New method for preparing tripropylene glycol
A technology for tripropylene glycol and dipropylene glycol, which is applied in the field of preparing tripropylene glycol, can solve the problems of low yield of tripropylene glycol, increase in manufacturing cost, etc., and achieves reduction in the generation of by-products, low energy consumption, and low cost. high rate effect
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Embodiment 1
[0015] The raw material dipropylene glycol is pumped into the static tubular reactor to the visible liquid level, and when the temperature is raised to 140°C, the system starts to feed continuously, wherein the feed amounts of the raw materials are: dipropylene glycol ( DPG) feed rate is 5.36L / h, propylene oxide (PO) feed rate is 1.32L / h, catalyst sodium ethoxide feed rate is 2.47mL / h. The reaction temperature is controlled at 120-140°C, the reaction pressure is not particularly limited, and the output is controlled at about 6.8L / h. Detection content: 43.2% of dipropylene glycol, 54.1% of tripropylene glycol, and 2.0% of tetrapropylene glycol.
Embodiment 2
[0017] The raw material dipropylene glycol is pumped into the static tubular reactor to the visible liquid level, and when the temperature is raised to 125°C, the system starts to feed continuously, wherein the feed amounts of the raw materials are: dipropylene glycol ( DPG) feed rate is 0.48m3 / h, propylene oxide (PO) feed rate is 0.17m3 / h, catalyst sodium methoxide feed rate is 2.00L / h. The reaction temperature is controlled at 110-130°C, the reaction pressure is not particularly limited, and the output is controlled at about 0.6 m3 / h. Detection content: dipropylene glycol 36.6%, tripropylene glycol 61.3%, and tetrapropylene glycol 1.7%.
Embodiment 3
[0019] The raw material dipropylene glycol is pumped into the static tubular reactor to the visible liquid level, and when the temperature is raised to 150°C, the system starts to feed continuously, wherein the feed amounts of the raw materials are: dipropylene glycol ( DPG) feed rate is 0.83m3 / h, propylene oxide (PO) feed rate is 0.28m3 / h, catalyst sodium methoxide feed rate is 3.44L / h. The reaction temperature is controlled at 150-160°C, the reaction pressure is not particularly limited, and the output is controlled at about 1.1 m3 / h. Detection content: dipropylene glycol 37.1%, tripropylene glycol 60.4%, and tetrapropylene glycol 2.4%.
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