Conversion of bark-rich biomass mixture into fermentable sugar by two-stage dilute acid-catalyzed hydrolysis [An article from: Bioresource Technology]
Book Details
Author(s)K.H. Kim, M. Tucker, Q. Nguyen
PublisherElsevier
ISBN / ASINB000RR5SMQ
ISBN-13978B000RR5SM7
MarketplaceFrance 🇫🇷
Description
This digital document is a journal article from Bioresource Technology, published by Elsevier in . The article is delivered in HTML format and is available in your Amazon.com Media Library immediately after purchase. You can view it with any web browser.
Description:
Despite high availability and low cost, bark has not actively been considered as a biomass feedstock for producing bio-based products due to its high content of extractives and lignin. In this study, to investigate the feasibility of utilizing bark-rich sawmill residues for producing value-added materials, the mixed Hemlock hog fuel/pin chips (85:15 by dry weight) from a local sawmill were converted into fermentable sugar by two-stage dilute sulfuric acid-catalyzed hydrolysis. Combining the sugar yields from the first-stage (190 ^oC for 150 s with 1.1% acid) and second-stage (210 ^oC for 115 s with 2.5% acid) hydrolyses, which aimed to maximize the recovery of mannose/galactose and glucose, respectively, 13.6 g of glucose (46% theoretical maximum), 10.5 g of mannose and galactose (98% theoretical maximum), and 2.8 g of xylose (85% theoretical maximum) were obtained per 100 g of the original dry feedstock.
Description:
Despite high availability and low cost, bark has not actively been considered as a biomass feedstock for producing bio-based products due to its high content of extractives and lignin. In this study, to investigate the feasibility of utilizing bark-rich sawmill residues for producing value-added materials, the mixed Hemlock hog fuel/pin chips (85:15 by dry weight) from a local sawmill were converted into fermentable sugar by two-stage dilute sulfuric acid-catalyzed hydrolysis. Combining the sugar yields from the first-stage (190 ^oC for 150 s with 1.1% acid) and second-stage (210 ^oC for 115 s with 2.5% acid) hydrolyses, which aimed to maximize the recovery of mannose/galactose and glucose, respectively, 13.6 g of glucose (46% theoretical maximum), 10.5 g of mannose and galactose (98% theoretical maximum), and 2.8 g of xylose (85% theoretical maximum) were obtained per 100 g of the original dry feedstock.
