水下隧道穿越管道保护效果测试评价

本文通过对四川气田北干线涪江隧道穿越管道阴极保护电参数的现场测试，取得了实际可信的基础数据，验证了处于水下隧道洞内的穿越段管道，能得到陆上强制电流阴极保护系统的有效保护，保护电流所必经的岩石层和锚喷钢筋混凝土层对保护电流没有构成屏蔽的结论，对管道工程设计和运行管理具有指导作用。     

基于B/S模式的CAPP制造资源管理系统的实现

许多企业内部建有Internet／Intranet网来加强企业内部的信息集成和共享。顺应这一趋势，文章提出了基于B／S模式的CAPP制造资源管理系统，利用网络编程语言VBScript实现制造资源的共享。文章首先通过和C／S模式比较，概述了B／S模式的优势，并建立了适合于动态变化环境的制造资源模型。最后结合应用实例探讨了利用ASP、ADO、SQL和ODBC技术实现制造资源的远程知识查询的理论和方法。     

油箱壁板裂纹分析

两批油箱壁板在加工完成后,放置一段时间后出现裂纹.通过对故障油箱壁板的裂纹宏观观察、断口的宏微观观察以及裂纹金相分析和材料的性能测试,对壁板裂纹的性质与原因进行了分析.结果表明,两批油箱壁板裂纹的性质均为应力腐蚀开裂,壁板上应力腐蚀裂纹的产生与壁板材料的热处理状态、壁板加工后较高的残余应力以及存放环境中的腐蚀介质有关.     

油井缓蚀剂研究与应用

油井缓蚀剂研究与应用崔忠兴(中原油田设计院,濮阳457001)1.前言中原油田已进入高含水期,油井系统腐蚀严重,直接影响了油田的正常生产l’].为了解决油井系统腐蚀问题,在中科院腐蚀所的专种“基础f,联合开发研制了!MC—SDeZS油井缓蚀剂.该剂以合成炔氧甲基胺和炔氧甲基季法盐衍生物,以这两种衍生物为主体成分复配辅助成分而成的水溶油分散吸附成股型缓蚀剂l’1.通过室内高温高压模拟评价试验.ZI口油井加药试验及测试表明l‘],平?...     

高层住宅结构设计

主要介绍长沙梦泽园高层住宅从基础到上部楼层各部位的结构设计,以及在设计、施工过程中所考虑的一些问题及处理方法。     

福氏志贺菌IgY的抑菌作用

目的探讨口服福氏志贺菌IgY在动物体内的抑菌作用。方法以福氏志贺菌制备免疫原,免疫母鸡,收集鸡蛋,提取IgY。以不同剂量的IgY口服免疫6日龄乳鼠,并分别以不同剂量的福氏志贺菌于不同时间攻击,观察体内抑菌作用。结果攻菌前口服特异性IgY的乳鼠,其直肠内分离菌的百分率明显低于攻击后口服IgY的乳鼠。抑菌作用随着口服IgY剂量的减少和攻菌量的增加而降低。口服大于3mg/只的特异性IgY,可使肠内特异菌减少50%以上。口服4mg/只可抵御10亿菌的攻击。结论福氏志贺菌特异性IgY可有效抑制该菌在乳鼠肠内的繁殖。     

湿法磷酸过滤设备和管道结垢原因分析及控制研究

分析湿法磷酸过滤设备与管道结垢的主要原因是氟硅酸钾、钠盐因磷酸液相温度下降而沉积下来。提出采用添加剂,抑制或提前析出氟硅酸钾、钠盐,同时进行了5种添加剂的实验室研究:均有较好的阻垢效果,但最终选择添加剂E(氟硅酸),阻垢率可达70%以上,添加量以0.5g/100g磷矿为宜。     

氯化铜脱除硫化氢气体制硫磺研究

A novel technology of removing H2S with cupric chloride solution was developed in this paper. Cupric as the form of CuS deposition, the CuS produced was then oxidized by excessive cupric ion in another reactor meanwhile cupric ion that has been consumed can be recovered by the oxidization of CuCl2- with oxygen in air,and the solution can be circulated. Moreover, the leaching kinetics of CuS by cupric ion was studied. The removal efficiency of H2S is close to 100%, and the required operating condition is mild. Compared with other wet oxidization methods, no raw material is consumed except O2 in air, the process has no secondary pollution and no problem of degradation and scale, and the absorbent is much stable and reliable.     

Current transients of passive iron observed during micro-indentation in pH 8.4 borate buffer solution

Micro-indentation test of passive iron electrode in deaerated pH 8.4 borate buffer solution was carried out to investigate the rupture and repair of passive film. During driving a conical diamond micro-indenter with a load of 0.1 N order downward to the electrode and driving upward from the electrode, a couple of anodic current peaks were observed. The first current peak spiked during loading was responsible for partial exposure of iron substrate to the solution due to rupture of the passive film when the indenter tip contacted. The second peak emerged during unloading when elastic deformation recovered, which was ascribed to repair at the ruptured sites. The second peak current was larger than the first one. Both peaks were sensitively influenced by electrode potential or concentration of sulfate ions containing in solution. The model for a series of rupture and repair processes of the passive film by micro-indentation was proposed to discuss the current transients.     

SULFUR RECOVERY WITH REDUCED EMISSIONS, LOW CAPITAL INVESTMENT AND HYDROGEN CO-PRODUCTION

The main disadvantage of the Claus process is that by introducing air as oxidant a large volume of tail gas is produced. This must be treated to reduce atmospheric emissions of sulfur-containing gases. The costs of the tail-gas unit are a significant fraction of the total capital and operating costs for sulfur recovery. A new process uses thermal decomposition of hydrogen sulfide in the presence of carbon dioxide instead of air oxidation. The products of this reaction are hydrogen, carbon monoxide, elemental sulfur, water vapor and carbonyl sulfide. Carbonyl sulfide is easily converted to H₂S and C0₂ by liquid- or vapor-phase hydrolysis. Unreacted H₂S and C0₂ are recovered by absorption and recycled to the reactor. Since no air is introduced, there is no tail gas and the tail-gas unit is eliminated, giving a substantial reduction in capital investment. The concentrations of sulfur-containing gases in the product streams depend only on the operation of the absorber and stripper units and can be controlled to very low levels by increasing stripper boil-up. Process operating costs depend on the level of sulfur recovery required and can also be much lower than those of the modified Claus Process.

The process chemistry depends on a shift in the equilibrium of H₂S decomposition caused by reaction of hydrogen with C0₂ by the reverse of the water-gas-shift reaction. Catalysts for this chemistry have been identified. Reactor conversion is further improved by rapid cooling of the reactor effluent gas. Other aspects of process design and operation confer further advantages with respect to the Claus process; however, the process equipment used is similar to that used in a Claus plant. Retrofit of existing plant to the new technology can therefore be considered.