Abstract:Equipment has been designed and assembled in such a way that direct microscopic observation of polymer particle formation in suspension polymerization of vinyl chloride and vinyl acetate is possible. The apparent mode of transformation from monomer droplets into polymer particles has thus been studied under two sets of conditions: (1) with agitation and (2) without agitation. In both cases, as the initial vinyl acetate/vinyl chloride ratio was raised, the apparent change in the shape and transparency of partic… Show more
“…In addition, the electrostatic stabilization (stability of primary particles) is affected by reaction temperature (6 1, 65,84). agitation level (62,63,71,87,96,101,102) and additive type and level (67,74,75,(78)(79)(80).…”
A review of relevant microscopic processes, both chemical and physical, which occur during suspension, bulk and emulsion polymerization (both before and after pressure drop) is given. The state of the art of kinetic modelling of monomer consumption rate, reactor pressure, molecular weight and short and long chain branching development and polymer chain microstructure is illustrated. The effects of diffusion-controlled termination and propagation reactions and the significant decrease in initiator efficiency and decomposition rate constant at high monomer conversions on the relative rates of various chemical reactions are discussed. The application of temperature programming and semibatch operation are emphasized. Finally, attempts to model polymer particle morphology are described.
“…In addition, the electrostatic stabilization (stability of primary particles) is affected by reaction temperature (6 1, 65,84). agitation level (62,63,71,87,96,101,102) and additive type and level (67,74,75,(78)(79)(80).…”
A review of relevant microscopic processes, both chemical and physical, which occur during suspension, bulk and emulsion polymerization (both before and after pressure drop) is given. The state of the art of kinetic modelling of monomer consumption rate, reactor pressure, molecular weight and short and long chain branching development and polymer chain microstructure is illustrated. The effects of diffusion-controlled termination and propagation reactions and the significant decrease in initiator efficiency and decomposition rate constant at high monomer conversions on the relative rates of various chemical reactions are discussed. The application of temperature programming and semibatch operation are emphasized. Finally, attempts to model polymer particle morphology are described.
“…The PVAc is soluble in VAM [59]. The monomer dissolves its polymer and the monomer droplets exhibit a viscous syrup step to finally leading to solid clear little spheres called beads.…”
Section: Suspension Polymerization Of Vinyl Acetate Monomermentioning
OATAO is an open access repository that collects the work of Toulouse researchers and makes it freely available over the web where possible.Liquid-liquid dispersion in a continuous oscillatory baffled reactor -Application to suspension polymerization
b s t r a c tReducing energy costs, improving safety, minimizing waste are the current aims of chemical engineering. Process intensification in fine chemistry has been extensively studied but less work refers to heterogeneous reactions involving two liquid phases. This paper focuses on batch to continuous suspension polymerization transposition and especially on the liquid-liquid dispersion step. The main features of suspension polymerization reaction are based on (i) the initial liquid-liquid dispersion requiring a controlled size and narrow distribution and (ii) on the control of the final particle size during the agglomeration step by avoiding fouling which is a bottleneck for continuous flow. For the continuous transposition, liquid-liquid dispersion and reaction studies are carried out in continuous oscillatory baffled reactor (COBR) which is a multipurpose reactor. Its suitability to overcome the bottlenecks is demonstrated through the investigation of the oscillating and flow conditions or the dispersed phase holdup. A controlled droplet size distribution can be achieved. Oscillation is the main parameter responsible for droplet breakage. The suitable conditions to obtain stable dispersion are determined. For one of the first times, COBR is used for suspension polymerization.
“…[9][10][11][12][13] The sizes of the polymer colloidal particles prepared so far lie in the range from 10 nm-10 mm depending on the method employed, which includes emulsion polymerization, 14 microemulsion polymerization, 15,16 miniemulsion polymerization, 17 soap-free polymerization, 18,19 dispersion polymerization, 20 seed polymerization, 21 and suspension polymerization. 22 Among these methods, microemulsion polymerization is the most commonly-used technique to prepare polymer colloids with diameters <100 nm and narrow size distributions. 15,16 Such small polymer particles are desirable for surface coatings because it takes only a short time for film formation and the particles can penetrate easily into porous substrates producing a film with good optical and mechanical properties.…”
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