Hierarchical Reduced Graphene Oxide-MnO_(2)@Polypyrrole Coaxial Nanotube Composite Hydrogel as a Potential Adsorbent for Cr(Ⅵ)Removal

A hierarchical reduced graphene oxide-MnO_(2)@polypyrrole coaxial nanotube composite hydrogel was prepared via oxidative polymerization of pyrrole in the presence of MnO_(2)nanotubes,followed by the hydrothermal treatment of graphene oxide and MnO_(2)@polypyrrole coaxial nanotubes.The stable composite hydrogel with a hierarchical network was composed of one-dimensional MnO_(2)@polypyrrole coaxial nanotube and two-dimensional graphene nanosheet and characterized by scanning electron microscope,Fourier transform infrared spectroscopy,X-ray diffraction,Brunauer-Emmett-Teller surface,and X-ray photoelectron spectroscopy measurements.The composite hydrogel can be used as an efficient adsorbent for Cr(Ⅵ)removal due to the synergistic interaction between graphene and MnO_(2)@polypyrrole and the hierarchical structure of the hydrogel.Moreover,the composite hydrogel is easily separated because of its stable monolith,and it is reusable(76.8%of removal ability remaining after five adsorption-desorption cycles).The simple fabrication and cost-effective separation process together with the excellent absorption performance endow the composite hydrogel with great potential for practical wastewater treatment.

Efficient removal of Al(Ⅲ)and P507 from high concentration MgCl_(2)solution based on in-situ reaction strategy

For a highly efficient recycling of a wastewater containing a high concentration of MgCl_(2),Al(Ⅲ)and P507 were scheduled to be removed in advance.In this study,the in-situ removal of Al(Ⅲ)and P507 from a high concentration MgCl_(2)solution at different pH values and Al/P molar ratios was investigated.The results showed that P507 formed organic complexes of Al_(x)(OH)_y^(Z+)-P507 at pH of 2.0-4.0.At pH of 4.0-5.0,Al(Ⅲ)precipitated and transferred into Al(OH)_(3)with a flocculent amorphous morphology.Active sites on the Al(OH)_(3)surface enhanced the removal efficiency of P507.At pH of 6.0-6.5,Al(Ⅲ)and Mg(Ⅱ)formed layered crystalline Al(OH)_(3)and MgAl_(2)(OH)_(8with)small pore channels and fewer active sites,resulting in a reduced removal efficiency of P507.When the Al/P molar ratio exceeded 13 and the pH was between 4.0 and 5.0,the removal rates of both Al(Ⅲ)and P507 were higher than98%,while the concentration loss of Mg(Ⅱ)was only 0.2%-0.9%.

TiO2-PES Fibrous Composite Material for Ammonia Removal Using UV-A Photocatalyst

This study focused on the development and characterization of TiO2-PES composite fibers with varying TiO2 loading amounts using a phase inversion process. The resulting composite fibers exhibited a sponge-like structure with embedded TiO2 nanoparticles within a polymer matrix. Their photocatalytic performance for ammonia removal from aqueous solutions under UV-A light exposure was thoroughly investigated. The findings revealed that PeTi8 composite fibers displayed superior adsorption capacity compared to other samples. Moreover, the study explored the impact of pH, light intensity, and catalyst dosage on the photocatalytic degradation of ammonia. Adsorption equilibrium isotherms closely followed the Langmuir model, with the results indicating a correlation between qm values of 2.49 mg/g and the porous structure of the adsorbents. The research underscored the efficacy of TiO2 composite fibers in the photocatalytic removal of aqueous under UV-A light. Notably, increasing the distance between the photocatalyst and the light source resulted in de-creased hydroxyl radical concentration, influencing photocatalytic efficiency. These findings contribute to our understanding of TiO2 composite fibers as promising photocatalysts for ammonia removal in water treatment applications.

