Bibliografia
1
BIBLIOGRAFIA
[1] Albert, M., Garcia, B.C., Kuhenert, C., Peschala, R.,& Maurer, G. (2000). Vapor-liquid equilibrium of aqueous solutions of formaldehyde and methanol.
A.I.Ch.E.J.,46,1676-1687.
[2] Astarita, G., & Savane, D.W. (1980). Gas absorption and desorption with reversibile instantaneous chemical reaction. Chem. Engng Sci., 35, 1755-1764. [3] Bell, R.P., Evans, F.R.S., & Evans, P.G. (1966). Kinetics of the dehydration of methylene glycol in aqueous solution. Proc. Roy. Soc. (London) Ser.A, 291,297-323.
[4] Billet, R., Schultes, M. (1999).Prediction of mass transfer columns with dumped and arranged packings. Trans IChemE, Vol. 77, Part A.
[5] Bourne, J.R., Von Stockar, U., & Coggan, G.C.(1974). Gas absorption with heat effects. I. Anew computation method. Ind.Eng.Chem.Process Des.Dev., 13,115-123.
[6] Brandani, V.,Di Giacomo, G. & Foscolo, P.U. (1980). Isothermal vapor-liquid equilibria for water-formaldehyde system. A predictive thermodynamics model. Ind.Eng. Chem. Process Des. Dev.19,179.
[7] Brunazzi, E., Paglianti A., Petarca L. (1996). Design of absorption columns equipped with structured packings. Rich Mac Magazine.78.459-463.
[8] Burnett, M.G. (1982). The mechanism of the formaldehyde clock reaction. J. Chem.Ed., 59, 160-162.
[9] Coulson & Richardson (1991).Chemical Engineering.Vol.1: Fluid flow,heat transfer and mass transfer. 5th ed., Butterworth Heinemann.
[10] Coulson & Richardson (1991).Chemical Engineering.Vol.6: Chemical Engineering Design. 3th ed., Butterworth Heinemann.
[11] Feintuch, H.M., & Treybal, R.E. (1978). The desing of adiabatic packed towers for gas absorption and stripping. Ind.Eng.Chem.Process Des.Dev., 17,505. [12] Hasse, H. & Maurer, G.,(1991). Vapor-liquid equilibrium of
Bibliografia
2 [13] Hitch, D.M., Rousseau, R.W., & Ferell, J.K. (1986). Simulation of
continuous separation processes: multicomponent, adiabatic absorption. Ind.Eng.Chem.Process Des.Dev., 25.699.
[14] Hitch, D.M., Rousseau, R.W., & Ferell, J.K. (1986). Simulation of continuous separation processes: unsteady state multicomponent, adiabatic absorption. Ind.Eng.Chem.Process Des.Dev., 26.1092.
[15] Iliceto, A. (1954). Sul sistema acqua-formaldeide. Nota VI. Equilibri delle fasi liquida e gassosa. Gazz. Chim. Ital., 84,536-552.
[16] Kelly, R.M., Rousseau, R.W., & Ferell, J.K. (1984). Design of packed, adiabatic absorbers: physical absorption of acid gases in methanol. . Ind.Eng.Chem.Process Des.Dev., 23.102.
[17] King, C.J. (1980). Separation Processes, 2nd ed., New York; McGraw-Hill. [18] Kogan, L.V. Blazhin, Y.M. Ogorodnikov, S.K.,& Kafarov, V.V. (1977).
Liquid-vapor equilibrium in the system formaldehyde-water. Zhur. Prikl. Khim., 50,2682-2687.
[19] Krishnamurthy, R. & Taylor, R. (1985a). A non-equilibrium stage model of milticomponent separation processes. Par I: Model description and method of solution. A.I.Ch.E.J., 31,449.
[20] Krishnamurthy, R. & Taylor, R. (1985b). A non-equilibrium stage model of milticomponent separation processes. Par II: Comparison with experiment. A.I.Ch.E.J., 31,456.
