共查询到16条相似文献，搜索用时 125 毫秒
1.
利用13X沸石分子筛净化含Pb~(2+)废水的实验研究 总被引：11，自引：0，他引：11
采用静态间歇法 ,实验研究了含Pb2 +废水的 pH值及吸附时间对 13X沸石分子筛吸附Pb2 +性能的影响 ,得出了最佳去除效果的优化条件为 :废水的 pH值接近中性 ,吸附时间 10min。通过吸附实验 ,确定了在Pb2 +初始浓度为 2 0mg/L的条件下 ,13X沸石对Pb2 +的吸附量为 2 1 4 2mg/g ,即每克沸石净化含Pb2 +废水的最大体积量约为 75 0mL。解析实验表明 ,加入沉淀剂 ,浓缩洗脱液中的Pb2 +即以PbS的形式生成沉淀 ,为回收金属铅提供了可能 ;13X沸石在循环使用 5次的条件下 ,对废水中Pb2 +的吸附率仍高达 98% ,重复使用性能良好。经处理后的净化水中Pb2 +的浓度小于 0 4mg/L ,显著低于国家废水排放标准GB8978 88的指标 ( 1 0mg/L)。 13X沸石对Pb2 +的主要吸附形式是离子交换和表面络合反应。 相似文献
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13X沸石分子筛对饮用水中NH_4~+-N吸附性能的实验研究 总被引：4，自引：1，他引：4
研究了 13X沸石分子筛对饮用水中低浓度NH+4 N的吸附性能 ,包括影响吸附的主要因素、沸石对NH+4 N的吸附效果、沸石的再生效果及沸石对NH+4 N的吸附机理。实验表明用NaOH处理的沸石比未处理的沸石对NH+4 N的吸附效果要好。在 pH值为 6 5～ 7 5、吸附时间为 2 0min、吸附温度为 2 0～ 30℃的条件下 ,沸石对NH+4 N的吸附率接近 10 0 % ,沸石对NH+4 N的吸附量可达 16 32mg/g。用直接焙烧法进行再生活化处理后的沸石对NH+4 N的吸附率仍接近 10 0 % ,沸石对NH+4 N的吸附机理是以离子交换吸附作用为主。 13X沸石吸附NH+4 N的过程符合Langmuir吸附等温模式。实验证明 ,利用 13X沸石净化含低浓度NH+4 N的饮用水具有良好的工业化应用前景。 相似文献
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13X沸石分子筛对水中Hg2+吸附性能的实验研究 总被引：5，自引：0，他引：5
13X沸石分子筛吸附水中Hg2+的实验研究表明,13X沸石在pH值为5~6、时间为20 min、温度为20~30 ℃条件下对Hg2+ 的吸附效果最佳。在13X沸石的用量为4 g/L的条件下对原始浓度为0.2 ~100mg/L的Hg2+进行吸附,吸附量由0.035 6 mg/g增加到21.87 mg/g。13X沸石可使原始浓度为0.01 mg/L的Hg2+降至0.002 mg/L以下。饱和NaCl溶液对吸附Hg2+后的13X沸石解吸效果良好,解吸后的13X沸石循环使用4次,对Hg2+的吸附率仍未降低,表明13X沸石的重复利用效果良好。通过在洗脱Hg2+ 的解吸液中加入Na2S·9H2O,可使Hg2+形成HgS沉淀进行回收,回收率可达90%以上。实验表明,13X沸石适用于对水中低浓度Hg2+的深度净化处理。 相似文献
4.
