好氧颗粒污泥对水溶液中酸性淡黄2G的生物吸附

利用好氧颗粒污泥对酸性淡黄2G溶液进行吸附脱色研究,考察了pH值、吸附剂用量、初始酸性淡黄2G的浓度、温度以及NaCl浓度对吸附过程的影响.实验结果表明,吸附过程对溶液pH值具有很高的依赖性,其最佳pH值为2.0.Temkin等温线在整个实验染料浓度范围内能够很好地描述吸附过程.吸附动力学符合准二级动力学模型.内部扩散和边界层扩散都可能影响生物吸附速率.热力学分析表明,吸附过程是一个自发的放热过程.采用FTIR分析的结果进一步揭示了颗粒污泥上官能团(如胺基、羧基和羟基等)可能是染料生物吸附的活跃结合位点.这些结果表明,好氧颗粒污泥可以作为吸附剂以去除水中的酸性淡黄2G。     

预处理青霉菌对中性红和孔雀绿的吸附

以青霉菌(Penicillium sp.)为吸附剂,对水溶液中染料中性红和孔雀绿进行了吸附研究.试验考察了预处理方法、pH值和重金属离子对吸附的影响,并对吸附机理进行了探讨.结果表明,在试验选用的预处理剂中,碳酸氢钠预处理的菌体吸附效果最好;溶液的pH值为5-6时,对染料的吸附量达到最大.当溶液中含有50mg·l-1Pb2+Zn2+Cu"任一种金属离子时,对菌体吸附中性红和孔雀绿均有抑制作用.碳酸氢钠处理菌体对中性红和孔雀绿的吸附过程可用准二级动力学模型来描述,相关系数均为0.9997.菌体吸附中性红和孔雀绿过程中有Na+,K+和Mg2+的释放,表明吸附过程中存在离子交换吸附机制.此外,吸附过程中静电吸附也起到一定的作用.     

模拟酸雨下H+-Ca2+在红壤表面的动力学特征

研究模拟酸雨下H Ca2 在红壤表面的反应动力学吸附特征 ,结果表明 :Ca2 的吸附动力学能很好地用一级动力学方程、抛物线扩散方程和Elovich方程 (R2 >0 97)拟合 .随溶液酸度的增加 ,Ca2 的最大吸附量显著降低 ,Ca2 吸附反应速率控制步骤是离子在颗粒内的扩散 ,扩散速率常数随酸度的增加而下降 .酸溶液pH值为 4 5和 5 6时 ,有H 的释放 ,H 的表观释放量能用一级动力学方程和扩散方程拟合 ,Elovich方程不宜拟合pH 5 6酸处理的动力学数据 ;酸溶液pH值为 3 5和 2 5时 ,有H 的消耗 ,H 消耗总量看作表观消耗量 ,用一级动力学方程、Elovich方程和扩散方程进行拟合 .比较相关系数和标准误差的大小 ,除pH值为 2 5的酸处理用扩散方程拟合结果较差外 ,这 3种动力学模型进行拟合均得到较满意的结果     

不同热解条件下制备的秸秆炭对铜离子的吸附动力学

研究了不同热解条件下制备的秸秆生物炭对铜离子的吸附动力学规律.以常见的玉米杆和番茄杆为原料,在限氧升温热解的条件下制备生物炭.研究不同热解温度(300、400、500、600、700℃)和不同热解时间(1、2、4、6、8 h)对秸秆生物炭吸附性能的影响,实验结果表明番茄杆样品T6004和玉米杆样品C6006分别获得对铜离子的最佳吸附效果,其去除率分别为98.40%和98.77%.通过批试验探明秸秆生物炭对Cu~(2+)的吸附动力学特征与机理,秸秆生物炭对Cu~(2+)的吸附动力学数据随时间的变化能很好地用准二级动力学方程进行拟合,说明生物炭对Cu~(2+)的吸附是一个复杂的过程,并不是简单的单层吸附.用颗粒内扩散模型进行拟合分析发现,热解时间和温度对秸秆生物炭的吸附边界层厚度均会产生不同程度的影响.此外,颗粒内扩散并非吸附过程的唯一控速步骤,表面吸附和液膜扩散共同控制吸附反应速率.     

