载银活性炭活化过硫酸钠降解酸性橙7

采用硝酸氧化的颗粒活性炭浸渍制备Ag/GAC活化剂,利用N₂吸附、 SEM、 FT-IR及XRD对Ag/GAC进行表征,得出Ag成功负载于颗粒活性炭上,并以Ag/GAC在常温常压下活化过硫酸钠(PS)产生硫酸根自由基(SO^－4 ·)降解偶氮染料酸性橙7(AO7). 考察了Ag负载量、 PS浓度、 Ag/GAC投加量、 初始pH对AO7降解效果的影响. 结果表明,当Ag负载量为12.7 mg ·g^-1、 n(PS) :n(AO7)为120 :1、 Ag/GAC投加量为1.0 g ·L^-1,降解180 min后AO7降解率达95.0%以上. 初始pH对Ag/GAC活化PS降解AO7有较大影响,pH为5.0时降解效果最优. 通过紫外可见光谱、 气相色谱-质谱(GC/MS)对AO7降解过程进行了探讨,在降解过程中AO7的偶氮键和萘环结构均被破坏,并检测出主要降解产物有邻苯二甲酸和乙酰苯.     

Investigation of the propensity of sulfide concentrates to spontaneous combustion in storage

Spontaneous combustion of sulfide concentrates can cause many serious problems during storage. In this study, two representative samples (sulfur-rich sulfide concentrate and iron-rich sulfide concentrate) were investigated for the self-heating behavior using the crossing-point temperature (CPT) method. The corresponding apparent activation energies were determined, 13.7366 kJ/mol for iron-rich sulfide concentrate and 21.3817 kJ/mol for sulfur-rich sulfide concentrate. Furthermore, the surface temperatures of sulfide concentrate stockpiles in different seasons were also measured by a thermal image apparatus. It was found the temperature for iron-rich sulfide concentrate stockpile was higher than that for rich-sulfur sulfide concentrate stockpile. These research results show iron-rich sulfide concentrate exhibits stronger propensity to spontaneous combustion than sulfur-rich sulfide concentrate. Particular attention should be paid to the fire hazard of iron-rich sulfide concentrate in daily safety check work. The combination of the CPT method with the infrared thermal image measurement provides a new approach for the risk assessment on the propensity of sulfide concentrates to spontaneous combustion during the production, storage and transportation. The useful data and experience achieved in this investigation can be also referenced in similar cases later.     

活化过硫酸盐对市政污泥调理效果的影响

常规污泥脱水技术只能将市政污泥含水率降到80%左右,难以满足日益严格的污泥处理处置要求.活化过硫酸盐产生硫酸根自由基SO4·-具有强氧化性,可用于破坏污泥的絮体结构.本研究利用Fe2+活化过硫酸钠(SPS)的方法进行污泥调理,以到达改善污泥的脱水性能的目的.结果表明,当Fe2+与S2O2-8投加量(以绝干污泥计)分别为25.88 mg·g-1、80 mg·g-1(Fe2+与S2O2-8摩尔比为1.1∶1)时,污泥毛细吸水时间CST和污泥比阻SRF降低率最大,滤液中蛋白质和多糖浓度达到最大.进一步的研究表明,污泥Zeta电位值由负向正变化,颗粒比表面积增大,絮体由密集的团状变成结构松散的层状结构,污泥脱水性能提高.     

可见光促有机物诱导铁还原的多相类芬顿体系强化效能与机制

近年来,亚铁离子活化过硫酸盐的类芬顿(Fe²⁺-PMS/PS)高级氧化技术发展日趋成熟,但因Fe³⁺无法还原导致反应停止的问题仍制约其大规模应用.结果发现,当把以双酚A（BPA）为代表的某些有机物与Fe³⁺和TiO₂混合,所形成的某种络合物可以拓宽TiO₂光响应范围捕获可见光,通过TiO₂将光生电子传递给Fe³⁺进行还原,从而实现Fe³⁺/Fe²⁺的无限循环.依据上述原理,构建了可见光下BPA-TiO₂-Fe³⁺-PS复合体系来降解BPA,并对其催化性能、催化机制和影响因素进行探讨.结果表明,该体系具有突出的催化性能,60 min内BPA(50 mg·L^-1)降解率达到93.1%,矿化度达到70%.同时验证该体系可以通过双酚A自生光电子还原Fe³⁺, 60 min还原得到的Fe²⁺稳...     

