纳米Al13的分离方法及混凝效果动态过程的研究

以相同Al13含量、不同浓度的PAC为原料,利用乙醇-丙酮混合溶剂法、SO4^2-／Ba^2 沉淀置换法以及柱层析法分离提纯纳米Al13形态,同时利用Al-Ferron逐时络合比色法、^27Al-NMR等多种现代分析手段进行分析鉴定,比较其分离效果,并采用烧杯实验法和透光率脉动检测技术对Al13形态以及PAC、AlCl3的絮凝效果及絮凝过程中絮集物形成和增长的变化差异作了对比性研究．实验结果表明,乙醇．丙酮混合溶剂法对Al13分离纯化效果最好,分离所得Al13平均粒径大,聚合程度高．柱层析法受柱体积的影响只对低浓度的PAC有较好的分离效果;SO4^2-／Ba^2 沉淀置换法虽具有较好的分离效果,但分离过程有其他杂质离子的加入,影响到产品品质．混凝效果和动态实验结果表明,Al13形态是在絮凝过程中起电中和作用的主要形态,具有较强的除浊及脱色能力,在混凝过程中当絮体受到剪切力的破坏时Al13形态比PAC和AlCl3具有更强重新絮凝的能力．     

聚硅氯化铝(PASiC)混凝剂的特性及絮凝动态过程

 采用共聚与复合两种制备工艺,分别制备出具有不同碱化度(B)和不同Al/Si摩尔比系列的商用聚硅氯化铝(PASiC)混凝剂,并分别采用颗粒粒径测定方法和流动电流(SC)测定技术研究比较了PASiC和聚合氯化铝(PAC)混凝剂的颗粒大小、电动特性和凝聚絮凝动态过程.结果表明,Al/Si摩尔比、B值和制备工艺影响PASiC的聚合和带电特性.Al/Si摩尔比越小和B值越大,PASiC的颗粒就越大;在相同的B值下,PASiC较PAC具有更大的颗粒粒径.PASiC的电中和能力较PAC有所下降,且Al/Si摩尔比越小,PASiC的电中和能力下降越多;与PAC相比,PASiC具有更快的凝聚絮凝速度和形成更大的絮体;且Al/Si摩尔比越小,PASiC形成的絮体就越大.     

聚合氯化铝中Alb形态去除腐殖酸的效果及机制研究

Alb形态[Al12AlO4(OH)247+]是聚合氯化铝(polyaluminiurn chloride,PAC)水解-聚合作用中形成的一种粒度小、所带正电荷多、聚集程度高及分子量大的多核羟基配合物.本试验采用乙醇.丙酮混合沉淀法分离PAC溶液中各种铝形态,提纯出Alb形态(Alb絮凝剂).研究投加量、pH及无机离子对Alb絮凝剂处理腐殖酸模拟水样絮凝效果的影响,并利用光散射颗粒分析仪(PDA2000)测定Alb絮凝剂对腐殖酸絮凝过程中絮体的形成与增长过程的动态变化,结合絮体的Zeta电位,对Alb絮凝剂的絮凝机制进行了初步探讨.结果表明,当投加量为4.3～6.3 ms/L、pH值为3.0～6.0时,Alb絮凝剂处理腐殖酸模拟水样达到最佳絮凝效果;NH4+、SiO32-、H2PO4-的存在明显抑制其絮凝性能.絮凝动力学过程和絮体Zeta电位表明,Alb絮凝剂在水处理中主要是通过电中和作用和吸附网捕卷扫作用共同起絮凝作用的.     

