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Impact of dual temperature profile in dilute acid hydrolysis of spruce for ethanol production

机译:双温度曲线对云杉稀酸水解对乙醇生产的影响

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Background The two-step dilute acid hydrolysis (DAH) of softwood is costly in energy demands and capital costs. However, it has the advantage that hydrolysis and subsequent removal of hemicellulose-derived sugars can be carried out under conditions of low severity, resulting in a reduction in the level of sugar degradation products during the more severe subsequent steps of cellulose hydrolysis. In this paper, we discuss a single-step DAH method that incorporates a temperature profile at two levels. This profile should simulate the two-step process while removing its major disadvantage, that is, the washing step between the runs, which leads to increased energy demand. Results The experiments were conducted in a reactor with a controlled temperature profile. The total dry matter content of the hydrolysate was up to 21.1% w/w, corresponding to a content of 15.5% w/w of water insoluble solids. The highest measured glucose yield, (18.3 g glucose per 100 g dry raw material), was obtained after DAH cycles of 3 min at 209°C and 6 min at 211°C with 1% H2SO4, which resulted in a total of 26.3 g solubilized C6 sugars per 100 g dry raw material. To estimate the remaining sugar potential, enzymatic hydrolysis (EH) of the solid fraction was also performed. EH of the solid residue increased the total level of solubilized C6 sugars to a maximum of 35.5 g per 100 g dry raw material when DAH was performed as described above (3 min at 210°C and 2 min at 211°C with 1% H2SO4). Conclusion The dual-temperature DAH method did not yield decisively better results than the single-temperature, one-step DAH. When we compared the results with those of earlier studies, the hydrolysis performance was better than with the one-step DAH but not as well as that of the two-step, single-temperature DAH. Additional enzymatic hydrolysis resulted in lower levels of solubilized sugars compared with other studies on one-step DAH and two-step DAH followed by enzymatic hydrolysis. A two-step steam pretreatment with EH gave rise to a considerably higher sugar yield in this study.
机译:背景技术软木的两步稀酸水解(DAH)在能源需求和资本成本上是昂贵的。然而,其优点在于可以在低严重性的条件下进行水解和随后去除半纤维素衍生的糖,导致在纤维素水解的更严格的后续步骤中糖降解产物的水平降低。在本文中,我们讨论了一种单步DAH方法,该方法在两个级别上合并了温度曲线。该配置文件应模拟两步过程,同时消除其主要缺点,即运行之间的洗涤步骤,这会导致能源需求增加。结果实验在具有受控温度曲线的反应器中进行。水解产物的总干物质含量高达21.1%w / w,相当于水不溶性固体含量的15.5%w / w。在含1%H2SO4的209°C下3分钟和211°C下6分钟的DAH循环后,测得的最高葡萄糖产量(每100克干原料18.3克葡萄糖)获得了总计26.3克葡萄糖每100克干原料中溶解的C6糖。为了估计剩余的糖势,还进行了固体部分的酶促水解(EH)。如上所述进行DAH时,固体残留物的EH使每100克干原料中溶解的C6糖的总量增加到最高35.5克(在210°C下3分钟,在211°C下1%H2SO4 2分钟) )。结论双温度DAH方法没有比单温度单步DAH产生明显更好的结果。当我们将结果与早期研究的结果进行比较时,其水解性能优于单步DAH,但不如两步单温DAH更好。与其他有关一步DAH和两步DAH然后进行酶水解的研究相比,额外的酶水解作用导致糖的溶解度降低。在这项研究中,用EH进行两步蒸汽预处理可显着提高糖产量。

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