UV/H2O2/Fe-FeOxH2x-3和UV/H2O2工艺降解水中富里酸的研究

采用硼氢化钠还原法制备核-壳结构的Fe-FeO_xH_2x-3复合材料，研究了富里酸在UV/H₂O₂和UV/H₂O₂/Fe-FeO_xH_2x-3两种不同反应体系下的降解情况。结果表明，核-壳结构Fe-FeO_xH_2x-3的存在，提高了UV/H₂O₂降解富里酸的反应速率，TOC去除达到84%。采用XAD树脂吸附法对反应前后的富里酸进行化学分级表征，结果表明，富里酸经反应后憎水酸（HoA）、弱憎水酸（WHoA）和憎水中性物质（HoN）都有所减少，进而转化为亲水性物质（HiM）；用超滤膜法对富里酸进行物理分级表征，考察了富里酸在反应前后分子量分布的变化情况。同时，富里酸经过反应后生成的中间产物降低了三氯甲烷生成趋势。     

O3、H2O2/O3及UV/O3在焦化废水深度处理中的应用

采用O₃、H₂O₂/O₃和UV/O₃等高级氧化技术(AOPs)对某焦化公司的生化出水进行深度处理，考察了O₃与废水的接触时间、溶液pH、反应温度等因素对废水COD去除率的影响，确定出O₃氧化反应的最佳工艺参数为：接触时间40 min，溶液pH 8.5，反应温度25℃，此条件下废水COD及UV₂₅₄的去除率最高可达47.14%和73.47%；H₂O₂/O₃及UV/O₃两种组合工艺对焦化废水COD及UV₂₅₄的去除率均有一定程度的提高，但H₂O₂/O₃系统的运行效果取决于H₂O₂的投加量。研究结论表明，单纯采用COD作为评价指标，并不能准确反映出O₃系列AOPs对焦化废水中有机污染物的降解作用。     

超临界CO2回收线路板工艺研究

采用正交试验设计进行了超临界CO₂回收废弃印刷线路板的实验。以温度、压强、时间和夹带剂为实验因素，通过对实验前后样本在重量、厚度、弯曲强度和断裂强度四方面变化的分析考察了各实验因素对实验效果的影响。实验结果表明，影响超临界CO₂法回收印刷线路板的最主要因素为温度、时间和夹带剂，超临界CO₂法回收废弃印刷线路板的最佳工艺条件：温度270℃，压强大于7.38 MPa，时间3 h，夹带剂(水)160 mL。实验进一步验证了压强对实验结果的非显著性影响。     

水体中常见无机阴离子对TiO2薄膜光催化降解甲醛的影响

选择了5种水体中常见的阴离子(Cl^-，SO^2-₄，HPO^2-₄/HPO^2-₄，HCO^-₃/CO^2-₃和NO^-₃)，分别考查了其对TiO₂薄膜光催化降解模拟甲醛废水的反应速率的影响；从上述离子的光吸收，对·OH的捕获及其生成的相应的无机自由基的氧化作用以及与甲醛的竞争吸附3个方面讨论了上述离子影响TiO₂薄膜光催化降解模拟甲醛废水的反应速率的原因。结果表明，HCO^-₃/CO^2-₃对TiO₂薄膜光催化降解甲醛具有抑制作用，Cl^-和SO^2-₄的影响不大，H₂PO^-₄/HPO^2-₄和NO^-₃具有促进作用。造成上述结果的主要原因是HCO^-₃/CO^2-₃具有很强的·OH捕获作用；Cl^-，SO^2-₄对·OH捕获作用以及竞争吸附都较弱；H₂PO^-₄/HPO^2-₄在TiO₂表面具有较强的吸附能力，释放出的H⁺起到了酸催化剂的作用；NO^-₃在紫外光的照射下可以产生·OH，此外NO^-₃作为电子受体而降低了TiO₂表面光生电子和空穴的复合几率。     

