EDTA直接滴定测定镍

参考磷酸在345~356℃时有强腐蚀性的特点,采有硫磷混合酸消解矿样,能使样品消解完全。本方法经加标校核证明,检测结果重现性好,准确度高。     

Novel Biocomposites Sheet Molding Compounds for Low Cost Housing Panel Applications

Biocomposites were made by a novel high volume processing technique named biocomposite sheet molding compound panel (BCSMCP) manufacturing process. This process design was inspired by the commercial glass fiber–polyester resin composite fabrication method called sheet molding compounding (SMC). This process yields continuous production of biocomposites on a large scale, and thus can be easily adopted in industries. A unique fiber dispersion method, which enabled uniform distribution of natural fibers, was used in this process. Consistency of the process was tested by evaluating the repeatability of the resultant materials mechanical properties. The low cost biocomposites produced as a result of the processing will be used for various panel applications such as housing and transportation. The molded samples were tested for various mechanical and thermal properties, in accordance with ASTM procedures. The biocomposites were made with various natural fibers including, big blue stem grass, jute, and industrial hemp. By combining different natural fibers in varying mass fractions, hybrid biocomposites were made using this process. Grass fiber reinforced polyester biocomposites processed by the SMC line showed very promising results.     

中国加油站VOC排放污染现状及控制

应用排放因子法估算了2002年度全国加油站VOC的排放量.在综合考虑经济,社会,人口等各方面因素后,通过调整现有的活动水平估算了未来20a内全国的燃油消耗情况,以及VOC排放的增长趋势.结果表明:2002年我国加油站VOC排放量为187.6×10³t,由此造成的经济损失达到了7.5×10⁸元人民币.在维持现有控制水平情况下,到2030年VOC排放量将达到1196×10³t,经济损失高达47.8×10⁸元人民币.比较了StageⅠ、StageⅡ油气回收系统以及ORVR的回收效率和成本,并对其可行性和经济适用性进行分析.结果表明:这3种回收技术的引进将会大规模的消减加油站VOC的排放,并且选择性的措施组合能够取得更好的效果.相对于StageⅡ回收系统,ORVR的效率更高费用更低.但是ORVR的引进需要比StageⅡ更长的时间,为了达到80%的普及率至少需要11a左右.为在短期内达到一定的控制要求,可优先考虑StageⅡ回收技术;但是从长期的环境和经济效应来看,ORVR才是最终的选择.     

有机改性粘土去除赤潮生物的机制研究

研究了季铵化合物改性粘土的制备条件对其去除赤潮藻效果的影响,探讨了该粘土体系高效除藻的机制.实验表明,十六烷基三甲基铵(HDTMA)可以有效地提高粘土的絮凝能力,同时HDTMA改性粘土中含有亚稳态HDTMA,增加了该改性粘土对赤潮生物的灭杀能力.改性粘土去除赤潮藻的能力与所吸附季铵化合物的杀藻能力、吸附量正相关,当老化时间延长、吸附季铵化合物稳定性增强时改性粘土除藻能力大大降低.结构不同的粘土对于吸附HDTMA的稳定化产生的空间阻力不同,在吸附量相同的情况下3层结构的蒙脱土中会有更多的亚稳态HDTMA产生;由于同离子效应,反应介质中高价金属阳离子的存在提高了亚稳态HDTMA的量,因此相应的改性粘土具有更高的赤潮藻去除能力.在60℃条件下吸附的HDTMA会更有效地占据粘土中的阳离子交换位,达到稳定态;而升高或降低温度都会有利于亚稳态HDTMA的出现,相应的改性粘土具有更高的赤潮藻去除能力.     

电解浮选用于活性污泥固液分离的研究

在装有Ti/RuO₂-IrO₂-TiO₂阳极、Ti阴极的电解浮选槽中进行了活性污泥固液分离的研究.考察了影响电解浮选性能的操作参数,这些参数包括水力停留时间、电流密度、进水SS浓度和进水pH值.研究表明,电解浮选是高效的固液分离单元,水力停留时间和电流密度是主要的影响因素.SS的去除率随着水力停留时间和电流密度的增加而增大;污泥负荷增加,SS的去除率下降;pH值影响电解产生微气泡的尺寸和污泥性质,但对SS的去除影响不大,实际应用中可以不调节pH值.进水SS约1 000mg/L时,当水力停留时间为20min,接触室电流密度为5 mA/cm²,分离区电流密度为2.5 mA/cm²,SS的去除率可达97%以上,此时的能耗为0.4～0.5(kW.h)/m³废水.电解浮选产生的浮渣含水率为95.9%,低于溶气气浮和二沉池的污泥含水率,对污泥减量化及其最终处置有较大的意义.     

基于微生物相互作用机理的完全耦合活性污泥模型研究

根据微生物生长机理,推导出微生物的耦合作用机理并在该机理的基础上改进了ASM3 Bio-P模型.假设活性污泥系统中有机物氧化过程、生物硝化过程、生物反硝化过程、生物除磷过程可同时存在,在ASM3 Bio-P模型上添加相关的开关函数,推导出完全耦合活性污泥模型(FCASM).基于计算机程序进行数值模拟,并将FCASM模拟结果与实测值以及ASM3 Bio-P模型模拟值进行对比.结果表明,完全耦合活性污泥模型对氨氮模拟的稳态出水值为1.90 g·m-3,ASM3 Bio-P模型模拟的氨氮稳态出水值为0 g·m-3,而实测的氨氮稳态出水值为1.50 g·m-3,完全耦合活性污泥模型的结果更接近真实值.     

