一类不连续复杂网络的指数同步研究

研究了具有不连续激活函数的复杂网络受非线性干扰通过时滞脉冲和反馈控制达到指数同步的问题,其中反馈控制和时滞脉冲控制用以克服不连续的激活函数对复杂动力网络造成的影响;基于Filippov解、微分包含、Lyapunov函数方法等,提出了几个充分条件,保证了不连续的复杂动力网络达到指数同步;研究结果是对以前结果的推广和改进,可直接应用于连续复杂动力网络;最后通过数值模拟验证了理论的有效性。     

Al掺杂对氧离子导体La2Mo2O9的氧离子扩散和导电性能影响

本文主要研究了Al掺杂效应对氧离子导体La2Mo2–yAlyO9-δ(y = 0.1, 0.2, 0.3)的影响,从XRD、DSC和介电测量中发现,Al3+在La2Mo2O9中的固溶度只有10mol%, 且不能抑制纯 La2Mo2O9的α/β相转变;在La2Mo2–yAlyO9-δ(y = 0, 0.1, 0.2)的介电损耗-频率谱中发现一Pd峰,其机制对应着氧离子的短程扩散,Al掺杂后La2Mo2O9样品的激活能比纯La2Mo2O9的要低,同时对应的电导率比纯La2Mo2O9高。     

微晶纤维素/1-丁基-3-甲基咪唑氯体系流变性能研究

离子液体1-丁基-3-甲基咪唑氯(BmimCl)可用作溶解微晶纤维素(MCC)的优良溶剂。通过稳态剪切和动态扫描测试考察了微晶纤维素离子液体溶液的流变性能。结果表明,所有浓度的MCC/BmimCl溶液在高剪切速率和低剪切速率表现出剪切变稀行为。温度和浓度对MCC/BmimCl溶液的黏弹性质产生重要影响。将复合黏度数据用于Cross模型,并利用Arrhenius公式计算了不同浓度MCC/BmimCl溶液的流动活化能。     

修饰性载体固定化漆酶

采用壳聚糖铜固定化和交联酶聚集体的方法固定化漆酶.探索了固定化前后漆酶的最适温度、pH,热稳定性和金属离子对其活性的影响,交联漆酶聚集体制备的条件.结果为:游离漆酶的最适温度是20℃,最适pH是4.6;壳聚糖铜固定化漆酶的最适温度是25℃,最适pH是4.0;交联漆酶聚集体的最适温度是15℃,最适pH是3.6.固定化后漆酶的热稳定性提高,不同金属离子影响固定化漆酶的活性,其中K+的激活作用尤为明显.制备交联漆酶聚集体最适戊二醛浓度为1%,最适交联时间是2 h.     

土壤重金属与酶活性沿城乡梯度的分布

以沈阳南部沿城乡梯度的3个代表性样区土壤为对象,研究了表层土壤的重金属与酶活性的变化及关系,为土地城市化利用下的重金属污染评价提供科学依据,亦为城市绿地和郊区农田的科学管理提供理论指导。研究结果表明,沿城乡梯度土壤重金属铜、锌、铅的全量及有效量总体呈递减趋势,内梅罗指数法评价结果显示,土壤重金属的单项及综合污染程度均表现城区高于郊区高于农村;土壤的蔗糖酶、脲酶和过氧化氢酶活性则均表现出相反的变化趋势,表明其对重金属胁迫的可能响应。相关分析表明,城市化条件下土壤的蔗糖酶、脲酶和过氧化氢酶活性可以作为土壤铜、锌、铅污染的评价指标。     

Encumbering the intramolecular π donation by using a bridge: A strategy for designing metal-free compounds to hydrogen activation

