正己烷和乙醇能形成共沸物,利用传统精馏方法很难将二者有效地分离,且二者的共沸物组成对压力较为敏感。本文利用化工流程模拟软件Aspen Plus V12,以Wilson-Radlish-Kwong方程为物性方法讨论正己烷和乙醇物系变压精馏的可行性。利用软...正己烷和乙醇能形成共沸物,利用传统精馏方法很难将二者有效地分离,且二者的共沸物组成对压力较为敏感。本文利用化工流程模拟软件Aspen Plus V12,以Wilson-Radlish-Kwong方程为物性方法讨论正己烷和乙醇物系变压精馏的可行性。利用软件内置的灵敏度分析工具优化了各塔的理论板数、进料位置和回流比,同时利用热集成的方法对该工艺进一步优化。结果表明:正己烷和乙醇物系可以通过变压精馏的方法进行有效分离;热集成流程比非热集成流程降低能耗1403.62 kW,再沸器节能可达39.64%。展开更多
为达到同步糖化发酵(simultaneous saccharification and fermentation,SSF)中菌株高温耐受能力提升的目的,该文以实验室保藏的马克斯克鲁维酵母(Kluyveromyces marxianus)GX-UN120为出发菌株,采用常压室温等离子体(atmospheric and roo...为达到同步糖化发酵(simultaneous saccharification and fermentation,SSF)中菌株高温耐受能力提升的目的,该文以实验室保藏的马克斯克鲁维酵母(Kluyveromyces marxianus)GX-UN120为出发菌株,采用常压室温等离子体(atmospheric and room temperature plasma,ARTP)诱变技术,结合高温胁迫筛选获得1株具有较好耐高温能力和产乙醇能力的菌株GX-UN127。结果表明,诱变菌株GX-UN127在48℃培养72 h,OD_(600)可达到1.27(原始菌株无法生长)。同时,当以100 g/L麸皮为原料,45℃SSF 12 h,诱变菌株GX-UN127发酵乙醇的产量可达7.6 g/L,较出发菌株提升15.2%。在此基础上,结合生理指标和代谢组学进一步探究诱变菌株耐受高温的生理机制,研究表明半胱氨酸和蛋氨酸代谢、谷胱甘肽代谢、精氨酸和脯氨酸代谢、甘油磷脂代谢等代谢途径与诱变菌株GX-UN127的更强高温耐受性密切相关。此诱变选育耐高温马克斯克鲁维酵母菌株的方案可行,为该类菌株进行SSF生产燃料乙醇提供理论支持。展开更多
Zeolitic Imidazolate Framework-8(ZIF-8)material was prepared by chemical precipitation method.The microstructure and physical properties of the as-prepared samples were characterized by XRD,BET,FESEM and UV spectropho...Zeolitic Imidazolate Framework-8(ZIF-8)material was prepared by chemical precipitation method.The microstructure and physical properties of the as-prepared samples were characterized by XRD,BET,FESEM and UV spectrophotometer.The self-made four-channel measurement device was used to test the gas sensitivity of ZIF-8 material toward ethanol gas under photo-thermal synergistic excitation.The results showed that the sample was typical ZIF-8(E_(g)=4.96 eV)with a regular dodecahedron shape and the specific surface is up to 1793 m^(2)/g.The as-prepared ZIF-8 has a gas response value of 55.04 to 100 ppm ethanol at 75℃ and it shows good gas sensing selectivity and repeated stability.The excellent gas sensitivity can be attributed to the increase of free electron concentration in the ZIF-8 conduction band by photo-thermal synergistic excitation,and the large specific surface area of ZIF-8 material provides more active sites for gas-solid surface reaction.The reaction mechanism of ZIF-8 material under multi-field excitation was also discussed.展开更多
One-step conversion of methane and formaldehyde into ethanol is a 100% atom-efficient process for carbon resources utilization and environment protection but still faces eminent challenges due to the lacking of effici...One-step conversion of methane and formaldehyde into ethanol is a 100% atom-efficient process for carbon resources utilization and environment protection but still faces eminent challenges due to the lacking of efficient catalysts. Therefore, developing active and stable catalysts is crucial for the co-conversion of methane and formaldehyde. Herein, twelve kinds of “Single-Atom”-“Frustrated Lewis Pair”(SA-FLP)dual-active-site catalysts are designed for the direct conversion of methane and formaldehyde to ethanol based on density functional theory(DFT) calculations and microkinetic simulations. The results show that the SA-FLP dual active sites can simultaneously activate methane at the SA site and activate formaldehyde at the FLP site. Among the twelve designed SA-FLP catalysts, Fe1-FLP shows the best performance in the co-conversion of methane and formaldehyde to ethanol with the rate-determining barrier of 1.15 e V.Ethanol is proved as the main product with the turnover frequency of 1.32 × 10^(-4)s^(-1)at 573 K and 3 bar.This work provides a universal strategy to design dual active sites on metal oxide materials and offers new insights into the effective conversion of methane and formaldehyde to desired C_(2) chemicals.展开更多