聚合氯化铝中Alb形态去除腐殖酸的效果及机制研究

Al_b形态［Al₁₂AlO₄(OH)₂₄⁷⁺］是聚合氯化铝（polyaluminium chloride, PAC）水解-聚合作用中形成的一种粒度小、所带正电荷多、聚集程度高及分子量大的多核羟基配合物.本试验采用乙醇-丙酮混合沉淀法分离PAC溶液中各种铝形态,提纯出Al_b形态（Al_b絮凝剂）.研究投加量、pH及无机离子对Al_b絮凝剂处理腐殖酸模拟水样絮凝效果的影响,并利用光散射颗粒分析仪（PDA2000）测定Al_b絮凝剂对腐殖酸絮凝过程中絮体的形成与增长过程的动态变化,结合絮体的Zeta电位,对Al_b絮凝剂的絮凝机制进行了初步探讨.结果表明,当投加量为4.3～6.3 mg/L、pH值为3.0～6.0时,Al_b絮凝剂处理腐殖酸模拟水样达到最佳絮凝效果;NH⁺₄、SiO^2-₃、H₂PO^-₄的存在明显抑制其絮凝性能.絮凝动力学过程和絮体Zeta电位表明,Al_b絮凝剂在水处理中主要是通过电中和作用和吸附网捕卷扫作用共同起絮凝作用的.     

Al_b形态处理模拟染料废水的效果及机制研究

采用乙醇-丙酮混合沉淀法分离聚合氯化铝(PAC)溶液中的Alb形态.通过对吸光度和Zeta电位的测定,研究了Alb形态的投加量和溶液pH对分散黄棕和直接紫2种模拟染料废水脱色效果的影响,并将其与PAC进行比较.利用光散射颗粒分析仪(PDA2000)和Mastersizer2000型激光粒度仪在线测定絮体粒径的变化情况,结合絮体的Zeta电位,对Alb形态的絮凝机制进行探讨.结果表明,与PAC比较,Alb形态处理模拟染料废水的最佳pH值范围较宽,在实验条件下,Alb形态形成的絮体的密实性较高,沉降性能较好,恢复能力较强.     

聚合氯化铝中Al_(13)形态水解稳定性的研究

采用聚丙烯酰胺凝胶柱层析法分离纯化聚合氯化铝(PAC)中的Al13形态,并采用Al-Ferron逐时络合比色法对比研究了Al13形态、PAC和Al13三种样品水解稳定性。研究结果表明Al13形态无论是对于稀释倍数、介质的pH值和水解时间都具有较高的水解稳定性,是给水和废水处理中的一种较为有效的Al形态。     

复合生物絮凝剂CBF-1的絮凝作用机理研究

采取PAC+絮凝剂的复配方式开展高岭土悬浊液烧杯实验,考察了复合生物絮凝剂CBF-1、CBF-1溶解物及微生物絮凝剂MBF8的絮凝特性,并借助iPDA仪分析和扫描电镜、光学显微镜观察等手段,比较分析了絮凝过程及絮体特性的差异.结果表明,各复配絮凝的浊度去除效果排序为CBF-1＞ CBF-1溶解物＞MBF8,CBF-1投加量1 mg·L-1时,浊度去除率可达到97.5％;絮体强度排序为CBF-1＞ CBF-1溶解物＞MBF8,絮体恢复因子排序为MBF8＞CBF-1溶解物＞CBF-1,絮体大小排序为CBF-1＞ CBF-1溶解物＞MBF8.单独投加PAC或投加PAC+MBF8的情况下,形成的絮体形态相对规整、密实;投加PAC+ CBF-1溶解物或投加PAC+ CBF-1形成的絮体则相对无序、疏松,CBF-1作用下絮体大、沉降快.CBF-1中高电荷MBF8组分及大分子羧甲基纤维素、羧甲基多聚糖等组分具有强的电荷中和与桥联协同增效作用;CBF-1还含有纤维素、木质素等大分子量且带多种官能团的不溶性组分,在桥联和吸附过程中也起着重要作用.     

