Method for producing butadiene from butanediols
AssigneesIfp Energies Nouvelles, Compagnie Generale Des Etablissements Michelin
InventorsNuno Pacheco, Margarita Dorato, Marc Jacquin, Rejane Dastillung, Sophie Couderc
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Abstract
The invention relates to a method for producing 1,3-butanediene from a butanediol feedstock that includes: a) A step for esterification of butanediol by a carboxylic acid to form the corresponding diester; b) A step for pyrolysis of the diester effluent obtained from step a); c) A step for distillation fed by at least the carboxylic acid effluent obtained from step a), and producing an aqueous distillate and a carboxylic acid residue; d) A step for drying the carboxylic acid that is fed at least by the carboxylic acid residue obtained from step c) and producing a water effluent and a carboxylic acid product that feeds step a).
Claims12
A method for producing 1,3-butadiene from butanediol, which method comprises at least:
- a) esterifying the butanediol by a carboxylic acid in a mixture comprising the butanediol, the carboxylic acid and a liquid pyrolysis effluent, in a reactive distillation column, in the presence of a homogeneous or heterogeneous acid catalyst, and at a pressure of between 0.01 and 1 MPa to form the corresponding diester, thereby producing at least a carboxylic acid effluent and a diester effluent;
- b) pyrolyzing the diester effluent obtained from a) in a reaction section at a temperature of between 500° C. and 650° C. thereby producing a reaction-section effluent, cooling said reaction-section effluent to a temperature that is less than 100° C., and feeding the cooled reaction-section to a separation section and separating at least a liquid pyrolysis effluent comprising at least 50% by weight of carboxylic acid and a vapor pyrolysis effluent comprising more than 90% by weight of butadiene, said liquid pyrolysis effluent feeding the esterification in a);
- c) distilling at least the carboxylic acid effluent obtained from a), in a distillation column at a pressure that is less than or equal to 1 MPa, at a temperature at the top of the column between 0 and 110° C. and a temperature at the bottom of the column between 100° C. and 120° C., and producing an aqueous distillate comprising the by-products of a) and b), and a carboxylicacid residue;
- d) drying the carboxylic acid residue obtained from c) and producing a water effluent and a carboxylic acid recycle that is fed to esterification in a).
Dependencies are inferred from the claim text.