杭锦2#土复合吸附剂对磷的吸附动力学

通过静态试验考察杭锦2#土/聚合硫酸铝复合吸附剂对生活污水中磷酸根的吸附特性,研究吸附过程的动力学模型,并从动力学角度探讨其吸附机理.结果表明,在杭锦2#土/聚合硫酸铝复合吸附剂用量5g·L-1、吸附时间60 min、废水pH值6.0、温度25℃、磷初始质量浓度小于16.72 mg·L-1条件下,磷酸根的去除率在96％以上;复合吸附剂对磷酸根的吸附动力学特征符合假二级方程,吸附速率在前10 min为内扩散控制,后期由膜扩散和内扩散共同控制,且膜扩散占主导地位;磷酸根的初始浓度越高,吸附质粒子的表观内扩散系数和表观传质系数越小;使用不同再生次数的再生吸附剂(添加量为5g·L-1)处理16.72 mg·L-1含磷生活污水,随着再生次数的增加,吸附能力有所下降,但磷酸根的去除率均大于89％.     

氢氧化镧改良沉积物对水中磷的吸附特征

考察了氢氧化镧改良沉积物对水中磷酸盐的吸附特征,并考察了被改良沉积物所吸附磷酸盐的形态分布特征.结果发现,氢氧化镧改良沉积物对水中低浓度磷酸盐的吸附可以采用线性模型进行描述,而对高浓度磷酸盐的吸附则适合采用Langmuir模型进行描述.准二级动力学比准一级动力学模型更适合用于拟合改良沉积物对水中磷酸盐的吸附动力学过程,膜扩散和颗粒内扩散共同控制了缓慢吸附阶段的速率.强碱性条件不利于改良沉积物对水中磷酸盐的吸附.溶液共存的Cl~-、SO_4~(2-)、HCO~3~-、Na~+、K~+和Mg~(2+)对改良沉积物吸附水中磷酸盐的影响较小,而溶液共存的Ca~(2+)会促进改良沉积物对水中磷酸盐的吸附.改良沉积物对水中磷酸盐的吸附能力明显强于未改良沉积物.改良沉积物的最大磷酸盐单位吸附量明显高于未改良沉积物,并且改良沉积物的最大单位吸附量随着氢氧化镧添加量的增加而增加.改良沉积物的初始吸附速率随着氢氧化镧添加量的增加也随之增加.改良沉积物的磷吸附-解吸平衡浓度(EPC0)明显低于未改良沉积物.被改良沉积物所吸附的磷酸盐中大部分(84%)以较为稳定的NaOH-rP和HCl-P形态存在,仅仅只有16%左右会以容易释放的NH_4Cl-P和BD-P形态存在.以上结果显示,添加氢氧化镧不仅可以增强沉积物对水中磷酸盐的吸附能力,而且可以降低沉积物中磷的释放风险,氢氧化镧是一种有希望的可以用于沉积物内源磷释放的改良剂.     

黄河中下游沉积物对磷酸盐的吸附动力学研究

研究了黄河中下游10个不同表层沉积物在黄河水体中对磷酸盐（P）的吸附动力学及其影响因素和吸附机理。结果表明：（1）不同黄河沉积物对P的吸附能力各不相同,但吸附量随时间的变化具有相同的变化趋势,吸附速率均在前8h内较快,以后逐渐趋缓,在48h时基本达到吸附平衡。不同黄河沉积物对P的吸附量均随P初始质量浓度的增加而增大,随沉积物含量增大而减小;（2）不同沉积物在不同P初始质量浓度下对P的吸附动力学均符合Lagergren二级吸附动力学模型及Weber-Morris扩散方程,求得二级吸附速率常数和扩散速率常数分别在11.9866～157.55g·mg^-1·h^-1和0.0005～0.0119mg·g^-1·h^-1/2之间,吸附过程由P在沉积物内扩散控制。     

