cellulase / Q000737:chemistry; D002482:Cellulose / Q000737:chemistry*; D002851:Chromatography, High Pressure Liquid; D003198:Computer Simulation; D043364:Endo-1,4-beta Xylanases / Q000737:chemistry; D000431:Ethanol / Q000737:chemistry*; D005285:Fermentation; D006868:Hydrolysis; D008031:Lignin / Q000737:chemistry*; D059027:Recycling; D013440:Sulfides / Q000737:chemistry; D013464:Sulfuric Acids / Q000737:chemistry; D014934:Wood / Q000737:chemistry*; D014990:Xylans / Q000737:chemistry*
chemical_list: D002241:Carbohydrates; D002254:Carbonates; D013440:Sulfides; D013464:Sulfuric Acids; D014990:Xylans; C036909:lignocellulose; D000431:Ethanol; C005686:sodium carbonate; D002482:Cellulose; D008031:Lignin; D002480:Cellulase; D043364:Endo-1,4-beta Xylanases; C033158:sulfuric acid; C033479:sodium sulfide