Pub Date : 2024-10-16DOI: 10.1016/j.biombioe.2024.107434
C.A. Prado, B.M.S. Loureiro, G.L. Arruda, J.C. Santos, A.K. Chandel
Hydrodynamic cavitation-assisted pretreatment of sugarcane bagasse tested in the, with the addition of yeast extract. This pretreatment was investigated using a 22 central composite design experiment. A total of 11 experiments were performed. The pretreated biomass was then tested for enzymatic hydrolysis for the sugars production. Various enzymatic loadings (15–20 FPU/g biomass) and concentrations of yeast extract (0.25–1 g/L) were studied during the enzymatic hydrolysis. Optimization of yeast extract insertion was performed to simultaneously facilitate the infusion of cellulolytic enzymes into the pores of the pre-treated bagasse concomitantly inhibiting enzyme absorption caused by residual lignin. The optimized results revealed an 81 % glucan hydrolysis yield and a 78 % xylan hydrolysis yield after the enzymatic hydrolysis under optimized conditions (20 FPU/g and 1 g/L of yeast extract). The hydrolysate rich in sugars derived from carbohydrate polymers and nitrogen sources derived from hydrolysis of yeast cream was assessed for biopigments production by Monascus ruber. The hydrolysate used for M. ruber fermentation showed the production of pigments with 15 AU (absorbance units) for yellow, 15 AU for orange and 20 AU for red after 9 days of fermentation. These results proved the efficiency of using yeast cream as a potential blocking agent of lignin in turn increasing the sugars production and a nitrogen source for the M. ruber for biopigments production from sugarcane bagasse hydrolysate.
在加入酵母提取物的情况下,对甘蔗渣进行了水动力空化辅助预处理试验。该预处理采用 22 中心复合设计实验进行研究。共进行了 11 次实验。然后,对预处理后的生物质进行了酶水解产糖测试。在酶水解过程中,研究了不同的酶负荷(15-20 FPU/克生物质)和酵母提取物浓度(0.25-1 克/升)。对酵母提取物的插入进行了优化,以同时促进纤维素分解酶注入预处理甘蔗渣的孔隙,同时抑制残留木质素造成的酶吸收。优化结果显示,在优化条件(20 FPU/g,1 g/L 酵母提取物)下进行酶水解后,葡聚糖水解率为 81%,木聚糖水解率为 78%。对富含来自碳水化合物聚合物的糖和来自水解酵母膏的氮源的水解物进行了评估,以确定是否可用于莫纳拉斯克氏菌(Monascus ruber)生产生物色素。用于酵母菌发酵的水解物显示,发酵 9 天后可产生黄色 15 AU(吸光度单位)、橙色 15 AU 和红色 20 AU 的色素。这些结果证明,使用酵母膏作为木质素的潜在阻断剂,可以提高糖的产量,同时也是 M. ruber 利用甘蔗渣水解物生产生物色素的氮源。
{"title":"Hydrodynamic cavitation assisted pretreatment of sugarcane bagasse in the presence of yeast cell mass for the production of sugars and their use for biopigments production by Monascus ruber","authors":"C.A. Prado, B.M.S. Loureiro, G.L. Arruda, J.C. Santos, A.K. Chandel","doi":"10.1016/j.biombioe.2024.107434","DOIUrl":"10.1016/j.biombioe.2024.107434","url":null,"abstract":"<div><div>Hydrodynamic cavitation-assisted pretreatment of sugarcane bagasse tested in the, with the addition of yeast extract. This pretreatment was investigated using a 2<sup>2</sup> central composite design experiment. A total of 11 experiments were performed. The pretreated biomass was then tested for enzymatic hydrolysis for the sugars production. Various enzymatic loadings (15–20 FPU/g biomass) and concentrations of yeast extract (0.25–1 g/L) were studied during the enzymatic hydrolysis. Optimization of yeast extract insertion was performed to simultaneously facilitate the infusion of cellulolytic enzymes into the pores of the pre-treated bagasse concomitantly inhibiting enzyme absorption caused by residual lignin. The optimized results revealed an 81 % glucan hydrolysis yield and a 78 % xylan hydrolysis yield after the enzymatic hydrolysis under optimized conditions (20 FPU/g and 1 g/L of yeast extract). The hydrolysate rich in sugars derived from carbohydrate polymers and nitrogen sources derived from hydrolysis of yeast cream was assessed for biopigments production by <em>Monascus ruber</em>. The hydrolysate used for <em>M. ruber</em> fermentation showed the production of pigments with 15 AU (absorbance units) for yellow, 15 AU for orange and 20 AU for red after 9 days of fermentation. These results proved the efficiency of using yeast cream as a potential blocking agent of lignin in turn increasing the sugars production and a nitrogen source for the <em>M. ruber</em> for biopigments production from sugarcane bagasse hydrolysate.</div></div>","PeriodicalId":253,"journal":{"name":"Biomass & Bioenergy","volume":"190 ","pages":"Article 107434"},"PeriodicalIF":5.8,"publicationDate":"2024-10-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142442847","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-10-13DOI: 10.1016/j.biombioe.2024.107425
Xiliang Chen , Jing-Jing Ji , Haian Xia, Baoli Fei
