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采用共沉淀法,通过改变透明质酸及氨水与铁离子的比例、反应物浓度、温度和反应体系大小等反应参数制备出透明质酸修饰的超小超顺磁氧化铁纳米颗粒(Fe3 O4@HA),并对所合成的样品进行了尺寸、形貌和磁性的表征.实验结果表明:使用共沉淀方法时,所制备的Fe3 O4@HA的饱和磁化率受反应参数的影响较小,且都介于55~80 emu/g之间;但纳米颗粒的形貌、水合粒径受反应参数的影响较大.对于初始反应体积为50 mL的体系,透明质酸1.5 g、铁离子0.9 mmol、氨水用量15 mL、温度为80℃是本实验筛出的最佳条件.此外,根据最佳反应条件进行30倍放大,可一次制备出2 L的Fe3 O4@HA溶液,证明本体系具备工业化生产的潜力. 相似文献
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叙述了以液相共沉淀法制备纳米磁性Fe3O4粒子的工艺,研究了反应搅拌速度、n(Fe3+)/n(Fe2+)的比例、pH值和熟化温度对制备纳米Fe3O4粒子的影响,并利用透射电镜表征观察Fe3O4纳米粒子的形貌。研究结果表明,在搅拌速度较快的情况下制备纳米级Fe3O4颗粒的最佳合成工艺条件为:n(Fe3+)/n(Fe2+)为1.8∶1(摩尔比),熟化温度70℃,熟化时间30 min,以氨水作沉淀剂最佳pH值是9左右,可制得纯度较高,粒径小于10 nmFe3O4磁性粒子。 相似文献
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分别采用热分解法及共沉淀油酸同步修饰法制备了2种可以在油相稳定分散的Fe3O4纳米粒子,并对热分解法制备Fe3O4纳米粒子的反应条件进行了优化,考察了热分解温度、熟化时间对颗粒粒径、形貌及磁性能的影响。通过TEM、VSM和FTIR等表征手段对2种方法制备的Fe3O4纳米粒子的油相分散稳定性、颗粒形貌及粒径、比饱和磁化强度及表面性质进行了比较。结果表明:热分解法制备的Fe3O4纳米粒子表现出更好的油相分散稳定性,共沉淀油酸同步修饰法制备的Fe3O4纳米粒子则表现出更好的磁响应性。 相似文献
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磁性Fe3O4纳米颗粒制备方法的比较 总被引:1,自引:0,他引:1
使用醇-水法、氢氧化钠共沉淀法和氨水共沉淀法制备磁性Fe3O4纳米颗粒.制得的纳米Fe3O4用饱和油酸钠的醇溶液进行改性.采用XRD,SEM,TEM,IR和振动样品磁强计等手段对制备的样品进行了表征研究.实验结果表明三种方法中,醇-水法和氨水共沉淀法所制备的纳米Fe3O4表面改性效果良好;氨水共沉淀法制备的颗粒磁性最强,但实验时间长;醇-水法制备的粉体粒径最小,但颗粒分散情况相对较差;氢氧化钠共沉淀法最简单,实验时间最短,收率也较高,但粉体性能不如其它两种. 相似文献
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共沉淀法制备纳米Fe3O4影响因素的研究 总被引:2,自引:0,他引:2
利用正交设计的数学方法进行实验设计,采用液相共沉淀法制备纳米级Fe3O4颗粒,考察不同影响因素对微球平均粒径大小的影响,寻找制备纳米颗粒的最佳条件.所考察的因素分别为胶溶化时HCl加入量、Fe3+与Fe2+的比例、共沉淀时的pH值、制备Fe3O4的晶化温度.结果表明,以胶溶化时加入HCl3mL、Fe3+与Fe2+的比例2:3、共沉淀时的pH值11和制备Fe3O4的晶化温度80℃为最佳实验条件为,此时制得的纳米粉体平均粒径可达16.3nm;并利用粒径分析仪和HRTEM对所制备纳米粉进行结构表征. 相似文献
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首先利用化学共沉淀法制备了具有超顺磁性的纳米Fe3O4颗粒,然后用油酸对其进行包覆,得到稳定的Fe3O4机油基磁流体。分别用XRD、IR、TEM、VSM和TGA对所制备的产物进行表征,探讨了油酸包覆Fe3O4纳米颗粒的形成机理。研究表明,所得磁流体具有高的饱和磁化强度和稳定性,制备的纳米Fe3O4颗粒的饱和磁化强度为79.886emu/g,用油酸包覆后的颗粒的饱和磁化强度达到73.991emu/g,油酸的包覆使得Fe3O4颗粒的饱和磁化强度有所降低。 相似文献
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磁性纳米四氧化三铁的制备工艺及其表面改性 总被引:3,自引:1,他引:2
采用共沉淀法制备纳米Fe3O4胶体溶液,并用油酸钠对其进行包覆改性。制备了不同条件下的纳米Fe3O4粒子,用X射线分析仪、振动样品磁强计、扫描电子显微镜、傅立叶红外光谱仪对产品进行分析表征。探讨了制备纳米Fe3O4的最佳工艺条件以及油酸钠改性的可行性。结果表明,Fe3+和Fe2+的摩尔比为4∶2时,反应1.0 h,50℃晶化1.0 h,制备的Fe3O4晶粒度为11.2 nm,磁饱和强度为56.337 emu/g;油酸钠用于Fe3O4改性,包覆效果良好。 相似文献
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乙烯酮(双乙烯酮)是十分重要的化工中间体,其下游产品较多。江苏某化工厂开发生产乙烯酮(双乙烯酮)下游产品三十多个,年生产规模三万多吨,是国内以乙烯酮(双乙烯酮)为中间体生产精细化学品的综合骨干企业。针对乙烯酮(双乙烯酮)下游产品废水特点,该厂结合企业实际,开展了产品优化,结构调整,清洁生产,资源循环利用,节水降耗等工作,从源头削减了污染物的生产。同时投资二千多万元新建预处理装置三套,6000m3/d废水生化处理装置一套,使全厂乙烯酮(双乙烯酮)下游产品的废水得到了有效的治理。 相似文献
