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    • 26. 发明授权
    • Process for producing acrolein
    • 制备丙烯醛的方法
    • US5326916A
    • 1994-07-05
    • US028534
    • 1993-03-08
    • Yoshinori KobayashiYasuo MatsumotoTadashi MizunoMasamitu Fukuda
    • Yoshinori KobayashiYasuo MatsumotoTadashi MizunoMasamitu Fukuda
    • C07B61/00B01J19/24C07C45/35C07C45/78C07C47/22C07C45/80
    • C07C45/35B01J19/2465C07C45/783
    • A process for producing acrolein which comprises bringing a reaction gas resulting from a catalytic oxidation of propylene into contact in a cooling tower with a condensate which is being circulated through the cooling tower and a circulating part, thereby to cool and separate the reaction gas and discharge an effluent gas from the cooling tower, the condensate in a bottom part of the cooling tower having a temperature of from 35.degree. to 50.degree. C., the effluent gas discharged from the cooling tower having a temperature of from 35.degree. to 55.degree. C., the temperature of the effluent gas being kept nearly equal to or higher than the temperature of the condensate in the bottom part of the cooling tower, and a process for producing acrolein which comprises bringing a reaction gas resulting from the catalytic oxidation of propylene into contact in a cooling tower with a condensate which is being circulated through the cooling tower and a circulating part, thereby to cool and separate the reaction gases, the period of the residence time of the condensate in the cooling tower and the circulating part being from 0.5 to 3 hours.
    • 一种制备丙烯醛的方法,其包括使由丙烯的催化氧化产生的反应气体在冷却塔中与冷却塔中循环的冷凝物和循环部分接触,从而冷却和分离反应气体并将其排出 来自冷却塔的废气,冷却塔底部的冷凝物的温度为35〜50℃,从冷却塔排出的流出气体的温度为35〜55℃ 流出气体的温度保持在冷却塔底部的冷凝水的温度近似等于或高于丙烯醛的制造方法,其特征在于,将由丙烯的催化氧化得到的反应气体 在冷却塔中与通过冷却塔循环的冷凝物和循环部分接触,从而冷却和分离反应物 冷凝塔和循环部分的冷凝水停留时间为0.5〜3小时。