Emissions of SO2, NO and N2O in a circulating fluidized bed combustor during co-firing coal and biomass

This paper presents the experimental investigations of the emissions of SO2, NO and N2O in a bench scale circulating fluidized bed combustor for coal combustion and co-firing coal and biomass. The thermal capacity of the combustor is 30 kW. The setup is electrically heated during startup. The influence of the excess air, the degree of the air staging, the biomass share and the feeding position of the fuels on the emissions of SO2, NO and N2O were studied. The results showed that an increase in the biomass shares resulted in an increase of the CO concentration in the flue gas, probably due to the high volatile content of the biomass. In co-firing, the emission of SO2 increased with increasing biomass share slightly, however, non-linear increase relationship between SO2 emission and fuel sulfur content was observed. Air staging significantly decreased the NO emission without raising the SO2 level. Although the change of the fuel feeding position from riser to downer resulted in a decrease in the NO emission level, no obvious change was observed for the SO2 level. Taking the coal feeding position R as a reference, the relative NO emission could significantly decrease during co-firing coal and biomass when feeding fuel at position D and keeping the first stage stoichiometry greater than 0.95. The possible mechanisms of the sulfur and nitrogen chemistry at these conditions were discussed and the ways of simultaneous reduction of SO2, NO and N2O were proposed.     

Thermal stabilization of chromium slag by sewage sludge: Effects of sludge quantity and temperature

To investigate the feasibility of detoxifying chromium slag by sewage sludge,synthetic chromium slag containing 3% of Cr(VI) was mixed with sewage sludge followed by thermal treatment in nitrogen gas for stabilizing chromium.The effects of slag to sludge ratio(0.5,1 and 2) and temperature(200,300,500,700 and 900°C) on treatment efficiency were investigated.During the mixing process before thermal treatment,59.8%-99.7% of Cr(VI) was reduced,but Cr could be easily leached from the reduction product.Increasing heating temperature and decreasing slag to sludge ratio strengthened the reduction and stabilization of Cr(VI).When the slag to sludge ratio was 0.5 and thermal treatment temperature was 300°C,the total leached Cr and Cr(VI) declined to 0.55 mg/L and 0.17 mg/L respectively,and 45.5% of Cr in the thermally treated residue existed as residual fraction.A two-stage mechanism was proposed for the reduction and stabilization of Cr.     

基于GH-B强度准则的节理岩质边坡稳定性分析

在岩质边坡工程数值模拟计算分析中,其难题之一就是如何较准确地确定岩体强度参数,而边坡岩体抗剪强度是影响计算分析成果的控制因素,也是支护设计成败的关键所在。采用GH-B强度准则对深水河大桥4号桥墩边坡进行了稳定性分析,同时与采用M-C强度准则的模拟结果进行了对比分析。结果表明:GH-B强度准则采用基于应力水平的塑性流动法则,更好地体现了节理岩体的变形和破坏机理,可有效反映岩体的非线性破坏特征,更加接近于工程实际,适于节理岩体的强度计算及稳定性分析。     

水稻秸秆生物炭对耕地土壤有机碳及其CO2释放的影响

为探究生物炭自身稳定性及其输入土壤后对于土壤本体有机碳的影响,本研究模拟自然条件,分别将500℃和700℃裂解的水稻秸秆生物炭(RBC500和RBC700)以0%(空白土壤)、3%、6%和100%(纯生物炭)的比例添加至耕地土壤进行室内培养实验,观测总有机碳(TOC)与易氧化态碳(EOC)含量的变化及CO2排放特征.结果表明,与空白土壤处理相比,土壤TOC、EOC含量均随水稻秸秆生物炭添加量的增加而升高;相同添加量条件下,RBC500对土壤TOC与EOC增加的贡献均高于RBC700.各处理土壤TOC含量在前30 d内均降低(最大降幅为15.8%),并于培养后期趋于稳定;土壤EOC含量在培养初30 d内均降低,当生物炭添加比例为3%和6%时,RBC500使土壤的EOC含量降幅分别为72.4%和81.7%,大于RBC700的61.3%和69.8%;培养结束时,添加相同裂解温度生物炭的土壤EOC值相近.培养前期土壤中EOC含量的下降可能与生物炭中易分解组分引起的矿化作用有关.在130 d培养期内,CO2累计排放量大小顺序为:土壤+生物炭混合处理<纯土壤处理<纯生物炭处理,可见,生物炭的土壤处理可以减少土壤CO2的排放,最大减排率可达41.05%.在一个长的时间尺度内,生物炭的土壤处理有利于土壤碳的固定.生物炭施用于土壤可作为碳储存载体.     

