Process for the manufacture of 1,2-dichloroethane
AssigneeSolvay (Societe Anonyme)
InventorsMichel Strebelle, Dominique Balthasart
Life of this patent
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Abstract
Process for the manufacture of 1,2-dichloroethane (DCE) starting from a stream of ethane which is subjected to a catalytic oxydehydrogenation (ODH) thus producing a gas mixture containing ethylene which is then dried and conveyed to a chlorination reactor supplied with a flow of chlorine so that at least 10% of the ethylene is converted to DCE. The stream of products derived from the chlorination reactor is then conveyed to an oxychlorination reactor in which the majority of the balance of ethylene is converted to DCE.
Claims22
A process for the manufacture of 1,2-dichloroethane starting from a stream of ethane, comprising:
- a) subjecting the stream of ethane to a catalytic oxydehydrogenation thus producing a gas mixture containing ethylene, unconverted ethane, water and secondary constituents;
- b) drying said gas mixture thus producing a dry gas mixture, wherein said gas mixture is optionally washed before or after said drying;
- c) after an optional additional purification step, conveying the dry gas mixture to a chlorination reactor supplied with a flow of chlorine so that at least 10% of the ethylene is converted to 1,2-dichloroethane;
- d) optionally isolating the 1,2-dichloroethane formed in the chlorination reactor from the stream of products derived from the chlorination reactor;
- e) conveying the stream of products derived from the chlorination reactor, from which the 1,2-dichloroethane has optionally been extracted in step d), to an oxychlorination reactor in which the majority of the balance of ethylene is converted to 1,2-dichloroethane, after optionally having subjected the latter to an absorption/desorption step e′), during which the 1,2-dichloroethane formed in the chlorination reactor is optionally extracted if it has not previously been extracted;
- f) isolating the 1,2-dichloroethane formed in the oxychlorination reactor from the stream of products derived from the oxychlorination reactor, wherein said 1,2-dichloroethane formed in the oxychlorination reactor is optionally added to the 1,2-dichloroethane formed in the chlorination reactor;
- and
- g) optionally recycling to step a) the stream of products derived from the oxychlorination reactor, from which the 1,2-dichloroethane has been extracted, optionally containing an additional stream of ethane previously introduced in one of steps b) to f), after having been optionally purged of gases and/or after an optional additional treatment in order to eliminate the chlorinated products contained therein.
A process for manufacturing vinyl chloride, comprising:
- a) subjecting the stream of ethane to a catalytic oxydehydrogenation thus producing a gas mixture containing ethylene, unconverted ethane, water and secondary constituents;
- b) drying said gas mixture thus producing a dry gas mixture, wherein said gas mixture is optionally washed before or after said drying;
- c) after an optional additional purification step, conveying the dry gas mixture to a chlorination reactor supplied with a flow of chlorine so that at least 10% of the ethylene is converted to 1,2-dichloroethane;
- d) optionally isolating the 1,2-dichloroethane formed in the chlorination reactor from the stream of products derived from the chlorination reactor;
- e) conveying the stream of products derived from the chlorination reactor, from which the 1,2-dichloroethane has optionally been extracted in step d), to an oxychlorination reactor in which the majority of the balance of ethylene is converted to 1,2-dichloroethane, after optionally having subjected the latter to an absorption/desorption step e′), during which the 1,2-dichloroethane formed in the chlorination reactor is optionally extracted if it has not previously been extracted;
- f) isolating the 1,2-dichloroethane formed in the oxychlorination reactor from the stream of products derived from the oxychlorination reactor, wherein said 1,2-dichloroethane formed in the oxychlorination reactor is optionally added to the 1,2-dichloroethane formed in the chlorination reactor;
- g) optionally recycling to step a) the stream of products derived from the oxychlorination reactor, from which the 1,2-dichloroethane has been extracted, optionally containing an additional stream of ethane previously introduced in one of steps b) to f), after having been optionally purged of gases and/or after an optional additional treatment in order to eliminate the chlorinated products contained therein;
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- h) subjecting the 1,2-dichloroethane so obtained to a pyrolysis thus producing vinyl chloride.
A process for the manufacture of polyvinyl chloride, comprising:
- a) subjecting the stream of ethane to a catalytic oxydehydrogenation thus producing a gas mixture containing ethylene, unconverted ethane, water and secondary constituents;
- b) drying said gas mixture thus producing a dry gas mixture, wherein said gas mixture is optionally washed before or after said drying;
- c) after an optional additional purification step, conveying the dry gas mixture to a flow of chlorine so that at least 10% of the ethylene is converted to 1,2-dichloroethane;
- d) optionally isolating the 1,2-dichloroethane formed in the chlorination reactor from the stream of products derived from the chlorination reactor;
- e) conveying the stream of products derived from the chlorination reactor, from which the 1,2-dichloroethane has optionally been extracted in step d), to an oxychlorination reactor in which the majority of the balance of ethylene is converted to 1,2-dichloroethane, after optionally having subjected the latter to an absorption/desorption step e′), during which the 1,2-dichloroethane formed in the chlorination reactor is optionally extracted if it has not previously been extracted;
- f) isolating the 1,2-dichloroethane formed in the oxychlorination reactor from the stream of products derived from the oxychlorination reactor and is optionally added to the 1,2-dichloroethane formed in the chlorination reactor;
- g) optionally recycling to step a) the stream of products derived from the oxychlorination reactor, from which the 1,2-dichloroethane has been extracted, optionally containing an additional stream of ethane previously introduced in one of steps b) to f), after having optionally being purged of gases and/or after an optional additional treatment in order to eliminate the chlorinated products contained therein;
- h) subjecting the 1,2-dichloroethane obtained to a pyrolysis thus producing vinyl chloride;
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- i) polymerizing the vinyl chloride to produce polyvinyl chloride.
Dependencies are inferred from the claim text.