炼钢厂炼焦车间土壤中PAHs的超临界流体萃取-色质联用分析方法研究

超临界流体萃取炼钢厂炼焦车间土壤中多环芳烃的最佳萃取条件为４０ＭＰａ，８０℃，０．５％甲醇动态改性液体ＣＯ２１０ｍＬ时，对土样进行超临界流体萃取，色质联用分析，并与索氏萃取法进行比较。土样中能准确定性的多环芳烃４４种，其中能定量分析的３１种。色谱定量的回收率均值为７８．５％￣１０４．１％，相对标准偏差为５．０％￣１５．６％。     

高级氧化技术在造纸废水处理中的研究进展

高级氧化技术是近几年很受关注的废水处理新技术，用其处理造纸废水的研究也在广泛展开。从这种技术的机理、研究现状及存在问题出发，阐述了这些新方法在造纸废水处理中的实验研究及应用的可能性。     

超临界流体萃取技术在环境样品前处理中的应用

综述了超临界流体萃取技术在环境样品前处理中的应用现状。重点介绍了对气体样品和固体样品中几种典型有机污染物的分离。     

水热氧化技术研究的进展

叙述水热氧化法的基本原理和研究进展，并重点介绍在高浓度乳化废水、含酚废水、含油污水和废碱液的处理中，最新试验研究以及它的优缺点和发展前景。     

超临界水氧化处理含油废水的实验研究

在间歇式超临界水氧化反应装置上进行含油废水的超临界水氧化实验研究,反应温度390～430℃、压力24～28MPa、反应时间30～90s。研究表明:超临界水氧化法是一种高效、快速的有机废弃物处理技术;随反应时间增加、温度升高,废水COD去除率显著增大;以幂函数方程描述了氧化剂过量时含油废水超临界水氧化的反应动力学规律,氧化反应对废水的反应级数为1级,在26MPa时,反应活化能和频率因子分别为(5896.83±243.68)J/mol和(0.0652±0.0028)s-1,模型计算值与实验值的误差为±13%。     

超临界锅炉过（再）热器氧化皮剥落分析

目前,我国新投产的火力发电机组容量大、参数高,超,瞄界和超超,瞄界机组已经成为我国的主力发电机组。随着机组参数的提高,锅炉过（再）热器管蒸汽侧氧化成为影响发电机组安全经济运行的主要因素之一。本文研究了超临界电站锅炉过（再）热器管氧化皮的形成原理和规律,分析了氧化皮的剥落模式及机理,探讨了氧化皮剥落的影响因素,并提出了控制氧化皮形成和剥落的对策,研究结果可对电厂氧化皮剥落问题提供指导作用。     

Decomposition reactions of epoxy resin and polyetheretherketone resin in sub- and supercritical water

Epoxy resin and polyetheretherketone (PEEK) resin were decomposed into their monomers such as phenol, cresols, and their analogues by thermal treatment in sub- and supercritical water in a 10-ml tubing bomb reactor. The addition of basic compounds such as Na₂CO₃ was effective in promoting the decomposition reaction of the resins. In the reaction of epoxy resin, the yield of identified products reached 10% for the reaction at 703K over 1h. In the reaction of PEEK resin, the total yield of phenol and dibenzofuran reached 88% for the reaction at 703K over 3h. Chemical participation of water in the decomposition reaction was confirmed by the reaction of dinaphthylether.     

氧芴在超临界乙醇中溶解度的实验研究

以乙醇为超临界溶剂,采用恒容加温法研究煤焦油洗油馏分中的氧芴在超临界乙醇中的溶解度。通过GC检测分析萃取余液的,结果表明在萃取温度为255℃、压力为7．0MPa时．氧芴在超临界乙醇中的溶解度达到0．01652g／mL,萃取效率达到106．5％,实验效果明显。研究得出,温度与压j々对于固体物质的超临界溶解度的具有明显的选择调节性．其中温度对于溶解度的影响较大。     

Coal energy conversion with carbon sequestration via combustion in supercritical saline aquifer water

The standard idea for deep saline aquifer sequestration is to separate carbon dioxide from a process stream, compress it, and inject it underground. However, since carbon dioxide is less dense than water, even at the high pressures found in aquifers, it is buoyant and will move towards the surface unless trapped by an impermeable seal. Also, significant energy expenditure is required to separate and compress carbon dioxide, even though neat carbon dioxide is not a desired product. These issues may be addressed by combining the idea of fast dissolution at the surface with supercritical water oxidation (SCWO). By burning coal at high pressure in supercritical water drawn from an aquifer, and then sequestering the entire pre-equilibrated effluent, all carbon from the fuel is captured, as well as all non-mineral coal combustion products including sulfur and metals.A possible block diagram of an SCWO-based electric power plant is proposed, including processes to handle salts from the aquifer brine and minerals from coal. The plant is thermodynamically modeled, using an indirectly fired combined cycle to convert energy from hot combustion products to work. This model estimates the overall thermal efficiency that can be achieved, and reveals unanticipated interactions within the plant that have significant effects on efficiency. The assumptions and results of the model highlight design challenges for an actual system.     

Investigating differential binding of polychlorinated dibenzo-p-dioxins/dibenzofurans in soil and soil components using selective supercritical fluid extraction

Supercritical fluid extraction (SFE) with pure carbon dioxide was performed at increasingly strong conditions to investigate differential binding of polychlorinated dibenzo-p-dioxins/dibenzofurans (PCDD/Fs) in two impacted soils, in their sieved size fractions, and in small (a few mg) samples of industry-related waste products separated from impacted soil. The binding strengths of PCDD/Fs were shown to be different in the two soils, and in their different soil particle size fractions. As might be expected based on surface area considerations, one soil showed the strongest binding in the smallest (<5 μm) sieved fraction. However, the other soil showed the strongest binding in the larger sized fractions, possibly indicating that process-related particles could be controlling PCDD/F binding. Selective SFE of various types of particles including black carbon and charcoal (separated from soil), and from a suspected process anode residue did show different PCDD/F binding behavior ranging from quite weak binding (charcoal) to very strong binding (anode particles). Shifts to the stronger SFE fractions in the soils after activated carbon treatment agreed well with the decreases previously found in the uptake of PCDD/Fs by earthworms, as well as decreases in their freely-dissolved aqueous concentrations in soil/water slurries. These results show that, as previously demonstrated for PAHs and PCBs, selective SFE can be a useful tool to investigate differences in PCDD/F binding behaviors in impacted soils and sediments and their component parts, as well as a rapid tool for estimating the effectiveness of activated carbon treatments on decreasing the bioavailability of PCDD/Fs in soils and sediments.