黄原酸化废弃污泥吸附Cu2+研究

将污水处理厂废弃污泥在碱性环境中用CS2处理,制备黄原酸酯类重金属吸附剂,探究一种有效的废弃污泥资源化途径.用傅里叶转换红外光谱(fourier transform infrared spectroscopy,FTIR)对污泥进行了表征,并通过批量实验研究了污泥对Cu2+的吸附性能以及pH和初始Cu2+浓度的影响.结果表明,黄原酸化成功引入了含硫基团,使黄原酸化污泥的吸附量相对于原始废弃污泥提高了20.6%~46.9%.当Cu2+初始浓度为25 mg·L-1时,黄原酸化污泥对Cu2+的去除率可达96.7%.吸附动力学遵循准二级动力学模型(Pseudo-second-order equation),平衡时间为3 h,吸附速率同时受膜扩散和颗粒内扩散两过程控制;吸附过程符合Langmuir等温模型和Freundlich等温模型,25℃下,由Langmuir模型得到的最大吸附量达142.92 mg·g-1(pH=5),且吸附容量随pH(1~5)及初始Cu2+浓度升高而升高.黄原酸化废弃污泥可作为高效重金属离子吸附剂,实现废弃资源的回收利用.     

从分子质量的变化分析有机物对GAC吸附内分泌干扰物(BPA)的影响

从分子质量分布的角度研究了水中有机物对颗粒活性炭(GAC)吸附双酚A(BPA)容量及吸附速率的影响.结果表明,相对于以去离子水为本底的BPA溶液来说,GAC吸附以滤后水、臭氧后出水和原水为本底的BPA溶液的Langmuir模型的最大吸附容量q_m值分别下降了29.95%、43.56%和44.44%,而其拟二级动力学模型的k₂值分别下降了43.05%、49.75%和56.38%.相对分子质量3 000以上,尤其是10 000以上的有机物堵塞GAC的二级微孔;3 000以下,尤其是1 000以下的有机物与BPA分子之间存在直接的竞争吸附,是导致GAC对BPA的吸附容量以及吸附速率下降的主要原因.     

Sorption of organic compounds to activated carbons. Evaluation of isotherm models

Sorption to ‘hard carbon’ (black carbon, coal, kerogen) in soils and sediments is of major importance for risk assessment of organic pollutants. We argue that activated carbon (AC) may be considered a model sorbent for hard carbon. Here, we evaluate six sorption models on a literature dataset for sorption of 12 compounds onto 12 ACs and one charcoal, at different temperatures (79 isotherms in total). A statistical analysis, accounting for differences in the number of fitting parameters, demonstrates that the dual Langmuir equation is in general superior and/or preferable to the single and triple Langmuir equation, the Freundlich equation, a Polanyi–Dubinin–Manes equation, and the Toth equation. Consequently, the analysis suggests the presence of two types of adsorption sites: a high-energy (HE) type of site and a low-energy (LE) type of site. Maximum adsorption capacities for the HE domain decreased with temperature while those for the LE domain increased. Average Gibbs free energies for adsorption from the hypothetical pure liquid state at 298 K were fairly constant at −15 ± 4 and −5 ± 4 kJ mol⁻¹ for the HE and LE domain, respectively.     

ADSORPTION OF PHOSPHATE BY RIVER PARTICULATE MATTER1

ABSTRACT: The adsorption of phosphate on particulate matter from the Illinois and Spoon Rivers was investigated. Adsoprtion reached equilibrium after 5 to 6 days and adsorption isotherms were linear for both constant and varying amounts of particulate matter. Adsorption was maximum at pH 8.3 – 8.4 and minimum at 6.0. Rates of adsorption were influenced by the equilibrium concentration of phosphate-P and were essentially the same for the Illinois and Spoon Rivers. However, the quantity of phosphate-P adsorbed per unit weight of particulate matter differed for the two streams with that in the Illinois River exhibiting an adsorption capacity 7 times that of the Spoon River.     