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The miscibility of various amorphous polybutadienes with mixed microstructures of 1,4 addition units (cis, 1,4 and trans 1,4) and 1,2 addition units have been investigated. The studies here involved optical transparency, differential scanning calorimetry, and small angle light scattering. It was found that a 90 percent (cis) 1, 4 addition polybutadiene was immiscible with high (91 percent) 1,2 addition polybutadiene. Reduction of the 1,2 content to 71 percent induced an upper critical solution temperature (UCST) with the cis 1,4 polymer. Polybutadienes with 50 percent and 10 percent 1,2 contents were miscible above the crystalline melting temperature of the cis 1,4 polybutadiene. Immiscibility of the 91 percent 1,2 addition polymer was also found with a 10 percent 1,2 polybutadiene. The latter polymer also exhibits an UCST with the 71 percent 1,2 polymer. The results are used to interpret the characteristics of blends of polybutadienes of varying microstructure. 相似文献
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以F类粉煤灰为例,详细介绍了测定粉煤灰中烧失量的步骤、计算数学模型、影响测量不确定度的因素以及各项测量不确定度分量评定,人员、设备、材料、方法、环境都是影响测量不确定的因素。 相似文献
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我厂3号回转窑(Φ4m×60m)生产线在1996年年底由SP窑(产量912t/d)改为NSP窑(产量1320t/d),预分解系统为四级旋风预热器带离线式分解炉 相似文献
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The objective of the study was to explore the effect of the degree of deacetylation (DD) of the chitosan used on the degradation rate and rate constant during ultrasonic degradation. Chitin was extracted from red shrimp process waste. Four different DD chitosans were prepared from chitin by alkali deacetylation. Those chitosans were degraded by ultrasonic radiation to different molecular weights. Changes of the molecular weight were determined by light scattering, and data of molecular weight changes were used to calculate the degradation rate and rate constant. The results were as follows: The molecular weight of chitosans decreased with an increasing ultrasonication time. The curves of the molecular weight versus the ultrasonication time were broken at 1‐h treatment. The degradation rate and rate constant of sonolysis decreased with an increasing ultrasonication time. This may be because the chances of being attacked by the cavitation energy increased with an increasing molecular weight species and may be because smaller molecular weight species have shorter relaxation times and, thus, can alleviate the sonication stress easier. However, the degradation rate and rate constant of sonolysis increased with an increasing DD of the chitosan used. This may be because the flexibilitier molecules of higher DD chitosans are more susceptible to the shear force of elongation flow generated by the cavitation field or due to the bond energy difference of acetamido and β‐1,4‐glucoside linkage or hydrogen bonds. Breakage of the β‐1,4‐glucoside linkage will result in lower molecular weight and an increasing reaction rate and rate constant. © 2003 Wiley Periodicals, Inc. J Appl Polym Sci 90: 3526–3531, 2003 相似文献