Recycling process for yttria-stabilized tetragonal zirconia ceramics using a hydrothermal treatment

The recycling process for 3 mol% yttria-stabilized tetragonal zirconia polycrystals (3Y-TZP) sintered at 1450°–1550°C was examined by applying low-temperature degradation of zirconia ceramics under hydrothermal conditions. Hydrothermal treatment at a temperature from 200° to 240°C can lead to the spontaneous disintegration of 3Y-TZP sintered bodies into powdery particles. The hydrothermally obtained zirconia powder was found to consist of primary particles and aggregated particles. Detailed X-ray diffraction measurement revealed the formation of a cubic zirconia phase in the 3Y-TZP sintered bodies, which seemed to inhibit the disintegration of aggregated particles toward the primary particle level. The reclaimed 3Y-TZP powder was sintered again through a conventional powder processing route. The mechanical properties and microstructure of recycled 3Y-TZP sintered specimens were examined by comparison with those of the original 3Y-TZP sintered bodies. Dense recycled 3Y-TZP sintered at a higher temperature exhibited higher fracture toughness to some degree than the original 3Y-TZP.     

电解法处理采油废水的研究

以提高电解处理工艺的效率、降低处理成本、易于实现工业化为目标,筛选出适合处理采油废水的高效电极材料,考察了电解法处理采油废水的各种影响因素,确定实验室电解氧化法处理采油废水的适宜条件.研究结果表明:以析氯阳极 铁阴极作为试验电极材料,在电流密度为15 mA/cm2,电解时间为80min,水板比约0.10 cm2/cm3,弱碱性,极板间距为10mm的条件下对采油废水进行电解处理,COD去除率可达到73.0%,NH3-N去除率可达到98.5%.     

湿热处理技术工艺发展现状与趋势展望

湿热处理技术近年来在国内外受到广泛的关注,此项技术主要应用于淀粉、餐厨垃圾的湿热水解均质化处理等方面.对此,研究人员开展了大量的研究工作,研究内容涉及湿热处理工艺影响因素研究、湿热处理工艺条件优化分析、湿热处理工艺对底物结构与性质的影响.总结前人的研究成果,沉淀目前湿热处理工艺成果应用与成果转化相关信息,并对湿热处理工艺的潜在应用领域做出初步展望.     

Noncatalytic liquefaction of tar with low-temperature hydrothermal treatment

Water at hydrothermal and supercritical conditions is considered a promising solvent for the degradation of hazardous waste into harmless compounds. Tar liquefaction experiments were conducted using a batch-type reactor at temperatures between 623 K and 673 K and at pressures between 25 and 40 MPa. A reaction mechanism for tar liquefaction is proposed. Moreover, on the basis of the experimental results, this method could become an efficient method for tar liquefaction, producing high yields of valuable chemical intermediates.     

臭氧氧化-三维电极电解联用技术深度处理造纸废水

采用臭氧氧化-三维电极电解联用技术深度处理造纸废水,通过单因素及正交实验法确定了最优工艺条件,并探讨了反应的动力学和机理。实验结果表明:废水处理的最优工艺条件为电极间距1.5 cm、电流密度9mA/cm~2、臭氧曝气量15 mL/min、活性炭填充量22 g/L、反应时间60 min,该工艺条件下,废水的COD去除率达93.70%;臭氧氧化-三维电极电解联用技术对废水中COD的去除过程符合一级反应动力学方程;臭氧氧化和三维电极电解间存在协同效应。     

The mild hydrothermal synthesis of hydrogrossular from coal ash

In this study, an attempt was made to synthesize hydrogrossular, a group of garnet minerals, under hydrothermal conditions at temperatures below 180°C, using coal ash, which is the solid waste from thermal power plants, as a starting material. A single phase corresponding to hydrogrossular was found at around 120°C, and the hydrogrossular coexisted with 11-Å tobermorite above 140°C. The hydrogrossular phase decreased with increasing reaction temperature, while that of 11-Å tobermorite increased concurrently. The physicochemical properties of the hydrogrossular obtained from the hydrothermal synthesis was characterized by X-ray diffraction thermogravimetry/differential thermal, analysis, scanning electron microscopy, Fourier transform infrared spectroscopy, and X-ray fluorescence spectroscopy. Received: September 4, 2000 / Accepted: March 7, 2001     

Using liquid waste streams as the moisture source during the hydrothermal carbonization of municipal solid wastes

Hydrothermal carbonization (HTC) is a thermal conversion process that can be an environmentally beneficial approach for the conversion of municipal solid wastes to value-added products. The influence of using activated sludge and landfill leachate as initial moisture sources during the carbonization of paper, food waste and yard waste over time at 250 °C was evaluated. Results from batch experiments indicate that the use of activated sludge and landfill leachate are acceptable alternative supplemental liquid sources, ultimately imparting minimal impact on carbonization product characteristics and yields. Regression results indicate that the initial carbon content of the feedstock is more influential than any of the characteristics of the initial liquid source and is statistically significant when describing the relationship associated with all evaluated carbonization products. Initial liquid-phase characteristics are only statistically significant when describing the solids energy content and the mass of carbon in the gas-phase. The use of these alternative liquid sources has the potential to greatly increase the sustainability of the carbonization process. A life cycle assessment is required to quantify the benefits associated with using these alternative liquid sources.     

