[1] Banu, I., (2009). “Modeling and optimization of tubular polymerization reactors”. Université Claude Bernard-Lyon I.
[2] Lynn, S. and J.E. Huff., (1971). “Polymerization in a tubular reactor”. AIChE Journal. 17(2): p. 475-481.
[3] Kleinstreuer, C. and S. Agarwal., (1986). “Coupled heat and mass transfer in laminar flow, tubular polymerizers”. International journal of heat and mass transfer. 29(7): p. 979-986.
[4] Chen, C. and E. Nauman., (1989). “Verification of a complex, variable viscosity model for a tubular polymerization reactor”. Chemical engineering science. 44(1): p. 179-188.
[5] Fan, S., Gretton-Watson, S., Steinke, J., Alpay, E., (2003). “Polymerization of methyl methacrylate in a pilot-scale tubular reactor: modeling and experimental studies”. Chemical engineering science. 58(12): p. 2479-2490.
[6] Baillagou, P. and D. Soong., (1985). “Molecular weight distribution of products of free radical nonisothermal polymerization with gel effect. Simulation for polymerization of poly (methyl methacrylate). Chemical engineering science. 40(1): p. 87-104.
[7] Baillagou, P. and D. Soong., (1985). “Major factors contributing to the nonlinear kinetics of free-radical polymerization”. Chemical engineering science. 40(1): p. 75-86.
[8] Pinto, J. and W. Ray., (1995). “The dynamic behavior of continuous solution polymerization reactors—VII. Experimental study of a copolymerization reactor”. Chemical engineering science. 50(4): p. 715-736.
[9] Soroush, M. and C. Kravaris., (1992). “Nonlinear control of a batch polymerization reactor: an experimental study”. AIChE journal. 38(9): p. 1429-1448.
[10] Perry, R.H., D.W. Green, and J.O. Maloney., (1984). “Perry's chemical engineer's handbook, in Perry's chemical engineer's handbook”. McGraw-Hill Book.
[11] Treybal, R.E. and E. Treybal Robert., (1968). “Mass-transfer operations”. Vol. 3. McGraw-Hill New York.
[12] Fogler, H.S., (1999). “Elements of chemical reaction engineering”. McGraw-Hill New York.
[13] Nauman, E.B., (2002). “Chemical reactor design, optimization, and scaleup”. Wiley New York etc.
[14] Scorah, M., R. Dhib, and A. Penlidis., (2006). “Modelling of free radical polymerization of styrene and methyl methacrylate by a tetrafunctional initiator”. Chemical engineering science. 61(15): p. 4827-4859.
[15] Garg, R.K., M. Vashishta, and V. Srivastava., (2007). “A Modeling Approach to Reaction of Non-Newtonian Fluids in Tubular Reactor”. Polymer-Plastics Technology and Engineering. 46(10): p. 965-971.
[16] Levenspiel, O., (1972). “Chemical reaction engineering”. Vol. 2. Wiley New York etc.
[17] Bird, R., W. Stewart, and E. Lightfoot., (1960). “Transport Phenomena”. Wiley New York etc.
[18] Merrill, L.S. and C.E. Hamrin., (1970). “Conversion and temperature profiles for complex reactions in laminar and plug flow”. AIChE Journal. 16(2): p. 194-198.
[19] Chhabra, R.., (1999). “Laminar boundary layer heat transfer to power law fluids: an approximate analytical solution”. Journal of chemical engineering of Japan. 32(6): p. 812-816.
[20] Chhabra, R.P. and J.F. Richardson., (1999). “Non-Newtonian Flow: Fundamentals and Engineering Applications”. Butterworth-Heinemann.