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Tytuł artykułu

Toluene Mono-nitration in a Semi-batch Reactor

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Języki publikacji
EN
Abstrakty
EN
Toluene mono-nitration in a semi-batch reactor was investigated with reaction calorimeter (RC1). The mixed acid HNO3/H2SO4/H2O (wt%) was used in proportion 13/66/21, which is similar to industrial parameters. The exothermic rates at different reaction temperatures were compared, and then the curves of heat generation rate after dosing were analyzed. The Maximal Temperature attainable by runaway of the desired Synthetic Reaction (MTSR) under different conditions were calculated for the course hazard evaluation. The results showed that the average reaction heat of mono-nitration was between 169.07~177.11 kJ mol-1, and the special heat of reactant was about 2 kJ kg-1 K-1. Average Ea of second order kinetic was about 30 kJ mol-1, and reaction rate was 10-4 mol s-1 l-1 order of magnitude when the strength of sulphuric acid was about 73.5%. It was also found that when temperature or stirring speed increases, the potential heat accumulation decreases.
Rocznik
Strony
37--47
Opis fizyczny
Bibliogr. 15 poz.
Twórcy
autor
autor
autor
autor
autor
  • Dept. of Safety Eng., Sch. of Chem. Eng., Nanjing Univ. of Sci. & Tech. (NUST), Nanjing, 210094, P R China, cc200707@hotmail.com
Bibliografia
  • [1] Dong Y., Improvement of Manufacture Technics in Toluene Mononitration, Modern chemistry engineering, 1998, (5), 20-21.
  • [2] Cai C., Lu C.X,. Nitration of Toluene with NO2-O2 System, Chinese Journal of Explosives & Propellants, 2003, 26(2), 1-2,21.
  • [3] Lu C.X., Nitration Theory, Jiangsu Science and Technology Publishing House, Nanjing 1993, 125-131.
  • [4] Hanson C., Marsland J.G., Macrokinetics of Toluene Nitration Chemical Engineering Science, Pergamon Press, 1971, Vol. 26, pp. 1513-1520.
  • [5] Hanson C., Ismail H.A.M., Macrokinetics of Toluene and Benzene Nitration under Laminar Condition, Chemical Engineering Science, 1977, 32, 775-777.
  • [6] Zaldivar J.M., Molga E., Alos M.A., Hernandez H., Aromatic Nitration by Mixed Acid. Fast Liquid-Liquid Reaction Regime, Chemical Engineering and Progressing, 1996, 35, 91-105.
  • [7] Zaldivar J. M., Barcons C., Hernandez H., Molga E., ibid., 1995, 35, 543-559.
  • [8] Chun-Yu Chen, Chia-Wei Wu, Thermal Hazard AssessmentaAnd Macrokinetics Analysis of Toluene Mononitration in a Batch Reactor, J. Loss Prevent. Industries, 1996, 9(5), 309-316.
  • [9] Kuo-Ming Luo, Jih-Guang Chang, The Stability of Toluene Mononitration In Reaction Calorimeter Reactor, ibid., 1998, 11, 81-87.
  • [10] D’Angelo F.A., Brunet L., Cognet P., Cabassud M., Modeling and Constraint Optimisation of an Aromatic Nitration in Liquid-Liquid Medium, Chem. Eng. J., 2003, 91, 75-8.
  • [11] Field John P., Strachan N., Dependence of the Rate Constanta and Activation Energy of Aromatic Nitration on Mixed Acid Composition, Ind. Chem. Prod, 1982, 21, 352-355.
  • [12] Albright L.F., Hanson C., Industrial and Laboratory Nitrations, ACS, Washington, 1976, 210-211.
  • [13] Gygax R., Chemical Reaction Engineering for Safety, Chem. Eng. Sci., 1988, 43(8), 1759-1771.
  • [14] Cox P.R., Strachan A.N., Two Phase Nitration of Toluene-I, ibid., 1972, 21, 457-463.
  • [15] Chapman J.W., Cox P.R., Strachan A.N., Two Phase Nitration of Toluene-III., ibid., 1974, 29, 1247-1251.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BAT1-0034-0048
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