好氧颗粒污泥沉降选择实验研究与定量描述

以序批式反应器培养的成熟好氧颗粒污泥为对象,研究沉淀高度对颗粒数、比重、污泥浓度、粒径分布及选择系数的影响.结果表明,随着沉淀高度的增加,污泥浓度在沉淀时间为30 s时由0.24 mg.L-1明显增加至6.07 mg.L-1,平均粒径从450μm增加到550μm,颗粒圆形度增加12.67%,而复杂度减小13.47%,说明粒径较大、形状较规则的颗粒沉降较快,从而更易在沉降选择过程中得以保留.根据选择压原理,结合颗粒污泥沉降实验结果引入选择系数.实验和计算结果显示,在任意沉淀高度,选择系数随粒径和密度的增大而增加.随着沉淀高度的增加,直径>600～800μm的颗粒选择系数增加,小颗粒趋势与之相反,说明增大排水比有利于大颗粒保留而絮体被筛选出反应器,而低的排水比会使污泥颗粒化过程放缓.该研究结果可望对加速污泥颗粒化过程和提高其稳定性提供科学的理论依据和指导.     

H2S匀圆杂选择性催化氧化工艺及催化剂研究现状

论述了石油流化催化裂化烟气中H2S气体的选择性催化氧化处理工艺和工艺中所使用的各种类型选择性氧化催化剂.目前已发展并投入使用的选择性氧化工艺主要有:Superclaus工艺、Euroclaus工艺、Clinsulf-Do工艺、BSR/Hi-Activity工艺、Selectox工艺和Modop工艺等,各工艺具有不同的特点和应用范围.H2S选择氧化催化剂主要包括以下几种体系:碳体系、SiC载体体系、分子筛体系、氧化物体系和柱撑黏土体系等.其中碳体系和氧化物体系的研究开展的较早较多,关于分子筛体系的研究近期有所减少,SiC是研究人员认为非常有潜力的一个载体体系,其相关体系研究也一直在进行之中,柱撑黏土体系还处于初步研究阶段,离实际应用尚有距离.     

Fe-MnOx-CeO2/ZrO2低温催化还原NO性能研究

以纳米ZrO2为载体,用浸渍法制备出Fe-MnOx-CeO2/ZrO2催化剂,考察了活性组分配比和助剂负载量对催化剂低温NH3选择性催化还原NO活性的影响,并对催化剂进行了XRD、SEM、EDS和BET表征;探讨了温度、H2O和SO2对Fe-MnOx-CeO2/ZrO2催化剂低温下NH3选择性催化还原NO的影响,结果表明,无SO2和H2O条件下,8%Fe-10%MnOx-CeO2/ZrO2催化剂具有良好的催化活性和稳定性.120℃时,催化剂的脱硝效率为85.23%,当温度升至180℃时,脱硝效率可达到92.0%.SO2和H2O共存条件下,催化剂易失活,采用傅立叶变换红外光谱对各反应阶段的催化剂进行了表征,对其失活机制进行深入研究,结果表明,催化剂失活的主要原因是催化剂表面硫酸铵盐的沉积和催化剂本身活性成分的硫酸盐化.     

基于生产工艺的水泥工业项目竣工环保验收监测重点分析研究

基于水泥工业的生产工艺特点,说明新型干法生产时代,水泥生产的主要产污环节及特征污染物,并分析其对生态环境的影响和危害,表明该行业属高能耗、高污染的产能过剩行业.根据建设项目竣工环境保护验收规范要求和工作实践经验,结合生产工艺、特征污染物和污染物总量控制等要求,从废水监测、废气监测、噪声监测等方面阐明水泥行业项目竣工环保验收的侧重点和注意事项,并指出污染防治设施、总量控制等几方面应重点关注的问题.     

分光光度法与离子色谱法测定降水中铵离子的对比

采用分光光度法和离子色谱法测定降水中铵离子,比对研究两种方法的测定原理、标准曲线和检出限。结果表明,两种方法对标准样品和实际样品分析测定均能达到质控要求,测定结果基本一致。离子色谱法方便快捷,污染少,结果准确可靠,可以同时测定多种阳离子。     

Lindet ypeF(K)沸石对Zn~(2+)的吸附研究

利用粉煤灰合成Linde type F(K)沸石吸附重金属Zn2+,考察吸附剂量、pH值、反应温度对Zn 2+吸附效果影响,研究沸石吸附Zn2+的等温线与动力学,得到了相应的模型。结果表明:吸附剂量、pH值、反应温度均对Zn2+去除效果影响显著。随着吸附剂量增大,Zn 2+去除效果不断提高,饱和吸附量逐渐减小。初始pH值为3~7时,沸石对Zn2+去除率随pH值升高迅速提高。反应温度越高,沸石吸附Zn2+到达平衡时间越短。沸石对Zn2+吸附过程符合Langmuir吸附等温式,其吸附为单分子层吸附;准二级反应动力学方程能很好描述沸石对Zn2+的吸附行为。     