美托洛尔在沉积物与活性污泥上的吸附行为

β-受体阻滞剂美托洛尔是最常用的临床治疗高血压药物,随生活污水进入污水处理系统后难以完全去除而影响生态环境,吸附是去除美托洛尔的有效方法之一.为评估美托洛尔在不同介质上的吸附行为,采用批平衡处理方法,分别探讨了吸附时间、初始浓度、溶液p H值、温度等条件下美托洛尔在污水处理厂活性污泥、珠江沉积物和湖泊沉积物上吸附行为.结果表明,3种吸附介质对美托洛尔的吸附过程均表现为先快速后缓慢的趋势,吸附平衡时间约为4 h且不受初始浓度的影响;酸性条件促进美托洛尔在介质上的吸附,离子强度的增大会抑制美托洛尔的吸附;美托洛尔在3种吸附介质上的动力学吸附过程符合伪二级动力学吸附模型,吸附常数为11.63—66.74 mg·(μg·min)~(-1).吸附过程包括物理吸附与化学吸附且以化学吸附为主,吸附反应比颗粒扩散、液膜扩散对吸附的影响更为显著,是反应的控制步骤.由于吸附介质的阳离子交换量和有机质含量的不同,3种吸附介质对美托洛尔的吸附等温线符合不同的拟合模型;热力学实验表明不同介质对美托洛尔吸附均为自发的放热反应.研究结果可为美托洛尔在天然环境中的去除技术和环境风险评价提供数据支撑.     

杭锦2~#土复合吸附剂对磷的吸附动力学

通过静态试验考察杭锦2#土/聚合硫酸铝复合吸附剂对生活污水中磷酸根的吸附特性,研究吸附过程的动力学模型,并从动力学角度探讨其吸附机理。结果表明,在杭锦2#土/聚合硫酸铝复合吸附剂用量5 g.L-1、吸附时间60 min、废水pH值6.0、温度25℃、磷初始质量浓度小于16.72 mg.L-1条件下,磷酸根的去除率在96%以上;复合吸附剂对磷酸根的吸附动力学特征符合假二级方程,吸附速率在前10 min为内扩散控制,后期由膜扩散和内扩散共同控制,且膜扩散占主导地位;磷酸根的初始浓度越高,吸附质粒子的表观内扩散系数和表观传质系数越小;使用不同再生次数的再生吸附剂（添加量为5 g.L-1）处理16.72 mg.L-1含磷生活污水,随着再生次数的增加,吸附能力有所下降,但磷酸根的去除率均大于89%。     

荔枝皮吸附孔雀绿的性能和机理

采用批量试验方法研究了荔枝皮对水中孔雀绿染料吸附的影响因素(吸附剂剂量、pH值和接触时间)、吸附等温线、吸附动力学和吸附热力学等,并探讨了其吸附机理。结果表明,荔枝皮和改性荔枝皮对孔雀绿的最佳吸附剂用量分别为4和2 g·L-1,最适pH值均为7.0,吸附平衡时间均为120 min;吸附过程均能用Langmuir和Freundlich等温线模型进行很好的描述,且均符合假二次动力学模型。荔枝皮和改性荔枝皮对孔雀绿的最大吸附量分别为72.46和169.49 mg·g-1。此外,吸附热力学试验结果表明,荔枝皮和改性荔枝皮对孔雀绿的吸附均属于自发吸热过程。     

不同炭化温度下烧制的竹炭对邻氯酚的吸附

研究了pH、吸附时间、竹炭投加量、邻氯酚初始浓度和吸附温度对不同炭化温度(500℃、700℃和900℃)下烧制的竹炭对邻氯酚的吸附特性的影响.结果表明,低pH值有利于3种竹炭对邻氯酚的吸附,其平衡吸附量均随初始浓度和吸附温度增大而增加,相同条件下,吸附量的大小依次为q900℃q500℃q700℃;500℃和700℃炭化温度下烧制的竹炭对邻氯酚的吸附表现出相似的变化规律,吸附时间为13h时基本达到平衡,而900℃炭化温度下烧制的竹炭的吸附则是一个快速吸附过程,30min内即达到吸附平衡;3种竹炭对邻氯酚的吸附皆是一个吸热过程,实验进行的吸附温度下,其吸附量的大小依次为q40℃q25℃q15℃.     

