高压实新疆阿尔泰膨润土微观结构随吸力变化特征

采用压汞法(MIP)和扫描电镜(SEM)法,在自由和侧限状态下,试验研究了高压实新疆阿尔泰膨润土在不同吸力条件下的微观结构变化特征。吸力的控制采用了气相法和渗析(液相)法。研究结果表明:(1)低吸力范围内,自由膨胀和侧限条件下的高压实膨润土土水特征存在明显差异;(2)膨润土在自由和侧限状态下的水化过程中呈现出了截然不同的微结构变化特征。自由膨胀条件下,土的吸水膨胀量主要来自土中大孔隙的逐渐膨胀。侧限状态下,随着控制吸力的降低,膨润土的大孔隙逐渐被压缩,较小孔隙的数量不断增加,土中孔隙分布变得更加均匀。     

零价铁复合有机膨润土处理染料废水的研究

针对目前印染废水处理现状及膨润土在水处理中回收困难等问题,提出将零价铁复合到有机膨润土中制成零价铁复合有机膨润土(ZVI-OB),以达到高效吸附并降解污染物的目的。以染料废水(Orange II) 作为研究对象,考察了废水中染料的初始浓度、pH以及吸附时间对ZVI-OB去除染料效率的影响,并研究了吸附后降解过程中时间和pH对污染物降解的影响以及降解前后膨润土层结构的变化。研究结果表明,ZVI-OB相对于CTMAB改性的有机膨润土而言,其吸附量有所降低,但ZVI-OB在吸附污染物之后能有效降解有机物。ZVI-OB在饱和吸附Orange II后经催化氧化,总有机碳含量降低为原来的19%,可以重复利用。     

膨润土接枝丙烯酸高吸水性树脂的抑尘性能研究

在微波辐射下制备了膨润土接枝丙烯酸高吸水性树脂(SAP)(一种加入聚乙烯醇(PVA),另一种不加入PVA)。结果表明:(1)红外光谱图表明,PVA与聚合网络形成了半互穿网络结构;X射线衍射图表明,膨润土与PVA、丙烯酸形成了具有无定形结构的复合产物。(2)不论是沙土堆还是尘土堆,喷洒膨润土接枝丙烯酸SAP溶液的抑尘效果明显比喷洒自来水好;喷洒膨润土接枝丙烯酸SAP溶液的尘土堆的抑尘效果好于沙土堆。(3)在温度为15℃时,考虑到节约成本的问题,首选不加入PVA的膨润土接枝丙烯酸SAP做抑尘剂;在温度为45℃时,加入PVA的膨润土接枝丙烯酸SAP适合做抑尘剂。(4)膨润土接枝丙烯酸SAP浓度越高,其耐蒸发性越高。     

改性膨润土作为垃圾渗透液防渗层的实验研究

本文以天然钠基膨润土为原料,采用水溶液聚合法,在室温条件下,通过改性聚丙烯酰胺对膨润土进行直接插层改性,制备了一种新型聚丙烯酰胺改性膨润土防渗材料。以此防渗材料作为防渗层,选用沈阳大辛填埋场的垃圾渗透液为处理对象,在动态实验下,就其对实际垃圾渗滤液中主要污染物去除的有效性和控制垃圾渗滤液渗透的可行性进行研究。抗渗性能测试结果表明,改性膨润土防渗性能较好,渗透系数为1．0×10^-7cm/s,达到固体废物填埋场的防渗材料国家标准1．0×10^-7cm／s的使用要求。改性膨润土防渗层对COD、氨氮、重金属离子去除效果较好,吸附作用较强,COD和氨氮最大去除率分别达到81％和91％,TFe、Zn^2＋和TCr的最大去除率分别达到71％、58％和73％。实验结果验证了本研究所制备的改性膨润土防渗材料具有优良的抗渗、截污性能。     

天然膨润土还原吸附Cr（Ⅵ）

以天然膨润土为吸附剂,还原吸附处理含Cr（Ⅵ）模拟废水。实验结果表明：以（NH₄）₂FeSO₄为还原剂吸附效果最佳;在还原剂加入量为理论值的0.8倍、膨润土加入量为6 g/L、吸附时间为30 min、吸附温度为30 ℃、初始Cr（Ⅵ）质量浓度为1 mg/L的条件下,Cr（Ⅵ）去除率可达99.6%,处理后模拟废水中总铬质量浓度低至0.003 mg/L。天然膨润土对Cr（Ⅵ）的还原吸附符合准二级动力学模型及Freundlich等温吸附模型。     

活性白土废水治理的实验研究

活性自土生产过程中产生大量的含微细白土颗粒的强酸性废水,处理效果一直不佳.实验改进白土生产工艺,通过粒度控制,从根本上减少白土生产过程中超细白土颗粒的产生,循环利用硫酸和洗涤水以减少成本和对环境的污染.并对影响活性自土质量的主要生产工艺条件进行了比较系统的试验研究,确定了最佳工艺条件.成功地制备了脱色率92.88%,过滤速度21.27mL/mim的高效植物油活性白土.     