The increasing depletion of fossil fuel resources promote the study of conversion of renewable biomass resources to valuable chemicals. Formic acid (FA) is regarded as desirable liquid hydrogen carrier. Glycolic acid (GA) has been extensively used for the treatment of photoaging and wrinkles. It is meaningful to explore novel catalysts for the selective oxidation of bio-platform molecules into FA and GA. Keggin-type polyoxometalates (POMs) were firstly explored as catalysts for the oxidation of 1,3-dihydroxyacetone (DHA), which is an important biomass-based platform molecule, to obtain GA and FA in the presence H2O2.The effect of catalyst structure and composition, and the reaction conditions on DHA oxidation were investigated. Among the chosen compounds, Cs3PMo12O40 exhibited the best catalytic activity, with 86.4 % and 82.6 % yields of GA and FA, respectively. The five successive recycling experiments indicated that Cs3PMo12O40 had good stability and reusability. The catalytic activity of Cs3PMo12O40 was better than that of the other types of catalysts reported. This work give a clue for utilizing POMs as catalysts for the valorization of biomass derivatives to useful fine chemicals under mild conditions.
化石燃料资源的日益枯竭促进了将可再生生物质资源转化为有价值化学品的研究。甲酸(FA)被认为是理想的液态氢载体。乙醇酸(GA)已被广泛用于治疗光老化和皱纹。探索将生物平台分子选择性氧化为 FA 和 GA 的新型催化剂很有意义。研究了催化剂的结构和组成以及反应条件对 DHA 氧化的影响。在所选化合物中,Cs3PMo12O40 的催化活性最好,GA 和 FA 的产率分别为 86.4% 和 82.6%。连续五次回收实验表明,Cs3PMo12O40 具有良好的稳定性和可重复使用性。Cs3PMo12O40 的催化活性优于其他类型的催化剂。这项工作为利用 POMs 作为催化剂,在温和条件下将生物质衍生物转化为有用的精细化学品提供了线索。
{"title":"Efficient Co-synthesis of glycolic acid and formic acid from 1,3-dihydroxyacetone by Keggin cesium phosphomolybdates","authors":"Xiliang Chen , Jing-Jing Ji , Haian Xia, Baoli Fei","doi":"10.1016/j.biombioe.2024.107425","DOIUrl":"10.1016/j.biombioe.2024.107425","url":null,"abstract":"<div><div>The increasing depletion of fossil fuel resources promote the study of conversion of renewable biomass resources to valuable chemicals. Formic acid (FA) is regarded as desirable liquid hydrogen carrier. Glycolic acid (GA) has been extensively used for the treatment of photoaging and wrinkles. It is meaningful to explore novel catalysts for the selective oxidation of bio-platform molecules into FA and GA. Keggin-type polyoxometalates (POMs) were firstly explored as catalysts for the oxidation of 1,3-dihydroxyacetone (DHA), which is an important biomass-based platform molecule, to obtain GA and FA in the presence H<sub>2</sub>O<sub>2</sub>.The effect of catalyst structure and composition, and the reaction conditions on DHA oxidation were investigated. Among the chosen compounds, Cs<sub>3</sub>PMo<sub>12</sub>O<sub>40</sub> exhibited the best catalytic activity, with 86.4 % and 82.6 % yields of GA and FA, respectively. The five successive recycling experiments indicated that Cs<sub>3</sub>PMo<sub>12</sub>O<sub>40</sub> had good stability and reusability. The catalytic activity of Cs<sub>3</sub>PMo<sub>12</sub>O<sub>40</sub> was better than that of the other types of catalysts reported. This work give a clue for utilizing POMs as catalysts for the valorization of biomass derivatives to useful fine chemicals under mild conditions.</div></div>","PeriodicalId":253,"journal":{"name":"Biomass & Bioenergy","volume":"190 ","pages":"Article 107425"},"PeriodicalIF":5.8,"publicationDate":"2024-10-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142434486","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-10-13DOI: 10.1016/j.biombioe.2024.107426
Marcelo B.W. Saad , Adilson R. Gonçalves
<div><div>Renewable alternatives to fossil fuels are now a worldwide effort, and biofuels can play an essential role in a sustainable energy matrix. The great potential of lignocellulosic biomass as feedstock for bioethanol production has been underexplored due to technological barriers and the costs involved. However, a new chapter in this history has been written recently after eight different biomass-to-ethanol processes achieved the industrial scale, leading bioethanol technologies to a new step of maturity due to challenges faced and lessons learned. The pretreatment of biomass has been recognized as the most complex step in the cellulosic ethanol production processes and the reason for the failure of some industrial initiatives. Pretreatment represents an essential process to prepare lignocellulosic material for subsequent hydrolysis and fermentation, and this review aims to describe the early and recent efforts to scale-up pretreatment systems and the current challenges of pretreatment operations. Since the early 2010s, a global running for cellulosic ethanol resulted in eight industrial facilities around the world; agricultural residues like corn stover, corn cob, wheat straw, sugarcane bagasse, and sugarcane straw were used by POET-DSM, Raízen, Beta Renewables, GranBio, Abengoa, DuPont, Clariant, and Longlive Bio-tech as feedstock for bioethanol production. Pretreatment technologies, including diluted acid, steam explosion, dilute ammonia, and mechanical refining, were then experienced industrially through batch or continuous systems performed in one or two conversion stages. The pretreatment systems employed by each cellulosic biorefinery are analyzed in this review, and the process conditions and strategies applied are