功能化氮杂环卡宾聚合树脂对Cu^(2+)的吸附研究

该研究制备了功能化氮杂环卡宾聚合树脂(PNO),旨在去除废水中Cu^(2+);基于静态和动态吸附实验,研究了PNO对废水中Cu^(2+)的吸附效果。结果表明:PNO对Cu^(2+)的最佳吸附条件为吸附剂投加量100 mg、吸附时间30 min、pH值4.0~5.9、温度298 K、转速150 r/min,最大吸附量为51.55 mg/g。PNO对Cu^(2+)的吸附过程符合Langmuir、Freundlich等温吸附模型和准二级动力学模型。动态吸附量随柱高增加、流速降低和进水Cu^(2+)浓度增加而增大。使用Thomas和Bohart-Adams模型拟合,相关系数R^(2)均大于0.92,预测值与实验值相符。经过5次静态吸附-解吸和3次动态循环再生后,PNO对Cu^(2+)的去除率仍达到第一次循环的96%以上,去除效果和再生性能良好。PNO对含铜废水高效处理具有广泛的应用前景。

磁性三乙烯四胺/单宁树脂对Cu^(2+)、Pb^(2+)的吸附性能研究

利用曼尼希反应将三乙烯四胺(TETA)固化到单宁(TA)基体表面,热溶剂法制得磁性单宁基树脂(MTETA-TA)。通过红外光谱、扫描电镜、比表面积及孔隙度分析仪、振动样品磁强计对M-TETA-TA进行表征,表明M-TETA-TA具有疏水性强、比表面积大的优势,Fe_(3)O_(4)的成功引入有效解决吸附剂回收难的问题。对含Cu^(^(2+))、Pb^(2+)废水溶液进行了静态吸附实验,探讨了其对金属的吸附性能。在pH为5的酸性条件下,吸附效果较好;Cu^(^(2+))和Pb^(2+)吸附动力学均符合准二级反应动力学模型,主要为化学吸附;Cu^(^(2+))的吸附等温线符合Langmuir模型,属单层吸附,理论吸附最大值为173.33 mg·g^(-1);Pb^(2+)的吸附等温线符合Sips模型,属多层吸附,理论吸附最大值为217.14 mg·g^(-1)。推测M-TETA-TA对Pb^(2+)的吸附除了螯合、氧化还原等化学反应,还存在静电和离子交换作用,氨基和酚羟基为主要参与官能团。循环再生5次后,仍有较高的吸附性能和磁性强度。

Salt-assisted Synthesis of Hollow Bi_2WO_6 Microspheres with Superior Photocatalytic Activity for NO Removal

Hollow Bi2WO6 microspheres are successfully synthesized by a facile ultrasonic spray pyrolysis（USP） method using NaCl as a salt template.The as-prepared hollow microspheres assembled as nanoplates with dimensions of approximately 41-148 nm and are dispersed with non-uniform pores on the template surface.By swapping the salt template with KC1 or Na2SO4,different morphologies of Bi2WO6 are obtained.The experimental results demonstrate that NaCl plays a key role on the formation of Bi2WO6 with hollow structures.The specific growth mechanism of hollow microspheres was studied in detail.The Bi2WO6 hollow microspheres exhibit an excellent photocatalytic efficiency for NO removal under solar light irradiation,which is 1.73 times higher than for the Bi2WO6 obtained in the absence of any salt template.This enhancement can be ascribed to the simultaneous improvement on the surface area and visible light-harvesting ability from the hollow structures.Electron spin resonance（ESR） results suggest that both radicals of ·OH and ·O2^- are involved in the photocatalytic process over the BWO-NaCl sample.The production of ·O2^- radicals offers better durability for NO removal.