电絮凝去除废水中多种重金属影响因素研究

目的以铁作为电极,研究电絮凝法处理含多种重金属废水的影响因素及效果。方法通过控制pH、停留时间、电流密度、电导率、废水初始浓度等因素至不同水平,考察处理效果、能耗及极板消耗的变化。结果随着停留时间、pH值及电流密度的升高,处理效果越好,但升高至一定程度后,处理效果提升并不明显;电导率对处理效果影响并不显著,但过低的电导率会增加能耗;废水初始浓度越高,要达到处理目标所需的能耗及极板消耗均越高。结论当pH为8.5~9.0、进水电导率为1500~2000μs/cm、停留时间为3~4 min、废水初始质量浓度20 mg/L、电流密度为13.2~19.8 A/m2时,处理效果最理想,对总铜、总镍、总铅、总锌、总镉及总铬的去除率达到99%以上,且能耗与极板消耗均为最低,电絮凝法更适合于重金属废水的深度处理。     

Study of cyanide removal from contaminated water using zinc peroxide nanomaterial

The present study highlights the potential application of zinc peroxide(ZnO_2)nanomaterial as an efficient material for the decontamination of cyanide from contaminated water. A process patent for ZnO_2 synthesis has been granted in United States of America(US Patent number 8,715,612; May 2014),South Africa,Bangladesh,and India. The ZnO_2 nanomaterial was capped with polyvinylpyrrolidone(PVP)to control the particle size. The PVP capped ZnO_2nanomaterial(PVP-ZnO_2)before and after adsorption of cyanide was characterized by scanning electron microscope,transmission electron microscope,X-ray diffractometer,Fourier transform infrared spectroscopy and time of flight-secondary ion mass spectrometry. The remaining concentration of cyanide after adsorption by PVP-ZnO_2 was determined using ion chromatograph. The adsorption of cyanide over PVP-ZnO_2 was also studied as a function of p H,adsorbent dose,time and concentration of cyanide. The maximum removal of cyanide was observed in p H range 5.8–7.8 within 15 min. The adsorption data was fitted to Langmuir and Fruendlich isotherm and it has been observed that data follows both the isotherms and also follows second order kinetics.     

Pd-MnO2 nanoparticles/TiO2 nanotube arrays (NTAs) photo-electrodes photo-catalytic properties and their ability of degrading Rhodamine B under visible light

Pd-MnO_2/TiO_2 nanotube arrays(NTAs) photo-electrodes were successfully fabricated via anodization and electro deposition subsequently; the obtained Pd-MnO_2/TiO_2 NTAs photo electrodes were analyzed by scanning electron microscopy(SEM), X-ray diffraction(XRD) and characterized accordingly. Moreover, the light harvesting and absorption properties were investigated via ultraviolet–visible diffuse reflectance spectrum(DRS); photo degradation efficiency was investigated via analyzing the photo catalytic degradation of Rhodamine B under visible illumination(xenon light). The performed analyses illustrated that Pd-MnO_2 codoped particles were successfully deposited onto the surface of the TiO_2 nanotube arrays;DRS results showed significant improvement in visible light absorption which was between400 and 700 nm. Finally, the photo catalytic degradation efficiency results of the designated organic pollutant(Rhodamine B) illustrated a superior photocatalytic(PC) efficiency of approximately 95% compared to the bare TiO_2 NTAs, which only exhibited a photo catalytic degradation efficiency of approximately 61%, thus it indicated the significant enhancement of the light absorption properties of fabricated photo electrodes and their yield of UOH radicals.     

Capability of cation exchange technology to remove proven N-nitrosodimethylamine precursors

N-nitrosodimethylamine(NDMA) precursors consist of a positively charged dimethylamine group and a non-polar moiety, which inspired us to develop a targeted cation exchange technology to remove NDMA precursors. In this study, we tested the removal of two representative NDMA precursors, dimethylamine(DMA) and ranitidine(RNTD), by strong acidic cation exchange resin. The results showed that pH greatly affected the exchange efficiency, with high removal(DMA 78% and RNTD 94%) observed at pH pk_a-1 when the molar ratio of exchange capacity to precursor was 4. The exchange order was obtained as follows: Ca~(2+) Mg~(2+) RNTD~+ K~+ DMA~+ NH_4~+ Na~+. The partition coefficient of DMA~+to Na~+was 1.41 ± 0.26, while that of RNTD~+to Na~+was 12.1 ± 1.9. The pseudo second-order equation fitted the cation exchange kinetics well. Bivalent inorganic cations such as Ca~(2+)were found to have a notable effect on NA precursor removal in softening column test. Besides DMA and RNTD, cation exchange process also worked well for removing other 7 model NDMA precursors. Overall, NDMA precursor removal can be an added benefit of making use of cation exchange water softening processes.