共查询到18条相似文献,搜索用时 62 毫秒
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以腈纶、水合肼、氢氧化钠为原料制得羧酸钠型离子交换纤维,研究了该纤维对Cu2+的吸附性能。结果表明:羧酸钠型离子交换纤维的交换容量可达4.89 mmol/g,25℃下,pH为5.0时,20 min可达到饱和吸附;CuSO4溶液浓度为2.32 mmoL/L,床流速为2.7 BV/min,穿透吸附时的床体积为149.0时,该纤维对Cu2+的动态穿透沉淀和吸附容量为1.66 mmol/L;该纤维经5次再生后其交换容量由再生前的4.89 mmol/g升高到4.97 mmol/g,饱和吸附时再生纤维吸附容量达到再生前的95.6%,其再生性能良好。 相似文献
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离子交换纤维对偏二甲肼的吸附性能 总被引:16,自引:3,他引:13
以火箭推进剂主要成分偏二甲肼为研究对象,通过配制模拟水样,采用强酸阳离子交换纤维对其中的偏二甲肼进行吸附,研究了偏二甲肼在离子交换纤维上的等温吸附线、吸附动力学和动态吸附,并将其动态吸附效果与732强酸阳离子交换树脂进行了对比. 结果表明,强酸阳离子交换纤维对偏二甲肼的吸附以液膜扩散为主,符合Boyd液膜扩散方程. 在291 K和研究的浓度范围内,离子交换纤维对偏二甲肼的吸附符合Freundlich等温吸附方程. 动态吸附结果表明,离子交换纤维对偏二甲肼的交换吸附速率大于离子交换树脂. 离子交换纤维柱的利用率高,相同条件下的处理量是树脂的3.86倍. 相似文献
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就FFA-1型弱碱性离子交换纤维对含10^2ppm级氢氟酸溶液的吸附容量、吸净率、最佳投料比、温度的影响,以及同D308大孔弱碱性树脂吸附速度的对比进行了研究。 相似文献
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离子交换纤维对低浓度二甲胺水溶液吸附性能研究 总被引:1,自引:0,他引:1
对离子交换纤维(IEF)吸附二甲胺(DMA)的特性进行了研究。等温吸附线研究表明,离子交换纤维对二甲胺的吸附符合Freundlich和Langmuir等温吸附方程。热力学研究表明,Freundlich模型可以很好地模拟二甲胺在离子交换纤维上的交换行为,交换反应的ΔG0,ΔH0,ΔS0,交换过程为自发的吸热过程。动力学研究表明,离子交换纤维对二甲胺的吸附以液膜扩散为主,其交换行为可采用Boyd液膜扩散方程描述。 相似文献
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弱碱性离子交换纤维对六价铬吸附性能的研究 总被引:2,自引:0,他引:2
以一种腈纶基弱碱性离子交换纤维为材料,探讨了纤维型式(氯型、氢氧型)对吸附量和再生性能的影响.考察了溶液pH、温度对氯型纤维吸附量的影响,并进行相应的动力学实验.结果表明:转为氯型的纤维吸附与再生性能明显优于相应的氢氧型纤维,该纤维在pH 2~3时吸附性能最好,温度越高吸附量越大.吸附过程符合准二级动力学模型(R2>0.998),吸跗在30 min内基本达到平衡.纤维对六价铬的吸跗容量可达376 mg·g-1(pH=2,G=300 mg·L-1),明显高于国外商品化的Fiban A-1离子交换纤维(152.9 mg·g-1);且经100次含铬电镀废水吸附再生循环后,六价铬去除率与纤维质量基本保持不变. 相似文献
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以超高交联聚丙烯-苯乙烯-二乙烯基苯(PP-ST-DVB)纤维为母体,分别经磺化、氯甲基化和胺化反应制得强酸或强碱离子交换纤维;研究了在低湿条件下对酸碱有害气体的动态吸附性能。结果表明:强酸离子交换纤维(交换容量为2.92 mmol/g)对NH_3气体的穿透吸附量约为40.95 mg/g,高于Fiban K-1磺酸型离子交换纤维的穿透吸附量;强碱离子交换纤维对SO_2气体的穿透吸附量约为77.50 mg/g,是Fiban A-1强碱离子交换纤维的1.55倍,自制的强酸、强碱离子交换纤维可多次再生使用。 相似文献
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离子交换树脂对铜离子吸附交换行为的研究 总被引:3,自引:1,他引:2
采用335弱碱性阴离子交换树脂交换吸附酞菁绿废水中高含量的铜离子。研究结果表明,335OH型树脂的交换吸附和脱附性能均优于701Cl,701OH及335Cl树脂,其干树脂的静态吸附交换容量大于120mg/g,工作交换吸附容量43.68mg/g,单柱20BV时铜的去除率可达93%以上,双柱串联处理60BV的去除率在99.91%以上,可确保出水中铜含量达到国家二级排放标准。选用8%HCl溶液为脱附剂,脱附率大于95%,从脱附液中可回收氧化铜,从而实现资源化的目的。树脂经再生后可重复使用,性能稳定,具有良好的应用前景。 相似文献
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《分离科学与技术》2012,47(1):56-63
The effects of pH on fumaric acid adsorption onto IRA900 ion exchange resin were studied. The optimum pH with the highest adsorption capacity depended on the fumarate concentration: the optimum pH was > 4.0 for fumarate concentrations < 5.0 g/L and < 3.0 for higher concentrations. Such different adsorption behaviors of IRA900 resins at different pHs were attributed to the different ion forms of fumarate present in solution at different pHs. Modeling results showed that the two-site-occupancy adsorption reaction between FA2? and resin active sites contributed to the high adsorption capacity at pH 5, whereas the intraparticle diffusion resulting from the hydrophobic interaction between H2FA and the hydrophobic resin backbone of IRA900 increased significantly and led to a higher adsorption capacity at pH 3. 相似文献
