Preparation method of thermoplastic polyurethane
A thermoplastic polyurethane and diisocyanate technology, applied in the field of thermoplastic polyurethane preparation, can solve problems such as complex thermoplastic polyurethane methods, and achieve the effects of eliminating quality fluctuation, simple and reliable preparation process, and satisfying the requirements of quality stability
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Embodiment 1
[0012] Embodiment 1: first 1000 kilograms of polytetrahydrofuran polyols, 517 kilograms of diphenylmethane diisocyanate and 99.7 kilograms of butanediol chain extenders are added to a reactor, such as a twin-screw reaction extruder, while adding an organotin catalyst 30ppm (relatively Polytetrahydrofuran polyol), after the reaction, it is directly extruded from the twin-screw to granulate.
[0013] According to the quality requirements of the product (melt index 3 ~ 5g / 10min), set the channel of the time-melt strength rheological curve, that is, set the curve of the product with a melt index of 3g / 10min as the upper limit, and set the product with a melt index of 5g / 10min This curve is set as the lower limit. In the production process, if the rheological curve formed by time and melt strength is lower than the lower limit, the screw speed is reduced from 170 rpm to 120 rpm to return the rheological curve to the channel.
Embodiment 2
[0014] Embodiment 2: first 500 kilograms of polytetrahydrofuran polyols, 275 kilograms of diphenylmethane diisocyanate and 49.9 kilograms of butanediol chain extenders are added to a reactor, such as a twin-screw reaction extruder, while adding an organotin catalyst 30ppm (relatively Polytetrahydrofuran polyol), after the reaction, it is directly extruded from the twin-screw to granulate.
[0015] According to the quality requirements of the product (melt index 16 ~ 18g / 10min), set the channel of the time-melt strength rheological curve, that is, set the upper limit of the curve for the product with a melt index of 16g / 10min, and set the product with a melt index of 18g / 10min This curve is set as the lower limit. In the production process, if the rheological curve formed by time and melt strength is lower than the lower limit, the amount of catalyst can be increased from 30ppm to 50ppm to make the rheological curve return to the channel.
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