钠化改性河南南部膨润土吸附亚甲基蓝性能分析

以河南南部天然钙基膨润土为原料,通过钠化改性得到了钠基膨润土.通过调控吸附剂用量、亚甲基蓝（MB）浓度、吸附时间、溶液pH值和温度,分析对比了天然钙基膨润土（PRT-1）、钙基提纯膨润土（PRT-1T）和钠基膨润土（PRT-1Na）对MB的去除效率.同时,对PRT-1T和PRT-1Na对MB的吸附动力学和吸附机制进行了研究.结果表明,由于PRT-1Na有更大的比表面积、更高的阳离子交换容量和更丰富的羟基结构,表现出对MB更好的吸附效果.在同等吸附条件下,PRT-1Na的吸附效果是PRT-1的4倍,PRT-1T是PRT-1的2倍.在20℃,pH为6,PRT-1Na用量为1.0 g,吸附时间为2 h,MB为500 mL,且初始浓度为500 mg·L^-1时,MB去除率高达99.89%.另外,PRT-1Na对MB染料废水的吸附既存在物理吸附也有化学吸附,Elovich模型对PRT-1T和PRT-1Na吸附MB染料废水的过程拟合度均高,但伪一级动力学模型对PRT-1Na拟合效果最好.     

Removal of polycyclic aromatic hydrocarbons and phenols from coking wastewater by simultaneously synthesized organobentonite in a one-step process

The optimal condition for a one-step process removing organic compounds from coking wastewater by simultaneously synthesized organobentonite as a pretreatment was investigated. Results showed that sorption of organic compounds by organobentonite was positively correlated to the cation surfactant exchange on the bentonite and the octanol-water partition coefficient (K_ow) of the solutes. With 0.75 g/L bentonite and 180 mg/L (60% of bentonite cation exchange capacity) cetyltrimethylammonium bromide, the removal efficiencies of the 16 polycyclic aromatic hydrocarbon (PAHs) specified by the US Environmental Protection Agency in coking wastewater except naphthalene were more than 90%, and that of benzo(a)pyrene was 99.5%. At the same time, the removal efficiencies of COD_Cr, NH₃-N, volatile phenols, colour and turbidity were 28.6%, 13.2%, 8.9%, 55% and 84.3%, respectively, and the ratio of BOD₅/COD_Cr increased from 0.31 to 0.41. These results indicated that the one-step process had high removal efficiency for toxic and refractory hydrophobic organic compounds, and could improve the biodegradability of the coking wastewater. Therefore it could be a promising technology for the pretreatment of toxic and refractory organic wastewater.     

Adsorption of mixed cationic-nonionic surfactant and its effect on bentonite structure

The adsorption of cationic-nonionic mixed surfactant onto bentonite and its effect on bentonite structure were investigated. The objective was to improve the understanding of surfactant behavior on clay mineral for its possible use in remediation technologies of soil and groundwater contaminated by toxic organic compounds. The cationic surfactant used was hexadecylpyridinium bromide (HDPB), and the nonionic surfactant was Triton X-100 (TX100). Adsorption of TX100 was enhanced significantly by the addition of HDPB, but this enhancement decreased with an increase in the fraction of the cationic surfactant. Part of HDPB was replaced by TX100 which decreased the adsorption of HDPB. However, the total adsorbed amount of the mixed surfactant was still increased substantially, indicating the synergistic effect between the cationic and nonionic surfactants. The surfactant-modified bentonite was characterized by Brunauer-Emmett-Teller specific surface area measurement, Fourier transform infrared spectroscopy, and thermogravimetric-derivative thermogravimetric/differential thermal analyses. Surfactant intercalation was found to decrease the bentonite specific surface area, pore volume, and surface roughness and irregularities, as calculated by nitrogen adsorption-desorption isotherms. The co-adsorption of the cationic and nonionic surfactants increased the ordering conformation of the adsorbed surfactants on bentonite, but decreased the thermal stability of the organobentonite system.     

利用皂土吸附和介电泳方法间接去除水中的Mn2+

水中重金属去除一直是水处理的技术难点.锰虽然是动物必需的微量元素之一,但是人和动物摄入过量的锰会对神经系统等产生毒害.利用皂土吸附水中的重金属Mn2+,在装有微电极阵列芯片的介电泳池研究装置中,通过调节外加交流电压,捕获悬浮液中的皂土从而间接去除Mn2+.吸附了微量重金属离子的皂土被捕获到电场强度较大的区域,发生了正介电泳.该研究为建立一种从废水中间接去除重金属离子的实际可行方法奠定了实验基础,不存在二次污染.