场发射显示器件中真空获得和维持工艺的改进

真空的获得和维持是目前FED研究工作中存在的主要困难之一。本文研究了在现有的传统封接排气以及消气工艺的实验条件下 ,进行了多种工艺改进 :设计了一种新型的三层FED器件结构 ,在这种结构中 ,实现了蒸散型消气剂和非蒸散型消气剂的共同使用 ;并采用了气体保护 ,以及电子轰击去气等有效措施 ,实现了FED器件内部持久的高真空度 ,为FED阴极高稳定、长寿命工作提供了有力的保障     

胆甾相液晶的光学特性

基于胆甾相液晶的特殊分子结构，综合阐述了胆甾相液晶的旋光性、选择性光散射和偏振光二色性等光学特性，揭示了它的光学特性主要源于它螺旋状的分子结构及其光学各相异性。     

波分复用系统中的交错复用器(Interleaver)技术

鉴于波分复用技术已成为光纤通信的发展方向，介绍几种新型的交错复用器的原理、结构等情况，对各种器件进行了比较。     

Multi-grid domain decomposition approach for solution of Navier–Stokes equations in primitive variable form

A new multi-grid (two-grid) pseudospectral element method has been carried out for solution of incompressible flow in terms of primitive variable formulation. The main objective of the proposed method is to apply the multi-grid technique solving the incompressible flow problems associated with three commonly encountered multi-grid environments. In domain decomposition terminology, it includes (I) partially overlapped subdomains, each of which has same types of grids; (II) partially overlapped subdomains, each of which has different types of grids; (III) local adaptive subdomains fully overlapped with the original computational domain (composite grids). The approach for flow problems, complex geometry or not, is to first divide the computational domain into a number of subdomains with the inter-overlapping area (partially or fully overlapped). In categories I and II, the fine-grid or coarse-grid subdomains can be defined by their representation, while in category III the fine-grid or coarse-grid subdomains are defined as usual. Next, implement the Schwarz Alternating Procedure (SAP) to exchange the data among subdomains, where the coarse-grid correction is used to remove the high frequency error that occurs when the data interpolation from the fine-grid subdomain to the coarse-grid subdomain is conducted. The strategy behind the coarse-grid correction is to adopt the operator of the divergence of velocity field, which intrinsically links the pressure equation, into this process. The solution of each subdomain can be efficiently solved by the direct (or iterative) eigenfunction expansion technique or preconditioned method with the least storage requirement, i.e. O(N²) in 2-D. Numerical results of (i) driven cavity flow (Re = 100,400) with Cartesian grids (category I) in each subdomain, (ii) driven cavity flow (Re = 3200) with local adaptive grids (category III) in each subdomain, and (iii) flow over a cylinder (Re = 250) with ‘O’ grids in one subdomain and Cartesian grids in another (category II) will be presented in the paper to account for the versatility of the proposed multi-grid method.     

广州市住宅直饮水设计定额的确定

对住宅直饮水系统的实际运营情况进行了分析,运营中出现的销售水量低于直饮水定额、制水设备实际工作时间低于额定时间及水表工作不正常等现象都反映了现行直饮水设计定额的不合理性,建议将用水量定额定为5～8L/(户·d),既符合实际情况又能满足居民远期需求。     

SISAK快速化学分离装置的建立

SISAK(Short-lived Isotopes Studies by the AKUFVE technique)技术是目前使用最广泛的快速化学分离方法之一,主要应用在短寿命核素的分离和鉴别、超重元素的人工合成以及化学性质研究等方面的工作中.本文简单地叙述了SISAK技术的流程、原理和发展现状,介绍了自行建立的国内第一套基于SISAK技术的快速化学分离装置,并通过从裂变产物中分离短寿命核素这一实例验证了SISAK技术在快速化学分离中的优越性.     

SJT-B助剂/表面活性剂/聚合物三元复合体系的黏度和界面张力研究

助剂SJT-B是10%的磷硅酸盐胶体溶液,含有Na^＋和K^＋、SiO3^2-和PO4^3-等离子,在活化状态下一部分SiO3^2-和PO4^3-生成具5个负电荷的聚磷硅酸根链状阴离子,后者可结合Ca^2＋、Mg^2＋而形成纳米磷硅酸盐胶态粒子,避免结垢并防止金属腐蚀。以助剂SJT-B代替NaOH,用大庆油田回注污水配制SJT-B/烷基苯磺酸盐/聚合物三元复合溶液,取SJT-B浓度为1.0-8.0 g/kg,石油磺酸盐浓度为0.5-4.0 g/kg,聚合物浓度为1.2 g/kg,按排列组合法得到25个实验配方。对照NaOH/石油磺酸盐/聚合物溶液组成为12/3.0/1.2 g/kg,初配黏度（45℃,7.34s^-1）27.3 mPa·s,界面张力（45℃）3.20×10^-3mN/m。初配各实验配方溶液黏度31.2-44.8 mPa·s,45℃老化30天后黏度降低率2.71%-36.97%;初始界面张力最低值1.13×10^-3mN/m,最高值4.34×10^-2mN/m,在界面活性图上,10^-3mN/m超低界面张力区出现在高SJT-B和烷基苯磺酸盐区,老化后该区扩大。筛选出的SJT-B/石油磺酸盐/聚合物体系组成为4.0/3.0/1.2 g/kg,其初始黏度为37.1 mPa·s,老化后黏度降低3.77%,初始界面张力1.79×10^-2mN/m。图2表3参8。     

Production of biodiesel from waste fryer grease using mixed methanol/ethanol system

Transesterification of waste fryer grease (WFG) containing 5–6 wt.% free fatty acid (FFA) was carried out with methanol, ethanol, and mixtures of methanol/ethanol maintaining the oil to alcohol molar ratio of 1:6, and initially with KOH as a catalyst. Mixtures of methanol and ethanol were used for transesterification in order to use the better solvent property of ethanol and rapid equilibrium using methanol. Formation of soap by reaction of FFA present in WFG with KOH instigated difficulty in the separation of glycerol from biodiesel ester. To untangle this problem, two-stage (acid and alkali catalyzed) method was used for biodiesel synthesis. More than 90% ester was obtained when two-stage method was used compared to ∼ 50% ester in single stage alkaline catalyst. In the case of mixed alcohol, a relatively smaller amount of ethyl esters was formed along with methyl esters. Acid value, viscosity, and cetane number of all the esters prepared from WFG were within the range of the ASTM standard. Esters obtained from WFG showed good performance as a lubricity additive.     

U(Ⅳ)-U(Ⅵ)同位素交换反应动力学研究 Ⅰ.Fe~(2+)对U(Ⅳ)-U(Ⅵ)同位素交换反应的催化作用

一、前言由于U(IV)-U(VI)同位素交换体系具有相当大的同位素效应和很好的稳定性,并且容易实现两相回流,这对于分离U同位素的工业应用都是十分有利的。但是,U(IV)-U(VI)同位素交换反应速度非常慢,常温下H~+浓度为1.0—4.0 mol/l时,速度常数为1.0×10~(-4)l~2/mol·s。因此要用U(IV)-U(VI)交换体系浓缩铀同位素,必须研究U(IV)-U(VI)交换反应动力学,找到加快交换反应的方法。