Removal of phenol by powdered activated carbon adsorption

In this study, the adsorption performance of powdered activated carbon (PAC) on phenol was investigated in aqueous solutions. Batch adsorption studies were performed to evaluate the effects of various experimental parameters like PAC type, PAC dose, initial solution pH, temperature and pre-oxidation on the adsorption of phenol by PAC and establish the adsorption kinetics, thermodynamics and isothermal models. The results indicated that PAC adsorption is an effective method to remove phenol from water, and the effects of all the five factors on adsorption of phenol were significant. The adsorption rate of phenol by PAC was rapid, and more than 80% phenol could be absorbed by PAC within the initial 10 min. The adsorption process can be well described by pseudo-second-order adsorption kinetic model with rate constant amounted to 0.0313, 0.0305 and 0.0241 mg·μg ^-1·min ^-1 with coal, coconut shell and bamboo charcoal. The equilibrium data of phenol absorbed onto PAC were analyzed by Langmuir, Freundlich and Tempkin adsorption isotherms and Freundlich adsorption isotherm model gave the best correlation with the experimental data. Thermodynamic parameters such as the standard Gibbs free energy (?G^o), enthalpy (?H^o) and entropy (?S^o) obtained in this study indicated that the adsorption of phenol by PAC is spontaneous, exothermic and entropy decreasing.     

Influences of charcoal and bamboo charcoal amendment on soil-fluoride fractions and bioaccumulation of fluoride in tea plants

High levels of fluoride in tea plants pose a potential health risk to humans who drink tea. It has been demonstrated that tea plant fluoride is closely related to the available fluoride in soil. But approaches that could be used to regulate the availability of fluoride in soil have been rarely seen. This study aims to investigate how the addition of charcoal and bamboo charcoal affected soil fluoride availability and bioaccumulation of fluoride in tea plants. In a microcosm experiment, tea plants were grown in the tea garden soil mixed with different amounts of charcoal and bamboo charcoal [that is, 0.5, 1.0, 2.5, and 5.0?% (w/w)]. Soil-fluoride fractions and fluoride accumulated in tea plants were determined using the sequential extraction and ion selective electrode method. Obtained results showed that both charcoal and bamboo charcoal additions significantly enhanced the concentrations of Fe/Mn oxide-bound fluoride, but significantly reduced the concentrations of water-soluble and exchangeable fluoride (p?相似文献   

Indigo carmine removal by charcoal from rice bran as an agricultural by-product

On the utilization of agricultural by-product, charcoal from rice bran was produced. The adsorption characteristics of indigo carmine onto charcoals from rice bran were investigated by the batch method. The yield and surface area of charcoal were decreased and increased with increase of carbonization temperature, respectively. The removal ratio of indigo carmine was high with the charcoal carbonized at higher temperature. In the relationship between the amount of indigo carmine adsorbed and the square root of elapsed time, a good linearity was recognized. The kinetic constant of adsorption removal for indigo carmine was rapid in the charcoal carbonized at higher temperature. The adsorption characteristics for indigo carmine removal by charcoal from rice bran were dominated by the value of their surface area.     

Accelerating effect of sodium chloride on mexiletine adsorption onto activated charcoal

The effective use of activated charcoal as an oral adsorbent for primary treatment of acute poisoning was investigated in vitro by evaluating the characteristics of mexiletine, an anti-arrhythmic drug, adsorbed onto activated charcoal in the presence of sodium chloride solutions at various concentrations. The equilibrium amount of mexiletine adsorbed onto activated charcoal was increased by the addition of sodium chloride. In particular, there was a marked increase in the amount adsorbed from a solution of lower mexiletine concentration. The removal rate is another important factor in the evaluation of activated charcoal, and a rapid decrease of mexiletine concentration by the addition of sodium chloride was recognized. The acceleration of mexiletine adsorption onto activated charcoal by the addition of sodium chloride was due to the occurrence of salting-out. It could be concluded that the administration of activated charcoal suspended in saline solution was more effective in the primary treatment of acute poisoning by mexiletine overdose.     