过硫酸钠缓释胶囊反应带修复苯胺污染地下水

针对有机污染地下水原位化学氧化修复中普遍存在的氧化剂过量使用、污染物反弹和二次污染问题,以苯胺（AN）为特征污染物,以活化过硫酸盐为氧化剂,采用硬脂酸为胶结剂,制备过硫酸钠（PS）和硫酸亚铁（FeSO₄）缓释胶囊,构建基于PS和FeSO₄缓释胶囊的可渗透反应屏障（PS-FeSO₄-PRB）,考查了缓释胶囊组分、地下水流速对PRB中活性物质释放和AN去除的影响.结果表明,当缓释胶囊中活性物质/硬脂酸为1/2,地下水流速为0.1mL/min时,48h后PRB中PS和Fe²⁺累计释放率分别为43.18%和14.98%.当PRB中FeSO₄/PS为1/9时,AN累计去除率达到95.37%,TOC累计去除率为57.07%.采用砂柱模拟AN污染地下水,比较了直接注射PS和FeSO₄与PS-FeSO₄-PRB两种处理方式的修复性能,4d内两者的AN累计去除率分别为35.22%和69.74%,TOC累计去除率分别为15.83%与14.88%.PS-FeSO₄-PRB修复效果明显高于直接注射处理.GC/MS分析表明,处理后产生了对苯醌、偶氮苯以及长链烷烃等产物,导致AN矿化率不高.pH值和Eh连续记录结果表明,PS-FeSO₄-PRB处理能够保持反应体系氧化还原电位和酸碱性的相对稳定.相比直接注射氧化剂,基于PS和FeSO₄-缓释胶囊的PRB处理中地下水的急性毒性更低,二次污染风险更小.     

MnFe2O4@HTC活化过硫酸盐体系除藻效能与机制

采用水热法和共沉淀法将MnFe₂O₄负载在水热炭（HTC）表面制备磁性MnFe₂O₄@HTC复合催化剂.采用SEM、XRD、BET、FTIR、XPS对催化剂进行表征,通过考察MnFe₂O₄/HTC负载比、过硫酸钠（PS）投加量、初始pH和不同化学体系对除藻效果的影响,探究无供氧条件下MnFe₂O₄@HTC活化PS体系除藻的效能.基于自由基屏蔽实验和XPS分析对MnFe₂O₄@HTC活化PS体系反应机制进行研究验证.结果表明,当初始藻浓度为1.4×10⁹个·L^-1（OD₆₈₀=0.14）,催化剂投加量为0.2 g·L^-1,PS投加量为0.4 g·L^-1,pH为6时,降解30 min,该体系除藻率可达到99%.在该体系中,MnFe₂O₄@HTC材料可将藻细胞吸附在材料表面,通过Mn、Fe的价态循环和HTC的协同效应反应催化PS产生空穴、¹O₂、·O₂^-、SO₄^-·和·OH多种氧化物质,使藻细胞破裂死亡.     

Bi-FeC2O4复合催化剂活化过硫酸盐降解罗丹明B

采用溶剂热法将Bi单质附着于草酸亚铁（FeO_x）上,制备了系列Bi-FeOx复合催化剂并用于活化过硫酸盐.通过X射线衍射仪（XRD）、傅里叶变换红外光谱仪（FT-IR）、扫描电子显微镜（SEM）、X射线光电子能谱仪（XPS）等表征方法对复合催化剂的结构、形貌和元素价态进行表征.以罗丹明B（RhB）为降解对象,研究了Bi-FeOx/过硫酸盐/可见光体系中Bi单质含量、催化剂投加量、pH及过硫酸盐浓度等因素对RhB的降解影响.在最佳条件下,反应5 min后,RhB的降解率高达99.8%.Bi的引入,使得复合催化剂增强了对可见光的吸收,提高了光生电子的传输效率,从而加速了对RhB的降解.     

