矿用救生舱内二氧化碳净化特性研究

煤矿救生舱是在矿井下发生事故后保护被困矿工生存、等待救援的密闭舱室设备。在救援过程中,二氧化碳的处理是舱内空气净化系统的一项主要功能。本文对救生舱内二氧化碳净化装置的功率、吸收效率、药剂床层厚度等因素进行了一系列试验,确定了救生舱二氧化碳的最优净化方式,并通过救生舱内真人生存试验对其进行了验证。最终得出救生舱内处理二氧化碳最佳反应条件为:药剂量20kg,最佳功率为100W;间歇式工作的运行时间与停机时间比例为2:3;在救生舱内8人生存模拟实验中,得出8kg药剂可供8人使用6.1h,平均吸收速率为1.34L/min。     

一种高效节能的生物三相流化床技术

将竖流式生物三相流化床改为封闭卧式生物三相流化床后 ,不但保留了竖流式生物三相流化床原有的优点 ,消除了竖流式生物三相流化床存在的一些缺陷 ,而且又新增了功能 ,特别是电耗下降近 4 0 %。并着重介绍封闭卧式生物三相流化床在地下车库或其它对高度有限制场所的应用实例。该设备在处理餐饮业废水和一些中、小型工业有机废水中有较高的推广价值。     

一种异形结构传爆药起爆威力实验研究

旨在研究一种新型高能传爆药装药结构,根据冲击波汇聚技术、拐角效应理论和有效装药理论等,设计了一种异形结构传爆药。利用主装药轴向钢凹法对多点同步起爆网络起爆的该异形结构传爆药柱起爆威力进行了实验研究。对实验数据进行对比分析,结果表明在达到相同起爆效果的情况下,利用多点同步起爆网络起爆的该异形结构传爆药柱相对于普通圆柱形传爆药柱的用药量有较大幅度的降低。研究成果对解决钝感弹药的起爆问题具有重大的现实意义。     

循环流化床烟气悬浮脱硫技术中试及机理分析

设计了新的循环流化床烟气悬浮脱硫中试装置,其烟气处理量达3500m³/h.首先进行了进料钙硫比(Ca/S)、过饱和温度对装置脱硫效率影响实验,进一步研究了脱硫塔内固体颗粒物循环和烟气流速等因素对脱硫装置性能的影响.对比实验研究表明:在Ca/S=1.2时,固体颗粒物的循环使系统脱硫效率提高15% 左右;脱硫塔内烟气设计流速可以偏高一些.本文同时对系统脱硫过程进行了机理分析,指出了延长脱硫剂有效停留时间的途径.     

The deflectors influence on flow complexity,bed morphology,sediment transport and water quality of urban lotic waters - A laboratory study

In this laboratory study different combinations of bed (sand, pebble gravel [gravel], and a mix of sand and gravel) and flow (typical and overtopping) were experimented with to investigate the impact of porous deflectors in flow diversity, water quality, and fish performance in prismatic open channels. Deflectors changed the gradually varied flow to a rapidly varied flow, as a sudden change in the water depth was observed at the deflectors, and this change was large for smooth beds. With the presence of gravel, the scouring near the downstream deflector was almost twice that of the sand bed, and with the scouring at its own upstream deflector, irrespective of whether the flow was typical or overtopping. This behavior was a result of sand mobilization due to shear stress and sand mobilization aided gravel transport. The mixed bed showed less gravel movement compared to the gravel-only bed. The percentage of sediment washed out was minor for all bed scenarios, indicating that sediment transport was local. Relative to the sand bed without deflectors (representing a typical urban canal), deflectors resulted in reduced and improved water quality (in terms of sediment load) for sand, and mixed bed, respectively. The fishes found refuge and were comfortable in the pool areas created by deflectors unlike in channels without deflectors where they showed exhaustion.     

EGSB出水回流对EGSB—SBR工艺处理果汁废水的影响

采用EGSB—SBR工艺处理实际果汁废水(COD 2 608~6 500 mg/L,p H 5.0~7.0)。在EGSB反应器成功启动及驯化完成的情况下,连续运行49 d。实验结果表明:第25天起,控制EGSB回流比为3.00∶1,EGSB反应器可在无须添加Na HCO3的条件下稳定运行,从而降低了废水处理成本;第25天起,平均进水COD,BOD5,SS分别为5 968,2 130,1 020 mg/L,平均出水COD,BOD5,SS分别降至131,11,50 mg/L,平均COD,BOD5,SS去除率分别为98%,99%,95%;组合工艺对该实际果汁废水具有良好的处理效果。     

微生物燃料电池的专利技术综述

检索了微生物燃料电池在中国的发明专利文献,综述了微生物燃料电池在废水处理中的应用及与现有技术中其他水处理技术耦合的专利进展,并对其实际应用的前景进行了展望。     

The use of nanovermiculite catalyst in the study of removal of the organic load and degradation of atrazine via ozone process in RPB reactor

Abstract

The main objective of this study is the degradation of a synthetic solution of atrazine by a modified vermiculite catalyzed ozonation, in a rotating packed bed (RPB) reactor. A 0.5?L RPB reactor was used to perform the experiments, using a Central Composite Design (CCD) response surface to construct the quadratic model based on the factors: pH, catalyst concentration and reactor rotation frequency. The response variable was the removal of the organic load measured in terms of Chemical Oxygen Demand (COD). After the complete quadratic model was constructed through the response surface, the COD degradation process had an optimal removal of 41% under the following conditions: pH 8.0, rotation of 1150?rpm and catalyst concentration 0.66?g L^?1.     

天然沸石床处理受污染景观水体的试验

采用天然沸石滤床对富营养化景观湖水进行净化试验,结果表明,天然沸石滤床能有效地净化受污染的湖水,CODCr、氨氮、总磷和浊度的去除率分别为35.8%、95.0%、66.7%和78.0%,沸石能有效地去除水中的氨氮,其作用机理包括离子交换和生物硝化两种作用。     

多孔球三相流化床冷态试验的研究

对多孔球为填料的三相流化床进行冷态试验研究,研究不同工况下气体空塔流速、填料静止高度、喷淋密度等因素对流化床阻力特性和脱硫效率的影响.试验表明,用多孔球替代空心球做填料,不仅可以消除空心球在流化过程中出现的问题,还可以适当提高脱硫效率.