电除尘器计算机智能控制系统的开发

阐述了IPC系统一的T／R微机控制设备、低压微机控制设备的技术特性以及该系统的构成和基本功能,并对其网络控制功能和智能化闭环控制功能作了重点讨论。     

某1 000 MW机组电除尘器气固两相流数值模拟

流场分布对电除尘性能至关重要。采用商业CFD软件,对某1 000 MW机组电除尘器进行了数值模拟。模拟过程中采用离散相模型（DPM）结合k-ε湍流模型,模拟颗粒运动轨迹。研究了在合理布置烟道走向,并在烟道内布置导流板、阻流板,在进口喇叭内布置气流分布板及导流叶片等措施条件下,电除尘器的气固两相流参数。结果表明：烟道内布置导流板及阻流板后,电除尘器各分室进口流量偏差均在±2%以内,出口流量偏差均不超过±0.5%,远优于标准要求;颗粒相质量流量分配偏差也均未超过5%,且各级粒径分布所对应偏差也明显减小;电除尘器各室入口截面烟气流速相对均方根差均不超过0.15,优于标准要求。     

静电除尘器气流分布数值模拟

简要分析了电除尘器在干法除尘系统中的重要作用。指出了除尘效率的高低是衡量除尘系统的关键参数,而气流分布是影响电除尘器效率的重要因素。通过计算流体力学软件对电除尘器内部流场进行数值模拟。根据主要影响气流分布的因素确定了4种方案进行模拟,并对结果进行对比分析,最终为电除尘器气流分布的设计提供了建议。     

SDBS/Na+对红壤胶体悬液稳定性的影响

土壤中普遍存在的有机污染物和无机离子与土壤胶体颗粒的相互作用深刻地影响着土壤中一系列物理、化学和生物学过程.选取红壤胶体作为对象,利用动态光散射技术研究了不同浓度十二烷基苯磺酸钠(SDBS)和Na+作用下红壤胶体颗粒的凝聚过程,并结合体系的pH和Zeta电位分析了SDBS/Na+与土壤胶体颗粒相互作用的机制.结果表明:①相同浓度Na+作用下,随着SDBS浓度的升高,土壤胶体悬液稳定性增强.例如120 mmol·L-1Na+作用下,随着SDBS浓度从0 mmol·L-1升高到10 mmol·L-1,凝聚体有效粒径从702 nm下降至193 nm,总体平均凝聚速率从28.6 nm·min-1减小到3.36 nm·min-1;②相同浓度SDBS作用下,随着Na+浓度的升高,体系Zeta电位绝对值显著降低,凝聚体有效粒径逐渐增大,凝聚速率逐渐加快;③仅SDBS作用下,随着SDBS浓度的升高,体系Zeta电位绝对值从47.6 mV增加到62.2 mV,体系pH从6.17升高到6.76,但均小于土壤胶体悬液本身的pH(6.89).因此,SDBS通过疏水作用和静电作用吸附于土壤胶体颗粒表面,增加了颗粒表面的负电荷数量,降低了作用于胶体颗粒表面的有效Na+浓度(SDBS疏水长链的空间阻碍和高浓度SDBS所形成的胶束结构对Na+的吸附),使得胶体悬液稳定性增强,需要添加更多的Na+才能发生凝聚.     

Measurement of minimum ignition energies (MIEs) of dust clouds – History,present, future

