Flower-like titanium dioxide as novel co-reaction accelerator for ultrasensitive “off–on” electrochemiluminescence aptasensor construction based on 2D g-C3N4 layer for thrombin detection

Journal of Solid State Electrochemistry - An ultrasensitive “signal-off–on” electrochemiluminescence (ECL) biosensor is constructed based on f1-TiO2/g-C3N4/PDA for thrombin...     

催化干气制乙苯技术工艺进展

催化干气制乙苯是利用石化副产干气中的乙烯与苯反应生产乙苯的过程,经过20多年的发展与创新,我们相继开发了具有自主知识产权的干气制乙苯第一代至第五代技术,并在石化行业得到了广泛应用.本文从工艺角度综述了催化干气制乙苯的技术发展历程.     

High selective ethylbenzene obtainment through alkylation of dilute ethene with gas phase-liquid phase benzene and transalkylation feed

A novel industrial process was designed for the highly selective production of ethylbenzene. It comprised of a reactor vessel, vapor phase ethylene feed stream, benzene and transalkylation feed stream. Especially the product stream containing ethylbenzene was used to heat the reactor vessel, which consisted of an alkylation section, an upper heat exchange section, and a bottom heat exchange section. In such a novel reactor, vapor phase benzene and liquid phase benzene were coexisted due to the heat produced by isothermal reaction between the upper heat exchange section and the bottom heat exchange section. The process was demonstrated by the thermodynamic analysis and experimental results. In fact, during the 1010 hour-life-test of gas phase ethene with gas phase-liquid phase benzene alkylation reaction, the ethene conversion was above 95%, and the ethylbenzene selectivity was above 83% (only benzene feed) and even higher than 99% (benzene plus transalkylation feed). At the same time, the xylene content in the ethylbenzene was less than 100 ppm when the reaction was carried out under the reaction conditions of 140–185 °C of temperature, 1.6–2.1 MPa of pressure, 3.0–5.5 of benzene/ethylene mole ratio, 4–6 v% of transalkylation feed/(benzene+transalkylation feed), 0.19–0.27 h^?1 of ethene space velocity, and 1000 g of 3998 catalyst loaded. Thus, compared with the conventional ethylbenzene synthesis route, the transalkylation reactor could be omitted in this novel industrial process.     

液相苯与稀乙烯变相催化分离生成乙苯的化学平衡、物料平衡和热量平衡计算

 提出了液相苯和稀乙烯变相催化分离制乙苯的反应示意图,对该烷基化反应部分的化学平衡、物料平衡和热量平衡进行了计算. 在温度185 ℃, 压力2.0 MPa, 乙烯1 mol/h, 氮4 mol/h, 新鲜苯3 mol/h的条件下, 烷基化反应后的绝热温升为175.6 ℃. 计算的温升、乙烯转化率和乙苯选择性结果与实验结果基本相符. 从反应段上部补充的35 ℃的新鲜苯与反应段流出的202.6 ℃气体进行热交换后,体系温度达到185.9 ℃, 稍高于反应温度(185 ℃). 但从反应段下部进入的35 ℃的稀乙烯与反应段流出的202.6 ℃的液体混合进行热交换时,由于稀乙烯使液体产物汽化,导致体系温度大幅度降低,平衡时体系温度仅为153.5 ℃, 远低于所要求的反应温度. 计算结果表明,需给体系提供91.5 kJ的热,或者将稀乙烯加热至523 ℃, 混合后体系平衡温度才能达到185 ℃.     

基于国产FPGA及DAC的任意波形发生器的设计

任意波形发生器作为测试测量设备的一种重要仪器,在航空航天的测量与控制技术领域中得到了广泛应用。当前市场成熟任意波形发生器产品多为国外产品或者国内厂商基于国外FPGA和DAC研制的产品。为了打破技术垄断,提高国产任意波形发生器的自主技术保障能力,研制基于国产芯片的任意波形发生器愈发重要。随着国产芯片设计技术提升,国产FPGA和DAC的性能显著提高,并得到了广泛应用。PXI总线作为当前仪器领域的主要总线类型之一,可以满足大部分测试仪器的通讯要求。基于国产FPGA和DAC器件,从硬件设计和软件设计两个方面出发,成功研制了一款采样率为100MSa/s的 PXI总线任意波形发生器模块,实现了43MHz信号输出,通过实验测试了模块的功能和性能,完全满足模块指标要求,充分证明了国产芯片在工程设计中的性能特性。     

