杂多化合物脱硫化氢动力学研究

在双搅拌、无浓度梯度气液反应器中考察了磷钼杂多化合物吸收H2S过程的宏观动力学行为.结果表明,吸收剂浓度提高,脱硫效果增强,当磷钼酸钠浓度超过6.25×10-3mol/L后,单一与复配体系对H2S的吸收速率均趋恒定.从工业操作角度来看,6.25×10-3mol/L是适宜的操作浓度温度提高,吸收效果略有降低,但变化幅度不大,实际操作温度可选择常温;进气H2S浓度提高,吸收效果增强.两种脱硫体系中,以复配体系脱硫性能为优.实验测得25℃下反应器中H2S的气、液相传质系数分别为:kGH-2S =8.201×10-10kmol/(m2.s.Pa),kLH-2S=3.440×10-4m/s.吸收反应对磷钼酸钠及硫化氢的反应级数分别为0.339与1.055.     

阿舍勒块状铜锌硫化物矿床基本特征

新疆阿舍勒块状铜锌硫化物矿床在阿尔泰克兰海西褶皱带玛尔卡库里深断裂的东北侧,产于中泥盆统阿舍勒组英安岩及英安质火山碎屑岩中,与次火山岩关系密切,矿床具有明显的分带性。矿体下盘矿化和围岩蚀变强烈。认为是与海底火山作用有关的黑矿型块状铜锌硫化物矿床。     

Electrochemical study of sulfide solution in the presence of surfactants

ｌｅｃｔｒｏｃｈｅｍｉｃａｌｓｔｕｄｙｏｆｓｕｌｆｉｄｅｓｏｌｕｔｉｏｎｉｎｔｈｅｐｒｅｓｅｎｃｅｏｆｓｕｒｆａｃｔａｎｔｓＹｉＱｉｎｇｆｅｎｇＤｅｐａｒｔｍｅｎｔｏｆＣｈｅｍｉｃａｌＥｎｇｉｎｅｒｉｎｇ，ＸｉａｎｇｔａｎＰｏｌｙｔｅｃｈｎｉｃＵ...     

水中硫化物在线检测仪的研制

介绍硫离子在线检测仪的测定原理和基本系统结构,仪器采用流动注射法(FIA),具有测定周期短、试剂用量少的优点,该方法(显色剂为对二甲氨基苯胺)测定波长为665nm,工作范围ρ=2.0～25.0mg·L-1。回收率为96.1%～101.8%。     

亚甲基蓝比色法测定大气中的硫化氢

用亚甲基蓝比色法测定分析大气中的硫化氢气体,方法灵敏、吸收效果好、稳定性和避光作用较为理想.适用于测定大气中的硫化氢气体.     

Hydrogen storage and distribution systems

Hydrogen storage and transportation or distribution is closely linked together. Hydrogen can be distributed continuously in pipelines or batch wise by ships, trucks, railway or airplanes. All batch transportation requires a storage system but also pipelines can be used as pressure storage system. Hydrogen exhibits the highest heating value per weight of all chemical fuels. Furthermore, hydrogen is regenerative and environment friendly. There are two reasons why hydrogen is not the major fuel of toady’s energy consumption: First of all, hydrogen is just an energy carrier. And, although it is the most abundant element in the universe, it has to be produced, since on earth it only occurs in the form of water. This implies that we have to pay for this energy, which results in a difficult economic task, because since the industrialization we are used to consuming energy for free. The second difficulty with hydrogen as an energy carrier is the low critical temperature of 33 K, i.e. hydrogen is a gas at room temperature. For mobile and in many cases also for stationary applications the volumetric and gravimetric density of hydrogen in a storage system is crucial. Hydrogen can be stored by six different methods and phenomena: high pressure gas cylinders (up to 800 bar), liquid hydrogen in cryogenic tanks (at 21 K), adsorbed hydrogen on materials with a large specific surface area (at T < 100 K), absorbed on interstitial sites in a host metal (at ambient pressure and temperature), chemically bond in covalent and ionic compounds (at ambient pressure), oxidation of reactive metals e.g. Li, Na, Mg, Al, Zn with water. These metals easily react with water to the corresponding hydroxide and liberate the hydrogen from the water. Finally, the metal hydroxides can be thermally reduced to the metals in a solar furnace.     

炼油厂恶臭污染物的防治

论述了炼厂恶臭气体的防治方法，主要从密闭的生产装置、酸性水储罐及污水处理系统几个方面进行了分析并提出了目前为解决恶臭污染采取的方法。     

紫外—双氧水和亚铁离子体系对硝基苯光降解的研究

研究了以５００Ｗ直管高压汞灯为光源，在双氧水和亚铁离子的体系中，对硝基苯进行光降解的可能性。结果表明，在实验条件下，本系统对硝基苯有明显的降解效果。浓度为５０ｍｇ／Ｌ的硝基苯经过６０ｍｉｎ的光照，其降解率可达９１．７％。此外，还探讨 铁离子浓度、双氧水浓度、硝基苯浓度、ｐＨ值等因素对光降解的影响。     

焦化厂蒸氨废水硫化物处理方法探讨

对焦化厂蒸氨废水中的有机物进行了ＧＣ／ＭＳ分析，发现酚类，吲哚，喹啉和硫醇是主要污染物成分。对旨在降低蒸氨废水硫化物含量的各种处理方法进行了比较。采用ＣＷＺ－０１吸附剂的吸附法能使废水中硫化物降至３０ｍｇ／Ｌ以下。     

Production of hydrogen by steam gasification of dehydrochlorinated poly(vinyl chloride) or activated carbon in the presence of various alkali compounds

Steam gasification of dehydrochlorinated poly(vinyl chloride) (PVC) or activated carbon was carried out in the presence of various alkali compounds at 3.0 MPa and 560°C–660°C in a batch reactor or in a semi-batch reactor with a flow of nitrogen and steam. Hydrogen and sodium carbonate were the main products, and methane and carbon dioxide were the minor products. Yields of hydrogen were high in the presence of sodium hydroxide and potassium hydroxide. The acceleration effect of the alkali compounds on the gasification reaction was as follows: KOH > NaOH > Ca(OH)₂ > Na₂CO₃. The rate of gasification increased with increasing partial steam pressure and NaOH/C molar ratio. However, the rate became saturated at a molar ratio of NaOH/C greater than 2.0.