discussed based on public information available. Furthermore, a historical background of the early developments of acid hydrolysis of cellulose and the transition to the modern pretreatment concept is provided. Typical batch reactors employed during the 1900s were replaced by continuous reactors aiming for high productivity. An overview of digesting systems used by the pulp and paper industry is explored, which were initially developed for pulping and recently adapted to perform biomass pretreatment. Special attention is paid to describing vertical and horizontal continuous digesters and mechanical disc refiners, the leading equipment used in industrial pretreatment systems. Additionally, current pretreatment challenges are discussed based on pilot and industrial experience. Biorefineries faced low throughput capacity due to unstable operation and high wear damage to equipment caused by mineral impurities. The impact of feedstock quality and preconditioning processes on pretreatment operation is also reviewed. Feedstock collection, storage, and cleaning have been considered critical operations for a successful pretreatment process; best practices from the non-wood pulping industry are analyzed, providing an important ref
{"title":"Industrial pretreatment of lignocellulosic biomass: A review of the early and recent efforts to scale-up pretreatment systems and the current challenges","authors":"Marcelo B.W. Saad , Adilson R. Gonçalves","doi":"10.1016/j.biombioe.2024.107426","DOIUrl":"10.1016/j.biombioe.2024.107426","url":null,"abstract":"<div><div>Renewable alternatives to fossil fuels are now a worldwide effort, and biofuels can play an essential role in a sustainable energy matrix. The great potential of lignocellulosic biomass as feedstock for bioethanol production has been underexplored due to technological barriers and the costs involved. However, a new chapter in this history has been written recently after eight different biomass-to-ethanol processes achieved the industrial scale, leading bioethanol technologies to a new step of maturity due to challenges faced and lessons learned. The pretreatment of biomass has been recognized as the most complex step in the cellulosic ethanol production processes and the reason for the failure of some industrial initiatives. Pretreatment represents an essential process to prepare lignocellulosic material for subsequent hydrolysis and fermentation, and this review aims to describe the early and recent efforts to scale-up pretreatment systems and the current challenges of pretreatment operations. Since the early 2010s, a global running for cellulosic ethanol resulted in eight industrial facilities around the world; agricultural residues like corn stover, corn cob, wheat straw, sugarcane bagasse, and sugarcane straw were used by POET-DSM, Raízen, Beta Renewables, GranBio, Abengoa, DuPont, Clariant, and Longlive Bio-tech as feedstock for bioethanol production. Pretreatment technologies, including diluted acid, steam explosion, dilute ammonia, and mechanical refining, were then experienced industrially through batch or continuous systems performed in one or two conversion stages. The pretreatment systems employed by each cellulosic biorefinery are analyzed in this review, and the process conditions and strategies applied are discussed based on public information available. Furthermore, a historical background of the early developments of acid hydrolysis of cellulose and the transition to the modern pretreatment concept is provided. Typical batch reactors employed during the 1900s were replaced by continuous reactors aiming for high productivity. An overview of digesting systems used by the pulp and paper industry is explored, which were initially developed for pulping and recently adapted to perform biomass pretreatment. Special attention is paid to describing vertical and horizontal continuous digesters and mechanical disc refiners, the leading equipment used in industrial pretreatment systems. Additionally, current pretreatment challenges are discussed based on pilot and industrial experience. Biorefineries faced low throughput capacity due to unstable operation and high wear damage to equipment caused by mineral impurities. The impact of feedstock quality and preconditioning processes on pretreatment operation is also reviewed. Feedstock collection, storage, and cleaning have been considered critical operations for a successful pretreatment process; best practices from the non-wood pulping industry are analyzed, providing an important ref","PeriodicalId":253,"journal":{"name":"Biomass & Bioenergy","volume":"190 ","pages":"Article 107426"},"PeriodicalIF":5.8,"publicationDate":"2024-10-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142434522","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-10-13DOI: 10.1016/j.biombioe.2024.107429