PAC与PDMDAAC复合絮凝剂中铝的形态分布

以具有不同碱化度(B)的聚合氯化铝(PAC)絮凝剂和具有不同黏度(h)的聚二甲基二烯丙基氯化铵(PDMDAAC)絮凝剂为原料制备出了系列PAC-PDMDAAC复合絮凝剂,分别采用Al-Ferron逐时络合比色法和27Al-NMR法比较研究了PAC-PDMDAAC复合絮凝剂与PAC絮凝剂中铝的形态分布,探讨了PAC的B值、PDMDAAC的含量(P%)和h对复合絮凝剂中铝的形态分布的影响.结果表明,PDMDAAC与PAC之间发生了一定的相互作用,表现为PAC-PDMDAAC复合絮凝剂中铝的各种形态的含量与PAC中铝的各种形态含量的不同,且随PDMDAAC的P%、h和PAC的B值变化而发生变化,这种变化势必影响其絮凝效果.仅从具有良好净水效果的Alb组分和Al¹³组分的含量高低来判断,P=10%的复合絮凝剂应具有良好的絮凝效果.处理黄河水的絮凝效果初步证明了该推断的正确性.     

微生物絮凝剂与聚合氯化铝复配的响应面优化

采用响应面分析法(RSM)对多粘类芽孢杆菌(GA1)所产絮凝剂(MBFGA1)与聚合氯化铝(PAC)配合处理高岭土悬浊液的过程进行了优化.设定的5 个影响因子分别为MBFGA1 投加量、PAC 投加量、pH 值、CaCl2 投加量、快搅速度.2 个响应值为絮凝率和絮体粒径.响应面实验分别拟合出了关于絮凝率和絮体粒径的二次模型,决定系数(R2)分别为0.7449 和0.8029,表明拟合情况良好.根据2 个响应值的分布情况,推算出最适粒径为0.7mm.同时,以絮凝率100%、絮体粒径0.7mm 为目标值,确定了最佳复配絮凝条件: MBFGA1 99.75mg/L, PAC121mg/L, pH 7.3, CaCl2 27mg/L, 快搅速度163r/min.通过分析比较, 发现PAC 在改变胶体表面电位使其脱稳聚沉方面有较强的能力,有利于MBFGA1 在絮凝后期吸附架桥作用的发挥.对提高絮凝效果、降低MBFGA1 运行成本具有很好的作用.     

絮凝方式对藻类絮体形态、强度及气浮的影响

 采用聚合氯化铝(PAC)作为混凝剂,利用混凝-气浮法处理含有较高浓度铜绿微囊藻(MA)的富藻水,在恒速絮凝和降速絮凝2 种方式下,研究PAC-MA 絮体的形态及强度对气浮的影响.结果表明,在PAC 投加量及能耗相同的条件下,采用降速絮凝比恒速絮凝处理效果更好.在PAC 投加量(以Al₂O₃ 计)为5.6 mg/L、快速混合搅拌强度(G)和时间分别为500s^-1 和1min、2 级降速絮凝G 值分别为100s^-1 和20s^-1、回流比为10%条件下,当絮凝时间为6~10min 时处理效果较好,最佳絮凝时间为8min;不同的絮凝方式对PAC-MA 絮体形态及强度有着显著影响,2 种絮凝方式形成的絮体形态相似时,降速絮凝形成的絮体强度更大;絮体的形态和强度共同影响气浮处理效果.     

Purification and characterization of Al13 species in coagulant polyaluminum chloride

Nano-Al₁₃ was separated and purified by four methods to investigate its characteristic, and was analyzed by Al-Ferron timed complexation spectrophotometer,²⁷ Al-NMR (nuclear magnetic resonance), and transmission electron microscopy (TEM). Coagulation efficiency of nano-Al₁₃, polyaluminum chloride (PAC), and AlCl₃ in synthetic water were also investigated by jar test. The dynamic process and aggregation state of kaolin suspensions coagulating with nano-Al₁₃, PAC, and AlCl₃ were also investigated. The experimental results indicated that the efficiency of gel column chromatography method was the highest for separating PAC solution with low Al concentration. Ethanol and acetone method was simple and could separated PAC solution with different Al concentrations, while silicon alkylation white block column chromatography method could separate PAC solution only with low Al concentration. The SO₄²−/Ba²⁺ displacement method could separate PAC solution with high Al concentration, but extra inorganic cation and anion could be introduced into the solution during the separation. The coagulation efficiency and dynamic experimental results showed that nano- Al₁₃ with a high positive-charged species was the main species of electric neutralization in coagulation process, and it could reduce the turbidity and increase the effective particles collision rate efficiently in coagulation process. Its coagulation speed and the particle size of coagulant formed were of greatest value in this study.     