Recovery of solid fuel from municipal solid waste by hydrothermal treatment using subcritical water

Hydrothermal treatments using subcritical water (HTSW) such as that at 234 °C and 3 MPa (LT condition) and 295 °C and 8 MPa (HT condition) were investigated to recover solid fuel from municipal solid waste (MSW). Printing paper, dog food (DF), wooden chopsticks, and mixed plastic film and sheets of polyethylene, polypropylene, and polystyrene were prepared as model MSW components, in which polyvinylchloride (PVC) powder and sodium chloride were used to simulate Cl sources.While more than 75% of carbon in paper, DF, and wood was recovered as char under both LT and HT conditions, plastics did not degrade under either LT or HT conditions. The heating value (HV) of obtained char was 13,886-27,544 kJ/kg and was comparable to that of brown coal and lignite. Higher formation of fixed carbon and greater oxygen dissociation during HTSW were thought to improve the HV of char.Cl atoms added as PVC powder and sodium chloride to raw material remained in char after HTSW. However, most Cl originating from PVC was found to converse into soluble Cl compounds during HTSW under the HT condition and could be removed by washing.From these results, the merit of HTSW as a method of recovering solid fuel from MSW is considered to produce char with minimal carbon loss without a drying process prior to HTSW. In addition, Cl originating from PVC decomposes into soluble Cl compound under the HT condition. The combination of HTSW under the HT condition and char washing might improve the quality of char as alternative fuel.     

Simultaneous determination of volatile and semivolatile organic compounds in soil

A microscale solvent extraction (MSE) method was developed for the simultaneous determination of volatile organic compounds (VOCs) and semivolatile organic compounds (SVOCs) in soil. Tests of precision, recovery, and comparability to other Environmental Protection Agency (EPA) methods have been completed, and the MSE method compares well to Soxhlet and sonication extraction. Based on these validation data, EPA has assigned number 3570 to this method. Method 3570 has several advantages, including reduced use of solvent and soil sample, generating much less laboratory waste. Laboratory space and labor requirements are reduced as compared to many other sample preparation methods. Consequently, Method 3570 can provide comparable chemical data at less cost or environmental impact.     

工业挥发性有机物处理技术分析与展望

挥发性有机物(VOCs)是大气污染物的主要来源之一。对现有工业VOCs处理技术进行了归类及概述,总结了各类技术中主要方法的工作原理、技术特点、适用范围和应用现状,包括吸收法、吸附法、膜分离法、冷凝法等回收技术,热氧化(燃烧)法、生物降解法、低温等离子法、光催化法等非回收消除技术,以及工业上典型的VOCs集成组合治理技术。指出,集成组合治理技术的研发是该领域未来的发展方向。     

真空紫外光对含氧挥发性有机物的矿化效果

以醛类、醚类和酯类化合物作为目标污染物,考察了真空紫外光解法对含氧挥发性有机物（OVOCs）的矿化效果。实验结果表明,几种OVOCs在真空紫外光照射下都能达到90%以上的矿化率,且OVOCs的物质结构越简单,官能团的反应活性越强,越容易被矿化。直链结构比环状结构OVOCs的矿化效果更好,且分子链越短矿化速率越快;具有五元环结构的OVOCs比具有六元环结构的反应速率更快;官能团的键能越弱,反应活性越强,越容易被矿化。     

Field application of reactive iron walls for in-situ degradation of volatile organic compounds in groundwater

Reactive walls containing metallic iron have been installed at several commercial sites in the United States to degrade chlorinated organic compounds in groundwater. Although the results of laboratory studies conducted to determine reaction mechanisms have been widely disseminated, little information has been published on the full-scale application of this technology. This article describes the construction, implementation, and cost of in-situ reactive walls at three commercial sites.     

Kinetics of biological methane oxidation in the presence of non-methane organic compounds in landfill bio-covers

In this experimental program, the effects of non-methane organic compounds (NMOCs) on the biological methane (CH₄) oxidation process were examined. The investigation was performed on compost experiments incubated with CH₄ and selected NMOCs under different environmental conditions. The selected NMOCs had different concentrations and their effects were tested as single compounds and mixtures of compounds. The results from all experimental sets showed a decrease in CH₄ oxidation capacity of the landfill bio-cover with the increase in NMOCs concentrations. For example, in the experiment using compost with 100% moisture content at 35 °C without any NMOCs the V_max value was 35.0 μg ${\text{CH}}_4{\text{h}}^{-1}{\text{g}}_{\text{wet wt}}^{-1}$. This value was reduced to 19.1 μg ${\text{CH}}_4{\text{h}}^{-1}{\text{g}}_{\text{wet wt}}^{-1}$ when mixed NMOCs were present in the batch reactors under the same environmental conditions. The experimental oxidation rates of CH₄ in the presence of single and mixed NMOCs were modeled using the uncompetitive inhibition model and kinetic parameters, including the dissociation constants, were obtained. Additionally, the degradation rates of the NMOCs and co-metabolic abilities of methanotrophic bacteria were estimated.     