1-Butene isomerization and metathesis over Mo/mordenite-alumina: Factors influencing product distribution and induction period

Effects of space velocity, reaction temperature and support acidity on product distribution and induction period in 1-butene isomerization and metathesis over Mo/mordenite-alumina were investigated. As revealed by the catalytic performance results, induction period and objective product were closely related to the reaction conditions. Lower space velocity led to longer induction period and higher propene yield. The optimal reaction temperature for propene production is around 150 °C and it shifted to 100 °C for ethene production. 1-Butene auto-metathesis predominated in the reaction network if the support with lower degree of sodium exchanged. And propene gradually became the dominant product upon increasing the support sodium exchange degree. 6Mo/H₁₀₀Na₀M-30Al catalyst with a support of full sodium exchange degree exhibited the highest propene yield.     

A Facile Top‐Down Protocol for Postsynthesis Modification of Hierarchical Aluminum‐Rich MFI Zeolites

High aluminum content constitutes a major hurdle for the postsynthesis modification of hierarchical zeolites. A facile protocol comprising fluorination and sequential alkaline treatment is presented for the postsynthesis modification of hierarchical Al‐rich MFI zeolites. By virtue of this protocol, uniform intracrystalline mesoporosity is introduced in an Al‐rich MFI zeolite (Si/Al=14.3). The obtained hierarchical zeolites exhibit a significant mesopore size distribution, centered around 6 nm, and show improved conversions in catalytic cracking of bulky aromatic molecules. The fundamental implications of the fluorination–alkaline treatment protocol are related to the formation of F‐bearing tetrahedral aluminum species in the antecedent fluorination step, which alleviates the resistance of Al sites to the alkaline medium and causes Al?F complexation for regulated hydrolysis of the Al species during the alkaline treatment process. This top‐down protocol and the derived mechanistic understandings are expected to be applied in the synthesis of hierarchical Al‐rich zeolites with other framework topologies.     

二维纳米材料g-C3N4在电化学发光中的应用研究

电化学发光(ECL)兼备电化学和化学发光的特点,灵敏度高、线性范围宽、背景干扰小,得到了广大分析科学研究者的关注;传统的ECL材料虽然发光效率高,但仍存在价格昂贵、负载量低等缺点。g-C₃N₄是一种不含金属的半导体纳米材料,主要以三嗪环或七嗪环为基本结构单元,通过层间的范德华力以及层内的C—N共价键结合,构成类石墨的二维层状结构,具有性质稳定、能带结构独特、生物兼容性好、环保无毒、易于功能化、原料价廉、制备过程简单等优点。自2012年g-C₃N₄首次被发现具备ECL的性能,至今已被广泛应用到ECL中。本文根据ECL的发光机理、传感器的作用效果、传感的信号类型以及不同的检测对象进行了分类,综述了近年来g-C₃N₄在ECL传感器构建中的研究进展,并阐述了g-C₃N₄在ECL发展中存在的挑战和前景。     

Highly selective ethylbenzene production through alkylation of dilute ethylene with gas phase-liquid phase benzene and transalkylation feed

A novel industrial process was designed for the highly selective production of ethylbenzene.It comprised of a reactor vessel,vapor phase ethylene feed stream,benzene and transalkylation feed stream.Especially the product stream containing ethylbenzene was used to heat the reactor vessel,which consisted of an alkylation section,an upper heat exchange section,and a bottom heat exchange section.In such a novel reactor,vapor phase benzene and liquid phase benzene were coexisted due to the heat produced by isothermal reaction between the upper heat exchange section and the bottom heat exchange section.The process was demonstrated by the thermodynamic analysis and experimental results.In fact,during the 1010 hour-life-test of gas phase ethene with gas phase-liquid phase benzene alkylation reaction,the ethene conversion was above 95%,and the ethylbenzene selectivity was above 83% (only benzene feed) and even higher than 99% (benzene plus transalkylation feed).At the same time,the xylene content in the ethylbenzene was less than 100 ppm when the reaction was carried out under the reaction conditions of 140-185℃ of temperature,1.6-2.1 MPa of pressure,3.0-5.5 of benzene/ethylene mole ratio,4-6 v% of transalkylation feed/(benzene+transalkylation feed),0.19-0.27 h-1 of ethene space velocity,and 1000 g of 3998 catalyst loaded.Thus,compared with the conventional ethylbenzene synthesis route,the transalkylation reactor could be omitted in this novel Industrial process.