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A process for the high-yield recovery of ethylene and heavier hydrocarbons from the gas produced by pyrolysis of hydrocarbons (1) in which the liquid products (12-15, 23) resulting from the fractionated condensation of a cracking gas (1) for the recovery of almost all the ethylene, are supplied to a distillation column (C1), called a de-ethanizer, at different intermediate levels. At the top of the de-ethanizer the vapor (31) of the column distillate is treated directly in an acetylene hydrogenation reactor (R1), the effluent containing virtually no acetylene being separated by a distillation (C2) column called a de-methanizer, into an ethylene- and ethane-enriched tail (43) product, while the head product (44) is recycled by compression or treated for subsequent recovery of ethylene.

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Procédé pour la récupération à grand rendement de l'éthylène et des hydrocarbures plus lourds à partir de gaz produit par pyrolyse des hydrocarbures (1) dans lequel les produits liquides (12-15, 23) résultant de la condensation fractionnée du gaz de craquage (1) pour la récupération de presque tout l'éthylène, alimentent une colonne de distillation (C1), dite dééthaniseur à différents niveaux intermédiaires, au sommet de laquelle, la vapeur (31) du distillat de colonne est traitée directement dans un réacteur d'hydrogénation d'acétylène (R1), l'effluent ne contenant presque plus d'acétylène étant séparé par une colonne de distillation (C2) dite déméthaniseur, en un produit de queue (43) enrichi en éthylène et éthane tandis que le produit de tête (44) est recyclé par compression ou traité pour une récupération ultérieure de l'éthylène.

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GE CT 2361853-3 GDAS 16 SLICE DCB Part Number: 2361853-3 Description: GDAS 16 SLICE DCB Manufacturer.

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