首页> 外国专利> CONVERSION METHOD OF HYDROCARBON BY TREATING WITHIN DISTILLATION ZONE CONTAINING CIRCULATORY REFLUX SUBSTANCE COMBINED WITH REACTION ZONE AND USING METHOD THEREOF FOR HYDROGENATION OF BENZENE

CONVERSION METHOD OF HYDROCARBON BY TREATING WITHIN DISTILLATION ZONE CONTAINING CIRCULATORY REFLUX SUBSTANCE COMBINED WITH REACTION ZONE AND USING METHOD THEREOF FOR HYDROGENATION OF BENZENE

机译:含循环回流物质与反应区结合的精馏区内处理的烃转化方法及其使用的苯加氢方法

摘要

PROBLEM TO BE SOLVED: To decrease the reflux rate and improve the conversion rate of hydrocarbon, wherein a portion of introducing a hydrocarbon material into a distillation column is drawn into a hydrogenation reactor placed at the outside of the distillation column to be hydrogenated followed by re-introduction into the distillation column at a higher position than the drawing position and at a lower temperature than the drawing temperature with continuous distillation. ;SOLUTION: When treating within a zone generating a vapor-distilled fraction of the top part and effluence of the bottom part after introducing a hydrocarbon material into a distillation column 2 through a duct 1, the liquid drawn through the duct 15 is hydrogenated with hydrogen through a tube line 4 followed by transporting said liquid into the top part of a hydrogenation reactor 3 where a conversion reaction of a portion of the hydrocarbon material (e.g. benzene) is performed. Then, after cooling effluence of reactor 3 preferably at least 10°C lower than the drawing temperature in a heat-exchanger 16, the cooled effluence is re-introduced into the distillation column 2 through the duct 17 at a higher position than that of the drawing tube line 15. As a result, this can also lead to reduction of the distillation zone size.;COPYRIGHT: (C)1999,JPO
机译:解决的问题:为了降低回流速率并提高烃的转化率,其中将将烃类材料引入蒸馏塔的一部分被吸入位于蒸馏塔外部的氢化反应器中进行氢化,然后再进行分离。 -在连续蒸馏的情况下,在比抽提位置高的位置和比抽提温度低的温度下将其引入蒸馏塔。 ;解决方案:在将烃类物质通过导管1引入蒸馏塔2后,在产生顶部蒸气馏分和底部流出物的区域内进行处理时,通过导管15抽出的液体会被氢气氢化通过管线4,然后将所述液体输送到氢化反应器3的顶部,在氢化反应器3的顶部进行一部分烃类材料(例如苯)的转化反应。然后,在反应器3的冷却流出物优选比热交换器16中的抽出温度低至少10℃之后,冷却后的流出物通过导管17在比冷凝器3高的位置处重新引入蒸馏塔2。拉管管线15。结果,这也可能导致蒸馏区尺寸的减小。;版权所有:(C)1999,JPO

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