Gheorghiţa Mitran , Tam Le Phuong Nguyen , Dong-Kyun Seo
The use of alternative sources of energy derived from biomass instead of those from fossil fuels represents a viable alternative to the ever-increasing fuel requirements. One of these products is hydrofuroin, an important precursor for jet fuel that can be obtained from furfural by reductive self-coupling using 1,4-butanediol as hydrogen donor, both reactants have the advantage to be biomass derived products. Manganese aluminate, MnAl2O4 has a promising candidate for the reaction mentioned above. The solvent (ethanol or butanol) influence on the sol-gel preparation method, as well as the nature of the catalyst (HNO3 or NH3) used to control the hydrolysis rate of the precursors, were the factors followed in the evaluation of the catalytic activity. Ethanol as solvent and basic medium (pH 8) generate materials with higher surface area, uniform particles with smaller sizes, preserve the Mn/Al ratio corresponding to the formula MnAl2O4, have higher Mn2+/Al3+ ratio compared to butanol as solvent and acidic medium (pH 2) for preparation. Therefore, the highest activity, including the conversion, yield in products and selectivity in hydrofuroin, was observed on these catalysts.
{"title":"Conversion of biomass derived furfural to a jet fuel precursor in the presence of 1,4-butanediol as hydrogen donor","authors":"Gheorghiţa Mitran , Tam Le Phuong Nguyen , Dong-Kyun Seo","doi":"10.1016/j.biombioe.2024.107429","DOIUrl":"10.1016/j.biombioe.2024.107429","url":null,"abstract":"<div><div>The use of alternative sources of energy derived from biomass instead of those from fossil fuels represents a viable alternative to the ever-increasing fuel requirements. One of these products is hydrofuroin, an important precursor for jet fuel that can be obtained from furfural by reductive self-coupling using 1,4-butanediol as hydrogen donor, both reactants have the advantage to be biomass derived products. Manganese aluminate, MnAl<sub>2</sub>O<sub>4</sub> has a promising candidate for the reaction mentioned above. The solvent (ethanol or butanol) influence on the sol-gel preparation method, as well as the nature of the catalyst (HNO<sub>3</sub> or NH<sub>3</sub>) used to control the hydrolysis rate of the precursors, were the factors followed in the evaluation of the catalytic activity. Ethanol as solvent and basic medium (pH 8) generate materials with higher surface area, uniform particles with smaller sizes, preserve the Mn/Al ratio corresponding to the formula MnAl<sub>2</sub>O<sub>4</sub>, have higher Mn<sup>2+</sup>/Al<sup>3+</sup> ratio compared to butanol as solvent and acidic medium (pH 2) for preparation. Therefore, the highest activity, including the conversion, yield in products and selectivity in hydrofuroin, was observed on these catalysts.</div></div>","PeriodicalId":253,"journal":{"name":"Biomass & Bioenergy","volume":"190 ","pages":"Article 107429"},"PeriodicalIF":5.8,"publicationDate":"2024-10-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142434487","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-10-11DOI: 10.1016/j.biombioe.2024.107415
Fan Liu , Liang Wu , Yue Qiu , Zhigang Liu , Yunan Chen , Jingwei Chen , Xiaoping Chen , Lei Yi , Bin Chen
A system of two-stage series supercritical water gasification of biomass is proposed to achieve high hydrogen production. The system design and process simulation were implemented via Aspen plus, and the thermodynamic performance of the system was analyzed. Meanwhile, a life cycle environmental assessment under different conditions was performed using SimaPro. Based on the fixed reaction concentration, results of thermodynamic analysis reveal that the energy efficiency and exergy efficiency of the system are related to temperatures of the first-stage gasification reactor and the second-stage oxidation reactor. When temperatures of FGR and SOR are 603°C and 833°C respectively, the system could reach the highest hydrogen production. Moreover, the energy efficiency and exergy efficiency could reach 54.9 % and 56.2 % respectively, while changes of temperatures of the first-stage oxidation reactor and the second-stage gasification reactor have no effect on efficiency. In addition, the maximum recoverable energy loss is induced by the waste heat of the effluent from Cooler, indicating the path of system optimization. By using organic Rankine cycle, the energy efficiency and exergy efficiency could reach 57.7 % and 59.3 % respectively. Meanwhile, the data from SimaPro shows LCI and LCIA of the system, which identified the main environmental burdens. Overall, this work has great advantages in terms of thermodynamics and environmental impact, while it faces both opportunities and challenges. This research reveals the feasibility of TSCWG and provides theoretical guidance for biomass cleaning conversion.
