优化有效组分研磨工艺及所得粉末灭火器的疏水性

Slavica Mihajlović, N. Djordjevic, M. Jovanović, M. Vlahović, Ljubinko Savić, A. Patarić, M. Blagojev
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摘要

本文介绍了一种磷酸一铵(MAP)作为粉末灭火器(PFE)活性成分的研磨工艺。目的是确定达到永久灭火所需MAP的最佳粒径的研磨时间。利用实验室陶瓷球磨机和振动杯磨机对MAP进行研磨。研磨过程是通过在精确规定的时间间隔内使用100 μ m筛网进行筛分来控制的。PFE的效率取决于有效组分中-100 μ m组分的比例,该比例必须超过60%。采用球磨机(单段磨矿)对- 3000 μ m mm粒径的MAP进行磨矿33 min后,获得了-100 μ m粒径比例为64%的最佳粒度。在两阶段工艺中,通过研磨相同的初始MAP样品(?在振动磨机中研磨10 min,可得到晶粒尺寸上限为300 μ m,平均晶粒直径为120 μ m的粉末。这个样本的大小进一步减少地面的陶瓷球磨机收益率报67.5%的分数粒度-100 ? m 19分钟。之后两级磨削过程的总时间是29分钟。通过分析地图需要的研磨时间粒度的要求的最低分数-100 ? m提供形成pfizer的有效性可以得出结论,64%的分数获得了33分钟的单级研磨后,而在两阶段过程中仅经过26分钟。因此,研磨时间减少了7分钟,节约了一定的能源。采用硬脂酸镁(MgSt)在球磨机中以2%的含量包覆PFE,获得了PFE的稳定性和疏水性。通过验证PFE与水滴接触疏水性的标准化程序对涂层进行了验证。所得PFE的组分质量比为MAP:AS:CC:QS:MgSt=55:20:18:5:2 (AS-硫酸铵;cs -碳酸钙,qs -石英砂),并通过化学和粒度分析进一步表征。PFE的灭火效率在受控条件下进行了测试,其中由燃烧固体材料和易燃液体引发的火灾。在这两种情况下,都实现了立即消除火焰,从而证明了本工作中获得的PFE在实际应用中的效率。
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Optimization of the active component grinding process and hydrophobization of the obtained powder fire extinguisher
This work presents a grinding process of monoammonium phosphate (MAP) as an active component in a powder fire extinguisher (PFE). The aim was to determine the grinding time for reaching the optimal particle size of MAP necessary for permanent fire extinguishing. MAP grinding was performed by using a laboratory ceramic ball mill and a vibrating cup mill. The grinding process was controlled by sieving using a 100 ?m sieve at precisely defined time intervals. The efficiency of a PFE depends on the share of the -100 ?m fraction of the active component, which has to exceed 60 %. The optimal grain size with 64 % of fraction of particle size -100 ?m was obtained after 33 min of grinding of ?3000 ?m mm grain size MAP by using a ball mill (single-stage grinding). In two-stage process, by grinding the same initial MAP sample (?3000 ?m) in the vibro mill for 10 min, powder with the upper limit grain size of 300 ?m and the mean grain diameter of 120 ?m was obtained. This sample with a reduced size was further ground in the ceramic ball mill yielding 67.5 % of the fraction of particle size -100 ?m after 19 min. The total time of the two-stage grinding process was 29 min. By analyzing the grinding time of MAP required to get the lowest required share of the fraction of particle size -100 ?m that provides the effectiveness of formed PFE it can be concluded that 64 % of this fraction was obtained after 33 min of single-stage grinding, while only after 26 min in the two-stage process. Thus, the grinding time was reduced by 7 min indicating certain energy savings. Stability and hydrophobicity of the obtained PFE were achieved by coating with magnesium stearate (MgSt) at the content of 2 % in a ball mill for 15 min. The coating was confirmed by the standardized procedure for verification of PFE hydrophobic properties in contact with water drops. To obtained PFE had component mass ratios of MAP:AS:CC:QS:MgSt=55:20:18:5:2 (AS-ammonium sulfate; CC-calcium carbonate, QS-quartz sand) and was further characterized by chemical and granulometric analyses. The fire extinguishing efficiency of the PFE was tested in controlled conditions, whereby fires were initiated by burning solid materials and flammable liquids. In both cases, immediate elimination of flames was achieved, thus proving the efficiency of the PFE obtained in this work for practical applications.
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