高Al13纳米聚合氯化铝的结构表征及混凝效果

采用AlCl36H2O和Na2CO3制备了聚合氯化铝(PAC),并采用SO42-/Ba2+沉淀-置换法分离提纯了其中的纳米Al13形态,应用27Al-NMR和XRD等现代实验技术对其中的Al13形态进行了分析表征,27Al-NMR结果表明,分离提纯后样品中的Al13含量明显高于PAC,XRD结果表明,Al13的衍射峰出现在2q角为5~25之间;混凝烧杯实验表明,纳米级PAC较传统的混凝剂AlCl3、Al2(SO4)3和PAC具有更好的除浊、脱色效果.     

Interference of iron as a coagulant on MIB removal by powdered activated carbon adsorption for low turbidity waters

Powered activated carbon (PAC) is widely used in water treatment plants to minimize odors in drinking water. This study investigated the removal of 2-methylisoborneol (MIB) by PAC adsorption, combined with coagulation using iron as a coagulant. The adsorption and coagulation process were studied through different case scenarios of jar tests. The analysis evaluated the effect of PAC dosing in the liquid phase immediately before or after the coagulant addition. Ferric sulphate was used as the coagulant with dosages from 10 to 30 mg/L, and PAC dosages varied from 10 to 40 mg/L. The highest MIB removal efficiency (about 70%) was achieved without the coagulant addition and with the highest PAC dosage (40 mg/L). Lower MIB removal efficiencies were observed in the presence of coagulant, showing a clear interference of the iron precipitate or coagulant in the adsorption process. The degree of interference of the coagulation process in the MIB removal was proportional to the ratio of ferric hydroxide mass to the PAC mass. For both cases of PAC dosing, upstream and downstream of the coagulant injection point, the MIB removal efficiency was similar. However, MIB removal efficiency was 15% lower when compared with experiments without the coagulant application. This interference in the MIB adsorption occurs potentially because the coagulant coats the surface of the carbon and interferes with the MIB coming in contact with the carbon’s surface and pores. This constraint requires an increase of the PAC dosage to provide the same efficiency observed without coagulation.     

Preparation and coagulation efficiency of polyaluminium ferric silicate chloride composite coagulant from wastewater of high-purity graphite production

The aim of the present work was to produce a polyaluminium ferric silicate chloride (PAFSiC) coagulant from acidic and alkaline wastewater of purifying graphite by roasting, and subsequently to evaluate coagulation efficiency of the reagent by treating surface water from the Yellow River as well as municipal wastewater in comparison with the conventional coagulant polyaluminium chloride (PAC). The PAFSiC coagulant was prepared by co-polymerization. The effects of (Al+Fe)/Si molar ratio, OH/(Al+Fe) molar ratio (i.e., value), coagulant dosage and pH value of test suspension on the coagulation behavior of FAFSiC and the stability of the PAFSiC were also examined. Results showed that PAFSiC performed more efficiently than PAC in removing turbidity, chemical oxygen demand (COD), and total phosphate (TP). The PAFSiC with a value of 2.0 and (Al+Fe)/Si ratio of 5 (PAFSiC 2.0/5) showed excellent coagulation effect for both turbidity and COD, while PAFSiC 1.0/5 was the best for TP. The optimum coagulation pH range of PAFSiC 2.0/5 was 5.0–9.0, slightly wider than that of PAC (6.0–8.0). The process can be easily incorporated into high-purity graphite production plants, thereby reducing wastewater pollution and producing a valuable coagulant.     