以Sr（NO3）2为核素源、新疆富蕴县所产斜发沸石为吸附剂,研究斜发沸石对Sr2＋的动力吸附/解吸效果。探讨吸附时间、Sr2＋初始浓度与吸附量的关系以及吸附机理。用pH=6的水溶液对饱和吸附了Sr2＋的斜发沸石进行解吸。结果表明：斜发沸石对Sr2＋的吸附在4 h能达到最大吸附率的99%,Freundlich吸附等温式能对吸附曲线进行很好的描述,单位质量沸石对Sr2＋的最大吸附量为38.34 mg/g,以阳离子交换吸附为主。4.5 h后解吸率为1.78%,解吸速率远小于吸附速率,解吸量与解吸时间的自然对数呈现明显的线性关系,用Elovich方程对解吸曲线进行拟合,R=0.9994,拟合方程为：qt=0.03375＋0.11916lnt。理论上将5%的Sr2＋解吸出来约需5044 d。该斜发沸石固Sr2＋能力很强,对于处理含Sr2＋放射性废液具有重要的意义。 相似文献
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13X沸石对Ni2+吸附性能的实验研究 总被引：8，自引：0，他引：8
在静态条件下，实验研究了13X沸石的用量、温度、时间、溶液pH值、初始Ni^2 质量浓度对Ni^2 吸附性能的。结果表明：在室温下，13X沸石对Ni^2 的吸附平衡时间为15min，对Ni^2 的最大吸附量为49.7mg/g沸石；静态等温吸附过程符合Langmiur吸附等温方程式；13X沸石对Ni^2 的吸附机理为离子交换吸附和表面络合吸附。 相似文献
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斜发沸石对钾离子的吸附/解吸动力学研究 总被引：1，自引：0，他引：1
以KCl为钾源、新疆某地所产斜发沸石为吸附剂,研究斜发沸石对K+的动力吸附与解吸效果,并探讨吸附时间、K+初始浓度与吸附量的关系。用pH=5的HCl溶液和(Ca2++Mg2+)浓度/(mmol.L-1)为1.6,3.2,6.4,12.8,19.2,25.6的混合溶液对饱和吸附了K+的斜发沸石进行解吸,实验结果表明:沸石对K+的吸附在4min能达到最大吸附率的96%,30min内达到平衡。Langmuir吸附等温式能对吸附曲线进行很好的描述。单位质量沸石对K+的最大吸附量为44.53×10-3,以阳离子交换吸附为主。pH=5的HCl溶液对K+的解吸量最小,随解吸溶液中(Ca2++Mg2+)浓度增加,解吸滞后系数减小,解吸速率远小于吸附速率。解吸量的自然对数与解吸时间的自然对数呈现明显的线性关系,用指数方程对(Ca2++Mg2+)浓度为25.6mmol/L的解吸曲线进行拟合,R=0.998,拟合方程为qt=3.890t0.210。理论上将吸附的K+全部解吸出来需要74.4d。 相似文献
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对福建沙县钾长石粉合成的13X沸石及其与取自山东铝业公司的赤泥混合使用时除砷的效果和适宜条件进行实验。结果表明，以单一的13X沸石为吸附剂时，改变沸石用量和溶液的酸度均不能有效去除砷；赤泥和沸石混合使用时对低浓度砷（〈5mg／L）具有良好的去除效果。适宜的吸附条件为赤泥用量2g／L，沸石用量1．5g／L，pH值约为8，平衡时间1h。实验表明，赤泥在混合吸附剂除砷过程中起着重要的作用，沸石与赤泥的合理混合使用，对于含砷重金属废水处理具有重要意义。对可能的机理进行了探讨。 相似文献
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以铁铝双金属离子低聚物为交联剂,制备了Fe/Al交联改性膨润土(MB),用于处理含偶氮染料的废水。通过改变吸附时间、pH和甲基橙废水浓度及掺加共存无机阴离子等因素,研究了MB对甲基橙的脱色效果。结果表明,改性后的膨润土吸附能力显著增强,对甲基橙有较好的吸附脱色性能。当材料用量0.0200 g,处理甲基橙废水20 mL,废水pH值小于4,处理时间2 h,甲基橙的脱色率可达95%。其吸附甲基橙的过程符合Fre-undlich等温吸附模式,对甲基橙的最大饱和吸附容量为384 mg/g。我国膨润土储量大、价格低,以Fe/Al交联剂为改性剂对天然膨润土进行了改性,得到的MB材料是一类很好的环境友好型吸附剂。 相似文献
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M. Akbari Binabaj S. M. Nowee N. Ramezanian 《International Journal of Environmental Science and Technology》2018,15(7):1509-1520
The removal of hexavalent chromium from wastewater streams has received an considerable attention in recent years, since it can cause harmful effects on the environment. Several approaches, including adsorption, are recognized to tackle this problem, but unfortunately most of these processes are impressed with practical conditions of the experiments. The main objective of this study was to recognize applicable conditions for Cr(VI) removal from an industrial drainage using nature-derived adsorbents (brown coal and modified zeolite) and to make the process more adaptive by using adsorbents conjointly. Batch experiments were carried out by agitating Cr(VI) stock solution with adsorbents at room temperature. The influence of main operating parameters was explored, and the best proportion of the adsorbents was determined. Maximum sorption of Cr(VI) onto brown coal was observed at pH = 4 by adding 60 g L?1 adsorbent to contaminated solution. In case of using zeolite, the modification process was required, and the pH indicated a weak influence in a wide range (2–8). Optimum dosage of modified zeolite for Cr(VI) removal was 10 g L?1. The hybrid application of adsorbents with the mass ratio of brown coal/modified zeolite at (3:1) was capable of removing more than 99% of Cr(VI) from contaminated wastewater in the natural pH range of the wastewater. The adsorption of Cr(VI) by brown coal and modified zeolite followed Langmuir and Freundlich isotherm models, respectively. Sorption of Cr(VI) onto both brown coal and modified zeolite fitted well to pseudo-second-order rate reaction. 相似文献
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《International Journal of Mineral Processing》2005,75(1-2):21-29
