Sulfur addition to aldimines: thioamides,not thiaziridines,as products; revision of an old report

The reaction of 4-(phenylimino)butan-2-ol with ammonium polysulfide in refluxing EtOH yields 3-hydroxy-N-phenylbutanethioamide as the only isolated product. The structure has been established by single-crystal X-ray diffraction. Treatment of N-benzylidenamines with ammonium polysulfide has proven a general method for the preparation of thiobenzamides.     

关于如何对低硫灰口铸铁进行孕育处理的探讨

研究了低硫情况下电炉熔炼如何改进孕育效果的方法．研究表明，对含硫较低铸铁的孕育方法的改进，不一定非要通过补硫或改善孕育剂的方法来实现；通过增加原有孕育剂的数量、改进孕育方法同样能改善孕育效果．     

循环流化床锅炉脱硫的工业试验及模型预测

通过在７５ｔ／ｈ循环流化床锅炉上所进行的试验研究,取得了加石灰石脱硫的动态特性。依据循环流化床锅炉运行特点,对原有的循环流化床锅炉脱硫模型进行了部分改进,成为已建的循环流化床锅炉总体数学模型的一个子模型。运用该模型对循环流化床锅炉炉内ＳＯ２的生成和脱除进行模拟,模拟结果与工业试验结果吻合。模拟结果还揭示了加石灰石脱硫对循环流化床锅炉运行的影响。     

Effect of the composition of some sulphide minerals on cyanidation and use of lead nitrate and oxygen to alleviate their impact

An investigation was carried out on synthetic ores containing high purity pyrite, pyrrhotite and chalcopyrite and on two gold ores currently processed to evaluate the impact of cyanicides on cyanidation and to improve the leaching performance by using a pre-leaching, injecting oxygen and adding lead nitrate. With regard to the synthetic ores, it was found that pyrrhotite did not generate a high cyanide consumption while pyrite and chalcopyrite were detrimental. Pre-leaching was deleterious for the ore containing chalcopyrite while pre-leaching with lead nitrate was very efficient to decrease the reactivity of the ore containing pyrite. The two gold ores studied had very different compositions. The low sulphide ore had a low sulphide content (1.36% S), present as pyrrhotite while the second had a very high sulphide content (20.2% S), in the form of pyrite, pyrrhotite and chalcopyrite. The efficiency of the process conditions was peculiar to the ores. The high sulphide ore required a stronger, longer pre-leaching period (12 h) with greater amounts of lime (7.0 kg/t) and lead nitrate (600 g/t) than the low-sulphide ore. The ore with a low sulphide content required a pre-leaching of only 1 h with a small quantity of Pb(NO₃)₂ (50 g/t) and leaching can be performed at 360 ppm NaCN to allow a recovery of 96.4% Au and a low cyanide consumption at 0.18 kg/t. As for the high sulphide ore, cyanidation had to be conducted at 560 ppm NaCN to recover 88.4% Au with a cyanide consumption of 0.80 kg/t. An increase in the amount of lime enhanced oxidation of soluble sulphides. Lead nitrate stabilized copper and iron dissolution by forming a passivation layer at the surface of sulphide minerals. Lead nitrate also prevented the formation of a passive layer at the surface of gold.     

Nitrate Removal in Sulfur: Limestone Pond Reactors

The feasibility of using sulfur:limestone autotrophic denitrification (SLAD) pond reactors to treat nitrate-contaminated water or wastewater after secondary treatment was investigated with four lab-scale continuously fed SLAD ponds. The start-up period, temperature effects, and effects of different feed solutions were evaluated. With an influent concentration of 30 mg NO3?–N/L at an HRT of 30 days, the pond reactors had an overall nitrate removal efficiency of 85–100%. Effluent nitrite concentrations were <0.2 mg N/L in all tests. Aerobic conditions could result in a decrease of the SLAD pH of the pond by 2 to 3 units and a large increase in sulfate production ( ～ 1600–1800?mg-SO42?/L). Under unmixed (anoxic) conditions, the pH and sulfate produced were maintained at approximately 5.5 to 5.6 and 400–600?mg-SO42?/L, respectively, in all the SLAD ponds. Temperature affected the pond reactors adversely. By assuming that a first-order reaction occurred in a SLAD pond reactor, the temperature-activity coefficient, θ was found to be 1.068. Treatment of nitrate-contaminated surface water and wastewater using SLAD pond systems is feasible only if (1) the chemical oxygen demand (COD)/nitrate–N (COD/N) ratio is low (<1.2 with an initial NO3? concentration of 30 mg-N/L), (2) sulfur:limestone granules are not covered by sediment, and (3) sulfur-utilizing but nondenitrifying bacteria (SUNDB) are greatly inhibited due to the lack of DO in the pond systems. The SLAD ponds are not feasible for the treatment of raw wastewater or surface water if they contain high concentrations of organic matters due to the possible inhibition of sulfur-based autotrophic denitrifiers by heterotrophs (including heterotrophic denitrifiers). In addition, a high sulfate and low DO concentration as well as a low pH in the SLAD effluent of the pond (even when the pond is operated in an unmixed mode) also will limit the application of SLAD pond processes.     

