建立了高效液相色谱串联质谱法测定泡面桶中总壬基酚迁移量的分析方法,并对市售泡面桶中壬基酚迁移进行了风险分析与评估。优化了色谱分离条件和固相萃取条件,线性范围1~500μg/L内线性关系良好,壬基酚的方法检出限为0.002~0.004μg/L,...建立了高效液相色谱串联质谱法测定泡面桶中总壬基酚迁移量的分析方法,并对市售泡面桶中壬基酚迁移进行了风险分析与评估。优化了色谱分离条件和固相萃取条件,线性范围1~500μg/L内线性关系良好,壬基酚的方法检出限为0.002~0.004μg/L,对实际样品迁移液进行加标回收试验,回收率在79.8%~105.2%之间,相对标准偏差(Relative Standard Deviation,RSDs)在1.74%~9.88%之间。应用该方法对市售54批泡面桶中壬基酚总迁移量进行测定,其中45件样品的迁移液中检出了壬基酚,壬基酚含量在0.006~0.079μg/L。根据检测结果对市售泡面桶中壬基酚的安全性进行了风险分析,壬基酚的最大每日摄入量为0.0237μg/d,远低于壬基酚的健康指导值3μg/d,说明市场上泡面桶相对比较安全,对人体健康存在较低风险。展开更多
In operating flotation plants, the viscosity of the pulp can vary significantly. Consequently, the resulting impact on bubble size is of interest as many plants experience seasonal changes in water temperature, or par...In operating flotation plants, the viscosity of the pulp can vary significantly. Consequently, the resulting impact on bubble size is of interest as many plants experience seasonal changes in water temperature, or particle size changes as ore hardness, mineralogy and throughput fluctuate. However, given its importance in flotation, there existed no mathematical relationship linking bubble size created in flotation machines to the key process variable of fluid viscosity. In this study, a program of investigation to develop such a model was utilizing a pilot-scale mechanical flotation machine, to investigate the effect of water viscosity due to temperature on bubble size distribution. The bubble sizes were determined using a specific bubble viewer and imaging technology. The temperature itself was varied as a method for introducing significant viscosity change. The viscosity-temperature effect introduced a correspondingly significant change in the water viscosity（1619 to 641 μPa·s）. It is suggested that a considerably stronger relationship may exist, yielding D32 versus（μ/μ20）0.776, and hence viscosity becomes an important design consideration for plants operating where pulp temperature fluctuations, very small particles or high solid fractions are present.展开更多
In order to effectively control the dust in the underground coal mine,this study proposes and develops a new technology for dust control by foam,and briefly demonstrates the advantage of the foam technology for dust c...In order to effectively control the dust in the underground coal mine,this study proposes and develops a new technology for dust control by foam,and briefly demonstrates the advantage of the foam technology for dust control,such as the good isolation performance,large contact area,high wetting ability,strong adhesion and so on.Besides,the details of the technology are introduced,including the foam agent,foam generator,and foam production process.Then the paper studies the relationship between the foaming agent concentration and liquid surface tension,and explains the principle of the foam generator.The technology is applied in heading face.The application results show that the foam has a remarkable effect on dust control in underground coal mines.展开更多
Density functional theory (DFT) simulation was performed to investigate the adsorption mechanisms between frothers and gas–liquid interface. In water phase, the polar head group of the frother molecule was connected ...Density functional theory (DFT) simulation was performed to investigate the adsorption mechanisms between frothers and gas–liquid interface. In water phase, the polar head group of the frother molecule was connected with water molecules by hydrogen bonding, while the non-polar group showed that hydrophobic property and water molecules around it were repelled away. The adsorption of water molecules on single frother molecule suggests that the complexes of α-terpineol-7H2O, MIBC-7H2O and DF200-13H2O reach their stable structure. The hydration shell affects both the polar head group and the non-polar group. The liquid film drainage rate of DF200 is the lowest, while α-terpineol and MIBC are almost the same. The adsorption layer of frother molecules adsorbed at the gas-liquid interface reveals that the α-terpineol molecules are more neatly arranged and better distributed. The DF200 molecules are arranged much more loosely than MIBC molecules. These results suggest that the α-terpineol molecule layer could better block the diffusion of gas through the liquid film than DF200 and MIBC. The simulation results indicate that the foam stability of α-terpineol is the best, followed by DF200 and MIBC.展开更多
