Pal Siddhartha, Joy Shereena, Trimukhe Kalpana D, Kumbhar Pramod S, Varma Anjani J, Padmanabhan Sasisanker
Praj Matrix R&D Center, Urawade, Pune, Maharashtra, India.
Department of Technology, Savitribai Phule Pune University, Ganeshkhind, Pune, Maharashtra, India.
3 Biotech. 2016 Dec;6(2):126. doi: 10.1007/s13205-016-0446-2. Epub 2016 Jun 7.
Pretreatment and enzymatic hydrolysis play a critical role in the economic production of sugars and fuels from lignocellulosic biomass. In this study, we evaluated diverse pilot-scale pretreatments and different post-pretreatment strategies for the production of fermentable sugars from sugarcane bagasse. For the pretreatment of bagasse at pilot-scale level, steam explosion without catalyst and combination of sulfuric and oxalic acids at low and high loadings were used. Subsequently, to enhance the efficiency of enzymatic hydrolysis of the pretreated bagasse, three different post-pretreatment process schemes were investigated. In the first scheme (Scheme 1), enzymatic hydrolysis was conducted on the whole pretreated slurry, without treatments such as washing or solid-liquid separation. In the second scheme (Scheme 2), the pretreated slurry was first pressure filtered to yield a solid and liquid phase. Following filtration, the separated liquid phase was remixed with the solid wet cake to generate slurry, which was then subsequently used for enzymatic hydrolysis. In the third scheme (Scheme 3), the pretreated slurry was washed with more water and filtered to obtain a solid and liquid phase, in which only the former was subjected to enzymatic hydrolysis. A 10 % higher enzymatic conversion was obtained in Scheme 2 than Scheme 1, while Scheme 3 resulted in only a 5-7 % increase due to additional washing unit operation and solid-liquid separation. Dynamic light scattering experiments conducted on post-pretreated bagasse indicate decrease of particle size due to solid-liquid separation involving pressure filtration provided increased the yield of C6 sugars. It is anticipated that different process modification methods used in this study before the enzymatic hydrolysis step can make the overall cellulosic ethanol process effective and possibly cost effective.
预处理和酶水解在从木质纤维素生物质经济生产糖类和燃料的过程中起着关键作用。在本研究中,我们评估了多种中试规模的预处理方法以及不同的预处理后策略,用于从甘蔗渣生产可发酵糖。对于中试规模的甘蔗渣预处理,使用了无催化剂的蒸汽爆破以及低负荷和高负荷的硫酸与草酸组合。随后,为提高预处理甘蔗渣的酶水解效率,研究了三种不同的预处理后工艺方案。在第一种方案(方案1)中,对整个预处理后的浆料进行酶水解,不进行洗涤或固液分离等处理。在第二种方案(方案2)中,首先对预处理后的浆料进行压滤,得到固相和液相。过滤后,将分离出的液相与固体湿滤饼重新混合形成浆料,然后用于酶水解。在第三种方案(方案3)中,用更多的水洗涤预处理后的浆料并过滤,得到固相和液相,其中仅对前者进行酶水解。方案2的酶转化率比方案1高10%,而方案3由于额外的洗涤单元操作和固液分离,仅提高了5 - 7%。对预处理后甘蔗渣进行的动态光散射实验表明,由于涉及压滤的固液分离导致颗粒尺寸减小,提高了C6糖的产率。预计本研究在酶水解步骤之前使用的不同工艺改进方法可使整个纤维素乙醇工艺有效且可能具有成本效益。