Decolourization of pulp and paper mill effluents using heat-treated coal: a comparison with activated charcoal

A comparison between activated charcoal and heat-treated coal for decolourization of pulp and paper mill waste water was studied. The heat-treated coal was prepared in an inert atmosphere at 800°C. The adsorption dynamics that include batch contact–time study, kinetics along with adsorption isotherms were carried out. The study shows that heat-treated coal is a suitable adsorbent and can be used for the decolourization of pulp and paper mill effluent streams. The maximum removal was achieved at the initial stages of contact, and the overall adsorption was a slow process. However, the equilibrium concentration in the case of both the adsorbents reaches at almost same time. The linear plot of the Lagergren model shows its applicability and first-order kinetics.     

The Adsorption of Lead and Copper from Aqueous Solution on Modified Peat–Resin Particles

Raw peat was modified with sulfuric acid, then mixed modified with resin to prepare the modified peat–resin particles. Using the batch experimental systems, the removal of heavy metals (copper and lead) on the modified peat–resin particles was investigated. The data of the adsorption isotherm could be fitted by the Langmuir equation well. The adsorption rate of heavy metals on modified peat–resin particles was very swift. The removal processes of heavy metals on modified peat–resin particles could be well described by pseudo-second order model. The adsorption rate of lead was affected by the initial heavy metal concentration, initial pH, particle size, agitation speed and particle mass. In the adsorption of heavy metals (lead and copper) on the modified peat–resin particles, ion exchange was the major reaction mechanism. Desorption data showed that the lead adsorbed by modified peat–resin particle could be desorbed by 0.5 N or 1.0 N HNO₃. The desorption rate was swift. The experiments indicated that the modified peat–resin particles have great potential for the removal of heavy metals from wastewater.     

Ⅱ.尾矿砂对重金属的吸附作用

本文研究了尾矿砂颗粒对Cu,pb,Cd三种重金属离子的吸附作用,以及各种环境条件因素对颗粒表面吸附作用的影响。实验结果表明,细微尾矿砂颗粒对溶液中的重金属离子具有较强烈的吸附作用,并且强烈地依赖于溶液的pH。根据表面络合反应,对尾矿砂颗粒表面基团可能参与的表面络合反应和吸附的重金属形态进行了讨论,并应用简化络合反应模式,求取了尾矿砂颗粒与Cu,Pb,Cd的表面络合形成的条件稳定常数pK_(ad)。     

Copper(II) ions’ removal from aqueous solution using green horse-chestnut shell as a low-cost adsorbent

The adsorption of copper(II) ions from aqueous solutions by the green horse-chestnut shell was studied in a batch adsorption system. It was determined how the parameters of the adsorption process, such as time, pH, copper(II) ions concentration and sorbent dose, influence the effectiveness of copper(II) ions’ removal. The adsorption process was fast and equilibrium was established about 10?min, and near 95–97% of Cu(II) ions were removed from aqueous solution. Maximum copper(II) ions’ adsorption occurred at around pH 5. The adsorption kinetics are also described, using pseudo-first-order model and pseudo-second-order model of type 1 and 2. A comparison of the kinetics models on the overall adsorption rate showed that the adsorption system was best described by the pseudo-second-order model of type 1 (r²?=?0.999) for all initial concentrations. Another key part of this study was the use of the Freundlich model to determine the adsorption isotherm and the experimental data were in strong correspondence with this model.     

Removal of congo red dye from water using carbon slurry waste

A cheaper adsorbent has been prepared from carbon slurry waste obtained from National Fertilizer Limited (NFL), Panipat and investigated for the removal of congo red, an anionic dye. Its adsorption on prepared carbonaceous adsorbent was studied as a function of contact time, concentration and temperature. The results have shown that carbonaceous adsorbent adsorbs dye to a sufficient extent (272 mg g^-1). A comparative study of adsorption results with those obtained on activated charcoal shows that the carbonaceous adsorbent is ~95% efficient as compared to activated charcoal. Thus, it can be fruitfully used for the removal of dyes from wastewaters.This work has been presented at the National Symposium on Biochemical Sciences: Health and Environmental Aspects (BSHEA—2003), Agra, India (2003).