基于湿润锋前进法的不同应力状态砂质黄土土柱渗流试验

由于试验装置的局限性,非饱和土渗透特性的研究大多未考虑应力对渗透系数的影响。为探讨水-力耦合作用下砂质黄土的渗透特性,自主研制了一套水-力耦合试验装置。采用湿润锋前进法探究了不同初始干密度和轴向力对非饱和渗透系数的影响,得到水-力耦合作用下非饱和黄土渗透性和轴向位移的演化规律。结果表明:(1)砂质黄土的渗透系数随基质吸力的增大而减小,在不同测试截面处渗透函数曲线出现分层现象;(2)土体的渗透系数随初始干密度和轴向力增大而减小;(3)随轴向力增大,不同初始干密度土柱的稳定渗透系数趋向一致;(4)砂质黄土具有较大的水敏性,在水-力耦合作用下土体结构破坏,导致湿化前后轴向位移差异较大。     

堆石混凝土单轴受压应力-应变全曲线试验方法研究

为了研究堆石混凝土应力-应变全曲线,采用碟形弹簧与钢柱组合成附加刚性元件增强压力机的刚性,研究了碟形弹簧并联与串联联结装置的变形量和刚度以及实现单轴受压端部减摩措施,提出了一种堆石混凝土单轴受压应力-应变全曲线的试验方法。在混凝土压力试验机上进行了堆石混凝土立方体试件单轴受压试验,测得了堆石混凝土受压应力-应变全曲线。试件破坏形态表明,采用的端部减摩措施有效,测得的应力-应变曲线下降段验证了碟形弹簧与钢柱组合装置能够吸收试件破坏时混凝土压力试验机存储的变形能。研究结果为在混凝土压力试验机上进行堆石混凝土单轴受压应力-应变全曲线提供了可行、简便、经济的测试方法。     

多目标优化策略在精馏过程中的应用研究

针对精馏塔自由度多,能耗大,扰动复杂多变,控制和优化要求高等特点,提出了一种基于动态矩阵控制(DMC)的二层多目标优化控制策略。在实现精馏过程控制目标的前提下,设计了二层优化指标,可在有多余自由度的情况下,进行二层控制和优化,实现精馏过程质量控制目标和经济运行优化。通过对Shell多侧线精馏过程的仿真研究,验证了二层多目标优化控制策略的有效性。与DMC控制相比,二层多目标优化控制策略可以明显改善精馏塔运行的经济性,实现增加收益的目标。     

钢管混凝土柱-混合梁节点抗震性能试验研究

提出适用于装配式大跨度组合框架结构的钢管混凝土柱-混合梁节点. 为了研究节点的抗震性能及受力机理,对2个足尺中柱节点试件进行低周往复加载试验. 2个试件分别采用混合梁端型钢翼缘削弱式(RBS)节点以及梁端普通型钢节点. 对2个节点的破坏形态、耗能能力、承载能力、延性以及混合梁的应变分布规律进行对比分析. 试验结果表明,对梁端型钢翼缘的削弱处理可以有效促进试件在翼缘削弱区形成塑性铰,避免梁端焊缝的脆性破坏. 相比型钢未经处理的节点,翼缘削弱节点展现出更好的延性和耗能能力;梁底附加钢筋屈服后的黏结滑移会影响节点的耗能能力,在锚固长度满足规范要求的前提下,应适当增加其配筋率,以防止过早出现附加钢筋屈服后的黏结滑移.     

再生砖混骨料混凝土柱的小偏心受压性能

通过小偏心受压性能试验对比研究3根的天然骨料混凝土柱和3根同强度全再生砖混骨料混凝土柱,强度分别为C25、C30和C35. 对6根柱进行加载试验,分析再生砖混骨料混凝土柱相比于同强度天然骨料混凝土柱在受力过程、破坏特征、变形能力与承载力等方面的差异. 试验发现,再生砖混骨料混凝土柱在小偏心加载至破坏的过程中,具有与天然骨料混凝土柱相似的3个受力阶段,且符合平截面假定. 与同强度的天然骨料混凝土柱相比,变形较大,但再生砖混骨料混凝土柱的极限承载力略高,原因可能在于两者轴心抗压强度的差异.     