{"title":"Thermodynamic and environmental analysis of two-stage series supercritical water gasification of biomass for hydrogen production","authors":"Fan Liu , Liang Wu , Yue Qiu , Zhigang Liu , Yunan Chen , Jingwei Chen , Xiaoping Chen , Lei Yi , Bin Chen","doi":"10.1016/j.biombioe.2024.107415","DOIUrl":"10.1016/j.biombioe.2024.107415","url":null,"abstract":"<div><div>A system of two-stage series supercritical water gasification of biomass is proposed to achieve high hydrogen production. The system design and process simulation were implemented via Aspen plus, and the thermodynamic performance of the system was analyzed. Meanwhile, a life cycle environmental assessment under different conditions was performed using SimaPro. Based on the fixed reaction concentration, results of thermodynamic analysis reveal that the energy efficiency and exergy efficiency of the system are related to temperatures of the first-stage gasification reactor and the second-stage oxidation reactor. When temperatures of FGR and SOR are 603°C and 833°C respectively, the system could reach the highest hydrogen production. Moreover, the energy efficiency and exergy efficiency could reach 54.9 % and 56.2 % respectively, while changes of temperatures of the first-stage oxidation reactor and the second-stage gasification reactor have no effect on efficiency. In addition, the maximum recoverable energy loss is induced by the waste heat of the effluent from Cooler, indicating the path of system optimization. By using organic Rankine cycle, the energy efficiency and exergy efficiency could reach 57.7 % and 59.3 % respectively. Meanwhile, the data from SimaPro shows LCI and LCIA of the system, which identified the main environmental burdens. Overall, this work has great advantages in terms of thermodynamics and environmental impact, while it faces both opportunities and challenges. This research reveals the feasibility of TSCWG and provides theoretical guidance for biomass cleaning conversion.</div></div>","PeriodicalId":253,"journal":{"name":"Biomass & Bioenergy","volume":"190 ","pages":"Article 107415"},"PeriodicalIF":5.8,"publicationDate":"2024-10-11","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142425323","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-10-10DOI: 10.1016/j.biombioe.2024.107417
Francisco Wendell Bezerra Lopes , Maria Rosiane de Almeida Andrade , Eduardo Lins de. Barros Neto , Jean-Michel Lavoie , Bruna Rego de Vasconcelos
The growth of the cannabis industry emphasizes the importance of valorizing renewable waste, which can be used to produce sustainable fuels. Gasification is an effective thermochemical process for converting biomass and waste into synthesis gas, providing a valuable renewable energy source. In this context, this study proposes the valorization of cannabis waste, specifically hemp, through the gasification process, using a downdraft gasifier and a mixture of air and steam as the gasifying agent to produce synthesis gas. The main operating parameters influencing the gasification process (biomass/steam ratio, equivalence ratio, and temperature) were evaluated, as well as the influence of the steam explosion as a pre-treatment of the cannabis waste. The highest H2, CO concentrations, and LHV were observed among the evaluated parameters at an S/B ratio of 1 ER = 0.25 and T = 900 °C. With H₂ contents above 40 % vol, the gasification process demonstrated significant potential for energy valorization of cannabis waste compared to other biomass sources.
