北石沟风井瓦斯抽放站监控系统技术改造

介绍了北石沟风井瓦斯抽放站监控系统技术改造的基本情况,重点阐述了瓦斯抽放监控部分、中心站部分的设备情况以及抽放监控系统的构造与功能。     

西安市利用陕北天然气的规划与方案

本文概述了西安市天然气供应现状，详细说明了利用陕北天然气规划指导思想、工程规模、供气范围、建设期限和用户发展规划，科学地论述了压力级制和储气量的确定，明确了资金来源、用款计划和材料的采用，重点突出、条理清楚．通过这篇文章，使我们能够全面了解到西安市综合利用陕北天然气的计算和未来发展方向，值得一读．     

煤与瓦斯突出预报的模糊聚类关联分析法

首先采用模糊聚类分析对煤与瓦斯突出的样本集合进行分类，建立不同突出程度的模糊模式。然后用关联分析确定待预报样本与模式的关联程度，以此预测预报样本的煤与瓦斯突出危险程度。这种预报方法相对于模糊聚类分类后，将模式与待预报样本组成新的样本集合，再进行聚类分析，以此分类结果进行预报法。不仅可靠程度高，而且能定量描述待报样本与模式的亲和程度。     

SL(2,R)上的Hardy-Littlewood极大函数的性质

本文给出了SL(2,R)上的Hardy-Littlewood极大函数mf的定义,利用Ergodic定理证明了Hardy-Littlewood极大函数的强(p,p)型性质,p>1.     

Preparation and properties of the SmOx/Rh(100) model surface

The preparation of SmOx/Rh(100) and CO adsorption on this model surface have been investigated with Auger electron spectroscopy (AES), X-ray photoelectron spectroscopy (XPS) and temperature programmed desorption spectroscopy (TDS). The oxygen adsorption on the SmRh alloy surface leads to the aggregation of Sm on the surface. The thermal treatment of this oxidized surface induces the further agglomeration of SmOx on the Rh(100) surface. Compared with CO TDS on the clean Rh(100) surface, three additional CO desorption peaks can be observed at 176, 331 and 600 K on the SmOx/Rh(100) surface. The CO desorption peak at 176 K may originate from CO adsorbed on SmOx islands, while the appearance of the CO adsorption peaks at 331 and 600 K, depending on the oxidation state of Sm, is attributed to CO species located at the interface of SmOx/Rh(100).     

基于J2EE体系结构实现网上购物系统

J2 EE体系结构采用组件的思想 ,将业务逻辑层从客户、服务器端独立出来 ,从而带来开发、使用和维护的便利 .在分析的基础上 ,给出了一个网上购物系统的设计模型和实现方法 .     

宜宾热源公司热电厂锅炉补给水处理工艺改造

分析了宜宾热源公司热电厂锅炉给水处理工艺的问题，指出因为原采用二级钠离子软化工艺水质不达标，造成频繁爆管，严重影响生产的不良后果．介绍了技术改造措施及效果：在原工艺基础上引入复床，将给水硬度控制在2．0μmol／L以下，碱度、氯根及电导率电得到控制，系统运行将近一年，水质稳定，锅炉运行正常安全，不仅消除了以前的生产隐患，而且节约了大量运行成本．     

Liquid-Liquid Equilibrium for 1-Butanol-Water-KF and 1-Butanol-Water-K2CO3 Systems

KF or K2CO3 was added into the 1-butanol-water system and two phases were formed： water-rich phase （water phase） and 1-butanol-rich phase （1-butanol phase）. The liquid liquid equilibrium （LLE） data for 1-butanol-water-KF and 1-butanol-water-K2CO3 systems were measured at 25℃ and showed that 1-butanol phase contained negligible salt and water phase contained negligible 1-butanol when the concentrations of KF and K2CO3 in the water phase were equal to or higher than 27.11% and 31.68% , respectively. Thus water could be separated efficiently from 1-butanol-water by adding KF or K2CO3 into the system. A theoretical calculation of LLE data was calculated by using the Pitzer theory to get water activity in the water phase, and by the models, such as the Wilson, NRTL or the UNIQUAC for the 1-butanol phase. For 1-hutanol-water-KF system, the experimental data were found in good agreement with the calculated results by using Pitzer theory and Wilson equa tion, while for 1-butanol-water-K2CO3 system, the experimental data were found in good agreement with the calculated results by using Pitzer theory and UNIQUAC eauation.