文摘建立了高效液相色谱串联质谱法测定泡面桶中总壬基酚迁移量的分析方法,并对市售泡面桶中壬基酚迁移进行了风险分析与评估。优化了色谱分离条件和固相萃取条件,线性范围1~500μg/L内线性关系良好,壬基酚的方法检出限为0.002~0.004μg/L,对实际样品迁移液进行加标回收试验,回收率在79.8%~105.2%之间,相对标准偏差(Relative Standard Deviation,RSDs)在1.74%~9.88%之间。应用该方法对市售54批泡面桶中壬基酚总迁移量进行测定,其中45件样品的迁移液中检出了壬基酚,壬基酚含量在0.006~0.079μg/L。根据检测结果对市售泡面桶中壬基酚的安全性进行了风险分析,壬基酚的最大每日摄入量为0.0237μg/d,远低于壬基酚的健康指导值3μg/d,说明市场上泡面桶相对比较安全,对人体健康存在较低风险。
基金the Chair in Mineral Processing at McGill University, under the Collaborative Research and Development Program of NSERC (Natural Sciences and Engineering Research Council of Canada) with industrial sponsorship from Vale, Teck Cominco, Xstrata Process Support, Agnico-Eagle, Shell Canada, Barrick Gold, COREM, SGS Lakefield Research and Flottec
文摘In operating flotation plants, the viscosity of the pulp can vary significantly. Consequently, the resulting impact on bubble size is of interest as many plants experience seasonal changes in water temperature, or particle size changes as ore hardness, mineralogy and throughput fluctuate. However, given its importance in flotation, there existed no mathematical relationship linking bubble size created in flotation machines to the key process variable of fluid viscosity. In this study, a program of investigation to develop such a model was utilizing a pilot-scale mechanical flotation machine, to investigate the effect of water viscosity due to temperature on bubble size distribution. The bubble sizes were determined using a specific bubble viewer and imaging technology. The temperature itself was varied as a method for introducing significant viscosity change. The viscosity-temperature effect introduced a correspondingly significant change in the water viscosity（1619 to 641 μPa·s）. It is suggested that a considerably stronger relationship may exist, yielding D32 versus（μ/μ20）0.776, and hence viscosity becomes an important design consideration for plants operating where pulp temperature fluctuations, very small particles or high solid fractions are present.
基金The financial support by the National Natural Science Foundation of China (No.51104153)the Fundamental Research Fundsfor the Central Universities (No.2011QNB11)
文摘In order to effectively control the dust in the underground coal mine,this study proposes and develops a new technology for dust control by foam,and briefly demonstrates the advantage of the foam technology for dust control,such as the good isolation performance,large contact area,high wetting ability,strong adhesion and so on.Besides,the details of the technology are introduced,including the foam agent,foam generator,and foam production process.Then the paper studies the relationship between the foaming agent concentration and liquid surface tension,and explains the principle of the foam generator.The technology is applied in heading face.The application results show that the foam has a remarkable effect on dust control in underground coal mines.
基金Projects(51574092,51874106)supported by the National Natural Science Foundation,ChinaProject supported by Special Program for Applied Research on Super Computation of the NSFC-Guangdong Joint Fund(the second phase),China
文摘Density functional theory (DFT) simulation was performed to investigate the adsorption mechanisms between frothers and gas–liquid interface. In water phase, the polar head group of the frother molecule was connected with water molecules by hydrogen bonding, while the non-polar group showed that hydrophobic property and water molecules around it were repelled away. The adsorption of water molecules on single frother molecule suggests that the complexes of α-terpineol-7H2O, MIBC-7H2O and DF200-13H2O reach their stable structure. The hydration shell affects both the polar head group and the non-polar group. The liquid film drainage rate of DF200 is the lowest, while α-terpineol and MIBC are almost the same. The adsorption layer of frother molecules adsorbed at the gas-liquid interface reveals that the α-terpineol molecules are more neatly arranged and better distributed. The DF200 molecules are arranged much more loosely than MIBC molecules. These results suggest that the α-terpineol molecule layer could better block the diffusion of gas through the liquid film than DF200 and MIBC. The simulation results indicate that the foam stability of α-terpineol is the best, followed by DF200 and MIBC.