强化混凝与超滤组合工艺净化湘江水——采用不同混凝剂的比较

采用强化混凝-超滤组合工艺对湘江水进行了净化研究,通过加入不同的混凝剂[Al₂(SO₄)3·18H2O、FeCl₃]以及粉末活性炭(PAC),比较了三者对于湘江水的处理效果和对膜过滤性能的影响.结果表明,混凝剂的选择与用量对水中污染物质的去除和膜过滤性能有很大的影响.经过组合工艺处理后,系统出水的浊度小于0.1NTU,TOC小于2mg/L,铁、锰的含量低于0.1mg/L.     

混凝-吸附处理黄河水及对氯消毒中氯衰减的影响

选用2种无机高分子混凝剂聚合氯化铁(PFC)和聚合氯化铝(PAC)处理黄河水,考察了混凝剂的投加量对浊度、UV254、DOC和高锰酸盐指数的去除效果,并结合混凝出水的Zeta电位分析其混凝机制.选择粉末活性炭与混凝联用,研究了混凝剂和吸附剂投加量以及二者的投加顺序对有机物去除效果的影响,并对混凝吸附后出水进行加氯消毒,考察水中残余氯随时间的变化.结果表明,2种混凝剂均有较高的浊度去除率(﹥90%).PAC对UV254、高锰酸盐指数和DOC的去除率分别为29.2%、26.1%和27.9%;PFC对三者的去除率分别为32.3%、23.3%和32.9%.PAC在混凝过程中,电中和作用占主导地位;PFC在混凝过程中,吸附架桥和电中和同时发挥作用.混凝-吸附联用处理黄河水样时,有机物的去除率随混凝剂和吸附剂投加量的增加而升高.先混凝后吸附工艺对UV254和DOC的去除效果优于先吸附后混凝工艺.先使用PAC混凝后吸附对UV254和DOC的去除率分别为95.2%和99.9%;对于PFC,先混凝后吸附对UV254和DOC的去除率分别为90.1%和99.9%.但是先投加粉末活性炭能提高矾花的沉降性能,且处理出水在保持持续消毒效果方面优于前者.     

混凝过程中铝与聚合铝水解形态的动力学转化及其稳定性

采用Ｆｅｒｒｏｎ逐时络合比色法，并结合电泳测定研究了混凝过程中氯化铝和聚合氯化铝的水解形态动力学转化及稳定性。结果表明，ＡＣ在混凝过程中所形成的水解形态完全不同于ＰＡＣ的预制水解聚合形态，其电荷及分子量均明显低于聚合铝且不稳定，ＡＣ随混凝条件如投加浓度、ＰＨ和混合时间而变，而ＰＡＣ－２５水解聚合形态不随混凝条件变化，始终保持稳定状态，ＡＣ水解沉淀规律与理论计算相符并形成无定形Ａｌ（ＯＨ）３絮体颗粒     

UF膜与混凝粉末活性炭联用处理微污染原水

采用混凝、粉末活性炭和UF膜分离的联用技术对黄浦江原水进行试验 ,结果表明 ,混凝、粉末活性炭可有效地去除溶解性有机物 .混凝处理主要去除大分子量的有机物 ,粉末活性炭主要去除低分子量的有机物 .混凝、粉末活性炭还能有效地去除三氯甲烷生成潜能 (THMFP) ,对于低分子量的THMFP ,混凝去除效果很差 ,而粉末活性炭去除很好 .试验还表明 ,混凝、粉末活性炭还可大大降低膜的滤饼层阻力 ,当混凝剂投加量为 4mg/L时 ,膜的滤饼层阻力最小 .     

壳聚糖助凝对PAC混凝过程的影响

以聚合氯化铝(PAC)为絮凝剂,壳聚糖(CTS)为助凝剂在Taylor-Couette反应器中进行混凝实验.采用粒子成像速度场仪(PIV)研究了不同内筒转速(水力学条件)下 CTS 助凝对PAC混凝过程中絮体形态和浊度的影响.结果表明,添加CTS后,相应的混凝效果都得到提高,但与单独使用PAC时产生的变化趋势一致,说明适宜的化学条件下,水力条件是制约混凝效果的关键因素;且添加助凝剂有助于降低混凝过程对流体力学条件的依赖性,提高混凝的稳定性.