Process for the preparation of butane-1,4-diol, γ-butyrolactone and tetrahydrofuran
AssigneeBASF SE
InventorsMichael W. M. Tuck, Michael A. Wood, Andrew G. Hiles
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AssigneeBASF SE
InventorsMichael W. M. Tuck, Michael A. Wood, Andrew G. Hiles
Estimating the term…
A process is described for the production of butane-1,4-diol, γ-butyrolactone and/or tetrahydrofuran. A vaporous stream containing maleic anhydride, water, and carbon oxides is contact in an absorption zone with a high boiling ester as solvent to form a solution of maleic anhydride in the high boiling ester which has a boiling point at the atmospheric pressure at least about 30° C. higher than that of maleic anhydride and is selected from di-(C1 to C4 alkyl) esters of alkyl dicarboxylic acids containing up to 3 carbon atoms, mono- and di-(C10 to C18 alkyl) esters of maleic acid, fumaric acid, succinic acid, and mixtures thereof, (C1 to C4 alkyl) esters of naphthalene-monocarboxylic acids, tri-(C1 to C4 alkyl) esters of aromatic tricarboxylic acids, and di-(C1 to C4 alkyl) esters of isophthalic acid. The maleic anhydride in the solution is stripped with a gaseous stream containing hydrogen thereby forming a vaporous stream comprising hydrogen and maleic anhydride, which is contacted in a hydrogenation zone with a heterogeneous hydrogenation catalyst to convert maleic anhydride to at least one C4 compound selected from butane-1,4-diol, γ-butyrolactone and tetrahydrofuran.
A process for the production of at least one C4 compound selected from butane-1,4diol, γ-butyrolactone and tetrahydrofuran, which includes the step of hydrogenation in the vapour phase of maleic anhydride in the presence of a heterogeneous hydrogenation catalyst, which process comprises:
Dependencies are inferred from the claim text.