An Immobilized‐Dirhodium Hollow‐Fiber Flow Reactor for Scalable and Sustainable C−H Functionalization in Continuous Flow

A scalable flow reactor is demonstrated for enantioselective and regioselective rhodium carbene reactions (cyclopropanation and C?H functionalization) by developing cascade reaction methods employing a microfluidic flow reactor system containing immobilized dirhodium catalysts in conjunction with the flow synthesis of diazo compounds. This allows the utilization of the energetic diazo compounds in a safe manner and the recycling of the dirhodium catalysts multiple times. This approach is amenable to application in a bulk‐scale synthesis employing asymmetric C?H functionalization by stacking multiple fibers in one reactor module. The products from this sequential flow–flow reactor are compared with a conventional batch reactor or flow–batch reactor in terms of yield, regioselectivity, and enantioselectivity.     

纳米氧化锰负载钛基电催化膜制备及处理含酚废水性能研究

以多孔钛膜为基膜,醋酸锰为锰源,采用溶胶凝胶法制备出负载纳米氧化锰的钛基电催化膜（nano-MnO_x/Ti膜）. 运用X射线衍射(XRD)、 X射线光电子能谱(XPS)、场发射扫描电子显微镜(FESEM)、循环伏安法(CV)、交流阻抗法（EIS）和计时电流法(CA)等测试手段,对MnO_x/Ti膜电极的微观形貌、晶型、电化学性能等进行表征. 结果表明：所得催化剂是由直径为50 nm的γ-MnO₂和Mn₂O₃纳米棒所组成,且均匀分布于Ti膜上,负载催化剂后钛膜电极电化学性能和催化性能明显提高,催化剂与基体之间键合的形成提高其稳定性. 以棒状nano-MnO_x/Ti膜电极为阳极构建电催化膜反应器(ECMR)处理含酚废水,当苯酚溶液浓度为10mmol·L^-1,电流密度为0.25mA·cm^-2、停留时间为15 min时,COD去除率可达95.1%.     

化学模拟在反应堆水化学课程中的应用

高温高压化学反应对反应堆设备的可靠性、反应堆性能的控制、核电站运行的安全持久性等具有重要影响,但相关实验难以在高校教学中开展。借助PHREEQC程序及最新热力学数据,建立了反应堆一回路硼酸-氢氧化锂添加配比、腐蚀沉淀物产生及二回路pH控制方案的化学反应模型。运用化学模拟来教学,促进了学生对所学知识的理解与掌握,丰富了现代教学方法。相关模型对核电企业的培训也具有一定参考价值。     

A Monte Carlo Method to Quantify the Effect of Reactor Residence Time Distribution on Polyolefins Made with Heterogeneous Catalysts: Part I—Catalyst/Polymer Particle Size Distribution Effects

Polyolefins are commercially produced in continuous reactors that have a broad residence time distribution (RTD). Most of these polymers are made with heterogeneous catalysts that also have a particle size distribution (PSD). These are totally segregated systems, in which the catalyst/polymer particle can be seen as a microreactor operated in semibatch mode, where the reagents (olefins, hydrogen, etc.) are fed continuously to the catalyst/polymer particle, but no polymer particle can leave. The reactor RTD has a large influence on the PSD of the polymer particles leaving the reactor, as well as in polymer microstructure and properties, polymerization yield, and composition of reactor blends. This article proposes a Monte Carlo model that can describe how particle RTD in a single or a series of reactors can affect the PSD of polymer particles made under a variety of operation conditions. It is believed that this is the most flexible model ever proposed to model this phenomenon, and can be easily modified to track all properties of interest during polyolefin production in continuous reactors with heterogeneous catalysts.     

