Process for the manufacture of thermoplastic polymer particles, thermoplastic polymer particles prepared thereby, and articles prepared therefrom
A thermoplastic polymer and particle technology, applied in the field of preparing thermoplastic polymer particles, can solve problems such as poor particle yield
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Embodiment 1
[0115]Examples 1-9 show polymer particles prepared from polycarbonate PC-2. As shown in Table 2 in Examples 1-6, by controlling the speed of the homogenization tool, the particle size distribution can be varied for a range of Dv50 values (5.6 to 21.7). This was determined by using two polymer concentrations (20% and 25%) and a range of oil bath temperatures (70 to 90°C) to determine homogenizer agitation speed (from 5,000 to 22,000 in rpm) and time (from 10 to 20 minutes) to complete. Examples 7-9 show conditions that do not result in proper dispersion or precipitation of the polymer. For each of Examples 7-9, agglomeration of the particles occurred during the precipitation step and the yield of the process was less than 30%. Without wishing to be bound by theory, it is believed that a number of components are responsible for stabilizing the emulsion under high temperature precipitation conditions, such as mixing intensity, volume ratio of immiscible solvents, homogenizati...
Embodiment 11-28
[0119] Examples 11-20 demonstrate the effect of homogenizer agitation speed and surfactant concentration on Dv50. In these examples, SDBS surfactant was used to prepare the aqueous polymer dispersions of the polymers. Two surfactant concentrations, 0.01 wt.% and 0.5 wt.% aqueous solutions were used in the following examples. For each example, 200 g of polymer was dissolved in 800 g of dichloromethane to yield a 20 wt.% polymer solution. The emulsion was prepared using a weight ratio of water to organic phase of 0.6. The examples demonstrate emulsion stability and particle size distribution while homogenizing at 2,800 and 15,000 rpm for extended periods of time (eg, at least 20 minutes). These two homogenization speeds represent control over the shear rate of the emulsion system. The emulsion was converted to an aqueous polymer dispersion using Method A for particle precipitation according to the method described above. Experimental variables and results are shown in Table ...
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