北京土壤对甲苯和萘的吸附及影响因素分析

通过静态吸附实验,研究了北京地区土壤对甲苯和萘的吸附行为,考察了温度和表面活性剂对甲苯和萘吸附的影响.结果表明,尽管7种土壤对甲苯和萘的吸附能力差别较大,但其吸附等温线均很好的符合Freundlich吸附模式;同一土壤中,萘的吸附量大于甲苯的吸附量.温度升高不利于甲苯和萘在土壤中的吸附.十六烷基三甲基溴化铵(CTAB)和十二烷基苯磺酸钠(SDBS)均利于甲苯和萘在土壤表面的解吸,CTAB和SDBS对甲苯和萘的解吸率最高分别可达27.5%、12.1%和64.3%、48.8%,说明SDBS的解吸效果更好.甲苯     

Biosorption of cadmium(Ⅱ) and lead(Ⅱ) ions from aqueous solutions onto dried activated sludge

The removal of heavy-metal ions from aqueous solutions by using dried activated sludge has been investigated in batch systems. Effect of solution pH, initial metal ion concentration, and temperature were determined. The results of the kinetic studies showed that the uptake processes of the two metal ions(Cd(Ⅱ) and Pb(Ⅱ)) followed the pseudo-second-order rate expression. The equilibrium data fitted very well to both the Langmuir and Freundlich adsorption models. The FT-IR analysis showed that the main mechanism of Cd(Ⅱ) and Pb(Ⅱ) biosorption onto dried activated sludge was their binding with amide I group.     

基于T-P模型的高低温环境型煤对甲烷吸附性能预测

为预测深部或浅部煤层不同温度和不同压力条件下的吸附等温线,选用型煤以高低温试验装置为依托,测试了温度为293.15,273.15,253.15 K的吸附等温线。基于T-P模型,利用等温吸附曲线对公式中的参数进行了合理的求解,探讨了一种简单的煤对瓦斯吸附等温线预测方法。研究表明:同一吸附平衡压力下,温度越低,煤的瓦斯吸附量越大;ε－ω吸附特征曲线与温度无关,呈现对数的形式;参数m和拟合度R2满足抛物线的关系,存在拟合效果最好时的参数m值。采用T-P模型预测得到的吸附等温线与实测的吸附等温线无论是趋势还是定量结果均十分吻合,其相对误差不超过5%。     

高分子除氯剂对水中氯离子的吸附机理

采用高分子除氯剂吸附水中的氯离子,考察了除氯剂投加量、反应时间、反应温度、竞争离子等对氯离子去除率的影响。实验结果表明:随着除氯剂投加量增加,氯离子去除率不断提高;吸附动力学符合拟二级动力学模型,表明化学吸附可能是氯离子吸附过程的速率控制步骤;Elovich模型表明除氯剂表面吸附的氯离子存在非均相扩散的吸附-脱附过程;Freundlich等温吸附模型能更好地描述吸附过程,结合热力学计算表明该过程是一个自发进行的吸热熵增的化学吸附过程,温度越高自发程度越大。     

活性炭对含铅废水吸附特性研究

采用静态法用活性炭吸附处理含铅废水,考察了活性炭对含铅废水的吸附特性。结果表明:活性炭对铅离子吸附平衡时间为100 m in;吸附等温方程为:Ce/qe=0.4298+0.0594Ce(25℃),该方程符合Langmu ir型吸附模式,不同温度下吸附平衡参数0RL1,表示该吸附为有利吸附。实验数据应用数学模型拟合,二级相关系数R2=0.9998,显示吸附过程动力学与二级动力学模型相关性较好;计算不同温度下各热力学参数:△Hθ大于零、△Gθ小于零,证实该吸附过程是一个自发吸热过程。△Sθ大于零,表明铅离子在固液界面有序性减小、混乱度增大。△Hθ值很小,说明该过程为物理吸附。     

柚皮粉对水中Cr(Ⅵ)的吸附性能研究

采用柚皮粉吸附去除水中Cr(Ⅵ)。考察了pH、吸附时间、柚皮粉用量和Cr(Ⅵ)初始浓度等因素对吸附效果的影响,测定了吸附等温线,对等温吸附规律及吸附机理进行了探讨。结果表明,pH、吸附时间、柚皮粉用量、Cr(Ⅵ)初始浓度、温度等因素对柚皮粉吸附水中Cr(Ⅵ)有显著影响。适宜的吸附条件为:pH 1.5,吸附时间6 h,柚皮粉用量0.5 g/100 mL,Cr(Ⅵ)初始浓度不大于10 mg/L,温度25℃。在该条件下,Cr(Ⅵ)的去除率可达98%以上。柚皮粉对水中Cr(Ⅵ)的等温吸附规律可用Freundlich、Langmuir和Temkin模式较好地描述,吸附呈单分层形式,吸附性能良好,吸附易于进行。柚皮细胞成分中的活性基团与Cr(Ⅵ)发生表面络合作用是吸附的主要机理。