Port reduction in parametrized component static condensation: approximation and a posteriori error estimation

We introduce a port (interface) approximation and a posteriori error bound framework for a general component‐based static condensation method in the context of parameter‐dependent linear elliptic partial differential equations. The key ingredients are as follows: (i) efficient empirical port approximation spaces—the dimensions of these spaces may be chosen small to reduce the computational cost associated with formation and solution of the static condensation system; and (ii) a computationally tractable a posteriori error bound realized through a non‐conforming approximation and associated conditioner—the error in the global system approximation, or in a scalar output quantity, may be bounded relatively sharply with respect to the underlying finite element discretization. Our approximation and a posteriori error bound framework is of particular computational relevance for the static condensation reduced basis element (SCRBE) method. We provide several numerical examples within the SCRBE context, which serve to demonstrate the convergence rate of our port approximation procedure as well as the efficacy of our port reduction error bounds. Copyright © 2013 John Wiley & Sons, Ltd.     

八氯甲基笼型倍半硅氧烷的合成及表征

以氯甲基三氯硅烷为原料,甲醇、氯仿和石油醚为混合溶剂,在浓盐酸和无水三氯化铁为催化剂的条件下水解缩合制备了八氯甲基笼型倍半硅氧烷(CM-POSS)。利用FT-IR、GPC、1 H-NMR、29Si-NMR和XRD等技术对产物的结构进行了表征,并通过TGA研究了其热稳定性。结果表明产物为八氯甲基笼型倍半硅氧烷,且热稳定性良好。     

直接法合成月桂酰基甲基牛磺酸钠

以月桂酸和N-甲基牛磺酸钠为原料,经直接缩合一步反应合成了月桂酰基甲基牛磺酸钠。考察了直接法缩合工艺中反应温度、反应时间、催化剂种类和用量、投料比、溶剂用量等对反应的影响。结果表明,优化反应条件为:月桂酸与N-甲基牛磺酸钠投料摩尔比为1.3∶1,催化剂硼酸用量为月桂酸质量的2%,溶剂用量为月桂酸质量的40%,215℃反应6 h。在上述条件下,N-甲基牛磺酸钠的转化率可达95%以上,粗产品经重结晶及干燥处理后纯度可达98%以上。     

Synthesis and characterization of MQ silicone resins

MQ silicone resins, which represent a broad range of hydrolytic condensation products of monofunctional silane (M) and tetrafunctional silane (Q), were synthesized by reaction of water glass with hexamethyldisiloxane. The optimum reaction time and the optimal reaction temperature is 30 min and 30–40°C, respectively. Concentrated hydrochloric acid is the best one among those catalysts tested. In large-scale experiments (420–1680 mL), the favorable feeding order is catalyst first, and then water glass, the mixture of hexamethyldisiloxane and ethanol last and most MQ silicone resin was observed. The structure of MQ silicone resin was characterized by FT-IR and GPC spectra. The MQ silicone resin shows narrow molecular weight distribution and the number average molecular weight of MQ silicone resin is 2917. The silicone pressure sensitive adhesive prepared from as-synthesized MQ resin has good tack (29#) and 180° peel adhesion (5.630N/20 mm). © 2012 Wiley Periodicals, Inc. J Appl Polym Sci, 2012     

冷凝法甲苯回收系统设计优化

针对典型工业挥发性有机物（VOC）甲苯设计一套冷凝法回收系统。该系统制冷部分采用冰箱系统常用的分立多循环结构,将回收流程分为预冷级和冷却级。运用物性软件REFPROP及通用流程模拟软件Aspen Plus对甲苯负荷及制冷流程进行模拟。通过对系统的模拟运行,研究该冷凝法甲苯回收系统的工作性能以及能耗影响因素,为系统的进一步设计优化提供理论依据。     

Layered precursors for new zeolitic materials: Synthesis and characterization of B-RUB-39 and its condensation product B-RUB-41

