Department of Chemical Engineering, Lund University, Box 124, SE-221 00 Lund, Sweden.
Biotechnol Biofuels. 2014 May 23;7:77. doi: 10.1186/1754-6834-7-77. eCollection 2014.
Mixing is an energy demanding process which has been previously shown to affect enzymatic hydrolysis. Concentrated biomass slurries are associated with high and non-Newtonian viscosities and mixing in these systems is a complex task. Poor mixing can lead to mass and/or heat transfer problems as well as inhomogeneous enzyme distribution, both of which can cause possible yield reduction. Furthermore the stirring energy dissipation may impact the particle size which in turn may affect the enzymatic hydrolysis. The objective of the current work was to specifically quantify the effects of mixing on particle-size distribution (PSD) and relate this to changes in the enzymatic hydrolysis. Two rather different materials were investigated, namely pretreated Norway spruce and giant reed.
Changes in glucan hydrolysis and PSD were measured as a function of agitation during enzymatic hydrolysis at fiber loadings of 7 or 13% water-insoluble solids (WIS). Enzymatic conversion of pretreated spruce was strongly affected by agitation rates at the higher WIS content. However, at low WIS content the agitation had almost no effect on hydrolysis. There was some effect of agitation on the hydrolysis of giant reed at high WIS loading, but it was smaller than that for spruce, and there was no measurable effect at low WIS loading. In the case of spruce, intense agitation clearly affected the PSD and resulted in a reduced mean particle size, whereas for giant reed the decrease in particle size was mainly driven by enzymatic action. However, the rate of enzymatic hydrolysis was not increased after size reduction by agitation.
The impact of agitation on the enzymatic hydrolysis clearly depends not only on feedstock but also on the solids loading. Agitation was found to affect the PSD differently for the examined pretreated materials spruce and giant reed. The fact that the reduced mean particle diameter could not explain the enhanced hydrolysis rates found for spruce at an elevated agitation suggests that mass transfer at sustained high viscosities plays an important role in determining the rate of enzymatic hydrolysis.
混合是一个耗能过程,先前已证明它会影响酶解。浓缩生物质浆料与高粘度和非牛顿粘度有关,在这些系统中混合是一项复杂的任务。混合不良会导致传质和/或传热问题以及酶分布不均匀,这两者都可能导致产率降低。此外,搅拌能量耗散可能会影响颗粒大小,进而影响酶解。本工作的目的是专门量化混合对粒度分布(PSD)的影响,并将其与酶解的变化联系起来。研究了两种截然不同的材料,即预处理过的挪威云杉和巨型芦苇。
在纤维负载为 7%或 13%不溶性固体(WIS)的酶解过程中,作为搅拌的函数,测量了葡萄糖水解和 PSD 的变化。在较高 WIS 含量下,预处理云杉的酶转化强烈受搅拌速率的影响。然而,在低 WIS 含量下,搅拌对水解几乎没有影响。在高 WIS 负荷下,搅拌对巨型芦苇的水解有一定的影响,但比云杉的影响小,在低 WIS 负荷下没有可测量的影响。在云杉的情况下,强烈的搅拌明显影响了 PSD,并导致平均粒径减小,而对于巨型芦苇,粒径的减小主要是由酶的作用驱动的。然而,搅拌后的粒径减小并没有增加酶解速率。
搅拌对酶解的影响不仅取决于原料,还取决于固体负荷。搅拌对所研究的预处理材料云杉和巨型芦苇的 PSD 有不同的影响。在高搅拌下,发现减小平均粒径并不能解释云杉水解速率的提高,这表明在持续高粘度下的传质在确定酶解速率方面起着重要作用。