Method for preparing monoisopropanolamine by virtue of reactive rectification
A technology of isopropanolamine and reactive distillation, applied in chemical instruments and methods, preparation of organic compounds, sustainable manufacturing/processing, etc., can solve the problem of high molar ratio of ammonia ring to feed ratio and high ratio of triisopropanolamine  , a large number of equipment and other problems, to achieve the effect of reducing side reactions, reducing energy consumption, saving equipment costs and operating costs
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Embodiment 1
[0029]Reactive distillation tower 1 is a sieve tray tower with 25 actual plates, and its operating pressure is 1.2MPa, which is used to ensure that the press is in a liquid phase state and an effective reaction phase state. mining. The temperature at the top of the tower is controlled at about 35°C, and the temperature at the bottom of the tower is 204-205°C. Water at 25°C enters from the first block of the reactive distillation column 1, and the feed flow rate is 400kg / h. Propylene oxide at 25°C enters from the second plate with a feed flow rate of 1160kg / h. Liquid ammonia enters from the 24th plate of the reactive distillation column 1; the feed flow rate is 340kg / h. The molar ratio of liquid ammonia to propylene oxide is 1:1; the condenser 2 in the tower is a total condenser, and the reboiler 3 in the tower is a kettle-type reboiler, and its heat load is 7863kw. The tower top consists of unreacted ammonia and a small amount of water and propylene oxide, and the bottom st...
Embodiment 2
[0033] Reactive distillation tower 1 is a stainless steel θ-ring packed tower with an equal plate height of 40 blocks. The operating pressure is 1.1 MPa, which is used to ensure that the press is in a liquid phase state and an effective reaction phase state. The top of the tower is fully refluxed and the temperature of the tower is controlled. At about 31°C, the temperature of the tower kettle is about 165°C. Water at 25° C. enters from the top of the reactive distillation column 1, and the feed flow rate is 400 kg / h. Propylene oxide at 25°C enters from a position slightly lower than the water feed, and the feed flow rate is 1160kg / h. Liquid ammonia enters from the bottom of the reactive distillation column 1, and the feed flow rate is 510kg / h. The feed molar ratio of ammonia to propylene oxide was 1.5:1. The condenser 2 in the tower is a total condenser, and the reboiler 3 in the tower is a kettle-type reboiler, and its heat load is 7391kw. The top composition includes unr...
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