EDTA优化纳米Pd/Fe对2,4-D的催化脱氯研究

采用EDTA优化纳米Pd/Fe催化脱氯水中2,4-二氯苯氧乙酸(2,4-D),并考察了EDTA投加浓度、pH、钯化率、温度等因素对2,4-D还原的影响.结果表明,EDTA的加入络合了纳米Pd/Fe在催化脱氯过程中生成的铁离子,抑制纳米Pd/Fe颗粒表面钝化层的形成,提高了体系的反应活性.适宜的EDTA浓度、低pH、高钯化率、低温等有利于2,4-D的还原脱氯.当EDTA浓度为25.0 mmol·L-1,纳米铁含量为1.0 g·L-1,初始pH=4.3、钯化率为0.5%,温度为25.0℃,搅拌速率为200 r·min~(-1)时,反应50 min,10.0 mg·L-1的2,4-D去除率及苯氧乙酸(PA)生成率均达到100%.     

Effect of MoO3 on vanadium based catalysts for the selective catalytic reduction of NOx with NH3 at low temperature

The selective catalytic reduction(SCR) activities of the MoO_3 doped V/WTi catalysts prepared by the incipient wetness impregnation method at low temperature were investigated.The results showed that the addition of MoO_3 could enhance the NO_ xconversion at low temperature and the best SCR activity was obtained when the dosage of MoO_3 reached5 wt.%. The NH3-TPD and DRIFTS experiments indicated that the addition of MoO_3 changed the type and number of acid sites on the surface of catalysts and reaction activities of acid sites were altered at the same time. The redox capacity and amount of active oxygen species got improved for V3Mo5/WTi catalyst, which could be confirmed by the H_2-TPR and transient response experiments. Water vapor inhibited the NO_xconversion at low temperature. Deposition of ammonium sulfate or bisulfate might be main reason for the loss of catalytic activity in the presence of SO_2 at low temperature. Choosing the suitable NH_3/NO ratio and elevation of reaction temperature both could weaken the influence of SO_2 on the SCR activity of the V3Mo5/WTi catalyst. Thermal treatment of the deactivated catalyst at350°C could get the low temperature activity recovered. The decrease of GHSV improved the de NO_x efficiency at low temperature and we speculated that the rational technological process and operation parameters could contribute to the application of this kind of catalysts in real industrial environment.     

原子吸收法测定海水中铁含量的不确定度评定

为了保证海水中铁元素含量的检测质量,更好地深入了解铁在整个海水体系的生物地球化学中扮演的角色,需科学地评定检测结果的分散性。文章依据《测量不确定度的评定与表示》(JJF1059-1999)的理论,以浙江近海海水为例,评定原子吸收法测定海水中铁含量的不确定度。测得浙江近海样品中铁的浓度为5.2μg/L,扩展不确定度U=0.8μg/L(k=2)。通过对各不确定度分量进行评定发现,利用该方法测定海水中铁含量时,对其合成标准不确定度的主要贡献来自于样品制备过程,尤其是萃取过程。     

“污泥+生物质”混合厌氧消化分类管理研究

污泥单独厌氧消化困难,产气量低,能量回收价值低.但“污泥+生物质”混合厌氧消化能够改善物料间的营养平衡,运行更平稳,既有效处理污泥,又能够提高甲烷产气量,更适合生产实际,符合行业发展趋势.分析了安阳市四家污水处理厂脱水污泥的重金属含量,依据土地利用限值标准,结合生产实际,把安阳市四个污水处理厂脱水污泥分类,分类混合厌氧消化处理后分类土地利用,既提高了污泥的土地利用,更强化了污泥土地利用的重金属管理.     

典型氢氧化细菌固碳特性种间差异及胞外有机物对固碳过程影响

化能自养细菌对全球CO₂固定具有重要的意义.研究了4种典型氢氧化细菌（HOB,分别是Alcaligenes hydrogenophilus DSM 2625、Pelomonas saccharophila DSM 654、Variovorax paradoxus DSM 30034和Acidovorax facilis DSM 649）的固碳特性及其种间差异性,并探究了胞外游离有机碳（EFOC）对不同种类HOB固碳效率差异性的影响.结果表明：①不同HOB自养培养过程中表观固碳量随时间呈显著差异性,其中,DSM 2625生长速度较快,其平均固碳量分别是DSM 654、DSM 649和DSM 30034的6.30、8.76和7.02倍.②不同HOB之间cbbL基因转录量与 表观固碳量的相关系数为0.980 （p<0.05）,cbbL基因转录量是造成不同菌种之间表观固碳效率差异的关键因素.③HOB细胞蛋白质含量与cbbL基因丰度和转录量之间也存在显著正相关,相关系数分别为0.999（p<0.01）和0.976（p<0.05）,即化能自养细菌CO₂同化途径所固定的有机碳进一步参与细胞蛋白质的合成,进而影响其生长速度和表观固碳效率.④HOB在自养培养过程中产生的EFOC对cbbL基因转录效率产生反馈抑制作用,且不同HOB之间,EFOC/TOC比例越低,表观固碳效率越高.     

