160 h of chemical-looping combustion in a 10 kW reactor system with a NiO-based oxygen carrier

Chemical-looping combustion, CLC, is a technology with inherent separation of the greenhouse gas CO₂. The technique uses an oxygen carrier made up of particulate metal oxide to transfer oxygen from combustion air to fuel. In this work, an oxygen carrier consisting of 60% NiO and 40% NiAl₂O₄ was used in a 10 kW CLC reactor system for 160 h of operation with fuel. The first 3 h of fuel operation excepted, the test series was accomplished with the same batch of oxygen carrier particles. The fuel used in the experiments was natural gas, and a fuel conversion to CO₂ of approximately 99% was accomplished. Combustion conditions were very stable during the test period, except for the operation at sub-stoichiometric conditions. It was shown that the methane fraction in the fuel reactor exit gas was dependent upon the rate of solids circulation, with higher circulation leading to more unconverted methane. The carbon monoxide fraction was found to follow the thermodynamical equilibrium for all investigated fuel reactor temperatures, 660–950 °C. Thermal analysis of the fuel reactor at stable conditions enabled calculation of the particle circulation which was found to be approximately 4 kg/s, MW. The loss of fines, i.e. the amount of elutriated oxygen carrier particles with diameter <45 μm, decreased during the entire test period. After 160 h of operation the fractional loss of fines was 0.00022 h⁻¹, corresponding to a particle life time of 4500 h.     

催化臭氧氧化—生物活性炭吸附组合工艺处理反渗透浓水

采用催化臭氧氧化—生物活性炭吸附组合工艺处理反渗透(RO)浓水,比较了4种催化剂催化臭氧氧化的性能,优化了初始RO浓水pH、臭氧氧化时间、生物活性炭柱空床停留时间(EBRT)等工艺条件。实验结果表明:以WP-01为催化剂催化臭氧氧化RO浓水时无需调节废水pH;臭氧氧化反应5 min时RO浓水的BOD5/COD达0.28,可生化性得到显著改善;WP-01催化剂重复使用30次其催化活性没有明显下降;生物活性炭吸附单元的EBRT控制在30 min左右,可确保出水COD稳定在50 mg/L以下,符合GB 18918—2002《城镇污水处理厂污染物排放标准》的一级A标准;催化臭氧单元处理每吨RO浓水的电费约为1.22元。     

组合式水生植物净化系统对Cu、Pb和Cd的去除与生物富集特征

选取再力花、美人蕉、水烛、旱伞草、梭鱼草、慈姑、菖蒲、水葫芦和大藻9种植物作为实验植物,构建成以高效净化重金属污染水体为主要功能的组合式水生植物高效净化系统（人工湿地＋生态浮床＋水生植物塘3个处理单元串联而成）,研究不同处理单元中水生植物对重金属Cu、Pb和cd的去除能力及富集特征。结果表明,该净化系统经过为期60d的连续运行,对Cu、Pb和Cd的去除率较为稳定,可分别达到Cu93．5％～96．1％、Ph94．5％～95．2％和Cd95．6％～97．4％,3种重金属出水浓度均可达到GB3838-2002Ⅲ类水排放要求;其中人工湿地单元对重金属去除贡献率最高,Cu、Pb和Cd分别为54．15％、33．61％和44．84％,其次为生态浮床处理单元,Cu、Pb和Cd的去除贡献率分别为38．61％、51．42％和38．56％,而水生植物塘主要起到深度处理作用,对Cu、Pb和cd的去除贡献率分别为7．24％、14．97％和16．6％。9种植物在系统运行期间,生长状况良好,且重金属累积量较高,尤其是生物塘系统中的水葫芦和大藻,实验期间其重金属生物富集系数（BCF）均在200以上。所选植物不同部位对3种重金属的吸收富集能力均表现为根最强。     

干化床和芦苇床稳定污泥过程中的腐殖化特征简

通过现场实验,考查污泥干化床和污泥干化芦苇床稳定污泥过程中的腐殖质变化特征,重点分析了污泥腐殖化率和污泥腐殖化指数的变化情况。系统运行了3年,包括前2年的污泥负荷期和第3年的自然稳定期,检测分析在第3年进行。实验结果表明,污泥腐殖质含量历月变化不大,基本在1.1%~2.1%范围;总体上污泥的腐殖化率具有上升趋势,同一时间样品芦苇床中污泥的腐殖化率略高于干化床;污泥腐殖化指数呈上升趋势,但芦苇床略低于传统干化床;4—11月,干化床中的污泥腐殖化指数从0.079升高到0.742,芦苇床从0.042升高到0.715。经过3 y的稳定化处理,污泥的腐殖化程度和腐熟度得到有效提高。     

