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Bio-hydrogen production by SSF of paper industry wastes using anaerobic biofilms: A comparison of the use of wastes with/without pretreatment

机译:SSF使用厌氧生物膜生产造纸废料的生物氢:预处理与未预处理之间废物使用的比较

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In this research, we carried out the process of simultaneous saccharification and fermentation (SSF) of paper industry wastes with/without chemical pretreatment, using reactors in batch with anaerobic biofilms developed in spheres covered with ixtle fiber cord. Biofilms were previously developed a UASB reactor using anaerobic sludge with acid/thermal pretreatment to remove hydrogen consuming bacteria. Subsequently, the process of saccharification and simultaneous fermentation (SSF) of paper industry waste without chemical pretreatment was evaluated using batch reactors with developed anaerobic biofilms. The key process parameters were: pH (4, 5 and 6) and enzyme loading of Celluclast enzyme (10, 40 and 70 FPU) at a temperature of 45 degrees C The results for hydrogen production with paper industry wastes without pretreatment showed optimal working conditions to maximize hydrogen production by SSF process at: pH (5) and an enzyme load of 70 FPU, so the maximum hydrogen yield obtained was 31.188 mmol/h x gSV. The results obtained from the evaluation of the process of SSF performed with paper industry wastes subjected to chemical pretreatment with H2SO4 2.5% showed the optimum working conditions to maximize hydrogen production: pH (4), an enzyme load of 70 FPU, the maximum value of hydrogen yield obtained was 55 844 mmol/h *gSV. The key process parameters were optimized by the response surface methodology (RSM) based on a two factor-three level central composite design (CCD), using as variables: pH (4.5 and 6), enzyme loading of Celluclast (R) (10, 40 and 70 UPF) and temperature (45 degrees C), for paper industry wastes with/without acid pretreatment. The results showed the analysis of variance was performed to test the importance of the polynomial equation of second order, so equations obtained for both residues (with/without pretreatment) describe the hydrogen yield in this study. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:在这项研究中,我们进行了有/无化学预处理的造纸工业废料同时糖化和发酵(SSF)的过程,使用的反应器与厌氧生物膜成批反应,该厌氧生物膜在被ixtle纤维帘线覆盖的球体中形成。生物膜以前是使用厌氧污泥进行酸/热预处理以去除耗氢细菌而开发的UASB反应器。随后,使用具有开发的厌氧生物膜的间歇式反应器,对未经化学预处理的造纸工业废料的糖化和同时发酵(SSF)过程进行了评估。关键的工艺参数为:pH(4、5和6)和Celluclast酶的酶负荷(10、40和70 FPU)在45摄氏度的温度下。未经预处理的造纸工业废料制氢结果显示最佳的工作条件为了通过SSF工艺在pH(5)和70 FPU的酶负载下最大限度地提高氢气产量,因此获得的最大氢气产量为31.188 mmol / hx gSV。对造纸工业废料进行2.5%H2SO4化学预处理的SSF工艺的评估结果表明,最佳的工作条件是最大程度地提高产氢量:pH(4),70 FPU的酶负荷,获得的氢气产率为55844mmol / h * gSV。关键工艺参数基于两因素三级中央复合设计(CCD),通过响应面方法(RSM)进行了优化,使用的变量包括:pH(4.5和6),Celluclast(R)的酶载量(10, 40和70 UPF)和温度(45摄氏度),适用于有/没有酸预处理的造纸工业废料。结果表明,进行方差分析是为了检验二阶多项式方程式的重要性,因此,针对两种残基(经过/未经过预处理)获得的方程式均描述了该研究中的氢气产率。 (C)2017氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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