金属改性碳脱除PH3和H2S动力学及反应机理研究

为综合利用黄磷尾气中的CO，通过计算平均活化能和测定XPS、TG/DTA和氮吸附特性的方法，研究了Cu²⁺和某金属离子Mn⁺改性碳脱除PH₃和H₂S的动力学和反应机理问题。结果表明：H₂S在金属改性碳上反应时平均活化能为134.4 J/mol为-0.76级反应，PH₃在金属改性碳上反应时平均活化能为1 247.6 J/mol为-0.8级反应；减小改性碳粒径增加流量可以显著提高其脱除PH₃和H₂S的速率；XPS、TG/DTA和孔径分布分析证明，改性碳净化H₂S和PH₃是一个催化吸附过程，H₂S和PH₃首先与氧在改性碳表面进行催化氧化反应，然后生成S和P₂O₅沉积吸附在改性碳表面。     

双频超声辐射协同H2O2降解偶氮染料废水的研究

采用双频超声协同H₂O₂降解酸性绿20染料废水，考察超声功率密度、染料初始浓度和pH、饱和气体及H₂O₂投加量等因素对酸性绿20降解效果的影响，结果表明，在给定实验条件下，双频降解效果优于单频超声波，且降解率随超声功率密度的增大而增大。酸性条件有利于酸性绿20的降解，当染料废水初始pH=4可取得最佳的降解效果；酸性绿20的降解效率随染料初始浓度的增大而降低，其优化初始浓度为40 mg/L。在反应体系中通入空气并投加H₂O₂，可取得最佳的降解效果。在优化实验条件下， 采用双频超声协同H₂O₂降解5 h，酸性绿20的色度和TOC去除率分别为94.6%和36.3%；分析降解前后的紫外可见光谱图可知，酸性绿20并非完全被降解为CO₂和H₂O，而是生成一些小分子有机中间体。     

O3/H2O2降解阿特拉津影响因素研究

采用O3/H2O2氧化去除水中内分泌干扰物阿特拉津，考察了反应条件及水质对去除的影响，并对反应机制进行了初步探讨。阿特拉津初始浓度2 mg/L，投量为7.5 mg/L的O₃单独氧化去除率为27.2%；相同O₃投量下，控制H₂O₂/O₃摩尔比为0.75，5 min阿特拉津的去除率最高可达96.5%；pH 值为7.5～8.5，温度在25～40℃的范围内，都维持了较高的去除率，表明H₂O₂/O₃体系对阿特拉津的去除效果良好，降解速度快，反应条件温和。0.5 mg/L的腐殖酸，对阿特拉津的去除影响不大，腐殖酸浓度为1、2和5 mg/L时，平均去除率分别为63.4%、50.7%和30.2%；碳酸氢钠的浓度为50和200 mg/L时，去除率分别为88.1%和73.8%，说明水质对阿特拉津的去除影响较大。叔丁醇的浓度为5和20 mg/L时，阿特拉津的去除率分别降低到44.7%和27.5%，去除率随自由基抑制剂叔丁醇增加而降低，说明H₂O₂/O₃降解阿特拉津主要为该体系产生的羟基自由基的贡献。     

光助Ce-Fe/Al2O3催化H2O2降解阳离子红GTL模拟废水

利用Ce-Fe/Al₂O₃为催化剂的非均相光Fenton体系降解阳离子红GTL模拟废水，考察了H₂O₂浓度、催化剂用量、初始pH值及不同工艺过程对降解效果的影响，通过紫外-可见漫反射光谱、红外光谱、XPS手段研究铁在反应中的价态变化。结果表明，在11 W低压汞灯照射下，非均相光Fenton体系能够有效地降解结构稳定的阳离子红GTL，在pH 6，反应温度20℃，时间90 min，Ce-Fe/Al₂O₃ 2 g/L，H₂O₂浓度340 mg/L，含50 mg/L阳离子红GTL模拟废水TOC去除率为92.40%；光Fenton反应中Fe(Ⅲ)转化为Fe(Ⅱ)。     