大麻产业的发展强调了可再生废物价值化的重要性,这些废物可用于生产可持续燃料。气化是一种有效的热化学工艺,可将生物质和废物转化为合成气,提供宝贵的可再生能源。在此背景下,本研究提出通过气化工艺对大麻废物(特别是大麻)进行价值评估,使用下吹气化炉和空气与蒸汽的混合物作为气化剂来生产合成气。对影响气化过程的主要操作参数(生物质/蒸汽比、当量比和温度)以及作为大麻废料预处理的蒸汽爆炸的影响进行了评估。在 S/B 比率为 1 ER = 0.25 和 T = 900 °C 时,所评估参数中的 H2、CO 浓度和 LHV 最高。在 H₂ 含量高于 40 % vol 的情况下,与其他生物质来源相比,气化工艺在大麻废弃物能源价值化方面具有巨大潜力。
{"title":"H2-rich syngas production from gasification of cannabis waste in a downdraft gasifier","authors":"Francisco Wendell Bezerra Lopes , Maria Rosiane de Almeida Andrade , Eduardo Lins de. Barros Neto , Jean-Michel Lavoie , Bruna Rego de Vasconcelos","doi":"10.1016/j.biombioe.2024.107417","DOIUrl":"10.1016/j.biombioe.2024.107417","url":null,"abstract":"<div><div>The growth of the cannabis industry emphasizes the importance of valorizing renewable waste, which can be used to produce sustainable fuels. Gasification is an effective thermochemical process for converting biomass and waste into synthesis gas, providing a valuable renewable energy source. In this context, this study proposes the valorization of cannabis waste, specifically hemp, through the gasification process, using a downdraft gasifier and a mixture of air and steam as the gasifying agent to produce synthesis gas. The main operating parameters influencing the gasification process (biomass/steam ratio, equivalence ratio, and temperature) were evaluated, as well as the influence of the steam explosion as a pre-treatment of the cannabis waste. The highest H<sub>2</sub>, CO concentrations, and LHV were observed among the evaluated parameters at an S/B ratio of 1 ER = 0.25 and T = 900 °C. With H₂ contents above 40 % vol, the gasification process demonstrated significant potential for energy valorization of cannabis waste compared to other biomass sources.</div></div>","PeriodicalId":253,"journal":{"name":"Biomass & Bioenergy","volume":"190 ","pages":"Article 107417"},"PeriodicalIF":5.8,"publicationDate":"2024-10-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142425322","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-10-10DOI: 10.1016/j.biombioe.2024.107423
Hong Tian , Huang Zhang , Zhangjun Huang , Xueliang Guo , Shan Cheng , Yang Yang , Yi Cheng , Jiawei Wang
Given the outstanding selective catalytic and deoxygenation abilities of ZSM-5, it has a great potential to enrich aromatics in catalytic biomass pyrolysis to oil, while metal oxides as catalysts have the ability to reduce the molecular size of compounds, which can weaken the limitation of ZSM-5 to macromolecular intermediates. In this study, metal oxides and ZSM-5 were chosen as catalysts to further extend the advantages of selective catalysis. In this paper, microscopic and bench-scale experiments for the conversion of biomass to high-yield aromatics using ZSM-5 and metal oxide catalysts were systematically investigated. In a dual catalyst pyrolysis study involving ZSM-5 and metal oxides (CaO, MgO, NiO, MoO3), PY-GC-MS, Tube Furnace experiments were used to evaluate various catalyst layouts. The influence of catalyst dose on three-phase product yields was examined in a bench-scale fixed bed reactor employing the optimal architecture and metal oxides. The findings revealed that the dual-catalyst arrangement was critical to improving bio-oil quality. The best yield (50.02 %) of monocyclic aromatic hydrocarbons (MAHs) was produced by combining Miscanthus with the metal oxides and then separating with ZSM-5. Among the four metal oxides, CaO had the greatest synergistic effect on MAHs and selectivity. The inclusion of CaO decreased the concentration of several oxygenated compounds, particularly the suppression of furans, phenols, and acids, which was extremely advantageous for improving bio-oil quality. The highest percentage of hydrocarbon production (64.61 %) in bio-oil was produced at a Miscanthus to CaO to ZSM-5 ratio of 1:2:4, however increasing catalyst dose reduces bio-oil yield (28.92 %).
