A reaction device and its application in continuous preparation of vegetable oil polyols
A technology of vegetable oil polyol and reaction device, which is applied in the chemical industry, can solve the problems of high performance requirements, high viscosity and low product quality, and achieves the effects of low performance requirements, solving the problem of pressure difference and good mixing effect.
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Embodiment 1
[0042] Embodiment 1: reaction device
[0043] A reaction device consisting of 4 to 10 glass reactors connected in series; the body of each glass reactor is 500mL; wherein, such as image 3 As shown, a jacket 2 is provided outside the still body 1 of the reaction kettle; a partition 3 is provided inside the kettle body 1 of the reaction kettle, and several arcs are arranged between each adjacent two-layer partition 3 The baffle 4, the arc baffle 4 is fixed on the partitions 3 on both sides; the two sides of the reactor body 1 are provided with hanging lugs.
[0044] Wherein, the top of the kettle body 1 is respectively provided with a thermometer interface 5, a material inlet 8 and a pressure gauge interface 7; the bottom of the kettle body 1 is provided with a material outlet 6; An outlet 9, a heat medium inlet 10 is provided at the lower part of the side wall of the jacket, and an emptying port 11 is provided at the bottom of the jacket.
[0045] Wherein, the kettle body 1 ...
Embodiment 2
[0053] Dissolve 22.0L epoxy olive oil in 66.0L tetrahydrofuran to make component A, and dissolve 1.4L sulfuric acid in 26.4L water to make component B. At the same time, pump them into 8-stage series glass reaction kettles, kettles 1, 2, and 3 The reaction temperature is 40°C, the reaction temperature of kettle 4, 5, 6, and 7 is 45°C, the reaction temperature of kettle 8 is 50°C, and the injection rates of components A and B are 102.0mL / min and 32.8mL / min, respectively. min, the reaction time is 30min, the reaction product is left to separate the liquid, the water phase is recovered, and the oil phase is used with 5wt%Na 2 CO 3 The aqueous solution was washed to neutrality, and then liquid-separated and rotary steamed to obtain olive oil polyol with a hydroxyl value of 222 mg KOH / g and a viscosity of 5440 mPa·s.
Embodiment 3
[0055] Dissolve 22.0L of epoxy peanut oil in 110.0L of tetrahydrofuran to form component A, and dissolve 2.2L of fluoroboric acid in 48.4L of water to form component B. At the same time, pump them into 6-stage series glass reactors. The reaction temperature of kettle 1 is 65°C, the reaction temperature of kettles 2 and 3 is 70°C, the reaction temperature of kettles 4 and 5 is 75°C, the reaction temperature of kettle 6 is 80°C, the injection rates of components A and B are 143.1mL / min, 56.8mL / min, the reaction time is 15min, the reaction product is left to separate liquids, the water phase is recovered, and the oil phase is 5wt%Na 2 CO 3 The aqueous solution was washed to neutrality, and then subjected to liquid separation and rotary evaporation to obtain a peanut oil polyol with a hydroxyl value of 265 mg KOH / g and a viscosity of 5710 mPa·s.
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Abstract
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