穿层爆破中控制孔对裂隙扩展作用机理试验研究

为研究控制孔在穿层爆破中对裂隙扩展的作用机理,在实验室内进行穿层爆破相似模拟试验。研究表明:煤岩体试块上表面产生了贯穿炮孔和控制孔的裂隙,侧面生成了多条不规则的裂隙,试块内部出现了包括沿控制孔方向发展的多个断裂面;炮孔和控制孔连线上产生了较高拉应力,炮孔和控制孔连线方向上拉应变峰值是炮孔45°方向上的拉应变峰值的1.12倍;爆破产生的压缩应力波P和在控制孔处反射生成的反射横波Sr、反射纵波Pr在控制孔附近的煤岩体上产生应力叠加,造成煤岩体损伤,最终形成贯穿裂隙。穿层爆破中控制孔对爆生裂隙的扩展起到导向作用,但由于穿层爆破中煤岩交界面的存在,使得应力波出现复杂的反射、透射、叠加效应,造成煤层内裂隙无序发育,工程现场应予以重视。     

灾害视角下基于隐患因素的生态安全演变机理与系统动力学特征

通过"灾害学"视角认识和理解生态安全,针对隐患因素对安全状态的影响,探讨了生态安全演变的隐患触发传递与响应控制机理,并从系统动力学的视角论述生态安全是反馈的动力系统和非线性的动态系统特征。研究表明,生态安全因素分析必须包含隐患因素分析;安全评价要素范围必须扩展。生态安全系统由隐患触发传递系统和响应控制管理系统组成,且两系统之间以及子系统各要素之间相互影响、相互联系,是隐患因素不断触发、传递、响应和控制的复合高阶演变过程,具有非线性灾变性、自组织及被组织性和有序与无序的动态性。     

Effects of WOx modification on the activity, adsorption and redox properties of CeO2 catalyst for NOx reduction with ammonia

A series of WO₃/CeO₂ (WOx/CeO₂) catalysts were synthesized by wet impregnation of ammonium metatungstate on a CeO₂ support. The resulting solid acid catalysts were characterized by X-ray diffraction (XRD), UV-Vis spectroscopy (UV-Vis), Raman spectroscopy (Raman), in-situ Fourier transform infrared spectroscopy (in-situ FT-IR) of ammonia adsorption, NH₃-TPD, H₂ temperature-programmed reduction (H₂-TPR), NH₃/NO oxidation and activity measurements for NOx reduction by NH₃ (NH₃-SCR). The results show that polytungstate (WOx) species are the main species of tungsten oxide on the surface of ceria. The addition of tungsten oxide enhances the Brönsted acidity of ceria catalysts remarkably and decreases the amount of surface oxygen on ceria, with strong interaction between CeO₂ and WOx. As a result, the N₂ selectivity of NH₃ oxidation and NH₃-SCR at high temperatures (> 300℃) is enhanced. Therefore, a wide working temperature window in which NOx conversion exceeds 80% (NOx conversion > 80%) from 200 to 450℃, is achieved over 10 wt.% WOx/CeO₂ catalyst. A tentative model of the NH₃-SCR reaction route on WOx/CeO₂ catalysts is presented.     

A+OSA活性污泥工艺剩余污泥减量特性研究

采用自动热量计对Anoxic (A) + oxic-settling-anaerobic(OSA)系统解偶联池进出污泥进行热值分析,以考察污泥量变动与能值变动的相互关系;通过解偶联池参数调整,了解污泥减量趋势,结合能量和物质平衡与常规水质指标测试,推测减量途径和特性.结果表明,解偶联池水力停留时间为5.56、 7.14和9 h时,整个系统污泥减量分别为1.236、 0.771和0.599 g/d.进出解偶联池的污泥含能水平发生了变化,随停留时间增加出流污泥的单位热值有高于进流污泥单位热值的趋势：5.56 h时,进出水热值没有显著差异;7.14 h时,进出水热值差值在99～113 J/g之间;9 h时,差值在191～329 J/g之间.解偶联池发生了污泥的衰减,停留时间延长,衰减程度越高.A+OSA系统污泥减量是解偶联池污泥衰减与AO主体反应区污泥产生率变化共同作用的结果.     

九龙江流域畜禽养殖业的生态环境问题及防治对策探讨

根据2001年畜禽养殖业统计数据，分析了九龙江流域畜禽养殖污染的现状和趋势。通过计算农田畜禽粪便负荷量，并采用猪粪当量负荷及有效农田面积，考虑各地农田畜禽粪便有机肥可消纳量，对九龙江流域畜禽粪便负荷量和承受程度进行警报与分级，系统地阐述了畜牧业发展中产生的生态环境问题，从技术和管理角度，提出消减畜禽养殖污染、促进生态环境良性循环的对策和措施。     

污水生物处理实际工艺中氧化亚氮的释放：现状与挑战

介绍了污水生物处理过程中N2O的产生途径,重点分析了污水厂典型脱氮工艺的N2O释放差异及其原因,提出了城市污水脱氮处理过程N2O减排的具体措施,并估算出全国城镇污水处理厂2011年N2O释放总量约为1.26×109g(以N计),对今后关于城市污水脱氮处理过程N2O产生及减排的研究趋势进行了评估.