文摘正己烷和乙醇能形成共沸物,利用传统精馏方法很难将二者有效地分离,且二者的共沸物组成对压力较为敏感。本文利用化工流程模拟软件Aspen Plus V12,以Wilson-Radlish-Kwong方程为物性方法讨论正己烷和乙醇物系变压精馏的可行性。利用软件内置的灵敏度分析工具优化了各塔的理论板数、进料位置和回流比,同时利用热集成的方法对该工艺进一步优化。结果表明:正己烷和乙醇物系可以通过变压精馏的方法进行有效分离;热集成流程比非热集成流程降低能耗1403.62 kW,再沸器节能可达39.64%。
文摘为达到同步糖化发酵(simultaneous saccharification and fermentation,SSF)中菌株高温耐受能力提升的目的,该文以实验室保藏的马克斯克鲁维酵母(Kluyveromyces marxianus)GX-UN120为出发菌株,采用常压室温等离子体(atmospheric and room temperature plasma,ARTP)诱变技术,结合高温胁迫筛选获得1株具有较好耐高温能力和产乙醇能力的菌株GX-UN127。结果表明,诱变菌株GX-UN127在48℃培养72 h,OD_(600)可达到1.27(原始菌株无法生长)。同时,当以100 g/L麸皮为原料,45℃SSF 12 h,诱变菌株GX-UN127发酵乙醇的产量可达7.6 g/L,较出发菌株提升15.2%。在此基础上,结合生理指标和代谢组学进一步探究诱变菌株耐受高温的生理机制,研究表明半胱氨酸和蛋氨酸代谢、谷胱甘肽代谢、精氨酸和脯氨酸代谢、甘油磷脂代谢等代谢途径与诱变菌株GX-UN127的更强高温耐受性密切相关。此诱变选育耐高温马克斯克鲁维酵母菌株的方案可行,为该类菌株进行SSF生产燃料乙醇提供理论支持。
基金supported by the National Natural Science Foundation of China(No.51864028)the Yunnan Province Science and Technology Major Project for Materials Genetic Engineering of Rare and Precious Metal(No.202002AB080001)+2 种基金the Yunnan Province Funds for Distinguished Young Scientists,(No.2019FJ005)the Science Research Foundation of Yunnan Provincial Education Department(No.2022J0441)the Sichuan Science and Technology Program(No.22QYCX0097)。
文摘Zeolitic Imidazolate Framework-8(ZIF-8)material was prepared by chemical precipitation method.The microstructure and physical properties of the as-prepared samples were characterized by XRD,BET,FESEM and UV spectrophotometer.The self-made four-channel measurement device was used to test the gas sensitivity of ZIF-8 material toward ethanol gas under photo-thermal synergistic excitation.The results showed that the sample was typical ZIF-8(E_(g)=4.96 eV)with a regular dodecahedron shape and the specific surface is up to 1793 m^(2)/g.The as-prepared ZIF-8 has a gas response value of 55.04 to 100 ppm ethanol at 75℃ and it shows good gas sensing selectivity and repeated stability.The excellent gas sensitivity can be attributed to the increase of free electron concentration in the ZIF-8 conduction band by photo-thermal synergistic excitation,and the large specific surface area of ZIF-8 material provides more active sites for gas-solid surface reaction.The reaction mechanism of ZIF-8 material under multi-field excitation was also discussed.
基金supported by the National Natural Science Foundation of China (Nos.22078257, 22038011 and 22108213)the China Postdoctoral Science Foundation (No.2021M692548)+1 种基金the Joint Fund of the Yulin University and the Dalian National Laboratory for Clean Energy (YLU-DNL Fund No.2022001)the Young Talent Support Plan of Shaanxi Province。
文摘One-step conversion of methane and formaldehyde into ethanol is a 100% atom-efficient process for carbon resources utilization and environment protection but still faces eminent challenges due to the lacking of efficient catalysts. Therefore, developing active and stable catalysts is crucial for the co-conversion of methane and formaldehyde. Herein, twelve kinds of “Single-Atom”-“Frustrated Lewis Pair”(SA-FLP)dual-active-site catalysts are designed for the direct conversion of methane and formaldehyde to ethanol based on density functional theory(DFT) calculations and microkinetic simulations. The results show that the SA-FLP dual active sites can simultaneously activate methane at the SA site and activate formaldehyde at the FLP site. Among the twelve designed SA-FLP catalysts, Fe1-FLP shows the best performance in the co-conversion of methane and formaldehyde to ethanol with the rate-determining barrier of 1.15 e V.Ethanol is proved as the main product with the turnover frequency of 1.32 × 10^(-4)s^(-1)at 573 K and 3 bar.This work provides a universal strategy to design dual active sites on metal oxide materials and offers new insights into the effective conversion of methane and formaldehyde to desired C_(2) chemicals.