Atmospheric emissions and attenuation of non-methane organic compounds in cover soils at a French landfill

In addition to methane (CH(4)) and carbon dioxide (CO(2)), landfill gas may contain more than 200 non-methane organic compounds (NMOCs) including C(2+)-alkanes, aromatics, and halogenated hydrocarbons. Although the trace components make up less than 1% v/v of typical landfill gas, they may exert a disproportionate environmental burden. The objective of this work was to study the dynamics of CH(4) and NMOCs in the landfill cover soils overlying two types of gas collection systems: a conventional gas collection system with vertical wells and an innovative horizontal gas collection layer consisting of permeable gravel with a geomembrane above it. The 47 NMOCs quantified in the landfill gas samples included primarily alkanes (C(2)-C(10)), alkenes (C(2)-C(4)), halogenated hydrocarbons (including (hydro)chlorofluorocarbons ((H)CFCs)), and aromatic hydrocarbons (BTEXs). In general, both CH(4) and NMOC fluxes were all very small with positive and negative fluxes. The highest percentages of positive fluxes in this study (considering all quantified species) were observed at the hotspots, located mainly along cell perimeters of the conventional cell. The capacity of the cover soil for NMOC oxidation was investigated in microcosms incubated with CH(4) and oxygen (O(2)). The cover soil showed a relatively high capacity for CH(4) oxidation and simultaneous co-oxidation of the halogenated aliphatic compounds, especially at the conventional cell. Fully substituted carbons (TeCM, PCE, CFC-11, CFC-12, CFC-113, HFC-134a, and HCFC-141b) were not degraded in the presence of CH(4) and O(2). Benzene and toluene were also degraded with relative high rates. This study demonstrates that landfill soil covers show a significant potential for CH(4) oxidation and co-oxidation of NMOCs.     

Hydrothermal carbonization of food waste and associated packaging materials for energy source generation

Hydrothermal carbonization (HTC) is a thermal conversion technique that converts food wastes and associated packaging materials to a valuable, energy-rich resource. Food waste collected from local restaurants was carbonized over time at different temperatures (225, 250 and 275 °C) and solids concentrations to determine how process conditions influence carbonization product properties and composition. Experiments were also conducted to determine the influence of packaging material on food waste carbonization. Results indicate the majority of initial carbon remains integrated within the solid-phase at the solids concentrations and reaction temperatures evaluated. Initial solids concentration influences carbon distribution because of increased compound solubilization, while changes in reaction temperature imparted little change on carbon distribution. The presence of packaging materials significantly influences the energy content of the recovered solids. As the proportion of packaging materials increase, the energy content of recovered solids decreases because of the low energetic retention associated with the packaging materials. HTC results in net positive energy balances at all conditions, except at a 5% (dry wt.) solids concentration. Carbonization of food waste and associated packaging materials also results in net positive balances, but energy needs for solids post-processing are significant. Advantages associated with carbonization are not fully realized when only evaluating process energetics. A more detailed life cycle assessment is needed for a more complete comparison of processes.     

Influences of chlorine content on emission of HCl and organic compounds in waste incineration using fluidized beds

HCl and some organic compounds are the precursors of polychlorinated dibenzo-p-dioxins and furans (PCDD/Fs) in municipal solid waste incinerators. In this work, a lab-scale fluidized bed incinerator is adopted to study the relationship between the organic and the inorganic chlorine contents of artificial wastes and the emissions of HCl and organic compounds. The lower threshold limit (LTL) of chlorine content below which HCl and organic compounds are not generated is studied. Experimental results showed that organic chlorides had a greater potential to release chlorine than inorganic chlorides. The generation of organic pollutants fell, but the emissions of HCl increased with the temperature. The concentrations of chlorophenols (CPs)/chlorobenzenes (CBs) increased with chlorine contents. No LTL existed for HCl regardless of whether CaO was added. The LTL for CPs was between 0.1 and 0.3wt% of inorganic chloride, but there was none for organic sources. For CBs, the LTL was between 0.5 and 1.0wt% for inorganics at 700 and 800 degrees C, but 0.1-0.3 wt% at 700 degrees C and 0.3-0.5 wt% at 800 degrees C for organics. The production of PAHs and benzene, toluene, ethylbenzene and xylene (BTEX) was related to the surplus hydrogen ions that were not reacted with the chlorine. Adding CaO inhibited the production of HCl, CBs and CPs, but did not seriously affect PAHs and BTEX.     

Photocatalytic degradation of organic pollution by converter dust under visible light: optimization and mechanism

Journal of Material Cycles and Waste Management - Photocatalytic decoloration pollutants using semiconducting materials have grabbed great attention in recent years. Herein, the Methylene Blue (MB)...