串联组合离子选择电极的研究——利用Ag2S电极测定废水中S2-离子含量

本文依据电池串联原理将多组电极串联组合,减少了因电动势测量误差而造成的测定浓度的相对误差,明显地提高了测定的精密度和准确度.对工业废水中S~(2-)离子含量的测定结果令人满意.其相对偏差低于2.5％,方法回收率为97.5—101.7％,明显优于现有离子选择电极测定方法.与比色法进行比较,测得结果基本一致.     

硫化钠处理含汞废水

为了消除汞污染,采用硫化钠沉淀含汞废水。研究结果表明,出水中汞的含量小于国家规定的排放标准（0.05mg/L）,沉渣体积小,且化学稳定性很好,易处置。此法具有工艺简单,操作方便,反应速度快,沉淀效率高,随废水中含汞浓度的高低投加不同量的硫化钠,根据废水量的大小,可连续处理和间歇处理,处理费用低等优点。该法可在中小型化工行业中推广应用。     

二甲基硫醚光解及二甲基二硫醚生成速率研究

用低压汞灯照射二甲基硫醚（ＤＭＳ）,在２０ｍ的长光池中用富里叶红外光谱仪测量其光解产物,结果表明二甲基硫醚光解生成二甲基二硫醚（ＤＭＤＳ）和乙烷。测量其不同光照时间的光解产物,结果表明Ｉｎ＾ｃ０／ｃｔ在直解坐标上是一条直线,说明了二甲基二硫醚生成按生一极反应进行,其生成的速率常数为８．７０×１０＾－５ｓ＾－１用低压汞灯照射ＤＭＳ＋Ｈ２Ｏ２体系,富里叶红外光谱检测其产物,在有足够的Ｈ２Ｏ２情况下,生     

SW型脱硫剂脱硫性能的研究

以硫酸烧渣为主要原料制备ＳＷ型脱硫剂,并对其脱硫性能进行了研究,对半水煤气、葡萄酒厂污水处理产生的沼气和焦炉煤气、水煤气中的Ｈ２Ｓ进行了工业脱硫试验,经半年以上运行证明,可使其Ｈ２Ｓ含量从３０００－５０００ｍｇ／ｍ＾３降为２０ｍｇ／ｍ＾３以下（符合国家标准）,当脱硫剂工作硫容达３０％时可返回硫酸生产中,再生周期一般为３个月,其主要性能达到国内外同类产品水平。     

光助MIL-101(Fe)活化过氧化氢氧化洛克沙胂及同步吸附生成的砷酸根

采用铁基金属有机框架(MIL-101(Fe))在模拟太阳光下活化过氧化氢氧化降解ROX—吸附去除生成的砷酸根.结果表明,光助MIL-101(Fe)(250mg/L)活化氧化剂H2O2(1.0mmol/L)体系可在120min内实现95.27％的ROX去除率,反应过程中形成的无机砷酸盐(As(Ⅴ))会吸附在MIL-101...     

硫化碱脱除二氧化硫工业烟气的可行性分析

分析了国内外烟气脱硫的研究现状,论述了用硫化碱脱除二氧化硫化工业烟气在理论上和实验上的可能性。     

卤素类阻燃剂的阻燃基础理论

本文从阻燃化学反应,化学键能,热传递和反应动力学角度分析勖类阻燃剂的阻燃机理。     

SO2在Co—Mo／AC催化剂上的还原

本文研究了活性焦（ＡＣ）担载Ｃｏ－Ｍｏ催化剂对ＳＯ２还原的催化性能。考查了催化剂不同的预处理方法,Ｈ２／ＳＯ２摩尔比和还原温度对还原过程硫产率的影响,并就硫化后的Ｃｏ－Ｍｏ和活性焦在催化床不同的构成对硫产率的影响进行了研究。结果表明,经硫化后的催化剂在ＳＯ２＋２Ｈ２→Ｓ＋２Ｈ２Ｏ反应有较高的催化活性,在最佳反应温度３００℃,Ｈ／ＳＯ摩尔比为３,空速６０００Ｌ;ｋｇ＾－１．ｈ＾－１条件下,生成硫的产     

Biological removal of air loaded with a hydrogen sulfide and ammonia mixture

The nuisance impact of air pollutant emissions from wastewater pumping stations is a major issue of concern to China. Hydrogen sulfide and ammonia are commonly the primary odor and are important targets for removal. An alternative control technology, biofiltration, was studied. The aim of this study is to investigate the potential of unit systems packed with compost in terms of ammonia and hydrogen sulfide emissions treatment, and to establish optimal operating conditions for a full-scale conceptual design. The laboratory scale biofilter packed with compost was continuously supplied with hydrogen sulfide and ammonia gas mixtures. A volumetric load of less than 150 gH2S/(m^3.d) and 230 gNH3/(m^3.d) was applied for about fifteen weeks. Hydrogen sulfide and ammonia elimination occurred in the biofilter simultaneously. The removal efficiency, removal capacity and removal kinetics in the biofilter were studied. The hydrogen sulfide removal efficiency reached was very high above 99%, and ammonia removal efficiency was about 80%. Hydrogen sulfide was oxidized into sulphate. The ammonia oxidation products were nitrite and nitrate. Ammonia in the biofilter was mainly removed by adsorption onto the carrier material and by absorption into the water fraction of the carrier material. High percentages of hydrogen sulfide or ammonia were oxidized in the first section of the column. Through kinetics analysis, the presence of ammonia did not hinder the hydrogen sulfide removal. According to the relationship between pressure drop and gas velocity for the biofilter and Reynolds number, non-Darcy flow can be assumed to represent the flow in the medium.     

川东北三高气田钻完井风险因素分析

分析了三高（高压、高产、高含硫）气田存在的主要有害因素,以及三高气田钻完井作业过程中存在的主要危险及其发生的潜在原因,并提出了相应的控制措施。针对我国三高气田区域地质环境的特殊性,分析了我国三高气田钻完井过程中可能诱发事故的特殊因素,并对应对措施进行了探讨。