Investigation the calcite hydrophobisation of different grain sizes

Mihajlovic, R Slavica; Sekulic, T Zivko; Radulovic, S Dragan; Jovanović, Dj.

doi:10.5937/mmeb1602031m

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“…Da bi se SGP uz pomoć pogonskog gasa uspešno izbacio iz aparata za gašenje požara neophodna je njegova "tečljivost", odnosno forma neaglomerisanog praha. Pojava očvršćavanja SGP nastaje kao posledica upijanja vlage iz atmosfere zbog hidrofilnih osobina pre svega monoamonijum fosfata i kalcijum karbonata koji ulaze u sastav mešavine [11,12]. Smanjenje hidrofilnih svojstava čestica i njihovo potpuno prevođenje u stanje hidrofobnosti postiže se dodavanjem različitih aditiva.…”

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Optimization of the active component grinding process and hydrophobization of the obtained powder fire extinguisher

Mihajlovic

Đorđević

Jovanović

et al. 2021

Hem Ind

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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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