ZIF-8/PEO杂化泡沫对TC和Cu^(2+)吸附研究

以提高金属有机骨架ZIF-8水处理中可回收性为目标,利用聚氧化乙烯PEO作为致孔剂,采用冰模板-冷冻干燥法制备金属有机骨架杂化泡沫ZIF-8/PEO,利用XRD、SEM、TG-DSC和N2吸附-脱附等表征手段,分析ZIF-8/PEO杂化泡沫的理化性能,研究ZIF-8/PEO对四环素TC和铜离子Cu^(2+)吸附性能及吸附机理。试验结果表明:ZIF-8/PEO形成了更加规则的网状结构且具有良好的机械强度和吸附性能。在吸附时间12 h,pH 7,吸附剂投加量40 mg,TC和Cu^(2+)初始浓度均为30 mg/L的最佳条件下,ZIF-8/PEO对TC和Cu^(2+)的吸附容量为107.55 mg/g和107.81 mg/g;等温吸附过程符合Langmuir模型,动力学过程符合拟二级动力学模型,ZIF-8/PEO吸附TC,Cu^(2+)属于自发、放热、趋于有序的过程。在循环吸附7次后,ZIF-8/PEO吸附剂对TC和Cu^(2+)的去除率仍在70%以上。

不同质量浓度Cu^(2+)和Ag^(+)对大麦成熟胚组培特性的影响

【目的】探究不同质量浓度Cu^(2+)和Ag^(+)对大麦成熟胚组培特性的影响。【方法】以Bowman、北青7号和光头大麦的成熟胚为材料,研究不同质量浓度Cu^(2+)和Ag^(+)对大麦成熟胚愈伤诱导率、长根率、长芽率、褐化率、绿化率、再分化率和愈伤湿质量的影响。【结果】Bowman、北青7号和光头大麦成熟胚的7种组培特性间存在不同程度差异。与对照相比,0.75 mg/L Cu^(2+)可减少10.43%的成熟胚长根、7.48%的成熟胚长芽、8.24%的愈伤组织褐化、20.74 mg的愈伤湿质量;4.00 mg/L Ag^(+)可提高6.47%的愈伤组织诱导率,可减少9.08%的成熟胚长根、7.96%的成熟胚长芽和9.67%的愈伤褐化;0.75 mg/L Cu^(2+)和4.00 mg/L Ag^(+)对愈伤细胞转绿、愈伤增殖和再分化均无抑制。【结论】适宜质量浓度的Cu^(2+)和Ag^(+)可有效抑制大麦成熟胚长根、长芽和愈伤组织褐化,Ag+还可有效提高愈伤诱导率;在基于MS培养基的大麦成熟胚愈伤组织诱导和再分化培养中,Cu^(2+)和Ag^(+)的适宜质量浓度分别为0.75和4.00 mg/L。研究结果可为构建大麦成熟胚的愈伤诱导及其再分化技术体系提供理论支持。

钠化污泥生物炭复合凹凸棒石对水体中Cu^(2+)的吸附效果研究

含铜废水严重威胁人体健康和环境安全,利用废弃污泥和凹凸棒石制备了钠化污泥生物炭复合凹凸棒石材料,并将其用于含Cu^(2+)废水的处理。利用SEM、XRD及FT-IR对材料的结构和表面性质进行了分析表征,复合材料表面的含氧官能团的络合或C=C键的Π电子作用是吸附重金属的主要机制。研究了复合材料对Cu^(2+)的吸附效果和机理,结果表明,污泥/凹凸棒石质量比2∶1,pH=5,添加量为1.5 g/L,Cu^(2+)初始浓度4 mg/L条件下,材料对Cu^(2+)有最大的吸附容量为3.339 mg/g。吸附过程更好地拟合了准二级动力学模型和Langmuir吸附等温式,表明材料对Cu^(2+)的吸附是单分子层化学吸附。利用响应面分析法预测,pH值为5.04,吸附剂添加量1.16 g/L,Cu^(2+)初始浓度3.60 mg/L是最佳吸附条件。钠化污泥生物炭复合凹凸棒石在实际含铜废水处理中是一种极具潜力的吸附剂。