PPS滤布对柴油机排放PM的过滤效率

基于柴油机实验台架和颗粒捕集装置,采用聚苯硫醚(PPS)针刺毡滤布过滤柴油机排放的颗粒物(PM)。利用称重法,以Whatman玻璃纤维滤纸为对比滤纸,间接测试了3种PPS滤布的过滤效率;同时实验探索了表面涂覆聚四氟乙烯的PPS滤布的深床过滤时间。实验结果表明,3种滤布在180℃的加热条件下将出现颜色和形态的变化;3种滤布在深床过滤期对PM的平均过滤效率分别为78.8%、76.9%和83.7%;表面涂覆聚四氟乙烯的PPS滤布的深床过滤时间为15~20 min,此后其过滤效率可接近100%。     

UASB处理硫酸盐有机废水的启动

为了考察上流式厌氧污泥床反应器(UASB)处理含硫酸盐有机废水的特性,采用有效容积为10 L的UASB,研究了启动运行过程中COD和SO2-4降解情况、出水VFA和pH值、产气量及颗粒污泥比产甲烷活性(SMA)变化状况。结果表明,接种厌氧颗粒污泥,保持进水COD为1 500 mg/L,SO2-4浓度为100 mg/L,将HRT由24 h缩短至12 h以提高负荷,经历55 d成功启动了UASB反应器;当HRT为12 h,进水COD和SO2-4负荷为3.0 kg/(m3·d)和0.20 kg/(m3·d),COD和SO2-4的去除率分别达到80%和89%,出水VFA为3 mmol/L,产气量达9.5 L/d,颗粒污泥的SMA为86.4 mL/(g VSS·d)。     

循环水养殖系统中流化床生物滤器净水效果影响因素

为优化流化床生物滤器的工作性能,采用新型填料玻璃珠作为滤器的基质,并将其应用于罗非鱼循环水养殖系统,研究了玻璃珠粒径、床层膨胀率、碱度和氨氮负荷4个可控因素对其处理养殖废水效果的影响。结果表明,流化床生物滤器挂膜23d后生物膜成熟稳定,当床层膨胀率低于160％时,床层增高和填料流失现象不明显。选用0．2～0．4mm粒径的玻璃珠为填料时,对TAN和NO2--N的去除率显著高于以0．4～0．6mm玻璃珠为填料的滤器;随着床层膨胀率的提高,滤器对TAN和NO2--N的去除率逐渐下降,但对TAN的去除负荷有一定的提高;碱度和TAN负荷的增加有利于滤器的硝化作用。流化床生物滤器对养殖水体中的TAN的平均去除负荷和NO2--N的去除率分别可以达到（673．11±23．26）g／（m3·d）和（90．24±3．45）％,显示出较好的硝化性能。     

循环流化床灰制备聚合双酸铝铁絮凝剂

为了提高循环流化床灰(CFB灰)的资源综合利用率对CFB灰制备聚合双酸铝铁(PAFCS)的可行性及工艺参数进行了研究,提出了以酸浸、水解、聚合和熟化等工艺过程,制备PAFCS混凝剂产品。重点对制备PAFCS絮凝剂的工艺参数进行研究,并利用红外光谱分析技术对PAFCS进行了结构表征及实验了PAFCS絮凝性能。结果表明,在相同条件下PAFCS的絮凝效果明显好于聚合氯化铝(PAC),用CFB灰制备PAFCS絮凝剂产品是可行的。     

旋转填充床中Fenton+O_3氧化降解模拟阿莫西林废水

以旋转填充床(RPB)作为反应装置,研究了Fenton工艺与Fenton+O3工艺处理模拟阿莫西林废水的效果,考察了FeSO4·7H2O的投加量、温度、旋转床转速、液体流量及pH对COD去除率的影响。实验表明,Fenton+O3工艺的COD脱除率及BOD5/COD相对于Fenton工艺分别提升26.7%和140%。该工艺在pH为3、温度为25℃、液体流量30 L/h、气体流量2.5 L/h、转速800 r/min、H2O2的投加量为1 mmol/L及Fe2+投加量为0.4 mmol/L的条件下,100 mg/L的模拟阿莫西林废水中COD的去除率达到57.9%,BOD5/COD从0增加到0.36,满足后续生化处理要求。     

Sorption and desorption of lindane by wood charcoal in fixed‐bed reactor

Abstract

Sorption and desorption of lindane (y‐HCH) by wood charcoal (WC) and wood charcoal treated by 1N HNO₃ (WCT) in fixed‐bed reactor (FBR) were investigated in this study. WCT revealed a better performance than WC, in removing lindane in FBR. The breakthrough of lindane was significantly affected by the size of WCT, flow rate to the FBR, and depth of WCT bed. The removal of lindane in the presence of mixture of other pesticides was considerably reduced. The design parameters for FBR were calculated based on the bed‐depth service time (BDST) approach. Many parameters Viz. depth of sorption zone, velocity of sorption, sorbent use rate, critical bed‐depth, bed efficiency, and service time, were determined for design of the fixed‐bed. Using the material balance principle, the characteristics of the wave‐front were evaluated and found that the wave‐front velocity is approximately equal to the sorption velocity determined from the BDST approach. Desorption studies were performed in dilute organic solvent media and they gave an excellent performance in regeneration process.