La2O3/ZnO/TiO2光催化降解活性艳红K-2BP的研究

采用溶胶-凝胶法制备了La₂O₃/ZnO/TiO₂复合光催化剂,以紫外灯为光源,活性艳红K-2BP为模型降解物,研究了La₂O₃/ZnO/TiO₂的光催化性能。结果表明：当锌和镧的掺杂量w(ZnO)=20%, w(La₂O₃)=0.5%, 煅烧温度为500℃时,La₂O₃/ZnO/TiO₂复合光催化剂的光催化活性最高；当催化剂投加量4 g/L,通气量800 mL/min,初始pH值3.12时,La₂O₃/ZnO/TiO₂对活性艳红K-2BP的降解效果最好。实验证明,La₂O₃/ZnO/TiO₂对活性艳红K-2BP的降解遵从Langmuir-Hinshelwood动力学模型,测得其反应速率常数k＝11.5 mg/(L·min)；吸附常数K＝2.88×10^-2 L/mg。     

用H2O2/Fe3+处理高浓度含甲醛废水的研究

研究采用H₂O₂/Fe³⁺催化氧化处理高浓度含甲醛废水，探讨了双氧水和催化剂投加量、反应pH及反应温度等操作条件对处理效果的影响，并通过酸溶解回用失活催化剂。结果表明，较优的操作条件为：H₂O₂/COD（质量比）=2.2～2.6，Fe³⁺/H₂O₂（摩尔比）=0.048～0.058，反应pH 1.80～2.68，反应温度50℃，反应时间40 min；在上述操作条件下，甲醛去除率达到99%以上，COD去除率达到85%以上。失活的催化剂可通过稀酸溶解后循环使用，其效果与三价铁盐作催化剂的基本相同。采用H₂O₂/Fe³⁺处理含甲醛废水具有比采用H₂O₂/Fe³⁺较优的效果。     

Non-controlled biogenic emissions to the atmosphere from Lazareto landfill, Tenerife, Canary Islands