Fe^(2+)、Cu^(2+)诱导工艺对柞木表板颜色变化规律的影响

木材中的木质素、抽提物等物质具有能与金属盐溶液产生颜色反应的特性。利用这一特性以硫酸亚铁、硫酸铜溶液作为诱导剂,通过正交试验得到色差最大时的工艺参数,探究金属Fe^(2+)、Cu^(2+)的诱导剂质量分数、诱导时间、干燥时间、干燥温度对实木复合地板柞木表板颜色变化的影响。结果表明:Fe^(2+)、Cu^(2+)的诱导剂质量分数对柞木表板色彩色调的影响极为显著(F值分别为20.4453、8.8442);柞木表板的明度色品指数(L^(*))、红绿轴色品指数(a^(*))、黄蓝轴色品指数(b^(*))均随着Fe^(2+)、Cu^(2+)的诱导剂质量分数、诱导时间、干燥时间的增加而逐渐减少,总色差(ΔE^(*))逐渐增大,最大为31.53、9.90,表板色调逐渐偏暗、偏绿、偏蓝;随着干燥温度的增加,Fe^(2+)、Cu^(2+)诱导时的柞木表板总色差都逐渐减小。

UiO-66-NH_(2)的改性及其吸附Cu^(2+)性能

通过溶剂热法合成了锆基金属有机框架材料中的UiO-66-NH_(2),用多巴胺(DA)对其进行后合成改性,制备了UiO-66-NH_(2)/PDA复合材料,用于去除重金属Cu^(2+)。探究了pH、初始ρ(Cu^(2+))、接触时间和温度对吸附过程的影响,结果表明,Cu^(2+)的吸附动力学和等温线数据分别符合准二级和Langmuir模型,吸附过程为自发吸热反应;初始ρ(Cu^(2+))=50 mg/L,pH=5.5,t<30 min,Cu^(2+)去除率为93%。

用于吸附养殖尾水中Cu^(2+)的温度敏感型淀粉基水凝胶制备及性能分析

为了快速移除水产养殖尾水中的铜离子(Cu^(2+)),合成了一种新型温度敏感多糖基水凝胶,以具有结构和性能优势的2-羟基-3-异丙氧基丙基淀粉醚(HIPS)和羧甲基淀粉钠(CMS)为原料,以乙二醇二缩水甘油醚(EDGE)和CaCl 2为交联剂,通过形成共价键和离子键的混合交联方式制备具有温度敏感性能的HIPS/CMS复合凝胶,利用傅里叶转换红外光谱(FT-IR)、扫描电镜(SEM)对复合凝胶的结构和内部形貌进行表征,研究复合凝胶的温度敏感性能,并探究了复合凝胶对水产养殖尾水中Cu^(2+)的吸附效果。结果表明:HIPS/CMS复合凝胶具有优异的温度敏感性能,当温度高于其体积相转变温度(VPTT,34.1℃)时,复合凝胶体积明显收缩,溶胀率从62.1倍下降至33.6倍;HIPS/CMS复合凝胶对水产养殖尾水中Cu^(2+)具有良好的吸附性能,最大吸附量可达25.2 mg/g;复合凝胶对Cu^(2+)吸附过程符合Langmuir吸附模型,属于单分子层化学吸附;利用该复合凝胶的温度敏感性能,可实现HIPS/CMS复合凝胶的回收再利用,并且经5次吸附-解吸循环后吸附量仍可达15.1 mg/g。研究表明,本研究制备的HIPS/CMS复合凝胶对养殖尾水中的Cu^(2+)的去除效果较好且绿色环保,可以重复使用。

Cu^(2+)污染原状黄土的物化及结构特性

为制定环境保护和土壤污染防治和修复策略,以及为污染场地工程建设提供理论支撑,该文研究了Cu^(2+)对原状黄土物化特性及结构特性的影响。通过制备不同掺量的Cu^(2+)污染黄土试样,进行了粒径分布、CaCO_(3)含量和pH值的测定。利用扫描电镜和激光粒度仪获得试样的SEM图像和粉粒各粒径含量,并借助分形理论深入分析了Cu^(2+)对原状黄土微观结构的影响机理。对Cu^(2+)污染的原状黄土试样进行了压缩试验,并对试样的综合结构势进行了分析。结果表明,随着Cu^(2+)掺量的增大,黏粒含量表现为先增后减,再增再减的趋势,粉粒含量则表现为先减后增,再减再增,砂粒含量保持不变;CaCO_(3)的含量呈线性减小;pH值先迅速减小,后保持不变;污染黄土试样的综合结构势先增大后减小,之后再增大再减小。总体而言,重金属Cu^(2+)的掺入,导致土壤pH值降低,主要胶结物质碳酸钙被溶解,而又因黏粒之间的静电引力和范德华力,黏粒聚集体的形态和成分发生变化,从而影响了土体的密实度和结构强度。

