Flash point of flammable binary mixtures: Synergistic behavior

被引:34
作者
Di Benedetto, Almerinda [1 ]
Sanchirico, Roberto [2 ]
Di Sarli, Valeria [2 ]
机构
[1] Univ Napoli Federico II, Dipartimento Ingn Chim Mat & Prod Ind, Ple Tecchio 80, I-80125 Naples, Italy
[2] CNR, Ist Ric Combust, Ple Tecchio 80, I-80125 Naples, Italy
关键词
Binary liquid mixtures; Intermolecular forces; Non-ideality; Flash point; Safety; VAPOR-LIQUID-EQUILIBRIUM; PREDICTION; MINIMUM; MODEL; EXPRESSION; ETHANOL; SYSTEMS; ENERGY;
D O I
10.1016/j.jlp.2018.01.005
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, the effects of intermolecular forces on Flash Point (FP) of various binary mixtures have been quantified through calculations taking into account their non-ideality. It has been shown that highly non-ideal mixtures with low-boiling azeotrope may have values of the FP lower than the lowest value of FP between those of the pure components. This behavior has been quantitatively linked to the activity coefficients showing that, when they are significantly higher than unity, a synergistic behavior arises strongly lowering the FP of the mixtures. All results were collected in a safety map that represents a starting point for risk evaluation. In conclusion, in the case of non-ideal mixtures with low-boiling azeotrope, from a safety point of view, measurements of the FP at different liquid compositions and/or calculations with reliable models are absolutely necessary, given that the lowest value of FP between those of the pure substances cannot be considered as the most conservative value.
引用
收藏
页码:1 / 6
页数:6
相关论文
共 32 条
[1]   STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS [J].
ABRAMS, DS ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1975, 21 (01) :116-128
[2]   FLAMMABILITY PROPERTIES OF HYDROCARBON SOLUTIONS IN AIR [J].
AFFENS, WA ;
MCLAREN, GW .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1972, 17 (04) :482-&
[3]   APPLICATION OF UNIQUAC EQUATION TO CALCULATION OF MULTICOMPONENT PHASE-EQUILIBRIA .2. LIQUID-LIQUID EQUILIBRIA [J].
ANDERSON, TF ;
PRAUSNITZ, JM .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (04) :561-567
[4]  
[Anonymous], FIRE MAT
[5]  
[Anonymous], 1984, VAPOUR PRESSURE PURE
[6]   The lower explosion point - A good measure for explosion prevention: Experiment and calculation for pure compounds and some mixtures [J].
Brandes, Elisabeth ;
Mitu, Maria ;
Pawel, Dieter .
JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2007, 20 (4-6) :536-540
[7]   Experimental determination and estimation of closed cup flash points of mixtures of flammable solvents [J].
Catoire, L ;
Paulmier, S ;
Naudet, V .
PROCESS SAFETY PROGRESS, 2006, 25 (01) :33-39
[8]   VAPOR-LIQUID-EQUILIBRIUM DATA FOR METHANOL, ETHANOL, METHYL ACETATE, ETHYL-ACETATE, AND O-XYLENE AT 101.3 KPA [J].
COSTALOPEZ, J ;
GARVIN, A ;
ESPANA, FJ .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1995, 40 (05) :1067-1071
[9]  
Crowl D.A., 2002, CHEM PROCESS SAFETY, VSecond
[10]   On the relation between azeotropic behavior and minimum / maximum flash point occurrences in binary mixtures of flammable compounds [J].
da Cunha, Sergio ;
Liaw, Horng-Jang ;
Gerbaud, Vincent .
FLUID PHASE EQUILIBRIA, 2017, 452 :113-134