[21] Krishnamurthy, R. & Taylor, R. (1985c). Simulation of packed distillation and absorption columns. Ind.Eng.Chem.Process Des.Dev., 24.513.
[22] Krishnamurthy, R. & Taylor, R. (1986).Absorber simulation and design using a non-equilibrium stage model. Can.J.Chem.Eng., 64.96.
[23] Levenspiel, O. Ingegneria delle reazioni chimiche. Edizione italiana 2nd ed., casa editrice ambrosiana Milano.
[24] Mark E. Davis. Numerical Methods & Modeling for chemical engineers. [25] Maurer, G. (1986). Vapor-liquid equilibrium of formaldehyde and water
containing multicomponent mixtures. A.I.Ch.E.J.,32,932-948.
[26] Onda, K., Takeuchi, H., & Okumoto, Y. (1968). Mass transfer coefficients between gas and liquid phases in packed columns. J. Chem. Eng. Japan,1,56-62.
Bibliografia
3 [27] Onda, K., Sada, E., Kobayashi, T., & Fujine, M. (1970). Gas absorption
accompanied by complex chemical reaction – I Reversible chemical reaction. J. Chem. Engng Sci.,25,753-760.
[28] Perry, R.H., Green, D.W. & Maloney, J.O., (1997). Perry’s Chemical Engineering Handbook, McGraw-Hill, New York.
[29] Raal, J.D., & Khurana, M.K. (1973). Gas absorption with large heat effects in packed columns. Can. J. Chem. Eng., 51,162.
[30] Reid, C.R., Prausnitz, J.M., & Poling, B.E. (1988). The properties of Gases and Liquids. 4th ed., New York; McGraw-Hill.
[31] Stockar, U. V., & Wilke, C.R. (1977). Rigorous and short-cut design calculations for gas absorption involving large heat effects. 1.A new computation method for packed gas absorbers. Ind.Eng.Chem.Fundam., 16.88-93.
[32] Suess, P., Spiegel, L. (1992). Hold-up of Mellapak structured packings.Chemical Engineering and Processing, 31,119-124.
[33] Sutton , H.C. & Downes, T.M. (1972). Rate of hydration of formaldehyde in aqueous solution. J.Chem.Soc.,Chem. Comm.,1-2.
[34] Treybal, R.E. (1969). Gas absorption and stripping in packed towers. Ind.Eng.Chem., 61,36.
[35] Ulmann. Formaldehyde Vol. 15. pag.1-34.
[36] Walker, J.F. (1964). Formaldehyde. 3rd ed., ACS Monograph Series, Reinhold, New York.
[37] William, J.P. (2001). Matlab 6 per l’ingegneria e le scienze. McGraw-Hill, New York.
[38] Winkelman, J.G.M., Sijbring, H., Beenackers, A.A.C.M. & De Vries,E.T. (1992). Modeling and simulation of industrial formaldehyde absorbers. Chem.Engng Sci.,47, 3785.
[39] Winkelman, J.G.M., & Beenackers, A.A.C.M. (1993). Simultaneous absorption and desorption with reversible first-order chemical reaction: analytic solution and negative enhancement factor. Chem.Engng Sci.,48, 2951-2955.
[40] Winkelman, J.G.M.,Ottens,M.,& Beenackers,A.A.C.M.(2000). The kinetics of the dehydration of methylene glycol. Chem.Engng Sci.,55 , 2065-2071.
[41] Winkelman, J.G.M., & Beenackers, A.A.C.M. (2000). Correlations for the density and viscosity of aqueous formaldehyde solutions. Ind.Eng.Chem.Res.,39, 557-562.
Bibliografia
4 [42] Winkelman, J.G.M., Voorwinde, O.,Ottens,M., Beenackers, A.A.C.M. &
Jansses, L.P.B.M. (2002). The kinetics of the hydration of formaldehyde. Chem.Engng Sci.,57 , 4067-4076.
