TY - JOUR
T1 - Influence of organic acid on thermal hazard of hydrogen peroxide
AU - Zang, Na
AU - Qian, Xinming
PY - 2012
Y1 - 2012
N2 - The effect of methanoic acid and acetic acid with hydrogen peroxide on oxidative desulphurization was investigated by accelerating rate calorimeter (ARC) in this paper. Their reaction order n, activation energy Ea and pre-exponential factor A were calculated from these curves before and after modification of instrument constant, i.e. thermal inertia factor of ARC. The adiabatic decomposition parameters obtained show that hydrogen peroxide is of a character, i.e. it can be easily decomposed by adding methanoic acid or acetic acid. The decomposition is the easiest and activation energy lower for adding methanoic acid, which is from 179.34 kJ·mol-1 to 84.25 kJ·mol-1 and 68.35 kJ·mol-1, respectively. The rate of temperature rise is the biggest and the rise of adiabatic temperature the highest, and the decomposition the most intense, and the risk the highest. Finally, the temperature of no return TNR and self accelerating decomposition temperature TSADT of hydrogen peroxide with some specific package were calculated by kinetic parameters, which were 312.77 K, 308.23 K respectively. However, in order to control fire or explosion of oxidative desulphurization process, the technological temperature of oil desulphurization should not be larger than their initial decomposition temperature 295.49 K and 324.38 K.
AB - The effect of methanoic acid and acetic acid with hydrogen peroxide on oxidative desulphurization was investigated by accelerating rate calorimeter (ARC) in this paper. Their reaction order n, activation energy Ea and pre-exponential factor A were calculated from these curves before and after modification of instrument constant, i.e. thermal inertia factor of ARC. The adiabatic decomposition parameters obtained show that hydrogen peroxide is of a character, i.e. it can be easily decomposed by adding methanoic acid or acetic acid. The decomposition is the easiest and activation energy lower for adding methanoic acid, which is from 179.34 kJ·mol-1 to 84.25 kJ·mol-1 and 68.35 kJ·mol-1, respectively. The rate of temperature rise is the biggest and the rise of adiabatic temperature the highest, and the decomposition the most intense, and the risk the highest. Finally, the temperature of no return TNR and self accelerating decomposition temperature TSADT of hydrogen peroxide with some specific package were calculated by kinetic parameters, which were 312.77 K, 308.23 K respectively. However, in order to control fire or explosion of oxidative desulphurization process, the technological temperature of oil desulphurization should not be larger than their initial decomposition temperature 295.49 K and 324.38 K.
KW - Accelerating rate calorimeter (ARC)
KW - Hydrogen peroxide
KW - Organic acid
KW - Thermal hazard
KW - Thermodynamic
UR - http://www.scopus.com/inward/record.url?scp=84891702481&partnerID=8YFLogxK
U2 - 10.1016/j.proeng.2012.08.198
DO - 10.1016/j.proeng.2012.08.198
M3 - Conference article
AN - SCOPUS:84891702481
SN - 1877-7058
VL - 45
SP - 526
EP - 532
JO - Procedia Engineering
JF - Procedia Engineering
T2 - 2012 8th International Symposium on Safety Science and Technology, ISSST 2012
Y2 - 23 October 2012 through 26 October 2012
ER -