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Journal of Chemical Engineering

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... [Pg.484]

Attarian, C., Baker, C.G. and Svrcek, W.Y., 1976. pH control of a continuous precipitator. Canadian Journal of Chemical Engineering, 54, 606-611. [Pg.299]

Bohlin, M. and Rasmuson, A.C., 1992. Application of controlled cooling and seeding in batch crystallization. Canadian Journal of Chemical Engineering, 70, 120-126. [Pg.301]

Jones, A.G. and Mydlarz, J., 1990a. Continuous crystallization of potash alum. MSMPR kinetics. Canadian Journal of Chemical Engineering, 68, 250-259. [Pg.311]

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. [Pg.313]

Momonaga, M., Yazawa, H. and Kagara, K., 1992. Reactive crystallization of methyl Q-methoxyimino acetoacetate. Journal of Chemical Engineering of Japan, 25, 237-242. [Pg.315]

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. [Pg.320]

Tavare, N.S., 1986. Crystallization kinetics from transients of an MSMPR crystallizer. The Canadian Journal of Chemical Engineering, 64, 752-758. [Pg.324]

Wachi, S., Morikawa, H. and Ueyama, K., 1987. Gas hold-up and axial dispersion in gas-liquid concurrent bubble column. Journal of Chemical Engineering Japan, 20, 309-316. [Pg.326]

Bauer, RE. Maciel, R. (2004) Incorporation of Environmental Impact Criteria in the Design and Operation of Chemical Processes. Brazilian Journal of Chemical Engineering, 21(3), 405-414. [Pg.269]

Figure 12.2 The operability region for the consecutive chemical reactions example [reprinted from the Canadian Journal of Chemical Engineering with permission]. 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]. 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].
Miranda, L.A.S., Henriques, J.A.P., and Monteggia, L.O., A full-scale UASB reactor for treatment of pig and cattle slaughterhouse wastewater with a high oil and grease content, Brazilian Journal of Chemical Engineering, 22 (4), 601-610, 2005. Available at http //www.sieclo.br/scielo.php. [Pg.1250]

Oliver, D.R. and Bragg, R., Flow patterns in viscoelastic liquids upstream of orifices, Canadian Journal of Chemical Engineering, 51, pp. 287-90 (1973). [Pg.138]

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. [Pg.328]

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. [Pg.328]

See other pages where Journal of Chemical Engineering is mentioned: [Pg.215]    [Pg.250]    [Pg.552]    [Pg.552]    [Pg.312]    [Pg.154]    [Pg.154]    [Pg.27]    [Pg.205]    [Pg.219]    [Pg.219]    [Pg.737]    [Pg.738]    [Pg.227]    [Pg.49]   


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