大冶铁矿分离浮选药剂对硫精矿脱水过程的影响

在实验室条件下对影响硫精矿滤饼水份的原理进行了研究。研究表明大冶铁矿分离浮选所用的药剂对硫精矿的脱水过程有影响,影响硫精矿滤饼水份的主要因素是分离浮选中作为黄铁矿抑制剂使用的石灰,同时Ｚ－２００＃捕收剂对硫精矿的滤饼水份也有不利影响,但其影响程度比石灰要小。用硫酸调节硫精矿矿浆的ＰＨ值可以降低其滤饼水份。     

横向光泵获得S_2紫外激光

用ＸｅＣｌ准分于激光器（３０８．１ｎｍ）横向泵浦Ｓ２激光器，又成功地实现了Ｓ２Ｂ－Ｘ态近ＵＶ波段的激光振荡。在波长３３０．９～３９０．０ｎｍ范围内观测到６条近ＵＶ激光输出。测量了有关的激光参数。     

真空感应炉坩埚材质对镍基合金Inconel 690氧硫含量的影响

研究和分析了200 kg和500 kg真空感应炉镁质（/%:97.60MgO、1.34CaO）、钙质（/%:98.70CaO、0.55MgO）和铝镁质（/%:85.57Al₂O₃、11.36MgO、2.47CaO）坩埚对所熔炼的Inconel 690镍基合金（/%:0.01～0.03C、27.0～31.0Cr、7.0～11.0Fe）中氧、硫含量的影响。结果表明,铝镁质坩埚冶炼的合金中氧含量最低,为（10～15）×10^-6[O]和（50～60）×10^-6[S];CaO坩埚冶炼的合金中硫含量最低,为10×10^-6[S]和（27～48）×10^-6[O];MgO坩埚冶炼的合金中氧、硫含量较高,为（50～60）×10^-6[S]和（24～35）×10^-6[O]。     

Sulfur Impregnation on Activated Carbon Fibers through H2S Oxidation for Vapor Phase Mercury Removal

Sulfur was impregnated onto activated carbon fibers (ACFs) through H2S oxidation catalyzed by the sorbent surface in a fixed-bed reactor. By changing the temperature and duration of the sulfur impregnation process, ACFs with different sulfur contents were developed. Characterization of ACFs before and after sulfur impregnation was conducted by surface area analysis, energy dispersive X-ray analysis, thermogravimetric analysis, X-ray photoelectron spectroscopy, and temperature programmed desorption. Vapor phase mercury adsorption experiments were carried out in a fixed-bed reactor. Sulfur was impregnated mainly as elemental sulfur and the amount of sulfur deposited on the ACF increased with an increase in impregnation temperature. Higher temperature leads to more uniform sulfur distribution inside the sorbent pores. The impregnation process can be explained by a combination of pore filling and monolayer adsorption, with the former mechanism predominating at low temperatures. In the absence of sulfur, the mercury adsorption capacity can be correlated with surface area and pore volume.     

空气氧化法生产焦锑酸钠过程氧化后液中硫的形态分析

通过试验提出了一种分析硫形态的方法,即用碘量-硫代硫酸钠滴定法分析了空气氧化法生产焦锑酸钠过程氧化后液中硫的形态;试验结果和理论值相符合,最后经过加入回收试验的验证,各种形态硫的回收率在99.5％-100．3％之间,可以看出此方法是一种准确、快速的硫形态的分析方法。