Deise Juliana da Silva Lima, Rafaela Couto, Juçara Cristina Pereira Souza, Marli Camassola, Roselei C. Fontana, Aldo José Dillon, José Geraldo da Cruz Pradella
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A batch-mode assay conducted across a range of initial carbon source (5 to 60 g L<sup>–1</sup>) confirmed the highest FPase activity (4.0 to 5.0 FPU mL<sup>–1</sup> at 120 h), in the range of 20–40 g BHD L<sup>–1</sup>. During these assays the agitation rate, controlled by dissolved O<sub>2</sub>, tended to stabilize at lower levels, indicating substrate limitation. Conversely, higher initial carbon source concentrations led to an excess of glucose, likely triggering carbon catabolite repression and inhibiting cellulase production. This insight prompted the development of a controlled pulsed fed-batch strategy, resulting in FPase activity of 11 FPU mL<sup>–1</sup> at 220 h using 90 g L<sup>–1</sup> BHD controlled fed into the bioreactor. An enzymatic hydrolysis procedure using the generated CEC was also optimized using a central composite rotational design (CCRD). The optimized enzyme hydrolysis conditions achieved a reducing sugar concentration of 80.9 g L<sup>–1</sup> in 48 h using 170 g L<sup>–1</sup> of BHD as the substrate at a ratio of 15 FPU of enzyme substrate per g of BHD. A preliminary economic assessment demonstrated that, for a first- and second-generation (1G + 2G) ethanol biorefinery, the cost contribution of enzymes would be about US$0.2/L of biofuel. In conclusion, an efficient and highly productive procedure was developed successfully for the production of a CEC. 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Conversely, higher initial carbon source concentrations led to an excess of glucose, likely triggering carbon catabolite repression and inhibiting cellulase production. This insight prompted the development of a controlled pulsed fed-batch strategy, resulting in FPase activity of 11 FPU mL<sup>–1</sup> at 220 h using 90 g L<sup>–1</sup> BHD controlled fed into the bioreactor. An enzymatic hydrolysis procedure using the generated CEC was also optimized using a central composite rotational design (CCRD). The optimized enzyme hydrolysis conditions achieved a reducing sugar concentration of 80.9 g L<sup>–1</sup> in 48 h using 170 g L<sup>–1</sup> of BHD as the substrate at a ratio of 15 FPU of enzyme substrate per g of BHD. A preliminary economic assessment demonstrated that, for a first- and second-generation (1G + 2G) ethanol biorefinery, the cost contribution of enzymes would be about US$0.2/L of biofuel. 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引用次数: 0
摘要
纤维素分解复合酶(CEC)的高成本一直是木质纤维素生物质生物产品商业化生产的重大障碍。本研究旨在利用各种形式的预处理甘蔗渣作为主要碳/诱导源,开发一种从乌森青霉菌(原棘青霉)中提取的具有成本效益的 CEC。在使用的不同预处理方法中,在生物反应器实验中,当初始浓度为 20 g BHD L-1 时,水热预处理后 NaOH 脱木质(BHD)产生了较高的 FPase 和木聚糖酶活性(4.5 FPU mL-1 和 120 IU mL-1)。在初始碳源(5 至 60 g L-1)范围内进行的批处理模式试验证实,在 20-40 g BHD L-1 的范围内,FP 酶活性最高(120 h 时为 4.0 至 5.0 FPU mL-1)。在这些试验中,由溶解氧控制的搅拌速率趋于稳定在较低水平,表明存在底物限制。相反,较高的初始碳源浓度会导致葡萄糖过量,很可能引发碳代谢抑制并抑制纤维素酶的产生。这一认识促使我们开发了一种受控脉冲喂料批处理策略,在向生物反应器控制喂入 90 g L-1 BHD 的情况下,220 小时后 FPase 活性达到 11 FPU mL-1。此外,还利用中央复合旋转设计(CCRD)对使用生成的 CEC 进行酶水解的程序进行了优化。以 170 g L-1 BHD 为底物,每克 BHD 的酶底物比率为 15 FPU,优化后的酶水解条件可在 48 小时内使还原糖浓度达到 80.9 g L-1。初步经济评估表明,对于第一代和第二代(1G + 2G)乙醇生物精炼厂,酶的成本贡献约为 0.2 美元/升生物燃料。总之,成功开发了一种高效、高产的 CEC 生产程序。它对酶水解预处理甘蔗渣特别有效。
Use of an inexpensive carbon source for the production of a cellulase enzyme complex from Penicillium ucsense S1M29 and enzymatic hydrolysis optimization
The high cost of cellulolytic enzyme complexes (CECs) has been a significant impediment to the commercial production of bioproducts from lignocellulose biomass. This study aimed to develop a cost-effective CEC derived from Penicillium ucsense (former Penicillium echinulatum), utilizing diverse forms of pretreated sugarcane bagasse as the primary carbon/inductor source. Among the different pretreatments used, the hydrothermal pretreatment followed by NaOH delignification (BHD) produced higher FPase and xylanase activities (4.5 FPU mL–1 and 120 IU mL–1) in bioreactor experiments at 20 g BHD L–1 initial concentration. A batch-mode assay conducted across a range of initial carbon source (5 to 60 g L–1) confirmed the highest FPase activity (4.0 to 5.0 FPU mL–1 at 120 h), in the range of 20–40 g BHD L–1. During these assays the agitation rate, controlled by dissolved O2, tended to stabilize at lower levels, indicating substrate limitation. Conversely, higher initial carbon source concentrations led to an excess of glucose, likely triggering carbon catabolite repression and inhibiting cellulase production. This insight prompted the development of a controlled pulsed fed-batch strategy, resulting in FPase activity of 11 FPU mL–1 at 220 h using 90 g L–1 BHD controlled fed into the bioreactor. An enzymatic hydrolysis procedure using the generated CEC was also optimized using a central composite rotational design (CCRD). The optimized enzyme hydrolysis conditions achieved a reducing sugar concentration of 80.9 g L–1 in 48 h using 170 g L–1 of BHD as the substrate at a ratio of 15 FPU of enzyme substrate per g of BHD. A preliminary economic assessment demonstrated that, for a first- and second-generation (1G + 2G) ethanol biorefinery, the cost contribution of enzymes would be about US$0.2/L of biofuel. In conclusion, an efficient and highly productive procedure was developed successfully for the production of a CEC. It was particularly effective for the enzymatic hydrolysis of pretreated sugarcane bagasse.
期刊介绍:
Biofuels, Bioproducts and Biorefining is a vital source of information on sustainable products, fuels and energy. Examining the spectrum of international scientific research and industrial development along the entire supply chain, The journal publishes a balanced mixture of peer-reviewed critical reviews, commentary, business news highlights, policy updates and patent intelligence. Biofuels, Bioproducts and Biorefining is dedicated to fostering growth in the biorenewables sector and serving its growing interdisciplinary community by providing a unique, systems-based insight into technologies in these fields as well as their industrial development.