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首页> 外文期刊>Journal of Analytical & Bioanalytical Techniques >Removal of Lead from Aqueous Solution on Activated Carbon and Modified Activated Carbon Prepared from Dried Water Hyacinth Plant
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Removal of Lead from Aqueous Solution on Activated Carbon and Modified Activated Carbon Prepared from Dried Water Hyacinth Plant

机译:从干水葫芦厂制备的活性炭和改性活性炭水溶液中除去铅

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In this work, the potential of activated carbon stems and leaves (ACS, ACL) prepared from dried water hyacinth stems and leaves (DS, DL) by chemical activation with phosphoric acid (1:3) and modified activated carbon stems and leaves (MACS, MACL) with nitric acid (1:1) for the removal of lead from aqueous solution was investigated. Carbon samples were produced with a reasonable yield about 75% and have a remarkable surface area (57.46, 71.83, 864.52, 493.78, 381.22, and 265.22 m2/g for DS, DL, ACS, and ACL, MACS and MACL, respectively and well developed pore structure. Batch adsorption experiments were conducted to study the effect of various operating parameters, pH of the solution (1 to 6), initial concentration of lead ions (50 to 400 mg /l), contact time (2-250 min), and temperature (298-323 K). It is obvious that the maximum adsorption of lead at pH 5 is in the order: MACS (175.63 mg/g) > MACL (164.56 mg/g) > DS (90.50 mg/g) > DL (66.60 mg/g) > ACS (36.00 mg/g) > ACL (33.40 mg/g). This may be attributed to the increase in the number of active sites on the modified activated carbon. The equilibrium data were analyzed using Langmuir and Freundlich isotherms. The results showed that the experimental data were fitted well by the Langmuir model. Kinetic results revealed that the adsorption process obeyed a pseudo-second order model and intra-particle diffusion was the rate controlling step. The thermodynamic studies revealed that the adsorption was spontaneous and endothermic process. Desorption of about 90% of the sorbed lead from carbon was achieved using about 0.6 M HCl.
机译:在这项工作中,通过用磷酸(1:3)和改性活性炭茎和叶(Macs)通过化学活化和叶(DS,DL)制备的活性炭茎和叶(ACS,ACL)的潜力从干水葫芦茎和叶(DS,D1)和改性活性炭研究了用于从水溶液中除去铅的硝酸(1:1)的Mac1。产生碳样品的合理收率约75%,具有显着的表面积(57.46,71.83,864.52,493.78,381.22,以及265.2222m 2 / g,分别为DS,DL,AC和ACL,MAC和MAC1开发的孔结构。进行批量吸附实验以研究各种操作参数,溶液的pH(1至6),铅离子初始浓度(50至400mg / L),接触时间(2-250分钟)和温度(298-323 k)。很明显,pH5铅的最大吸附是有序:Mac(175.63mg / g)> Mac1(164.56mg / g)> Ds(90.50 mg / g) > DL(66.60mg / g)> ACS(36.00mg / g)> AC1(33.40mg / g)。这可能归因于改性活性炭上的活性位点数的增加。使用均衡数据Langmuir和Freundlich等温机构。结果表明,朗马尔模型很好地安装了实验数据。动力学结果表明,吸附过程遵循了伪-Second阶模型和粒子衍射是速率控制步骤。热力学研究表明,吸附是自发性和吸热过程。使用约0.6M HCl实现从碳的约90%的吸附铅的解吸。

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