Degradation of aqueous Rhodamine B by plasma generated along the water surface and its enhancement using nanocrystalline Fe-, Mn-, and Ce-doped TiO2 films

The degradation of aqueous Rhodamine B (RhB) was examined using a dual-channel spark switch module designed to regulate the steepness of pulsed high voltage with microsecond rise time. Depending on the energy per pulse, a spark along the water surface (SPWS) or streamer along the water surface (STWS) was formed. STWS was found to have a better degradation effect and energy efficiency toward RhB than SPWS at the same power; however, addition of H₂O₂ amounts resulted in increased degradation, the effect being more pronounced using SPWS. The initial concentration of RhB also appeared to influence the rate constant of the degradation reaction. Furthermore, TiO₂ films doped with Fe, Mn, and Ce were found to enhance the degradation performance of plasma. A possible reaction mechanism of plasma formation along the water surface was concluded by determination of the main inorganic products in the liquid and gas phases.     

Kinetics of peanut shell pyrolysis and hydrolysis in subcritical water

Biomass is recognized as an important solution to energy and the environmental problems related to fossil fuel usage. The rational utilization of biomass waste is important not only for the prevention of environmental issues, but also for the effective utilization of natural resources. Pyrolysis and hyrolysis in subcritical water are promising processes for biomass waste conversion. This paper deals with hydrolysis and pyrolysis of peanut shells. Hydrolysis and pyrolysis kinetics of peanut shell wastes were investigated for the in-depth exploration of process mechanisms and for the control of the reactions. Hydrolysis kinetics was conducted in a temperature range of 180–240 °C. A simplified kinetic model to describe the hydrolysis of peanut shells was proposed. Hydrolysis activation energy as well as the pre-exponential factor was determined according to the model. The target products of peanut shell hydrolysis, reducing sugars, can reach up to 40.5 % (maximum yield) at 220 °C and 180 s. Pyrolysis characteristics were investigated. The results showed that three stages appeared in this thermal degradation process. Kinetic parameters in terms of apparent pyrolysis activation energy and pre-exponential factor were obtained by the Coats–Redfern method.     

电渗透脱水污泥干燥特性曲线及干燥模型

通过电渗透脱水技术及自然风干技术两种预处理方式降低污泥含水率,当污泥初始含水率相近时,研究经两种方式处理后污泥的干燥特性曲线,并对电渗透脱水污泥干燥特性曲线的优势情况进行探讨。在40—120℃的低温条件下,研究电渗透脱水污泥（泥饼厚度为3．5mm）的干燥特性曲线并分析其干燥特性。通过所得电渗透脱水污泥的干燥特性曲线,引人薄层污泥干燥模型进行数值分析。结果表明,在实验条件下,电渗透脱水污泥的干燥速率要优于自然风干污泥的干燥速率。随着温度的升高,电渗透脱水污泥的干燥速率随之升高,干燥到所需含水率的时间则随之减少。Logarithmic模型比其他模型更适合描述薄层电渗透脱水污泥在低温条件下的干燥特性。     

青虾池塘养殖环境效率分析

为以环境友好型效率标准合理引导青虾池塘养殖生产活动,将淡水养殖对环境的影响纳入效率研究的范畴,以青虾池塘养殖为例,分别运用SBM模型和CCR模型,计算了青虾池塘养殖的环境效率和经济效率,以及各投入要素的使用情况。并运用相关分析、配对样本T检验和方差齐次性检验等技术进行比较研究。研究结果表明：当前我国青虾池塘养殖的环境效率（考虑环境因素的经济效率）仅为0476 9,而传统的经济效率（不考虑环境因素的经济效率）为0696 7,前者显著低于后者,且波动性更强。所有的要素投入都存在过量现象。除电费、虾苗和药物投入外,其他各项投入在环境效率中的过量程度均大于经济效率;具有固定成本性质的投入品,如劳动力投入和机械投入的过量程度更为严重;利用率过低致使肥料投入过量程度高于饲料投入。农户资源配置过程中忽视环境成本是根本原因,应引起高度重视     

