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US 6,930,199 B2Granted
Process for the preparation of diisocyanates
AssigneeBayer MaterialSceince AG
InventorsJürgen Meyn, Herbert Stutz
Life of this patent
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Abstract
The invention relates to a process for the preparation of isocyanates in the gas phase, in which the possibilities for back-mixing and byproduct formation are reduced by improving the mixing of the starting materials in a tubular reactor.
Claims15
A process for the preparation of diisocyanates and triisocyanates of the general formula (I)
- R(NCO)n (I),
- in which
- R represents a (cyclo)aliphatic or aromatic hydrocarbon radical having up to 15 carbon atoms with the proviso that at least 2 carbon atoms are arranged between two NCO groups, and
- n represents the number 2 or 3,
- the process comprising gas phase phosgenating the corresponding diamines and/or triamines of the general formula (II)
- R(NH2)n (II),
- in which
- R represents a (cyclo)aliphatic or aromatic hydrocarbon radical having up to 15 with the proviso that at least two carbon atoms are arranged between two amino groups, and
- n represents the number 2 or 3,
- by providing a tubular reactor which has a double-walled guide tube extending centrally in the direction of the axis of rotation of the tubular reactor, a concentric annular gap being formed between the inner and the outer wall of the double walled guide tube, and the ratio of the cross-sectional area of the tubular reactor, which area is bounded by the inner wall of the double-walled guide tube, to the cross-sectional area of the tubular reactor, which area is bounded by the wall of the tubular reactor and the outer wall of the double-walled guide tube, being 1:0.5 to 1:4,
- heating the diamines and/or triamines in vapour form and phosgene separately from one another to temperatures of 200° C. to 600° C.,
- feeding the diamines and/or triamines in vapour form to the tubular reactor via the concentric annular gap at a mean flow velocity of 20–150 m/s, and
- feeding the phosgene to the tubular reactor over the remaining cross-sectional areas of the tubular reactor at a mean flow velocity of at least 1 m/s.
10 more elements
Dependencies are inferred from the claim text.