脲醛呋喃树脂中氮含量的测定

脲醛呋喃树脂中的含氮量,一般采用克氏定氮法,方法繁琐,费时较长,不利于快速分析的要求,本文利用气相色谱法对脲醛呋喃树脂中的氮含量进行分析测定,并建立了测定方法.方法简捷、快速、重现性好,加标回收率在100.8～109.0之间,准确度较高,可很好的满足工业生产中快速分析的要求.     

气相色谱法检测消毒产品中的正丙醇与乙醇

使用HP-Plot Q色谱柱与FID检测器检测消毒剂中复配的正丙醇与乙醇含量,最大方法相对偏差(RSD)为2.14%,最小方法回收率为100.0%,乙醇与正丙醇的检出浓度为0.025%,是一种快速准确的一针检测法。     

MS Binding Assays for Glycine Transporter 2 (GlyT2) Employing Org25543 as Reporter Ligand

This study describes the first binding assay for glycine transporter 2 (GlyT2) following the concept of MS Binding Assays. The selective GlyT2 inhibitor Org25543 was employed as a reporter ligand and it was quantified with a highly sensitive and rapid LC-ESI-MS/MS method. Binding of Org25543 at GlyT2 was characterized in kinetic and saturation experiments with an off-rate of 7.07×10⁻³ s⁻¹, an on-rate of 1.01×10⁶ M⁻¹ s⁻¹, and an equilibrium dissociation constant of 7.45 nM. Furthermore, the inhibitory constants of 19 GlyT ligands were determined in competition experiments. The validity of the GlyT2 affinities determined with the binding assay was examined by a comparison with published inhibitory potencies from various functional assays. With the capability for affinity determination towards GlyT2 the developed MS Binding Assays provide the first tool for affinity profiling of potential ligands and it represents a valuable new alternative to functional assays addressing GlyT2.     

Continuous size fractionation of magnetic nanoparticles by using simulated moving bed chromatography

The size fractionation of magnetic nanoparticles is a technical problem, which until today can only be solved with great effort. Nevertheless, there is an important demand for nanoparticles with sharp size distributions, for example for medical technology or sensor technology. Using magnetic chromatography, we show a promising method for fractionation of magnetic nanoparticles with respect to their size and/or magnetic properties. This was achieved by passing magnetic nanoparticles through a packed bed of fine steel spheres with which they interact magnetically because single domain ferro-/ferrimagnetic nanoparticles show a spontaneous magnetization. Since the strength of this interaction is related to particle size, the principle is suitable for size fractionation. This concept was transferred into a continuous process in this work using a so-called simulated moving bed chromatography. Applying a suspension of magnetic nanoparticles within a size range from 20 to 120 nm, the process showed a separation sharpness of up to 0.52 with recovery rates of 100%. The continuous feed stream of magnetic nanoparticles could be fractionated with a space-time-yield of up to 5 mg/(L∙min). Due to the easy scalability of continuous chromatography, the process is a promising approach for the efficient fractionation of industrially relevant amounts of magnetic nanoparticles.     

Review on the effect of heat exchanger tubes on flow behavior and heat/mass transfer of the bubble/slurry reactors

Bubble/Slurry bubble column reactors(BCR/SBCR) are intensively used as multiphase reactors for a wide range of application in the chemical, biochemical and petrochemical industries. Most of these applications involve complicate gas–liquid/gas–liquid–solid flow behavior and exothermic process, thus it is necessary to equip the BCR/SBCR with heat exchanger tubes to remove the heat and govern the performance of the reactor. Amounts of experimental and numerical studies have been carried out to describe the phenomena taking place in BCR/SBCRs with heat exchanger tubes. Unfortunately, little effort has been put on reviewing the experiments and simulations for examining the effect of internals on the performance and hydrodynamics of BCR/SBCR. The objective of this work is to give a state-of-the-art review of the literature on the effects of heat exchanger tubes with different types and configurations on flow behavior and heat/mass transfer, then provide adequate information and scientific basis for the design and the development of heat exchanger tubes in BCR/SBCR, ultimately provide reasonable suggestions for better comprehend the performance of different heat exchanger tubes on hydrodynamics.