紫外催化过硫酸盐深度处理垃圾焚烧厂渗滤液

为研究垃圾焚烧厂渗滤液生化出水的处理特性,对比了单独紫外(UV)体系、单独过硫酸盐(PS)体系以及紫外/过硫酸盐(UV/PS)体系深度处理垃圾渗滤液效果,发现UV/PS体系对渗滤液中有机污染物的去除效果较另外两体系的效果优异,因此采用UV/PS体系处理典型难降解有机物腐殖酸并考察体系的处理效能.在初始腐殖酸浓度为200mg/L、PS投加量为25mmol/L、初始pH值为4的条件下,UV₂₅₄最大去除率为89.62%,TOC最大去除率为76.17%.研究温度、初始pH值、药剂投加比例等因素对UV/PS工艺处理渗滤液的影响,结果表明,工艺处理效果良好,最优条件为温度为35℃、pH值为4、加药比为2、运行24h,COD的去除率最大为82.64%,TOC的最大处理效能为66.69%,同时该体系对色度的去除能力符合拟二级动力学方程.本文可为垃圾焚烧厂渗滤液深度处理提供数据依据.     

Oxidative degradation of phenol by sulfidated zero valent iron under aerobic conditions: The effect of oxalate and tripolyphosphate ligands

After adding either organic or inorganic ligands, sulfidated nano-zero-valent iron (SnZVI) was used for aerobic degradation of phenol, and the effect of the ligand species on oxidation performance was investigated. We found that SnZVI hardly degraded phenol in the absence of ligand addition. Ligands initiated and promoted the degradation of pollutants by SnZVI. The data herein show that a characteristic inorganic ligand, tripolyphosphate (TPP), is more effective in enhancing oxidation than a characteristic organic ligand oxalate. In addition to the scavenging of reactive oxidants by the organic ligand, more ferrous ion (Fe(II)) dissolution from SnZVI in the TPP system is another cause for the superior enhancement by the inorganic ligand. In the oxalate system, as the sulfur content of SnZVI increased, the oxidation efficiency increased because FeS shell promoted the transfer of electrons to produce more reactive oxygen species (ROS). In TPP system, the effect of sulfur content on oxidation performance is more complex. The SnZVI with low sulfur content showed poor oxidation performance compared with that of nZVI. Further experiments proved that sulfidation might weaken the complexation of TPP with surface bound Fe, which would slow down the ionic Fe(II) dissolution rate. Therefore, sulfidation has the dual effects of enhancing electron transfer and inhibiting the complexation of inorganic ligands. In addition, the mechanisms of ROS generation in different ligand systems were investigated herein. Results showed that the critical ROS in both the oxalate and TPP systems are hydroxyl radicals, and that they are produced via one-electron activation of O₂.     

KOH活化小麦秸秆生物炭对废水中四环素的高效去除

活化是提高生物炭吸附性能的重要手段.以小麦秸秆为研究对象,KOH为活化剂,制备KOH活化生物炭（K-BC）,同时制备原状生物炭（BC）作为对照.对生物炭进行比表面积和孔径、元素分析、XPS、FTIR、Raman、XRD和pH_pzc等表征,考察KOH活化对生物炭理化性质的影响,并探究生物炭对水体中四环素的吸附性能和机制.结果表明,KOH活化之后生物炭的比表面积和孔体积可达996.4 m²·g^-1和0.45 cm³·g^-1.KOH活化会制造更多的碳结构缺陷,影响生物炭的官能团和表面电性.拟二级动力学和Langmuir模型可以较好地拟合生物炭吸附四环素的过程.环境温度升高能提高生物炭对四环素的吸附量.K-BC吸附四环素是自发、吸热和无序度增加的过程.K-BC对四环素的最大吸附量理论可达到491.19 mg·g^-1（实验温度为45℃）.结合吸附后生物炭的Raman、FTIR和XPS表征,发现孔隙填充和π-π作用是K-BC吸附四环素的主要机制,氢键和络合作用也发挥重要作用.此外,K-BC还具有良好的循环使用性能.综上所述,KOH活化小麦秸秆生物炭是有效和可行的,可用于废水中四环素的去除.