煤燃烧过程中有机钙固氟效果研究

选择醋酸钙镁、醋酸钙2种有机钙为固氟剂,在固定床管式炉上对它们的固氟效果进行了初步研究,并分析了粒径、温度、钙硫比等对试验结果的影响.通过与传统固氟剂碳酸钙的固氟效果进行比较发现:在相同实验条件下,这2种有机钙具有良好的固氟效果,高温阶段效果更加明显,温度为1 000～1 100℃时,醋酸钙镁的固氟率是碳酸钙的1.68～1.74倍,醋酸钙的固氟率为碳酸钙的1.28～1.37倍.     

Modeling thermal analysis for predicting thermal hazards relevant to transportation safety and runaway reaction for 2,2′-azobis(isobutyronitrile)

The pure decomposition behavior of 2,2′-azobis (isobutyronitrile) (AIBN) and its physical phase transformation were examined and discussed. The thermal decomposition of this self-reactive azo compound was explored using differential scanning calorimetry (DSC) to elucidate the stages in the progress of this chemical reaction. DSC was used to predict the kinetic and process safety parameters, such as self-accelerating decomposition temperature (SADT), time to maximum reaction rate under adiabatic conditions (TMR_ad), and apparent activation energy (E_a), under isothermal and adiabatic conditions with thermal analysis models. Moreover, vent sizing package 2 (VSP2) was applied to examine the runaway reaction combined with simulation and experiments for thermal hazard assessment of AIBN. A thorough understanding of this reaction process can identify AIBN as a hazardous and vulnerable chemical during upset situations. The sublimation and melting of AIBN near its apparent onset decomposition temperature contributed to the initial steps of the reaction and explained the exothermic attributes of the peaks observed in the calorimetric investigation.     

Effects of cultivation strategies on the cultivation of Chlorella sp. HQ in photoreactors

Heterotrophic cultivation caused high level of ROS and high lipids accumulation. HMTC is the best culture strategy for improving the microalgal biomass. Chlorella sp. HQ had great nutrient removal capacity under five culture strategies. The effects of cultivation strategies (including autotrophic cultivation (AC), heterotrophic cultivation (HC), fed-batch cultivation (FC), heterotrophic+ autotrophic two-stage cultivation (HATC), and heterotrophic+ mixotrophic two-stage cultivation (HMTC)) on the growth and lipid accumulation of Chlorella sp. HQ and its total nitrogen (TN) and total phosphorus (TP) removal in secondary effluent were investigated in column photoreactors. The results showed that the TN and TP removal rates ranged between 93.72%–95.82% and 92.73%–100%, respectively, under the five different strategies. The microalgal growth potential evaluated by the maximal growth rate (R_max) was in the order of HMTC>HC>FC>AC>HATC. The values of biomass, total lipid yield, triacylglycerols (TAGs) yield, and total lipid content of the microalga cultivated in the last 5 d increased significantly, but the TAGs productivities of the five strategies were lower than those in the first 7 d. Compared with all the other cultivation strategies, the TAGs productivity and yield after 12 d of cultivation under the heterotrophic condition reached the highest values accompanying the highest level of intracellular reactive oxygen species (ROS), in which the TAGs yield reached 40.81 mg/L at the end of the cultivation period. The peaks in TAGs yield and ROS level suggested that HC was beneficial for lipids accumulation via regulating the cellular redox status and exerting ROS stress on microalgal cells. In summary, HMTC was the best cultivation strategy for improving the microalgal biomass and HC was the best strategy for microalgal TAGs accumulation to produce biodiesel.     

Recovery of Ni(II) from real electroplating wastewater using fixed-bed resin adsorption and subsequent electrodeposition

Resin adsorption and subsequent electrodeposition were used for nickel recovery. Treated wastewater can meet the Electroplating Pollutant Discharge Standard. The spent resin is completely regenerated by 3 BV of 4% HCl solution. 95.6% of nickel in concentrated eluent was recovered by electrodeposition. Effective recovery of high-value heavy metals from electroplating wastewater is of great significance, but recovering nickel ions from real electroplating wastewater as nickel sheet has not been reported. In this study, the pilot-scale fixed-bed resin adsorption was conducted to recover Ni(II) ions from real nickel plating wastewater, and then the concentrated Ni(II) ions in the regenerated solution were reduced to nickel sheet via electrodeposition. A commercial cation-exchange resin was selected and the optimal resin adsorption and regeneration conditions were investigated. The resin exhibited an adsorption capacity of 63 mg/g for Ni(II) ions, and the average amount of treated water was 84.6 bed volumes (BV) in the pilot-scale experiments. After the adsorption by two ion-exchange resin columns in series and one chelating resin column, the concentrations of Ni(II) in the treated wastewater were below 0.1 mg/L. After the regeneration of the spent resin using 3 BV of 4% (w/w) HCl solution, 1.5 BV of concentrated neutral nickel solution (>30 g/L) was obtained and used in the subsequent electrodeposition process. Using the aeration method, alkali and water required in resin activation process were greatly reduced to 2 BV and 3 BV, respectively. Under the optimal electrodeposition conditions, 95.6% of Ni(II) in desorption eluent could be recovered as the elemental nickel on the cathode. The total treatment cost for the resin adsorption and regeneration as well as the electrodeposition was calculated.