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表面活性剂-纳米颗粒相互作用与智能体系的构建(Ⅱ)相反电荷表面活性剂-纳米颗粒相互作用(i)——开关转移构建开关性Pickering乳状液和Pickering泡沫 被引量:1
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作者 陈钊 蒋建中 崔正刚 《日用化学工业》 CAS CSCD 北大核心 2019年第8期492-502,共11页
表面能够部分被水润湿、部分被油润湿的胶体颗粒具有表面活性,能够吸附到油(空气)/水界面稳定Pickering乳状液和Pickering泡沫。大多数无机纳米颗粒在水介质中表面是带电的,由于过于亲水而不具有表面活性或者表面活性偏低。一种简单的... 表面能够部分被水润湿、部分被油润湿的胶体颗粒具有表面活性,能够吸附到油(空气)/水界面稳定Pickering乳状液和Pickering泡沫。大多数无机纳米颗粒在水介质中表面是带电的,由于过于亲水而不具有表面活性或者表面活性偏低。一种简单的方法是在无机纳米颗粒的分散液中加入微量的带相反电荷的离子型表面活性剂,它们会通过静电作用吸附到颗粒表面,形成疏水性单分子层,从而提高颗粒表面的亲油性,赋予颗粒表面活性。这种作用被称为原位疏水化作用(hydrophobization in situ)。本讲座将讨论如何利用原位疏水化作用赋予无机纳米颗粒表面活性,以及如何借助于开关性表面活性剂与纳米颗粒的相互作用,将表面活性剂的开关转移给颗粒,进而构建开关性Pickering乳状液和Pickering泡沫。 展开更多
关键词 原位疏水化 表面活性颗粒 Pickering乳状液 Pickering泡沫 开关转移
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粉剂除草剂颗粒表面改良后防除杂草试验初报
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作者 徐建明 薛朝标 +1 位作者 毛善国 李才生 《安徽农业科学》 CAS 北大核心 2007年第10期2937-2938,共2页
研究了粉剂除草剂(14%乙.苄可湿性粉剂)颗粒表面活性改良后除草剂对稻田杂草的除草效果。结果表明,两试验点每公顷用改良后除草剂600 g 15 d后的防效达到88.2%、79.7%,与常规除草剂750 g的防效相当;30 d后,其防效仍为89.1%、88.0%,但常... 研究了粉剂除草剂(14%乙.苄可湿性粉剂)颗粒表面活性改良后除草剂对稻田杂草的除草效果。结果表明,两试验点每公顷用改良后除草剂600 g 15 d后的防效达到88.2%、79.7%,与常规除草剂750 g的防效相当;30 d后,其防效仍为89.1%、88.0%,但常规除草剂750 g/hm2的防效明显下降,仅为64.6%和73.7%。因此,除草剂改良后能显著减少使用量、提高防除效果和延长除草有效期。 展开更多
关键词 颗粒表面活性改良 除草剂 防除效果
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纳米SiO2/十二烷基氨基丙酸钠协同稳定的pH响应性Pickering乳状液 被引量:12
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作者 刘凯鸿 林琪 +2 位作者 崔正刚 裴晓梅 蒋建中 《高等学校化学学报》 SCIE EI CAS CSCD 北大核心 2017年第1期85-93,共9页
用纳米SiO_2颗粒与微量氨基酸型两性表面活性剂十二烷基氨基丙酸钠作复合乳化剂,以正癸烷为油相,制备了pH响应性O/W型Pickering乳状液.室温下该乳状液在pH≤4.0时稳定,在pH≥6.0时不稳定,因此,可以通过改变水相的pH值使乳状液在稳定和... 用纳米SiO_2颗粒与微量氨基酸型两性表面活性剂十二烷基氨基丙酸钠作复合乳化剂,以正癸烷为油相,制备了pH响应性O/W型Pickering乳状液.室温下该乳状液在pH≤4.0时稳定,在pH≥6.0时不稳定,因此,可以通过改变水相的pH值使乳状液在稳定和破乳之间多次循环.在酸性水介质中,氨基酸型两性表面活性剂分子呈阳离子状态,可通过静电作用吸附到带负电荷的SiO_2颗粒表面,产生原位疏水化作用,使其转变为表面活性颗粒;而在中性和碱性水介质中,氨基酸型两性表面活性剂呈两性或阴离子状态,不能产生原位疏水化作用,因而导致乳状液破乳.相关作用机理通过吸附量、Zeta电位及接触角等实验数据得以论证.该刺激-响应性Pickering乳状液在乳液聚合、油品输送以及燃料生产等领域具有重要的应用价值. 展开更多
关键词 pH响应性表面活性颗粒 pH响应性Pickering乳状液 原位疏水化作用 吸附 静电作用
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Effect of solids on pulp and froth properties in flotation 被引量:7
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作者 张炜 James A.Finch 《Journal of Central South University》 SCIE EI CAS 2014年第4期1461-1469,共9页
Froth flotation is a widely used process of particle separation exploiting differences in surface properties. It is important to point out that overall flotation performance(grade and recovery) is a consequence of the... Froth flotation is a widely used process of particle separation exploiting differences in surface properties. It is important to point out that overall flotation performance(grade and recovery) is a consequence of the quality and quantity of the solid particles collected from the pulp phase, transported into the froth phase, and surviving as bubble-particle aggregates into the overflow. This work will focus on studying these phenomena and will incorporate the effects of particle hydrophobicities in the 3-phase system. Solids are classed as either hydrophilic non-sulphide gangue(e.g. silica, talc), hydrophilic sulphide(e.g. pyrite), or hydrophobic sulphide(e.g. sphalerite). Talc