宝钢中厚板分公司煤干燥机除尘系统风量调整技术探究

文章针对宝钢股份中厚板分公司炼铁厂煤干燥机除尘系统吸尘点冒灰,粉尘无组织排放超标的现象进行了测试分析,数据表明主要由除尘系统风量匹配不佳、吸尘点风量不合理造成。笔者通过不断调整阀门及风机档板开摩,测试调整后的风量、除尘性能、岗位粉尘浓度等参数,确定了一个合理的系统风量,不仅可以达到环境排放及职业卫生的要求,而且充分挖掘了除尘系统潜力,达到了节能降耗、经济运行的目的,同时对类似除尘系统风量匹配不佳、扬尘等问题也形成了有效的解决方案。     

黄棕壤不同粒级组分对镉的吸附动力学与热力学研究

采用一次平衡法研究了黄棕壤不同粒级组分(粘粒≤2 μm、粉粒2～20 μm、细砂粒20～200 μm、粗砂粒200～2000 μm)对镉的吸附动力学与热力学,并采用拉格朗日假一级动力学方程、假二级动力学方程、颗粒内扩散模型对试验数据进行拟合.结果表明,2种温度下各粒级组分对镉的吸附均可分为快反应和慢反应2个阶段,0～15 min内为快反应阶段,吸附量达到饱和吸附量的95%以上,此后为慢反应阶段;随着温度由25℃升高到45℃,各组分对镉的饱和吸附量增加了4.86%～25.3%;各组分对镉的吸附动力学符合拉格朗日假二级动力学方程,吸附过程以化学吸附为主;二级动力学吸附速率常数表明,随着各组分粒级增大,吸附速率降低;在试验温度范围内随着温度升高,吸附速率加快;吸附过程的限速步骤为颗粒间扩散;各粒级组分对镉的吸附为吸热反应,反应能自发进行.     

南四湖及主要入湖河流表层沉积物对磷酸盐的吸附特征

研究了南四湖及其主要河流人湖口18个表层沉积物对磷的吸附能力、吸附动力学及其吸附等温线,并对湖区沉积物对磷吸附特征及其理化特征之间的关系进行了探讨.结果表明,对于处于不同营养水平的沉积物,对磷酸盐的吸附具有一致的特征.在前10h沉积物对磷酸盐的吸附量基本达到或超过平衡吸附量的80%,并且在0～1.0 h内吸附反应迅速.在本研究条件下,表层沉积物的cEPC的变化范围为0.010～0.157mg·L-1, Qmax的变化范围是86.74～118.32 mg·kg-1, TQmax的变化范围是99.97～281.11 mg·kg-1·cEPC、NAP、m、Qmax和TQmax与Ads-P都具有显著的正相关关系,沉积物Ads-P含量可以作为指导南四湖水体污染程度的一项指标. m与TQmax之间具有显著的正相关性,吸附效率不仅体现的是对外来磷的吸附效率,还应当包含对本身释放磷的再吸附的效率.对于南四湖沉积物TQmax、NAP和Qmax起到同样的贡献.沉积物的NAP与cEPC之间呈显著正相关性,总的趋势就是,当上覆水中磷含量相等时,具有高的NAP的沉积物易于向上覆水体释磷,反之具有较低NAP的沉积物易从水中吸附磷.     

Effectiveness of fluidized pellet bed for removing soluble contaminants

Fluidized pellet bed (FPB) has been successfully applied in water and wastewater treatment. However, the removal mechanism of contaminants especially the soluble ones, is still unclear. This study aimed to evaluate the e ectiveness of FPB reactor for removing soluble contaminants from synthetic wastewater. By only coagulation through jar test operation with addition of polyaluminium chloride (PACl) as primary coagulant and polyacryamide (PAM) as coagulant-aid, the removals of soluble chemical oxygen demand (COD), total phosphorus (TP), and NH4 +-N were found to be only 2.2%–7.5%, 5.7%–25.5%, and 9.9%–18.5%, respectively. However, by FPB operation under the same dosage of coagulants, these values increased to 82.7%, 37.2%, and 50%, indicating that the formation of pellets in the FPB e ectively enhanced the removal of soluble contaminants. By careful comparison of the settleablility and filterability of the pollutants after coagulation, the originally soluble contaminants could be divided into three groups, namely: (1) coagulated-andsettleable, (2) coagulated-but-nonsettleable, and (3) uncoagulable. It was found that not only the first two groups but also a large part of the third group could be e ectively removed by FPB operation. However, the mechanism for the removal of the uncoagulable pollutants by FPB operation still needs further investigation.     

