Washing Lime-Pretreated Rice Straw with Carbonated Water Facilitates Calcium Removal and Sugar Recovery in Subsequent Enzymatic Saccharification.

IF 1.2 Q4 BIOCHEMISTRY & MOLECULAR BIOLOGY Journal of applied glycoscience Pub Date : 2019-01-20 eCollection Date: 2019-01-01 DOI:10.5458/jag.jag.JAG-2018_0003
Kenji Yamagishi, Masakazu Ike, Di Guan, Ken Tokuyasu
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Abstract

Generally, Ca(OH)2 pretreatment of lignocellulosics for fermentable sugar recovery requires a subsequent washing step for calcium removal and pH control for optimized saccharification. However, washing Ca(OH)2-pretreated feedstock with water is considered problematic because of the low solubility of Ca(OH)2 and its adsorption to biomass. In this study, we estimated the availability of carbonated water for calcium removal from the slurry of Ca(OH)2-pretreated rice straw (RS). We tested two kinds of countercurrent washing sequences, four washings exclusively with water (W4) and two washings with water and subsequent two washings with carbonated water (W2C2). The ratios of calcium removal from pretreatment slurry after washing were 64.2 % for the W4 process and 92.1 % for the W2C2 process. In the W2C2 process, 49 % of the initially added calcium was recovered as CaO by calcination. In enzymatic saccharification tests under a CO2 atmosphere at 1.5 atm, in terms of recovery of both glucose and xylose, pretreated, feedstock washed through the W2C2 process surpassed that washed through the W4 process, which could be attributed to the pH difference during saccharification: 5.6 in the W2C2 process versus 6.3 in the W4 process. Additionally, under an unpressurized CO2 atmosphere at 1 atm, the feedstock washed through the W2C2 process released 78.5 % of total glucose residues and 90.0 % of total xylose residues. Thus, efficient removal of calcium from pretreatment slurry would lead to not only the recovery of added calcium but also the proposal of a new, simple saccharification system to be used under an unpressurized CO2 atmosphere condition.

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用碳酸水洗涤石灰预处理过的稻草有利于后续酶解糖化过程中钙的去除和糖的回收。
通常,用于可发酵糖回收的木质纤维素的Ca(OH)2预处理需要随后的洗涤步骤以去除钙并控制pH以优化糖化。然而,用水洗涤Ca(OH)2预处理的原料被认为是有问题的,因为Ca(OH)2的溶解度低,它对生物质的吸附。在这项研究中,我们估计了从Ca(OH)2预处理稻秆(RS)浆中去除钙的碳酸水的可用性。我们测试了两种逆流洗涤顺序,四次纯水洗涤(W4)和两次纯水洗涤和随后的两次碳酸水洗涤(W2C2)。水洗后预处理浆中钙的去除率W4工艺为64.2%,W2C2工艺为92.1%。在W2C2工艺中,49%的初始添加钙通过煅烧回收为CaO。在1.5 atm CO2气氛下的酶解糖化试验中,经过W2C2工艺洗涤的预处理原料的葡萄糖和木糖的回收率超过了通过W4工艺洗涤的原料,这可能是由于糖化过程中的pH值差异:W2C2工艺为5.6,而W4工艺为6.3。此外,在1atm的无加压CO2气氛下,经W2C2工艺洗涤的原料释放出总葡萄糖残基的78.5%和总木糖残基的90.0%。因此,有效地去除预处理料浆中的钙不仅可以回收添加的钙,还可以提出一种新的、简单的糖化系统,该系统可以在无加压的CO2气氛条件下使用。
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来源期刊
Journal of applied glycoscience
Journal of applied glycoscience BIOCHEMISTRY & MOLECULAR BIOLOGY-
自引率
9.10%
发文量
13
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