GOAL, SCOPE AND BACKGROUND: [corrected] Historically, landfills have been the simplest form of eliminating urban solid waste with the minimum cost. They have been the most usual method for discarding solid waste. However, landfills are considered authentic biochemical reactors that introduce large amounts of contaminants into the environment in the form of gas and leachates. The dynamics of generation and the movement of gas in landfills depend on the input and output parameters, as well as on the structure of the landfill and the kind of waste. The input parameters include water introduced through natural or artificial processes, the characteristics of the urban solid waste, and the input of atmospheric air. The main output parameters for these biochemical reactors include the gases and the leachates that are potentially pollutants for the environment. Control systems are designed and installed to minimize the impact on the environment. However, these systems are not perfect and a significant amount of landfill gas could be released to the atmosphere through the surface in a diffuse form, also known as Non-controlled emission. In this paper, the results of the Non-controlled biogenic gas emissions from the Lazareto landfill in Tenerife, Canary Islands, are presented. The purpose of this study was to evaluate the concentration of CH4 and CO2 in the soil gas of the landfill cover, the CH4 and CO2 efflux from the surface of the landfill and, finally, to compare these parameters with other similar landfills. In this way, a better understanding of the process that controls biogenic gas emissions in landfills is expected. METHODS: A Non-controlled biogenic gas emission survey of 281 sampling sites was carried out during February and March, 2002. The sampling sites were selected in order to obtain a well-distributed sampling grid. Surface landfill CO2 efflux measurements were carried out at each sampling site on the surface landfill together with soil gas collection and ground temperatures at a depth of 30-40 cm.The CH4 efflux was computed from CO2 efflux and from the ratio CH4/CO2 in the soil gas. Soil gas samples were collected at a depth of 30-40 cm using a metallic probe and 20 cc hypodermic syringes, and later stored in evacuated 10 cc vacutainers for laboratory analysis of bulk composition. The gas sample was introduced in a vacutainer filled with deionized water and displacing the water until the vacutainer was filled with the gas sample in order to avoid air contamination from entering. The surface landfill temperature of the landfill was measured at a depth of 40 cm using a digital thermometer type OMEGA 871A. Landfill gases, CO2 and CH4, were analyzed within 24 hours using a double channel VARIAN micro-GC QUAD CP-2002P, with a 10 meter PORAPLOT-Q column, a TCD detector, and He as a carrier gas. The analysis temperature was 40 degrees C and the injection time was 10 msec. Surface landfill CO2 efflux measurements were performed using a portable NDIR spectrophotometer Licor-800 according to the accumulation chamber method (Chiodini et al. 1996). The data treatment, aimed at drawing the flux map and computing the total gas output, was based on the application of stochastic simulation algorithms provided by the GSLIB program (Deutsch and Journel 1998). RESULTS: Diffuse CH4 and CO2 efflux values range from negligible values up to 7,148 and 30,573 g m(-2) d(-1), respectively. The spatial distribution of the concentration and efflux of CO2, CH4 and soil temperature, show three areas of maximum activity in the landfill, suggesting a non-uniform pattern of diffuse degassing. This correlation between high emissions and concentration of CO2, CH4 and soil temperatures suggests that the areas of higher microbial activity and exothermic reactions are releasing CO2 and CH4 to the atmosphere from the landfill. Taking into consideration the spatial distribution of the CO2 and CH4 efflux values as well as the extension of the landfill, the Non-controlled emission of CO2 and CH4 to the atmosphere by the Lazareto's landfill are of 167 +/- 13.3 and 16 +/- 2.5 t d(-1), respectively. DISCUSSION: The patterns of gas flow within the landfill seem to be affected by boundary materials at the sides. The basalt layers have a low permeability and the gas flow in these areas is extensive. In this area, where a basalt layer does not exist, the flow gas diffuses toward the sea and the flux emissions at the landfill surface are lower. This behavior reflects the possible dissolution of gases into water and the deflection of gases towards the surface at the basalt boundary. The proximity to the sea, the installation of a palm tree garden and, as a result, the contribution of water coming from the watering of this garden has reactivated the system. The introduction of sea water into the landfill and the type of boundary could be defining the superficial gas discharges. CONCLUSIONS: Results from this study indicate that the spatial distribution of Non-controlled emission of CO2 and CH4 at the Lazareto's landfill shows a non-uniform pattern of diffuse degassing. The northeast, central and northwest areas of the Lazareto's landfill are the three areas of high emissions and concentration of CO2 and CH4, and high temperatures. The correlation between high emissions and the concentration of CO2, CH4, and the high temperatures suggest that the areas of higher microbial activity and exothermic reactions are releasing more CO2 and CH4 to the atmosphere from the landfill. A high concentration of CO2 is probably due to the presence of methanotrophic bacteria in the soil atmosphere of the landfill. Patterns of gas flow within the landfill seem to be affected by boundary materials (basalt layers) of low permeability, and side boundaries of the flux emissions at the surface are higher. At the sides of seawater and sediment boundaries, flux emissions at the landfill surface are lower. This behavior reflects a possible dissolution of gases into the water and the deflection of gases towards the surface at the basalt boundary. With this study, we can compare the data obtained in this landfill with other landfills and observe the different levels of emission. The proximity to the sea and the installation of the palm tree garden palms and, as a result, the contribution of water coming from the watering of this garden has reactivated the system. Many landfills worldwide located in similar settings could experience similar gas production processes. RECOMMENDATIONS AND PERSPECTIVES: The need for investigating and monitoring sea water and sediment quality in these landfills is advisable. Concentrations and fluxes of contaminants and their impact in the area should be assessed. With this study we can compare the data obtained in these landfills with other landfills and observe the different levels of emission.     

Relationship between carbon dioxide/methane emissions and the water quality/sediment characteristics of Taiwan's main rivers

River and sediment have unique carbon dynamics and are important sources of the dominant greenhouse gases (GHG), carbon dioxide (CO2) and methane (CH4). To understand the relationship between CO2/CH4 emissions and water quality/sediment characteristics, we have investigated critical parameters in the river water. Eight parameters of water quality (dissolved oxygen, oxidation-reduction potential [ORP], chemical oxygen demand, biochemical oxygen demand [BOD5], suspended solid, nitrate [NO3-], NH4+, and bacteria) and four sediment characteristics (total organic carbon [TOC], total nitrogen [T-N], NO3-, and ammonium [NH4+]) were measured in two of the larger rivers in Taiwan, and relevant environmental conditions were recorded. The experimental results indicated that CO2 emissions from the river were mainly affected by BOD5 concentrations and the levels of bacteria. CH4 emissions, on the other hand, were greatly affected by the ORP in the river. The correlation between CO2 emissions and sediment characteristics was insignificant (R2 < 0.3). However, TOC and T-N in the sediment may lead to increases in CH4 emissions into the atmosphere. A deeper analysis of the relationship between the different parameters and GHG emissions by ANOVA and the multiple regression method revealed that CO2 emission (y) was significantly related to bacteria number (x1) and BOD concentration (X2). The regression equation takes the form y = 0.00032x1 + 3.18089x2 + 25.37304. Also, the regression relationship between CH4 emission (y) and ORP (x) in the river can be described as y = -0.825216x + 169.02257. The relationship between CH4 emission and sediment characteristics may be described as y = 5.073962x1(TOC) + 2.871245x2(T-N) - 12.3262. Extra sampling data were collected to examine the feasibility of the developed multiple regression equations. The experimental results suggest that the emissions of such GHGs as CO2 and CH4 from rivers can be predicted using the regression equations developed here. Moreover, the emissions may be reduced by manipulating the proper factors.     