The use of natural zeolites for environmental applications is gaining new research interests mainly due to their properties and significant worldwide occurrence. The present work describes the characterization of a natural Chilean zeolite and the results as adsorbent for ammonia from aqueous solutions. The zeolitic-rich tuff sample, mainly composed of clinoptilolite and mordenite, consisted of 13 μm mean volumetric particle diameter, 55 m2 g−1 (methylene blue adsorption) and 177 m2 g−1 (nitrogen adsorption) of specific surface area. Particles were negatively charged over a broad pH range (with or without ammonia) and 1.02 meq NH4+ g−1 cation-exchange capacity. The ammonia removal appears to proceed through ion-exchange and rapid kinetics (rate constant of 0.3 min−1) at neutral pH value, with removal capacities up to 0.68 meq NH4+ g−1. The Langmuir isotherm model provided excellent equilibrium data fitting (R2=0.97). Results indicate a significant potential for the Chilean natural zeolite as an adsorbent/ion-exchange material for wastewater treatment and water reuse applications. 相似文献
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Ismael S. Ismael Ahmed Melegy Tomas Kratochvíl 《Geotechnical and Geological Engineering》2012,30(1):253-262
Hazardous metal cations enter water through the natural geochemical route or from the industrial wastes. Their separation
and removal can be achieved by adsorptive accumulation of the cations on a suitable adsorbent. In the present work, toxic
Pb(II) ions are removed from water by accumulating it on the surface of natural zeolite in three different forms; one untreated
and two treated samples, one sample treated with 2 M HCI solution and other is treated with 3 M NaOH solution. Natural zeolite
is mainly composed of clinoptilolite, and mordenite, with amount of non-zeolite phase (smectite and illite) and C and CT opal.
The adsorption experiments are carried out using a batch process in environments of different pH, initial Pb(II) concentration,
interaction time and amount of zeolites. Treated zeolite samples show high exchange capacity for Pb(II) compared to untreated
sample, however, acid-treated sample shows an exceedingly good exchange capacity. Equilibrium data fitted well with the Langmuir
isotherm model with maximum adsorption capacity of 115, 126, and 132 mg g−1 of untreated natural zeolites, alkali-treated zeolites and acid-treated zeolites respectively. The rates of adsorption were
found to confirm to pseudo-first order kinetic with good correlation and the overall rate of lead ions uptake. 相似文献
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The adsorption of cadmium from simulated mining wastewater by coal waste (CW) and calcination-modified coal waste (MCW) was investigated. Effects of pH, initial concentration, particle size of adsorbent, adsorbent dosage and temperature were studied in batch experiments. The adsorption efficiency for cadmium increased with increasing pH, and the optimum pH for cadmium adsorption onto MCW and CW was 6.0 and 6.5, respectively. Kinetic experiments showed that the adsorption equilibrium was reached within 120 min and followed pseudo-second-order model well. The adsorption isotherm data fit Langmuir and Freundlich models, and the adsorption capacity of cadmium on the two adsorbents increased with increasing temperature from 298 to 318 K. MCW had a higher adsorption capacity of cadmium than CW, because calcination treatment can make CW to have more loose structure and higher specific surface area. Thermodynamic parameters, the Gibbs free energy change (?G0), enthalpy change (?H0) and entropy change (?S0), were calculated and the results showed that the adsorption of cadmium on CW and MCW was spontaneous and endothermic. Fourier transform infrared studies indicated silanol and aluminol groups were responsible for cadmium binding. The desorption results indicated that the two adsorbents could be used repeatedly at least three times without significant decrease in the adsorption capacity for cadmium. The results suggested that modified CW could have high potential as low-cost adsorbent for cadmium removal. 相似文献
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活化沸石除铵及其动力学过程研究 总被引：1，自引：1，他引：1
对新型水处理材料活化沸石去除水中氨氮的各项性能进行了研究。单因素影响试验表明,沸石用量、粒径、溶液温度、浓度、pH值及吸附时间对去除效果有重要影响。据此确定了最佳静态试验条件,在该条件下,活化沸石对水中的氨氮有较好的去除效果,可将生活污水中的120 mg/L氨氮降到40 mg/L。动态小试确定了小试设备的工艺参数,该处理设备在实际运行过程中,吸附周期为64 h,处理效果良好。动力学研究表明,活化沸石除铵是离子交换与吸附两种行为共同作用的结果,该过程符合Freundlich等温式,动力学方程可用一级反应来描述。 相似文献