焙烧条件对浆态床CO甲烷化Ni-Al2O3催化剂性能的影响

结合行星式球磨机,采用机械化学法制备Ni-Al₂O₃催化剂,考察了焙烧温度和焙烧时间对Ni-Al₂O₃催化剂晶相结构、还原特征、孔道结构和浆态床CO甲烷化性能的影响。通过XRD、H₂-TPR、BET、XPS和TPH等方法对反应前后催化剂进行表征。结果表明,焙烧温度从350℃升高到700℃,活性前体NiO仍在载体表面高度分散,催化剂还原峰温向高温方向偏移。其中,450℃条件下焙烧所获得的cat-450试样比表面积最大,为350 m²/g。评价结果显示,焙烧温度从350℃升高到700℃,CO转化率、CH₄选择性和收率均呈先升高后降低的趋势,于450℃达到最大值,分别为97.8%、88.2%和86.2%。另外,焙烧时间对催化剂的还原性能影响较小,对载体Al₂O₃的晶相结构有一定影响。随焙烧时间延长,CO转化率稍有降低,而后增大;焙烧时间为4 h,CH₄选择性和收率均较大。     

固定化β-葡萄糖醛酸酶反应器的制备及其在4-甲基亚硝胺基-1-(3-吡啶)-1-丁醇的O-糖苷化合物分析中的应用

采用溶胶-凝胶法,以丙烯酰胺作为单体,制备了基于有机-硅胶杂化整体柱的β-葡萄糖醛酸酶反应器。优化了硅酸甲酯和γ-(甲基丙烯酰氧)丙基三甲氧基硅的物质的量的比、丙烯酰胺和聚乙二醇的用量,以及水浴温度等制备条件,获得了孔隙均匀、通透性良好、机械强度高的有机-硅胶杂化整体柱。采用光学显微镜和扫描电镜表征杂化整体柱。进一步将β-葡萄糖醛酸酶共价键合在整体柱上,以4-甲基亚硝胺基-1-(3-吡啶)-1-丁醇(NNAL)的O-糖苷化合物(NNAL-O-Gluc)为底物研究酶反应器的水解效果,实验结果证明酶反应器在室温条件下的水解效率大大提高,实现了NNAL-O-Gluc高效水解与分析,解决了目前NNAL-O-Gluc分析中前处理水解效率低的问题。     

High throughput tryptic digestion via poly (acrylamide-co-methylenebisacrylamide) monolith based immobilized enzyme reactor

A poly (acrylamide-co-methylenebisacrylamide) (poly (AAm-co-MBA)) monolith was prepared by thermal polymerization in the 100 or 250 μm i.d. capillary. The monolithic support was activated by ethylenediamine followed by glutaraldehyde. Trypsin was then introduced to form an immobilized enzyme reactor (IMER). The prepared IMER showed a reliable mechanical stability and permeability (permeability constant K = 2.65 × 10⁻¹³ m²). With BSA as the model protein, efficient digestion was completed within 20 s, yielding the sequence coverage of 57%, better than that obtained from the traditional in-solution digestion (42%), which took about 12 h. Moreover, BSA down to femtomole was efficiently digested by the IMER and positively identified by matrix assisted laser desorption/ionization-time of flight mass spectrometry (MALDI-TOF MS). To test the applicability of IMER for complex sample profiling, proteins extracted from Escherichia coli were digested by the IMER and further analyzed by nanoreversed phase liquid chromatography-electrospray ionization-mass spectrometry (nanoRPLC-ESI-MS/MS). In comparison to in-solution digestion, despite slightly fewer proteins were positively identified at a false discovery rate (FDR) of ∼1% (333 vs 411), the digestion time used was largely shortened (20 s vs 24 h), implying superior digestion performance for the high throughput analysis of complex samples.     

Voltammetry Under Microfluidic Control,a Flow Cell Aproach

A generic approach to the design, construction and experimental characterization of novel microelectrochemical reactors (MECR) is presented. Structurally well‐defined rectangular microchannels incorporating electrochemical sensors were fabricated using a propriety photosensitive glass and photolithographic techniques. Microelectrode sensors were produced via evaporation to yield, gold, silver or platinum bands of approximate lengths 10–50 μm. The approach outlined permits cells of dimensions in the range: height 50–100 μm, width 100–500 μm and length 1–3 cm to be accurately constructed, in single or array configurations and were characterized via a voltammetric study utilizing electrolyte solutions containing N,N,N′N′‐Tetramethyl‐1,4‐phenylenediamine. In all cases, the test cells were constructed so that the three dimensional hydrodynamic boundary layer within the cells would significantly influence the reagent transport and therefore the observed current density at the microelectrodes. The current/flow rate relationship observed was analogous to the response of the observed within the macroscopic channel flow cells, where typically the cell design is restricted to configurations where a two dimensional transport analysis can be performed.