Impact of urbanization on hydrochemical evolution of groundwater and on unsaturated-zone gas composition in the coastal city of Tel Aviv, Israel

The coastal city of Tel Aviv was founded at the beginning of the 20th century. The number of its inhabitants and its water consumption increased rapidly. This study analyses a 15-year record (1934-1948) of pre-industrial development of groundwater chemistry in the urban area. Archive data on concentrations of major ions, dissolved gases (CO2 and O2), organic matter, and pH were available for each half-year during the period of 1934-1948. The major factors causing changes in the chemistry of groundwater flowing in three sandy sub-aquifers have been seawater encroachment due to overpumping, and infiltration of effluents from pit-latrine collectors. Influence of these factors decreases with depth. Landward-penetrating seawater passed through clayey coastal sediments, interbedded among sands and calcareous sandstones, and spread into the Kurkar Group aquifer. This has led to exchange of sodium (dominant in seawater) with calcium adsorbed on clay particles, enriching groundwater with calcium. Intensity of cation exchange decreases inland and with depth. Infiltration of pit-latrine effluents has introduced large amounts of ammonium into the unsaturated zone. Its rapid oxidation in unsaturated sediments has caused massive nitrate production, accompanied by pore-water acidification. This process induces dissolution of vadose carbonate, resulting in enrichment of groundwater recharge in calcium. Anthropogenically induced dissolution of calcite in the unsaturated zone has been the major factor for the increase of Ca2+ concentration in groundwater, accounting for about 80% of this increase. In the interface zone, an additional 20% of calcium has been supplied by cation exchange. Owing to pH increase caused by denitrification in the aquifer, Ca(2+)-rich waters supersaturated with calcite could be formed, especially in the capillary fringe of the uppermost sub-aquifer, which could induce calcite precipitation and ultimately lead to the cementation of sandy aquifers. Urban development has caused drastic changes in the gas content in the unsaturated zone and in groundwater. Carbon dioxide was intensively generated by nitrification-denitrification processes, by hydration of urea, to a lesser degree by oxidation of organic matter, and probably by anoxic biodegradation of organics. Between 1934 and 1948, concentrations of CO2 in unsaturated sediment air rose from 3.2% to 7.6%. In the unsaturated zone, oxygen consumption for oxidation of ammonium and organic matter lowered O2 concentrations in sediment air to unusually low values of 3.9-12.9%. Nitrification in the urban unsaturated zone could thus serve as a pump, sucking in atmospheric oxygen at a rate of about 0.3-0.5 g m-2 day-1. The extreme concentrations of CO2 and O2 in unsaturated sediments have been preserved due to production and consumption of gas under conditions of diminishing areas open to the atmosphere, uncovered by buildings and by roads.     