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《溶剂提取与离子交换》2012,30(4):350-371
Alternative chemicals for the regenerant of ion exchangers have been the subject of research for the past sixty years. The advances spanning this time period have been significant and demonstrated at the laboratory, pilot, and commercial scale. The use of carbon dioxide as a regenerant has several significant benefits including cost savings, waste minimization, and carbon dioxide sequestration, with applications including: chemical synthesis, desalination, demineralization, metals removal and hardness removal. Having originally been pursued as a means of reducing costs of regenerant chemicals, regeneration with carbon dioxide has also been described as a non-polluting separation process and has shown significant environmental benefits. Its use as a regenerant circumvents the use of brines, strong acids, or other aggressive chemicals and with the advent of new materials such as ion exchange fibers, the list of potential applications will continue to grow. This review discusses some of the significant advances during the history of this environmentally benign regeneration process. 相似文献
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以辣椒树脂为原料,采用静态吸附法确定了201×7型阴离子交换树脂吸附辣椒碱的最优工艺和提取机理。通过可见分光光度法测定了辣椒碱的质量浓度,并绘制出了不同pH的吸附等温线,建立了离子交换吸附辣椒碱的动力学模型。实验结果表明:该树脂吸附辣椒碱的最优pH值为5.5,当pH5.0或pH6.0时,Langmuir方程能够更好地拟合该吸附过程;而当pH=5.0~6.0时,辣椒碱的吸附等温线更符合Freundlich方程。在pH=5.5、308.15K下,较高的辣椒树脂的质量浓度能显著提高离子交换速率,且初期(t30 min)800~1200r/min的搅拌速率有利于吸附过程。通过计算得出,树脂吸附辣椒碱模型的速率常数k0=2.11×10-3s-1、活化能Ea=12.6 k J/mol、反应级数为0.268,并利用Freundlich模型解析获得了最优pH值(5.5)下阴离子交换树脂吸附辣椒碱的动力学方程。 相似文献
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《分离科学与技术》2012,47(15):3409-3430
Abstract Separation of nitrophenols (NP) has been studied by selective solubilization in organic solvents of different polarities. o‐NP dissolves very well in heptane and toluene while intermolecular hydrogen bonding among p‐NP molecules decreases its solubilization in these solvents. Thus partial separation of o‐/p‐nitrophenols is achieved by selective solubilization of o‐NP in heptane. The trace amounts of p‐NP from the o‐NP solutions are removed by its selective sorption on basic ion exchange resins. The sorption of nitrophenols, individually and in mixtures, is experimentally determined from their solutions in heptane, toluene, and methanol by using weakly basic Indion‐850 and Duolite A‐308 resins and strongly basic Indion‐810 resin. The equilibrium adsorption studies show very selective adsorption of p‐NP from heptane with a high loading capacity on Indion‐850. 相似文献