{"title":"Balancing bio-oil quality and yield during rapid pyrolysis of Miscanthus using ZSM-5 and metal oxides","authors":"Hong Tian , Huang Zhang , Zhangjun Huang , Xueliang Guo , Shan Cheng , Yang Yang , Yi Cheng , Jiawei Wang","doi":"10.1016/j.biombioe.2024.107423","DOIUrl":"10.1016/j.biombioe.2024.107423","url":null,"abstract":"<div><div>Given the outstanding selective catalytic and deoxygenation abilities of ZSM-5, it has a great potential to enrich aromatics in catalytic biomass pyrolysis to oil, while metal oxides as catalysts have the ability to reduce the molecular size of compounds, which can weaken the limitation of ZSM-5 to macromolecular intermediates. In this study, metal oxides and ZSM-5 were chosen as catalysts to further extend the advantages of selective catalysis. In this paper, microscopic and bench-scale experiments for the conversion of biomass to high-yield aromatics using ZSM-5 and metal oxide catalysts were systematically investigated. In a dual catalyst pyrolysis study involving ZSM-5 and metal oxides (CaO, MgO, NiO, MoO<sub>3</sub>), PY-GC-MS, Tube Furnace experiments were used to evaluate various catalyst layouts. The influence of catalyst dose on three-phase product yields was examined in a bench-scale fixed bed reactor employing the optimal architecture and metal oxides. The findings revealed that the dual-catalyst arrangement was critical to improving bio-oil quality. The best yield (50.02 %) of monocyclic aromatic hydrocarbons (MAHs) was produced by combining Miscanthus with the metal oxides and then separating with ZSM-5. Among the four metal oxides, CaO had the greatest synergistic effect on MAHs and selectivity. The inclusion of CaO decreased the concentration of several oxygenated compounds, particularly the suppression of furans, phenols, and acids, which was extremely advantageous for improving bio-oil quality. The highest percentage of hydrocarbon production (64.61 %) in bio-oil was produced at a Miscanthus to CaO to ZSM-5 ratio of 1:2:4, however increasing catalyst dose reduces bio-oil yield (28.92 %).</div></div>","PeriodicalId":253,"journal":{"name":"Biomass & Bioenergy","volume":"190 ","pages":"Article 107423"},"PeriodicalIF":5.8,"publicationDate":"2024-10-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142425321","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-10-09DOI: 10.1016/j.biombioe.2024.107422
Zhigang Liu , Youwen Yang , Yunan Chen , Lei Yi , Liejin Guo , Yun Chao , Huiming Chen
Recently, biomass gasification process has gained lots of attention because of sustainable energy sources utilization. Being renewable energy source, biomass can serve as a viable replacement for fossil fuels. The process gasification is the conversion of organic substance via thermochemical process where syngas is produced along with the solid product termed as char. Such process is also well known for the generation of heat and power and synthesize the second-generation biofuels and hydrogen production. Unfortunately, tar formation in gasifiers during biomass gasification remains a main problem to commercialization. In the current review we focus at recent advancements in catalytic biomass gasification about supercritical water catalytic gasification and discuss on gasification process, parametric impact, biomass-pretreatment and catalytic deactivate mechanism in order to overcome the challenges and improve the catalytic yield. Future direction and critical prospective of catalytic biomass gasification are also discussed in this review.
{"title":"A review on catalytic hydrogen production from supercritical water gasification of biomass","authors":"Zhigang Liu , Youwen Yang , Yunan Chen , Lei Yi , Liejin Guo , Yun Chao , Huiming Chen","doi":"10.1016/j.biombioe.2024.107422","DOIUrl":"10.1016/j.biombioe.2024.107422","url":null,"abstract":"<div><div>Recently, biomass gasification process has gained lots of attention because of sustainable energy sources utilization. Being renewable energy source, biomass can serve as a viable replacement for fossil fuels. The process gasification is the conversion of organic substance via thermochemical process where syngas is produced along with the solid product termed as char. Such process is also well known for the generation of heat and power and synthesize the second-generation biofuels and hydrogen production. Unfortunately, tar formation in gasifiers during biomass gasification remains a main problem to commercialization. In the current review we focus at recent advancements in catalytic biomass gasification about supercritical water catalytic gasification and discuss on gasification process, parametric impact, biomass-pretreatment and catalytic deactivate mechanism in order to overcome the challenges and improve the catalytic yield. Future direction and critical prospective of catalytic biomass gasification are also discussed in this review.</div></div>","PeriodicalId":253,"journal":{"name":"Biomass & Bioenergy","volume":"190 ","pages":"Article 107422"},"PeriodicalIF":5.8,"publicationDate":"2024-10-09","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142425479","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-10-08DOI: 10.1016/j.biombioe.2024.107421
Josefin Winberg , Johan Ekroos , Lars Eklundh , Henrik G. Smith
{"title":"Constraints on the availability of marginal land for bioenergy production in southern Sweden","authors":"Josefin Winberg , Johan Ekroos , Lars Eklundh , Henrik G. Smith","doi":"10.1016/j.biombioe.2024.107421","DOIUrl":"10.1016/j.biombioe.2024.107421","url":null,"abstract":"","PeriodicalId":253,"journal":{"name":"Biomass & Bioenergy","volume":"190 ","pages":"Article 107421"},"PeriodicalIF":5.8,"publicationDate":"2024-10-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142425478","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Modern biotechnology is increasingly focused on microorganisms with unique metabolic properties that can address critical challenges in fuel and food production. Population growth and climate change have significantly impacted food and fuel availability levels. There is growing research into methanotrophic organisms to meet global demand and ensure sustainable resource use. These organisms are easy to cultivate and require very little carbon source and energy. Methanotrophs are already being used as feedstock in biofuel production and as supplements in animal nutrition. These organisms produce a chemical called one carbon (C1) that is inexpensive, sustainable, and can be used as a building block for other chemical resources. C1- chemicals are raw materials for various products and precursors that are used in our daily lives. Moreover, a soluble C1 substrate, methanol is a renewable resource increasingly used in biofuel, food, and nutraceutical industries. Various valuable metabolites have already been produced, demonstrating the potential of C1-based bio-manufacturing. With growing interest, researchers are now engineering proteins such as MMO (pMMO, sMMO) and MDH to enhance the production of desired biofuels and food-grade chemicals. MMO and MDH proteins are being developed as a biotechnological feedstock for high-value chemicals, contributing to the sustainability of fuel and food systems. This article provides a concise overview of the different aspects of methanotrophs, with a particular emphasis on the properties, engineering, and biotechnological applications of MMO and MDH enzymes, providing insights into the biological and industrial relevance of methanotrophs.