Effects of water vapor pretreatment time and reaction temperature on CO(2) capture characteristics of a sodium-based solid sorbent in a bubbling fluidized-bed reactor

CO(2) capture from flue gas using a sodium-based solid sorbent was investigated in a bubbling fluidized-bed reactor. Carbonation and regeneration temperature on CO(2) removal was determined. The extent of the chemical reactivity after carbonation or regeneration was characterized via (13)C NMR. In addition, the physical properties of the sorbent such as pore size, pore volume, and surface area after carbonation or regeneration were measured by gas adsorption method (BET). With water vapor pretreatment, near complete CO(2) removal was initially achieved and maintained for about 1-2min at 50 degrees C with 2s gas residence time, while without proper water vapor pretreatment CO(2) removal abruptly decreased from the beginning. Carbonation was effective at the lower temperature over the 50-70 degrees C temperature range, while regeneration more effective at the higher temperature over the 135-300 degrees C temperature range. To maintain the initial 90% CO(2) removal, it would be necessary to keep the regeneration temperature higher than about 135 degrees C. The results obtained in this study can be used as basic data for designing and operating a large scale CO(2) capture process with two fluidized-bed reactors.     

Analysis of a solar still with photovoltaic modules and electrical heater - Energy and exergy approach

The availability of drinkable water, along with food and air, is a fundamental human necessity. Because of the presence of higher amounts of salt and pollution, direct use of water from sources such as lakes, sea, rivers, and subsurface water reservoirs is not normally suggested. Solar is still a basic technology that can use solar energy to transform accessible waste or brackish water into drinkable water. Exergy analysis is a strong inferential technique for evaluating the performance of thermal systems. Exergy is becoming more popular as a predictive tool for analysis, and there is a rising interest in using it. In this paper, performance analysis on the aspect of energy and exergy from the proposed solar still (PSS) (conventional solar still with the photovoltaic modules-AC heater) was analyzed on three different water depths (W_d) conditions (1, 2, and 3 cm). Using a solar still with an electric heater, the daily potable water production was found as 8.54, 6.37, and 4.43 kg, for the variations in water depth (W_d) of 1, 2, and 3 cm respectively. The energy and exergy efficiency of the PSS at the W_d of 1, 2, and 3 cm were 75.67, 51.45, and 37.21% and 5.08, 2.29, and 1.03%, respectively. At 1 cm W_d, PSS produced the maximum freshwater yield as compared to the other two water depths. When the W_d is increased from 1 to 2 cm and from 1 to 3 cm, the yield is decreased up to 27.3 and 52.7%, respectively. Similarly, the energy and exergy efficiency is decreased up to 36.8 and 53.2% and 50.4 and 80.6%, respectively. The water cost of the modified solar still is calculated as 0.028 $/kg for the least water thickness.

     

Adsorption of CO2 from flue gas streams by a highly efficient and stable aminosilica adsorbent

Three ordered mesoporous silicas (OMSs) with different pore sizes and pore architectures were prepared and modified with amine functional groups by a postgrafting method. The carbon dioxide (CO2) adsorption on these amine-modified OMSs was measured by using microbalances at 348 K, and their adsorption capacities were found to be 0.2-1.4 mmol g(-1) under ambient pressure using dry 15% CO2. It was found experimentally that the CO2 adsorption capacity and adsorption rate were attributed to the density of amine groups and pore volume, respectively. A simple method is described for the production of densely anchored amine groups on a solid adsorbent invoking direct incorporation of tetraethylenepentamine onto the as-synthesized OMSs. Unlike conventional amine-modified OMSs, which typically show CO2 adsorption capacity less than 2 mmol g(-1), such organic template occluded amine-OMS composites possessed remarkably high CO2 uptake of approximately 4.6 mmol g(-1) at 348 K and 1 atm for a dry 15% CO2/nitrogen feed mixture. The enhancement of 8% in CO2 adsorption capacity was also observed in the presence of 10.6% water vapor. Durability tests done by cyclic adsorption-desorption revealed that these adsorbents also possess excellent stability.     

啤酒厂废水处理技术浅析

根据国内啤酒废水水质水量特点，比较分析了国内啤酒废水治理技术和可供选择的治理方案，同时综合实例，指明了清洁生产是啤酒行业治理污染的必然选择，指出啤酒行业可以通过节约用水、啤酒酵母回收利用以及CO2回收利用等途径，实施清洁生产，从而实现经济效益、社会效益、环境效益三个统一。     

Emissions from carpet combustion in a pilot-scale rotary kiln: comparison with coal and particle-board combustion

