多级孔ZSM-5分子筛对亚甲基蓝的吸附性能

以多级孔ZSM-5分子筛为吸附剂,吸附水中的亚甲基蓝（MB）,考察了吸附条件对吸附效果的影响,并探讨了吸附的热力学和动力学特征。实验结果表明：在溶液pH为11、分子筛加入量为800 mg/L、吸附温度为303.15 K、吸附时间为60 min、初始MB质量浓度为20 mg/L的条件下,该分子筛对MB的吸附率达97%;溶液pH为5~12时,吸附率均达89%以上,说明该分子筛具有宽的pH适应范围;该分子筛对MB的吸附热力学符合Langmuir和Freundlich方程,293.15~313.15 K的饱和吸附量达50.51~62.11 mg/g,吸附为吸热、自发过程;吸附动力学符合拟二级动力学方程。     

非活性黑根霉菌对废水中重金属离子的吸附

为探讨发酵工业中废弃的菌丝体黑根霉菌（Ｒｈｉｚｏｐｕｓｎｉｇｒｉｃａｎｓ）对水中重金属离子的吸附特性,考察ｐＨ、浓度、共存离子等因素对吸附能力的影响,进行了实验室吸附试验,绘制出吸附等温线,并由Ｌａｎｇｍｕｉｒ曲线和Ｆｒｅｕｎｄｌｉｃｈ曲线求出相应参数。对化学改性前后的黑根霉进行了吸附对比。初步分析了吸附机理。结果表明,黑根霉在ｐＨ＝３—６．５范围内,对Ｐｂ２＋、Ｃｕ２＋、Ｍｎ２＋、Ｃｒ（ＶＩ）几种主要重金属离子都有吸附作用,其中吸附Ｐｂ２＋能力最高,饱和吸附量可达８８ｍｇ／ｇ。经化学改性的黑根霉可不同程度地提高吸附能力。用０．５ｍｏｌ／ＬＨＣＩ和ＮａｏＨ可以洗脱和再生。     

Biomass from phytopathogens and culture conditions improve Penicillium chrysogenum antimicrobial activity and antifungal compounds production

The present study evaluated the effect of culture conditions and phytopathogenic strain co-culture on the production of antimicrobial metabolites and antifungal activity of Penicillium chrysogenum R1, which PCR identified. Antimicrobial activity was determined using the Hunter-Hunter experimental design with three factors (pH, incubation temperature, and inoculum, at two levels each). The antifungal metabolites, β 1-3 glucanase and chitinase, produced in the presence of live and inactivated Fusarium oxysporum Fsox C11 biomass, were evaluated using HPLC-MS and GC-MS. Results showed that P. chrysogenum inhibited the growth of five phytopathogenic fungal strains, and the most significant inhibition was observed for F. oxysporum Fsox C11. The best conditions to achieve the highest antifungal activity of the cell-free extract were pH 7, 28°C, 1 × 10⁶ spores/mL, and 144 h of fermentation, observing 86% inhibition of F. oxysporum Fsox C11 growth. Production of antifungal metabolites such as 1,4-benzoquinone imine, viridicatic acid, phenol-5-methyl-2-(1-methyl ethyl), and hydrolytic enzymes β 1-3 glucanase and chitinase was detected. The results define the perspective in designing new processes and products for biocontrol phytopathogens.     

露天矿山安全管理中异级群组共生决策研究

为解决露天矿山安全管理中利益博弈问题,探究利益相关主体间的共生形成过程,基于共生理论构建以管理者和员工为主体的共生决策博弈模型,并通过稳定性分析和数值仿真探究各主体共生决策的影响因素和演化路径。研究结果表明：博弈主体的共生决策与共生效益、收益分配系数、共生成本、机会主义收益、问责惩罚等因素密切相关;通过分析16种不同参数情形,得到4个演化均衡点;运用Matlab软件进行数值仿真,检验模型准确性,为促进企业安全管理工作共生发展提出相关对策和建议。     

Global variability of food waste chemical composition and its consequences on the production of biofuels and chemical compounds

Journal of Material Cycles and Waste Management - The use of food waste (FW) for the production of biofuels and value-added compounds is growing worldwide. However, the significant chemical...     

张家界体验旅游产品设计与开发

随着体验经济时代的到来,旅游消费者消费理念日趋成熟,人们寻求个性化的服务,追求灵活性、冒险性与多样性,追求真实与差异,对旅游产品提出了更高的要求.在分析张家界旅游产品现状的基础上,提出开发体验旅游产品的设想以及整体设计方案,并从加强体验意识、明确市场定位等方面提出全面开发体验旅游产品的具体建议.     

浅谈兵团中小企业可持续发展与环境保护

新疆生产建设兵团（简称兵团）的中小企业在兵团经济中占有重要地位,但在企业发展的同时,在污染负荷中所占的比例也在相应地上升。本文分析了兵团中小企业的发展现状及带来的环境问题,并提出了解决对策。     

A DFT study on the carbamates formation through the absorption of CO2 by AMP

DFT calculations in gas and aqueous solution phases have been performed to study the mechanism of carbamate formation by the absorption of CO₂ in 2-amino-2-methyl-1-propanol (AMP). The results reveal the importance of considering the effect of water as solvent for the reaction to proceed. Furthermore water molecules play an important role as a basic reactant leading to stable intermediates formation. These results point at a single-step, third order reaction as the most probable mechanism for the formation of carbamate by the absorption process.     

氮、硫掺杂TiO2-壳聚糖微球的制备及其可见光催化性能

采用溶胶-凝胶法制备N、S掺杂TiO2光催化剂,将其与壳聚糖(CS)溶液共混交联,制取N、S掺杂的TiO2-CS(NSTC)微球光催化剂.通过扫描电子显微镜、X射线衍射技术对NSTC微球的形态和晶型结构进行了表征.研究表明,在焙烧温度为450℃、n(N):n(S):n(Ti)=3:3:1的条件下,制备的NSTC微球的可见光催化降解性能最佳.用在最佳条件下制得的NSTC微球在可见光下催化处理pH为3、质量浓度为20 mg/L的甲基橙溶液,反应240 min,甲基橙降解率可达94.1%.NSTC微球重复进行6次可见光催化降解实验,甲基橙降解率仍可达90.0%.     

渗透汽化复合膜分离废水中的低浓度甲醇

采用两种商品化渗透汽化复合膜--GKSS-GS膜和PDMS-P膜分离模拟低浓度甲醇废水,考察了操作温度、甲醇质量分数、废水流量对膜渗透汽化性能的影响.实验结果表明:随温度升高、废水中甲醇质量分数的增大,两种膜的渗透通量都呈增加趋势;GKSS-GS膜的分离系数变化较明显,而PDMS-P膜的分离系数变化较小;废水流量对渗透通量和分离系数的影响均较小.在最佳条件下,GKSS-GS膜的渗透通量为914.6 g/(m~2·h),分离系数为5.6;PDMS-P膜的渗透通量为1 887.2 g/(m~2·h),分离系数为4.8.