现代生物技术越来越关注具有独特代谢特性的微生物,这些微生物可以应对燃料和食品生产中的关键挑战。人口增长和气候变化严重影响了粮食和燃料的供应水平。为满足全球需求并确保资源的可持续利用,对养甲烷生物的研究日益增多。这些生物易于培养,只需要很少的碳源和能量。甲烷营养生物已被用作生物燃料生产的原料和动物营养补充剂。这些生物产生一种称为一碳(C1)的化学物质,这种化学物质价格低廉、可持续,并可用作其他化学资源的组成部分。一碳化学品是我们日常生活中各种产品和前体的原材料。此外,作为一种可溶性 C1 底物,甲醇是一种可再生资源,在生物燃料、食品和保健品行业的应用日益广泛。目前已生产出各种有价值的代谢物,证明了以 C1 为基础的生物制造的潜力。随着研究兴趣的不断增加,研究人员正在对 MMO(pMMO、sMMO)和 MDH 等蛋白质进行工程改造,以提高所需生物燃料和食品级化学品的产量。MMO 和 MDH 蛋白正在被开发为高价值化学品的生物技术原料,为燃料和食品系统的可持续发展做出贡献。本文简要概述了甲烷营养体的各个方面,特别强调了 MMO 和 MDH 酶的特性、工程学和生物技术应用,为甲烷营养体的生物学和工业相关性提供了见解。
{"title":"Structural-level insights into the functional proteins MMO and MDH from methanotrophic bacteria for their reaction mechanism","authors":"Chandrabose Selvaraj , Rajendran Vijayakumar , Veeramuthu Ashokkumar","doi":"10.1016/j.biombioe.2024.107413","DOIUrl":"10.1016/j.biombioe.2024.107413","url":null,"abstract":"<div><div>Modern biotechnology is increasingly focused on microorganisms with unique metabolic properties that can address critical challenges in fuel and food production. Population growth and climate change have significantly impacted food and fuel availability levels. There is growing research into methanotrophic organisms to meet global demand and ensure sustainable resource use. These organisms are easy to cultivate and require very little carbon source and energy. Methanotrophs are already being used as feedstock in biofuel production and as supplements in animal nutrition. These organisms produce a chemical called one carbon (C1) that is inexpensive, sustainable, and can be used as a building block for other chemical resources. C1- chemicals are raw materials for various products and precursors that are used in our daily lives. Moreover, a soluble C1 substrate, methanol is a renewable resource increasingly used in biofuel, food, and nutraceutical industries. Various valuable metabolites have already been produced, demonstrating the potential of C1-based bio-manufacturing. With growing interest, researchers are now engineering proteins such as MMO (pMMO, sMMO) and MDH to enhance the production of desired biofuels and food-grade chemicals. MMO and MDH proteins are being developed as a biotechnological feedstock for high-value chemicals, contributing to the sustainability of fuel and food systems. This article provides a concise overview of the different aspects of methanotrophs, with a particular emphasis on the properties, engineering, and biotechnological applications of MMO and MDH enzymes, providing insights into the biological and industrial relevance of methanotrophs.</div></div>","PeriodicalId":253,"journal":{"name":"Biomass & Bioenergy","volume":"190 ","pages":"Article 107413"},"PeriodicalIF":5.8,"publicationDate":"2024-10-07","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142425339","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}