Canadian Journal of Chemical

Mackay, D. and R. S. Matsugo, 1973, Evaporation Rates of Liquid Hydrocarbon Spills on Land and Water, Canadian Journal of Chemical Engineering, 51,434-439... 

Attarian, C., Baker, C.G. and Svrcek, W.Y., 1976. pH control of a continuous precipitator. Canadian Journal of Chemical Engineering, 54, 606-611. 

Bohlin, M. and Rasmuson, A.C., 1992. Application of controlled cooling and seeding in batch crystallization. Canadian Journal of Chemical Engineering, 70, 120-126. 

Jones, A.G. and Mydlarz, J., 1990a. Continuous crystallization of potash alum. MSMPR kinetics. Canadian Journal of Chemical Engineering, 68, 250-259. 

Kotaki, Y. and Tsuge, H., 1990. Reactive crystallization of calcium carbonate by gas-liquid and liquid-liquid reactions. Canadian Journal of Chemical Engineering, 68, 435 42. 

Roliani, S. and Paine, K., 1987. Measurement of solids concentration of a soluble compound in a saturated slurry. Canadian Journal of Chemical Engineering, 65, 163. 

Tavare, N.S., 1986. Crystallization kinetics from transients of an MSMPR crystallizer. The Canadian Journal of Chemical Engineering, 64, 752-758. 

Figure 12.2 The operability region for the consecutive chemical reactions example [reprinted from the Canadian Journal of Chemical Engineering with permission].

Figure 14.1 Vapor-liquid equilibrium data and calcidated values for the n-pentane-acetone system, x andy are the mole fractions in the liquid and vapor phase respectively [reproduced with permission from Canadian Journal of Chemical Engineering].

Oliver, D.R. and Bragg, R., Flow patterns in viscoelastic liquids upstream of orifices, Canadian Journal of Chemical Engineering, 51, pp. 287-90 (1973). 

Yin, G. Ni, Y., (1998) Quantitative description of the chloride effect on chlorine dioxide generation from the C102-H0C1 reaction. Canadian Journal of Chemical Engineering, 76, 921-926. 

Ni, Y. Wang, X. (1996) Mechanism and kinetics of chlorine dioxide reaction with hydrogen peroxide under acidic conditions. Canadian Journal of Chemical Engineering, 75, 31-36. 

Lee, L.S., Chen, T.W., Haunh, T.N., and Pan, W.Y. (1989) Four lump kinetic model for fluid catalytic cracking process. Canadian Journal of Chemical Engineering, 67, 615. 

Govier and Omer, in a recent article in the Canadian Journal of Chemical Engineering, have summarized the present (G4) state of knowledge concerning the calculation of pressure drop and other quantities in two-phase flow The principal flow patterns are understood in a qualitative way and the effect on flow pattern of the major variables, mainly the lineal or maffi velocities of the phases, is recognized. In nearly all cases the real significance of the viscosities of the phases, the possible separate roles of the densities of the phases, and the influence of the diameter of the pipe is not known. 

Beltran F J, Encinar J M, Garcia-Araya J F (1992 b) Absorption Kinetics of Ozone in Aqueous o-Cresol Solutions, Canadian Journal of Chemical Engineering 70 141-147. 

Metha Y M, George C E, Kuo C H (1989) Mass Transfer and Selectivity of Ozone Reactions, The Canadian Journal of Chemical Engineering 67 118-126. 

St -Denis C E, Fell C J (1971) Diffusivity of oxygen in water, Canadian Journal of Chemical Engineering 49 885. 

S. Zine, A. Sayari and A. Ghorbel, Catalytic Nitroxydation of Paraxylene over chromium oxide Based catalysts the Canadian Journal of chemical Engeneering, vol. 65 February, 1987 pp 127 - 131. 

Rahman, M.H., Wasiuddin, N.M. and Islam, M.R. (2004) Experimental and numerical modeling studies of arsenic removal with wood ash from aqueous streams. Canadian Journal of Chemical Engineering, 82(5), 968-77. 

Sagitova, F Bejan, D Bunce, N.J. and Miziolek, R. (2005) Development of an electrochemical device for removal of arsenic from drinking water. Canadian Journal of Chemical Engineering, 83(5), 889-95. 

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