碳源类型及进水量分配对CMICAO工艺脱氮除磷的影响

研究了分别以葡萄糖和乙酸钠为碳源时多点交替进水阶式A2/O(CMICAO)工艺氮磷的去除效果,以及在不同进水C/N比时各进水量分配对脱氮除磷效果的影响.结果表明,在相同的进水COD浓度下,乙酸钠比葡萄糖更适合作为碳源,更能提高脱氮除磷效率.以葡萄糖为碳源时,COD为200 mg/L、C/N比为5、缺氧池与厌氧池进水配比为1∶2时,出水COD、TN、氨氮和TP浓度分别为28.5、10.8、2.1和0.5 mg/L,均达到国家一级A排放标准.若采用葡萄糖作为碳源,投加量以使进水C/N比为5～7.5为宜,外加碳源时缺氧池与厌氧池进水分配比可统一采用1∶1.     

两级氧化法处理油田压裂返排液

采用两级氧化法处理油田压裂返排液。在次氯酸钠、次氯酸钙、过氧化氢、高锰酸钾4种氧化剂中,次氯酸钠的氧化效果最好。以次氯酸钠作为一级氧化剂,进行一级氧化处理;再分别采用次氯酸钙、过氧化氢、高锰酸钾进行二级氧化处理。在次氯酸钠加入量为40mL/L、一级氧化反应时间为30min、二级氧化反应时间为30min、初始废水COD为3976mg/L的条件下,二级氧化剂过氧化氢、次氯酸钙、高锰酸钾的最佳加入量分别为80,40,40mL/L,对应的COD去除率分别为82.60%,71.50%,83.50%。     

颗粒状污泥活性炭流化床吸附处理含铜矿山废水

以城市污水处理厂活性污泥为原料,通过高温热解制备了颗粒状污泥活性炭吸附剂。在自制的流化床吸附装置上研究了该吸附剂对含铜矿山废水的吸附处理效果。实验结果表明：在初始废水pH6、吸附剂加入量15g/L、废水循环流量6.0L/min、吸附时间120min的最佳吸附条件下,废水中Cu²⁺去除率达98.2%。     

紫外辐照-催化湿式过氧化氢氧化技术处理酸性大红GR染料废水

采用自制的负载型CuO-ZnO-CeO2/γ-Al2O3催化剂,常温常压下通过紫外辐照-催化湿式氧化技术处理酸性大红GR模拟染料废水。考察了催化剂加入量、H2O2加入量、废水pH、反应时间、初始酸性大红GR质量浓度等对废水脱色率的影响。实验得到最佳工艺条件为初始酸性大红GR质量浓度200mg/L,催化剂加入量10.0g/L,H2O2加入量2.0mL/L,废水pH4,反应时间2h。最佳工艺条件下废水脱色率达99.33%。     

半胱氨酸合钴溶液膜吸收法处理NO废气

在中空纤维膜接触器中以半胱氨酸合钴溶液为吸收液,采用膜吸收法处理NO废气。研究了对传质系数和NO去除率的影响因素,以及吸收液循环使用效果。实验结果表明:在进气流速为0.005 m/s、进气中NO质量浓度为650.14 mg/m3、吸收液pH为9、吸收液中半胱氨酸合钴浓度为0.017 mol/L、吸收液流速为0.003 m/s、吸收液温度为50℃的优化工艺条件下,吸收时间在55 min之内时,NO去除率保持在98%以上;吸收时间超过55 min之后,NO去除率迅速下降。吸收液经SO2还原处理后可多次循环使用,吸收效果基本不变。     

改性SiO2气凝胶对废水中Fe3+的吸附性能

制备了改性SiO₂气凝胶,考察了经不同类型、不同配比的改性剂改性的SiO₂气凝胶对模拟含Fe³⁺废水的吸附处理效果。实验结果表明：改性SiO₂气凝胶的最佳制备条件为三甲基氯硅烷（TMCS）作改性剂,V（TMCS）#x02236;V（正己烷）=1#x02236;5;当改性SiO₂气凝胶加入量为75g/L、吸附时间为4h、Fe³⁺质量浓度为10mg/L时,模拟含Fe³⁺废水的Fe³⁺去除率为98.32%,剩余Fe³⁺质量浓度为0.168mg/L;采用改性SiO₂气凝胶动态吸附处理流量为420mL/h、Fe³⁺质量浓度为100mg/L的模拟含Fe³⁺废水,吸附后废水中剩余Fe³⁺质量浓度仅为0.196mg/L。