两种磁性生物炭耦合Diaphorobacter sp.DFA4去除2,4-DFA和Cu^(2+)的特性

以橘子皮为原料,氯化铁、镍锰铁氧体为磁性介质,制备了氯化铁和镍锰铁氧体改性生物炭(分别记为FBC和MBC),重点考察FBC和MBC介导Diaphorobacter sp.DFA4耦合体系去除2,4-二氟苯胺(2,4-DFA)和Cu^(2+)的特性。结果表明:在0.5~2.0 g/L FBC/MBC的介导作用下,Diaphorobacter sp.DFA4对2,4-DFA和Cu^(2+)的去除效果明显提升。当2,4-DFA初始质量浓度为100~900 mg/L时,相比纯菌Diaphorobacter sp.DFA4培养体系,FBC和MBC介导耦合体系对2,4-DFA的降解强化倍数分别为2.24~4.04倍和1.96~4.71倍,Cu^(2+)去除率则分别由59.70%~69.95%提升至88.57%~93.20%和82.12%~88.20%。当pH为6.0~8.0时,较纯菌Diaphorobacter sp.DFA4培养体系,MBC、FBC介导耦合体系对2,4-DFA的去除率分别提高了15.35%~36.32%和22.43%~37.42%,对Cu^(2+)的去除率则分别提高了37.63%~42.34%和43.61%~47.83%;当盐度由0提高至4%时,两个耦合体系对2,4-DFA的去除率基本保持在85%及以上,而纯菌Diaphorobacter sp.DFA4培养体系对2,4-DFA的去除率则由77.98%降至55.19%。机理分析发现,耦合体系可诱导分泌更多的腐殖酸,且在偏碱条件下,FBC更有利于促使腐殖酸的分泌。

Removal of nitrogen and phosphorus in a combined A^2/O-BAF system with a short aerobic SRT

A bench-scale anaerobic/anoxic/aerobic process-biological aerated filter （A^2/O-BAF） combined system was carded out to treat wastewater with lower C/N and C/P ratios. The A^2/O process was operated in a short aerobic sludge retention time （SRT） for organic pollutants and phosphorus removal, and denitrification. The subsequent BAF process was mainly used for nitrification. The BAF effluent was partially returned to anoxic zone of the A^2/O process to provide electron acceptors for denitrification and anoxic P uptake. This unique system formed an environment for reproducing the denitdfying phosphate-accumulating organisms （DPAOs）. The ratio of DPAOs to phosphorus accumulating organisms （PAOs） could be maintained at 28% by optimizing the organic loads in the anaerobic zone and the nitrate loads into the anoxic zone in the A^2/O process. The aerobic phosphorus over-uptake and discharge of excess activated sludge was the main mechanism of phosphorus removal in the combined system. The aerobic SRT of the A^2/O process should meet the demands for the development of aerobic PAOs and the restraint on the nitrifiers growth, and the contact time in the aerobic zone of the A^2/O process should be longer than 30 min, which ensured efficient phosphorus removal in the combined system. The adequate BAF effluent return rates should be controlled with 1--4 mg/L nitrate nitrogen in the anoxic zone effluent of A^2/O process to achieve the optimal nitrogen and phosphorus removal efficiencies.

