Device and process for synthesizing series products of polyester polyol
A technology of polyester polyol and series products, applied in the field of polyester polyol, can solve problems such as low applicability of process technology raw materials, poor adjustability of product performance indicators, no targeted measures for production, etc., and achieve flexible product performance indicators Controllable, simple method, and the effect of improving the control range
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Embodiment 1
[0029] Embodiment 1: as figure 1 As shown, a device for synthesizing polyester polyol series products, including: static mixer M1, feed heater E1, reactor R1, reactor circulating pump P2, reactor powder feed hopper V1, blending tank R2 , blending powder feed hopper V4, distillation tower T1, all gas phase condenser E4, defoaming separator V2, vacuum pump P1, gas-liquid separation tank V3, polyester polyol primary cooler E2 and polyester polyol two stage cooler E3;
[0030] The top of the reactor R1 is equipped with a powder feeding port, a reactor gas phase outlet, a reactor inert gas inlet and a reactor liquid phase material outlet at the bottom, and the reactor R1 powder feeding port is provided with a reactor powder feed hopper V1, the gas phase outlet of the reaction kettle is connected to the side feed port of the distillation tower T1, and the side is equipped with a feed port of the reaction kettle and a return material inlet of the distillation tower, and the return m...
Embodiment 2
[0044] Embodiment 2: In the present embodiment, adopt the device identical with embodiment 1 to carry out polyester polyol series product synthesis, its processing step is:
[0045]2.1. First, purge the whole system with nitrogen. After the purge is completed, start to add diethylene glycol, the addition amount is 410kg. Turn on the reactor circulation pump P2, and the diethylene glycol is heated to 150°C by the feed heater E1. At this time Start to add phthalic anhydride (PA) preheated to 140°C, the addition amount is 250kg, add 25g of terephthalic acid (PIA) powder through the reactor powder feed hopper V1, turn on the reactor stirring device, The material heater E1 and the reactor R1 self-heating system maintain the temperature of the material in the reactor R1 at 220°C for 8 hours. At this time, the pressure of the reactor R1 is a slight positive pressure. Keep it at 30kPa, add 340g of catalyst - n-butyl titanate (TBT) at this time, continue to react for 6 hours, and then ...
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