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按照JJF1059-1999《测量不确定度评定与表示》建立了数学模型,对骨质瓷中磷酸三钙含量的测量不确定度进行了评定;分析不确定度分量及其来源,计算了各分量的不确定度,最后计算出检测结果的合成标准不确定度和扩展不确定度。检测结果和不确定度评定结果为(38.26±0.20)%、k=2,沉淀洗涤造成沉淀损失引起的测量不确定度分量最大。 相似文献
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本文介绍了高频红外碳硫分析仪示值误差测量不确定度的评定。建立了高频红外碳硫分析仪测定焊剂中碳、硫含量测量结果不确定度数学模型,从8个方面评定了不确定度分量的贡献,分别计算其相对标准不确定度,最终得到合成标准不确定度和扩展不确定度。依据《JJF 1059.1-2012测量不确定度评定与表示》,对焊剂中碳硫含量测定结果的不确定度进行评定,为日常检测工作提供指导。结果表明,方法的检测结果可信度较高,适于焊剂中碳、硫含量的测定。 相似文献
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建立了液相色谱法测定嘧霉胺悬浮剂中嘧霉胺含量的数学模型,通过对测定过程中不确定度分量来源的分析,计算了各不确定度分量,并计算出合成不确定度和扩展不确定度。同时,对测定结果进行了描述,达到了对测量不确定度合理评定的目的,反映了实验室的检测技术水平和检测设备水平。 相似文献
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It is important to develop an energy- and cost-efficient method of concentrating phosphoric acid because it is widely used in several industries. Three different ceramic membranes, namely, a silicon carbide (SiC) membrane, a TiO2-coated SiC membrane, and a sandwich membrane of TiO2 between SiC, were successfully applied for the selective separation of water from spent phosphoric acid. SiC was selected as raw material, TiO2 as supporting material. The membrane was characterized by various instruments to check all parameters. Using the solution diffusion, statistical modeling of these membranes was performed and the membrane parameters, such as membrane diffusivity and mass transfer coefficient, were calculated. By reducing the porosity of the membrane, the desired separation can be improved. 相似文献
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湿法(浓)磷酸化学法脱氟净化的研究 总被引:5,自引:0,他引:5
试验研究了湿法(浓)磷酸两种化学脱氟法,即氟硅酸钾一乙醇沉淀法和氟铝酸钠沉淀法。认为,后者优于前者,比I.M.C真空蒸汽深度脱氟法更经济,更适合于中小企业。文中关键探讨了铝在脱氟过程中的机理,同时对湿法(浓)磷酸(选择性)净化做了综述。 相似文献
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俞政一 《硫磷设计与粉体工程》2007,(5):1-8
磷矿酸解反应并非是离子间的交换,而是功能基团之间的交换。因此,磷酸萃取过程的P2O5萃取率、磷酸及后继产品性质、磷石膏结晶晶形和过滤性能与磷矿物特性有关。影响装置生产能力的主要因素是泡沫而不是反应时间和温度;磷酸快速萃取技术的核心是提高萃取和料浆过滤系统的温度。 相似文献
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Valentin G. Greb Martin Bertau Axel Düker Andreas Geisbauer Peter Fröhlich 《化学,工程师,技术》2021,93(11):1827-1832
Petrochemical catalysts are widely used in the industry. For the production of cumene, zeolite-based catalysts containing phosphoric acid are applied. Over the time, coking deactivates the surface, and the catalyst has to be exchanged and disposed of. Different process approaches for recycling the phosphoric acid-containing catalysts were investigated. Related preliminary investigations have shown that calcination of the used catalyst is necessary prior to reprocessing. By digesting the catalyst with hydrofluoric acid, ∼96 % phosphate was recovered. However, this process is very costly in terms of process technology. More promising is digestion by basic or acidic routes. Several options are possible here, and digestion with H3PO4 proved to be particularly suitable. Here, phosphate yields reached up to 98.8 %, with a positive balance of economic efficiency at the same time. The catalyst can be produced and recycled in the same plant with the same reagents, what constitutes a major breakthrough towards sustainability in industrial catalysis. 相似文献
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针对磷酸生产用水的特殊性,总结了大装置磷酸生产用水封闭循环使用存在的问题,并因地制宜地找到了解决此问题的方法。 相似文献
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Halil Durak YaŞar Genel Soner Kuşlu Sabri Çolak 《Chemical Engineering Communications》2013,200(2):245-251
The aim of the study was to investigate the optimization of the dissolution of tincal ore in phosphoric acid solutions at high temperatures in a batch reactor. The effect of the following parameters on the dissolution process was investigated: the reaction temperature, the phosphoric acid concentration, the particle size, and the solid-to-liquid ratio. The best conditions for the dissolution were determined using the 24 factorial experimental design method. The optimum values of the parameters were experimentally determined. The effective parameters were the reaction temperature, the phosphoric acid concentration, the particle size, and the solid-to-liquid ratio. The optimum conditions resulted in the maximum boron dissolution at an acid concentration of 1 M, reaction temperature of 85°C, particle size of 4.75 mesh, and solid-to-liquid ratio of 1/6 g · mL?1. Under these optimum conditions, the best dissolution yield was 98.26%. 相似文献
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Marzieh Bakhshi Hamid Reza Mortaheb Mohammad Hassan Amini 《Journal of surfactants and detergents》2021,24(3):491-499
Demands for phosphoric acid are growing rapidly in various industries. This has highlighted the importance of optimizing its production and purification methods. Phosphoric acid can be produced by a wet process. However, due to the presence of many organic and inorganic impurities in the wet product, purification of the resulting product is a major concern in this industry. Removal of trace metal impurities (such as magnesium, cadmium, chromium, zinc, etc.) from produced phosphoric acid in a wet process was investigated by foam fractionation in a semi-batch setup using sodium dodecyl sulfate (SDS) as the surfactant. Effects of inlet air velocity, surfactant concentration, and surfactant selectivity were investigated. The optimum air velocity and surfactant concentration were obtained as 0.020 cm/min and 0.7 g/L, respectively. At the optimum condition, the total removal efficiency and enrichment factor reached were 70.2% and 4.39, respectively, while the acid loss was 8.3%. The total metal removal efficiency was increased to 95.3% in a two-stage experimental run. 相似文献