Removal of SO_2 and NO_x by Pulsed Corona Combined with in situ Ca(OH)2 Absorption

Removal of SO2 and NOx by pulsed corona combined with in situ alkali absorption was experimentally investigated.In the reactor,a plate-wire-plate combination is devised for generating pulsed corona and then alkaline absorbent slurries were introduced into the reactor by a continuous band conveying system to capture the gaseous reaction products.It was found that both SO2 and NO could be removed by corona combined with in situ alkali absorption.The removal of SO2 increased to 75%with the corona discharge,compared with 60%removal only with Ca(OH)2 absorption.About 40%removal of NO was reached by pulsed corona combined with in situ Ca(OH)2 absorption.It was found that SO2 and NO in the gas stream are oxidized to SO3 and NO2 by pulsed corona respectively,and then absorbed by the alkali in the reactor.The removals of SO2 as well as NO were higher with Ca(OH)2 as the absorbent,compared with using CaCO3 or ZnO.

Simultaneous removal of NO and SO_2 from dry gas stream using non-thermal plasma

In order to investigate the feasibility of sequential removal NO and SO2 using non-thermal plasma and adsorbent simultaneously, the removal of NO and SO2 from dry gas stream （NO/SO2/N2/O2） with very little O2 using non-thermal plasma was investigated using a coaxial dielectric barrier discharge. Comparative experiments were carried out in the dry gas stream with and without Ar respectively at O2 concentration of 0.1%. The results showed that NO could be removed remarkably and it would be enhanced in the presence of Ar in the dry gas stream. It seems that SO2 could not be removed unless there is Ar in the dry gas stream. The mechanism of removal of NO and SO2 in the dry gas stream was discussed.

Cd^(2+) removal from wastewater by sulfate reducing bacteria with an anaerobic fluidized bed reactor

A process of treatment for containing Cd 2+ wastewater by sulfate reducing bacteria with upflow anaerobic fluidized bed reactor has been studied. When the concentration of COD and Cd 2+ in the influent were 270 5mg/L and 100mg/L respectively and hydraulic retention time was 4 hours, the removal rate of COD and Cd 2+ were higher than 73 8% and 99 8% respectively. The reactor can treat as high as 1000mg/L of concentration of Cd 2+ . The highest removal velocity rate of Cd 2+ reached 2999 1mg/(L·d). And the possible relationship between sulfate reducing bacteria and methanogenic bacteria was discussed.

5-磷酸吡哆醛缩合罗丹明B席夫碱合成及对Cu^(2+)的识别研究

合成了吡哆醛-5-磷酸罗丹明B席夫碱.通过紫外-可见光光谱法研究了该化合物对Cu^(2+)的识别能力:在丙酮-水(体积比1∶1)混合体系中,加入Cu^(2+)后,在526 nm处出现了一个新的吸收峰,并且随着Cu^(2+)的加入,吸收强度逐渐增强.在(0.25~10)×10^(-6) mol/L的浓度范围内,检测结果呈现出良好的线性关系(R^(2)=0.9993),检测限为2.30×10^(-7) mol/L.

SO_2/Hg removal from flue gas by dry FGD

To study the mechanism of SO2 and Hg removal from flue gas, an experimental packed bed reactor was designed to simulate the dry FGD, where a mixture of lime and fly ash in ratio 1：3 w/w was used as the S02 and Hg sorbent, and steam at temperature of 100 ℃ was applied for activation of the sorbent, while the activation time set to 20 rain. The experimental factors including the SO2/Hg sorbent characteristics, 50% breakthrough time for SO2/Hg removal, sorbent packed bed depth and reaction temperature were investigated. The experimental results show that after steam activation, the BET specific surface area and specific pore volume increased from 37.8 to 45.5 m^2/g and from 0.42 to 0.51 cm^3/g, respectively. With activation of the sorbent by steam, the 50% breakthrough times of SO2 and Hg removal increased from 34 to 42 rain and from 23 to 45 rain, respectively. When the packed bed depth was increased from 5 to 25 ram. the 50% breakthrough times for Hg and S02 removal increased from 12 to 52 rain and from 6 to 47 rain, respectively. With the increase of the reaction temperature, the 50% breakthrough of SO2/Hg removal decreased accordingly. Steam activation can efficiently improve SO2/Hg removal simultaneously.