is a surface-active species of gangue that has been shown to behave differently from silica(frother adsorbs on the surface of talc particles). Both are common components of ores and will be studied in detail. The focus of this work is to investigate the role of solids on pulp hydrodynamics, froth bubble coalescence intensity, water overflow rate with solids present, and in particular, the interactions between solids, frother and gas on the gas dispersion parameters. The results show that in the pulp zone there is no effect of solids on bubble size and gas holdup; in the froth zone, although hydrophilic particles solely do not effect on the water overflow rate, hydrophobic particles produce higher intensity of rates on water overflow and bubble coalescence, and many be attributed to the water reattachment. 展开更多
关键词 flotation frothers bubble size coalescence gas holdup hydrophobicity
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Effect of Fe_2O_3/SiO_2 ratio on maghemite-silica particulate nanocomposites
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作者 ANG Bee Chin YAACOB Iskandar Idris NURDIN Irwan 《Journal of Central South University》 SCIE EI CAS 2013年第11期2954-2959,共6页
Abstract: Maghemite-silica particulate nanocomposites were prepared by modified 2-step sol-gel process. Superparamagnetic maghemite nanoparticles were successfully produced using Massart's procedure. Nanocomposites ... Abstract: Maghemite-silica particulate nanocomposites were prepared by modified 2-step sol-gel process. Superparamagnetic maghemite nanoparticles were successfully produced using Massart's procedure. Nanocomposites consisting of synthesized maghemite nanoparticles and silica were produced by dispersing the as-synthesized maghemite nanoparticles into the silica particulate form. The system was then heated at 140 ℃for 3 d. A variety of mass ratios of Fe2O3/SiO2 was investigated. Moreover, no surfactant or other unnecessary precursor was involved. The nanocomposites were characterized using XRD, BET and AGM. The XRD diffraction patterns show the reflection corresponding to maghemite nanoparticles and a visible wide band at 20 from 20° to 35° which are the characteristics of the amorphous phase of the silica gel. The patterns also exhibit the presence of only maghemite and SiO2 amorphous phase, which indicates that there is no chemical reaction between the silica particulate gel and maghemite nanoparticles to form other compounds. The calculated crystallite size for encapsulated maghemite nanoparticles is smaller than the as-synthesized maghemite nanoparticles indicating the dissolution of the nanoparticles. Very high surface area is attained for the produced nanocomposites (360-390 m^2/g). This enhances the sensitivity and the reactivity of the nanocomposites. The shapes of the magnetization curves for nanocomposites are very similar to the as-synthesized maghemite nanoparticles. Superparamagnetic behaviour is exhibited by all samples, indicating that the size of the maghemite nanoparticles is always within the nanometre range. The increase in iron content gives rise to a small particle growth. 展开更多
关键词 maghemite nanoparticles NANOCOMPOSITES SOL-GEL SILICA
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