Condensation of layered silicate precursors leads to new, all silica zeolite frameworks. In order to introduce catalytic functionality, boron has been substituted into the silicate layer of RUB-39 in a single step synthesis process. Condensation of the silicate layer to the zeolite framework of RUB-41, RRO framework structure type, preserved B as constituent of the material. Analysis of structural details obtained from Rietveld analysis of powder diffraction data, ¹¹B and ²⁹Si NMR experiments of the as synthesized precursor as well as of the zeolite condensation product, and crystal chemical reasoning indicates segregation of B on one specific T-site. This T-site is buried in the silicate anionic layer of the precursor shielding the additional negative charge introduced by the trivalent T-atom.     

气相流化床聚乙烯冷凝技术的应用与运行优化

介绍了气相流化床聚乙烯冷凝技术特点,分析了气相流化床聚乙烯冷凝模式操作参数的相互影响关系,提出了装置投料开车及冷凝模式下稳定运行的优化措施。运行结果表明,在冷凝操作模式下应确定各参数的安全操作范围,冷凝操作的进入或退出应尽快完成。装置开车阶段对原料和回收液(气)要预先取样分析合格,投催化剂后出现静电大幅波动应消除杂质来源再提负荷,进冷凝操作模式时原始种子床粉料应排出彻底,为防止反应器爆聚应提高对异常现象的判断及处置速度。装置运行阶段应强化原料质量和原料精制床精制效果的监控。     

三苯二恶嗪型酸性蓝AXG的合成研究

由2,5-二氨基苯磺酸和四氯苯醌一缩合制得缩合物2,5-双(4-氨基-3-磺酸基苯胺)-3,6-二氯苯醌(A);该缩合物在15%发烟硫酸和过氧二硫酸铵作用下,发生分子内环合制得3,10-二氨基-6,13-二氯三苯二恶嗪-4,11-二磺酸(B);在氧化剂过氧化苯甲酰的作用下,B与苯亚磺酸钠二缩合得到三苯二恶嗪型酸性蓝AXG。本文对一缩合反应、环合反应、二缩合反应的物料配比、反应温度、反应时间等因素进行了探讨,找出了较佳反应条件。     

A Simple Method for Control Rod Worth Evaluation with Diffusion Codes

To present a simple method for calculating the worth of control rods in multiregion reactor cores, the well model approximation is applied to the finite difference diffusion code. The results of calculation are compared with experimental results obtained on the ōzenji Critical Facility, and also with calculations using transport equivalent constants. With its simplicity, the method proposed is accurate enough to suffice amply for most cases where only the reactivity is the end result sought, although the application of this method is limited to control rods inserted in the core region, and gives no information about the detailed neutron flux distribution around the control rod.     

Oxidative pyrolysis of kraft lignin in a bubbling fluidized bed reactor with air

Fast pyrolysis of kraft lignin with partial (air) oxidation was studied in a bubbling fluidized bed reactor at reaction temperatures of 773 and 823 K. The bio-oil vapors were fractionated using a series of three condensers maintained at desired temperatures, providing a dry bio-oil with less than 1% water and over 96% of the total bio-oil energy.Oxygen feed was varied to study its effect on yield, composition, and energy recovery in the gas, char and oil products. The addition of oxygen to the pyrolysis process increased the production of gases such as CO and CO₂. It also changed the dry bio-oil properties, reducing its heating value, increasing its oxygen content, reducing its average molecular weight and tar concentration, while increasing its phenolics concentration. The lower reaction temperature of 773 K was preferred for both dry bio-oil yield and quality.Autothermal operation of the pyrolysis process was achieved with an oxygen feed of 72 or 54 g per kg of biomass at the reaction temperatures of 773 and 823 K, respectively. Autothermal operation reduced both yield and total energy content of the dry bio-oil, with relative reductions of 24 and 20% for the yield, 28 and 23% for the energy content, at 773 and 823 K.