Nearly 130 years ago Holtzwart and von Meyer (1891) demonstrated by experiments that explosible dust clouds could be ignited by inductive electric sparks. Then more than half a century passed before the publication of the important quantitative research of Boyle and Llewellyn (1950) and Line et al. (1959). They worked with capacitive electric sparks and found that the minimum capacitor energies ½CU² required for ignition of various dust clouds in air decreased substantially when a large series resistance, in the range 10⁴–10⁷ Ω, was introduced in the discharge circuit. When considering that the net energies of the sparks themselves were only of the order of 10% of the ½CU² discharged, the minimum net spark energies required for ignition with a large series resistance were only a few per cent of the net energies required without such a resistance.Line et al. observed that the essential effect of increasing the series resistance, and hence increasing the discharge time of the sparks, was to reduce the disturbance of the dust cloud by the blast wave from the spark. This phenomenon was explored further by Eckhoff (1970, 2017), and subsequently by some simple experiments by Eckhoff and Enstad (1976). Franke (1974, 1977) and Laar (1980) confirmed the additional finding of Line et al. (1959) that the minimum ½CU² for ignition is also substantially reduced by including a series inductance in the discharge circuit, rather than a series resistance. The basic reason is the same as with a large series resistance, viz. increased spark discharge time and hence decreased disturbance of the dust cloud by blast wave from the spark. For this reason inclusion of an appreciable series inductance in the spark discharge circuit is an essential element in current standard MIE test methods.In experiments with spark ignition of transient dust clouds produced by a blast of air in a closed vessel, it is necessary to synchronize the occurrence of the spark with the formation of the dust cloud. The precision required from this type of synchronization is typically of the order of 10 ms, which can be obtained even by mechanical arrangements, such as rapid change of spark gap length, or of the distance between two capacitor plates. The present paper reviews some methods that have been/are being used for achieving adequate synchronization of dust cloud appearance and spark discharge. Some current standard experimental methods for determining MIEs of dust clouds experimentally have also been reviewed. The same applies to some theories of electric-spark ignition of dust clouds.At the end of paper some suggestions for possible future modifications of current standard methods for measuring MIEs of explosible dust clouds are presented. With regard to justifying significant modifications of existing standard methods, the “bottom line” is, as quite often in many connections, that any modifications should be based on realistic cost/benefit evaluations.     

功能化层状复合材料的制备及其电催化性能

目的制备一种新型功能化离子液体修饰层状复合材料,研究其对L-酪氨酸(L-Tyr)的电催化氧化行为。方法通过静电自组装方式将氮氧自由基功能化离子液体(TEMPO-IL)与钙铌酸钾(KCa_2Nb_3O_(10))进行复合,并运用XRD,FTIR,SEM,HRTEM等测试手段对所作材料的微观形貌和结构进行分析表征。另外,将其作为电极修饰剂修饰于电极表面通过电化学工作站测试其电化学性质。结果该修饰电极对于电催化氧化L-Tyr有着较高的电化学活性。同时实验还表明,当L-Tyr的浓度在1×10~(-4)~1.16×10~(-2) mol/L之间时,峰电流值与L-Tyr浓度呈良好的线性相关,检测下限为6.2×10~(-5) mol/L(信噪比为3)。结论静电自组装是一种能够快捷、高效的制备层状复合材料方法,且得到的复合材料显示出在生物传感器方面的应用前景。     

旋风静电除尘器流场分布测试研究

利用五孔探针系统对直筒式旋风静电除尘器模型的三维流场进行了测定与分析.结果表明:随着入口风速、供电电压增加,旋风静电除尘器内气流的切向和径向速度分别增加,各截面轴向速度沿半径的分布基本相似;与旋风除尘器相比,旋风静电除尘器内气流的切向速度和径向速度的变化更为平缓,入口风速为8.5 m/s时,在0.3～0.5倍简体直径时,切向速度达最大.     

电除尘器的设计与探讨

介绍了电除尘器的工作原理、结构特性、基本参数和总体设计计算。这种电除尘器可广泛使用于冶金、化工、轻工 ,水泥和矿山等工业部门 ,随着人们对生态环境质量要求的不断提高 ,电除尘器将成为环保的重要设备     

处理高浓度粉尘的除尘器的选择

密相干塔烟气脱硫工艺是一种半于法烟气脱硫工艺,布袋除尘器用来处理该系统中的高浓度粉尘,在国内还没有广泛地应用.通过对布袋除尘器和静电除尘器的技术经济比较,说明布袋除尘器优于静电除尘器,并通过中试验证布袋除尘器在此工艺中的适用性.     

南钢炼铁厂4#高炉矿槽除尘系统的改造

从吸尘罩、系统管网、电改袋、卸输灰系统等方面介绍了南钢炼铁厂4#高炉矿槽除尘系统的改造情况,总结了4#高炉矿槽除尘系统改造的经验,为类似除尘系统的改造提供了范例.