广州市污水污泥中的重金属及其农用探讨

分析了广州市6种污水污泥中重金属(Zn,Cu,Pb,Cr,Mn和Ni)质量分数及其存在形态,并对污泥农业利用过程中施用的最大量进行了估算.结果表明:广州不同来源污水污泥中.(Cu),w(Zn),w(Mn)和,(Ni)较高,变幅较大,而w( Ph )和w( Cr)低.除一种污泥中w(Cu)超标外,其他重金属基本符合国家农用控制标准(G1318918-2002),但所有污泥中重金属质量分数都超过广州市农田土壤平均值.不同重金属以及同一重金属在不同污泥中的形态分布也不同,其中Zn,Mn和Ni的潜在迁移性强,Cu和Cr中的还原态占有很大的比例,污泥中Pb主要以还原态和残渣态存在.根据广州市主要旱地赤红色土壤静态环境容量和动态环境容量计算表明,污泥农用过程中Cu和Zn是主要监控污染元素,不同来源污泥的最大施用量有明显差异.为保证土壤环境的安全,建议将Cu和Zn作为控制城市污水污泥农用过程中最高施用量的计算参考指标.     

Dynamic contact angle effects on gas-liquid behaviors in the cathode of proton exchange membrane fuel cell with stirred tank reactor design

Liquid water management is still a critical issue in the improvement of proton exchange membrane fuel cell (PEMFC) performance. In this work, for the first time, the liquid water behavior and transport inside the cathode of a PEMFC with a stirred tank reactor (STR) design, rather than the conventional PEMFC flow channel design, are numerically studied. The dynamic contact angle (DCA) is applied to multiple wall boundaries in the numerical model through a user-defined-function (UDF) code, i.e., STR-DCA model. Another numerical model with the static contact angle (SCA) and same operating conditions, i.e., STR-SCA model, is also developed for comparison. The volume of fluid (VOF) method is employed in the simulation to track the gas-liquid interface. The results show that the liquid water distribution and transport are significantly different between these two models, indicating the remarkable effects of DCA on the simulation results. It is also verified the capability of STR-PEMFC to reduce the liquid water flooding, showing the potential of this channel-less type fuel cell in the further development.     

UASB反应器反硝化处理工业废水

采用絮状污泥成功启动升流式厌氧污泥床(UASB)反应器处理含甲酸、苯胺、环已酮、NO3-等的工业废水。UASB反应器以低负荷启动,10天后逐渐提高进水COD,出水COD保持在710~770 mg/L,COD去除率为40%~60%;出水TOC保持在115~314 mg/L,TOC去除率由60.3%逐渐升高至87.2%,最终维持在81%左右;出水中ρ(NO3-)维持在134~176 mg/L,NO3-去除率为90%左右,系统稳定后NO3-去除率几乎为100%。在进水COD容积负荷不超过5.00 kg/(m3·d)的条件下,实际COD容积负荷稳定在2.00 kg/(m3·d)左右,实际TOC容积负荷稳定在1.00 kg/(m3·d)以上。当进水COD容积负荷不大于4.48 kg/(m3·d)时,COD去除率为55%~74%,TOC去除率为63%~87%,NO3-去除率大于95%。     

水生生物对三唑磷的物种敏感度分布研究

针对水环境中日益严重的有机磷农药污染问题,选择广泛使用的三唑磷作为研究对象,利用其对水生生态系统中不同营养层次生物物种的半数效应浓度(median effective concentration, EC₅₀),建立了基于对数-逻辑斯蒂分布的水生生物物种敏感度分布(species sensitivity distribution, SSD)模型,并采用概率图和吻合度检验方法对该模型进行了检验和评价.结果表明,水生生物对三唑磷的 SSD 服从对数-逻辑斯蒂分布,其参数为 α=-0.4788±0.2381,β=0.7546±0.1078.基于该 SSD 模型,获得三唑磷的 5% 危害浓度(hazardous concentration for 5% of the species, HC₅)值为 1.992×10^-3 mg/L,并推导出三唑磷的最大浓度基准值(criteria maximum concentration, CMC)值为 9.96×10^-4 mg/L.对 HC₅、CMC 与单一物种的安全浓度的比较研究指出,基于 SSD 方法制定环境质量标准更为严格,也更接近于真实的生态环境.另外,根据渤海莱州湾海域中三唑磷的监测数据,预测了其对物种的潜在影响比例(potentially affected fraction, PAF)为 0.36%,对该水域生态环境的影响处于较低风险水平.     

体积压力板仪试验操作误差分析

体积压力板仪不仅可用于测试非饱和土的脱湿曲线,还能测试其浸湿曲线,对研究土壤与水分之间的物理关系具有重要意义.本文对2bar体积压力板仪的试验操作原理和步骤进行了详细说明,重点对试验操作中可能产生的误差和各种影响因素进行了分析,并以武汉市汉阳黏土土-水特征曲线试验为例,分析了导致试验误差产生的各种影响因素,以为采用体积...     

应用Modified Gompertz模型对城市生活垃圾沼气发酵的拟合研究

尽管Modified Gompertz模型与料菌比和发酵浓度之间没有直接的函数和变量关系,但是料菌比和浓度的变化必然导致Modified Gompertz模型参数的改变,因此可以通过Modified Gompertz模型参数的变化特征对料菌比和发酵浓度是否适宜作出合理的评价.据此本研究将采用中温批量发酵,分别设计单因素...