On the basis of the FLP (frustrated Lewis pair) principle, a new strategy has been proposed to construct the “frustration” in designing metal-free hydrogen activation compounds, by using FMO (frontier molecular orbital) analyses and quantum mechanics calculations. Unlike the known FLPs which use bulky substituents to prevent them from forming stable Lewis acid/base complexes, the new approach encumbers the intramolecular π donation from the electron donor to the acceptor (e.g. in BH₂NH₂) by using a CH₂ bridge (giving BH₂CH₂NH₂). The strategy is simple and effective. Its effectiveness is demonstrated by the small hydrogen activation energy (12.0 kcal/mol) of the model molecule (BH₂CH₂NH₂), which is significantly less than the 42.7 kcal/mol of BH₂NH₂ and also less than the 18.5 kcal/mol of BH₂PH₂ whose derivative, R₂PB(C₆F₅)₂, has been experimentally shown to be able to activate hydrogen. We also exemplified how to use the strategy to design experimentally more realizable molecules. The example shows promises as a hydrogen activation agent. The strategy can be used to design metal-free catalysts for direct hydrogenation.     

基于STC单片机的便携式固定化酶生物传感分析仪

基于对无电环境下快速分析的需求,设计了便携式固定化酶生物传感分析仪,仪器采用STC12C5A32S2单片机作为主控制器,大容量锂离子可充电电池作为工作电源,能连续工作8小时以上。用葡萄糖固定化酶生物传感器对仪器样机进行测试表明,仪器对样品测定的重复性及对不同浓度样品的线性响应均有很好的结果。     

补料分批发酵提高耐高温α-淀粉酶发酵活力的研究

对耐高温α-淀粉酶分批发酵与补料分批发酵工艺进行了研究,结果表明,在35t发酵罐生产条件下,初糖淀粉质量浓度为200g/L,当发酵液中还原糖DE值降至25mg/mL以下时,开始3～5L/min流速流加复合营养盐培养基,使发酵液中DE值维持在20～25mg/mL水平,控制总糖质量浓度为245g/L,在最佳补料分批发酵工艺条件下,放罐酶活力为15600U/mL,较分批发酵的9649U/mL提高61.7%,同时每标吨酶耗淀粉量可降低20%.     

氯化锌活化大麻布活性炭纤维的孔结构

以大麻布为原料,氯化锌为活化剂,在不同活化温度下制备大麻布活性炭纤维样品。采用低温氮气吸附和密度函数理论(DFT)等对样品的孔结构和表面能量分布等表面织构特征进行了研究。结果表明,样品BET比表面积随活化温度的升高呈现先增大后减小的变化趋势,800℃时达到最大值915 m2/g;样品是典型的微孔材料,孔分布集中于2 nm以下的微孔范围内,只有极少部分的中孔,基本没有大孔;样品的表面能量分布较宽,为不均匀性表面;随活化温度的升高,样品碘吸附量呈先增大后减小的变化趋势,与微孔孔容、总孔容以及由BET比表面积的变化趋势一致。     

A micro-sphere catalyst complex with nano CaCO3 precursor for hydrogen production used in ReSER process

This paper describes the preparation and evaluation of a micro-sphere catalytic complex for the hydrogen production in a Reactive Sorption Enhanced Reforming (ReSER) process. The catalytic complex made by a spray technique has a dual function containing Ni as a catalytic material and CaO as an adsorption material used in the ReSER process. The attrition characteristics of the catalytic complex are acceptable for the commercial used. The nano CaCO3 material used as a precursor of CaO showed a desirable durability with a CO2 sorption capacity of 0.6 mol CO2/kg after 10 repeating cycles under the carbonation temperature of 600 ℃, a CO2 partial pressure of 0.02 MPa, and a calcination temperature of 750 ℃ in N2 measured by a thermal gravimetric analyzer. The testing of the catalytic complex for ReSER showed a hydrogen yield of over 95 % (v/v) in the laboratory fixed fluidized bed reactor. The catalytic system has an attractive prospect in the ReSER process for hydrogen production, especially in the fluidized mode where reactor and regenerator combined in a cycling process.