闽南城市区域空气中挥发性有机物的污染特征

采用美国EPA TO-15的方法,研究了2011年3月份闽南城市区域空气中VOCs的含量及其污染特征。结果表明:1)漳州工业区空气的VOCs浓度为200.5μg/m3,污染较为严重;厦门交通干道VOCs浓度为74.0μg/m3,泉州商住区的VOCs浓度77.1μg/m3,污染较轻。2)漳州工业区采样点TOP5占TVOCs的比例最高,达77.3%;厦门交通干道与泉州商住区两采样点的TOP5占TVOCs的比例相近,分别为64.1%和62.0%。在所有的采样点中出现的TOP5组分比较集中,主要包括甲苯、苯、二氯甲烷、异丙醇、乙酸乙酯、1,1-二氯乙烯、萘等。3)机动车尾气的排放、工业溶剂的挥发和废气排放可能是厦漳泉三地大气VOCs的主要排放源。4)厦漳泉的BTEX主要来源于汽车尾气和汽油挥发;其中厦门和泉州BTEX浓度相比较处在较低污染水平,漳州处在中等水平。     

介质材料在可渗透反应墙中的应用进展

可渗透反应墙正发展成为修复污染地下水技术的新方向,其中介质材料是可渗透反应墙成功修复污染地下水的关键。可渗透反应墙介质材料可以细分为还原型、吸附型、沉淀型和降解型介质材料等四类,并分别从不同类型的介质材料的反应机理、应用情况以及存在的问题等方面加以阐述。可渗透反应墙介质材料的选择应在其反应机理的基础上,结合实际的地下水环境条件、污染源、人类活动和经济费用等加以综合考虑,以保证可渗透反应墙长期有效经济安全地运行。     

城市化影响杭州城市热环境的数值模拟研究

通过对城市区域的气候要素进行精细化数值模拟,可以研究城市化对城市热环境的重要影响.利用WRF/UCM模式,以杭州为例,通过采用不同的下垫面土地利用分类数据,分析量化历史城市化进程对月尺度城市热环境的影响,并进一步设计了敏感性模拟试验,研究杭州地区在理想化条件下城区面积增加约2倍时,城市热环境的变化情况.模拟结果表明,杭州地区在2010~2017年的城市化进程中,城区面积约增加了1倍,导致8月热岛强度等级高于”无”（Ht>0.5℃）的区域扩大了91%,且主城区的2m平均气温增加了0.4℃,但中心城区热岛强度等级没有明显提升.杭州城区面积在2017年基础上约增加2倍时,8月热岛强度等级高于”无”的区域扩大157%,1846.4km²的中心城区热岛强度等级由”弱”或”无”（Ht≤1.5℃）提升为”中等”（1.5相似文献   

Removal kinetics of phosphorus from synthetic wastewater using basic oxygen furnace slag

Removal kinetics of phosphorus through use of basic oxygen furnace slag (BOF-slag) was investigated through batch experiments. Effects of several parameters such as initial phosphorus concentration, temperature, BOF-slag size, initial pH, and BOF-slag dosage on phosphorus removal kinetics were measured in detail. It was demonstrated that the removal process of phosphorus through BOF-slag followed pseudo-first-order reaction kinetics. The apparent rate constant (k_obs) significantly decreased with increasing initial phosphorus concentration, BOF-slag size, and initial pH, whereas it exhibited an opposite trend with increasing reaction temperature and BOF-slag dosage. A linear dependence of k_obs on total removed phosphorus (TRP) was established with k_obs = (3.51 ± 0.11) × 10^− 4 × TRP. Finally, it was suggested that the Langmuir–Rideal (L–R) or Langmuir–Hinshelwood (L–H) mechanism may be used to describe the removal process of phosphorus using BOF-slag.     

Removal kinetics of phosphorus from synthetic wastewater using basic oxygen furnace slag

Removal kinetics of phosphorus through use of basic oxygen furnace slag(BOF-slag)was investigated through batch experiments. Effects of several parameters such as initial phosphorus concentration, temperature, BOF-slag size, initial p H, and BOF-slag dosage on phosphorus removal kinetics were measured in detail. It was demonstrated that the removal process of phosphorus through BOF-slag followed pseudo-first-order reaction kinetics. The apparent rate constant(kobs) significantly decreased with increasing initial phosphorus concentration, BOF-slag size, and initial p H, whereas it exhibited an opposite trend with increasing reaction temperature and BOF-slag dosage.A linear dependence of kobson total removed phosphorus(TRP) was established with kobs=(3.51 ± 0.11) × 10- 4× TRP. Finally, it was suggested that the Langmuir–Rideal(L–R)or Langmuir–Hinshelwood(L–H) mechanism may be used to describe the removal process of phosphorus using BOF-slag.