The use of post-consumer carpet as a potential fuel substitute in cement kilns and other high-temperature processes is being considered to address the problem of huge volumes of carpet waste and the opportunity of waste-to-energy recovery. Carpet represents a high volume waste stream, provides high energy value, and contains other recoverable materials for the production of cement. This research studied the emission characteristics of burning 0.46-kg charges of chopped nylon carpet squares, pulverized coal, and particle-board pellets in a pilot-scale natural gas-fired rotary kiln. Carpet was tested with different amounts of water added. Emissions of oxygen, carbon dioxide, nitric oxide (NO), sulfur dioxide (SO2), carbon monoxide (CO), and total hydrocarbons and temperatures were continuously monitored. It was found that carpet burned faster and more completely than coal and particle board, with a rapid volatile release that resulted in large and variable transient emission peaks. NO emissions from carpet combustion ranged from 0.06 to 0.15 g/MJ and were inversely related to CO emissions. Carpet combustion yielded higher NO emissions than coal and particle-board combustion, consistent with its higher nitrogen content. SO2 emissions were highest for coal combustion, consistent with its higher sulfur content than carpet or particle board. Adding water to carpet slowed its burn time and reduced variability in the emission transients, reducing the CO peak but increasing NO emissions. Results of this study indicate that carpet waste can be used as an effective alternative fuel, with the caveats that it might be necessary to wet carpet or chop it finely to avoid excessive transient puff emissions due to its high volatility compared with other solid fuels, and that controlled mixing of combustion air might be used to control NO emissions from nylon carpet.     

Occurrence of carbon monoxide during organic waste degradation

The concentrations of carbon monoxide (CO) and other gases were measured in the emissions from solid waste degradation under aerobic and anaerobic conditions during laboratory and field investigations. The emissions were measured as room temperature headspace gas concentrations in reactors of 1, 30, and 150 L, as well as sucked gas concentrations from windrow composting piles and a biocell, under field conditions. The aerobic composting laboratory experiments consisted of treatments with and without lime. The CO concentrations measured during anaerobic conditions varied from 0 to 3000 ppm, the average being 23 ppm, increasing to 133 ppm when methane (CH4) concentrations were low. The mean/maximum CO concentrations during the aerobic degradation in the 2-L reactor were 101/194 ppm without lime, 486/2022 ppm with lime, and 275/980 ppm in the 150-L reactors. The presence of CO during the aerobic composting followed a rapid decline in O2 concentrations Significantly higher CO concentrations were obtained when the aerobic degradation was amended with lime, probably because of a more extreme depletion of oxygen. The mean/maximum CO concentrations under field conditions during aerobic composting were 95/1000 ppm. The CO concentrations from the anaerobic biocell varied from 20 to 160 ppm. The hydrogen sulfide concentrations reached almost 1200 ppm during the anaerobic degradation and 67 ppm during the composting experiments.     

Occurrence of Carbon Monoxide during Organic Waste Degradation

Abstract

The concentrations of carbon monoxide (CO) and other gases were measured in the emissions from solid waste degradation under aerobic and anaerobic conditions during laboratory and field investigations. The emissions were measured as room temperature headspace gas concentrations in reactors of 1, 30, and 150 L, as well as sucked gas concentrations from windrow composting piles and a biocell, under field conditions. The aerobic composting laboratory experiments consisted of treatments with and without lime. The CO concentrations measured during anaerobic conditions varied from 0 to 3000 ppm, the average being 23 ppm, increasing to 133 ppm when methane (CH₄) concentrations were low. The mean/maximum CO concentrations during the aerobic degradation in the 2-L reactor were 101/194 ppm without lime, 486/2022 ppm with lime, and 275/980 ppm in the 150-L reactors. The presence of CO during the aerobic composting followed a rapid decline in O₂ concentrations Significantly higher CO concentrations were obtained when the aerobic degradation was amended with lime, probably because of a more extreme depletion of oxygen. The mean/maximum CO concentrations under field conditions during aerobic composting were 95/1000 ppm. The CO concentrations from the anaerobic biocell varied from 20 to 160 ppm. The hydrogen sulfide concentrations reached almost 1200 ppm during the anaerobic degradation and 67 ppm during the composting experiments. There is a positive correlation between the CO and hydrogen sulfide concentrations measured during the anaerobic degradation experiments.