PROCESS FOR SEPARATING TECHNICALLY PURE 2,4- DIISOCYANATOTOLUENE OR ISOMER MIXTURES HAVING AN INCREASED CONTENT OF 2,4-DIISOCYANATOTOLUENE FROM ISOMER MIXTURES OF 2,4-AND 2,6 DIISOCYANATOTOLUENE

A PROCESS FOR SEPARATING TECHNICALLY PURE 2, 4-DIISOCYANATOTOLUENE OR ISOMER MIXTURES HAYING AN INCREASED CONTENT OF 2,4-DIISO- CYANATOTOLUENE FROM ISOMER MIXTURES OF 2,4- AND 2,6-DIISOCYANATOTOLUENE Technically pure 2, 4-diisocyanatotoluene or an isomer mixture having an increased 2, 4-diisocyanato...

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Hauptverfasser: HAUSSER, WERNER, WISSNER, ADOLF, MITROWSKY, ALEXANDER
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creator HAUSSER, WERNER
WISSNER, ADOLF
MITROWSKY, ALEXANDER
description A PROCESS FOR SEPARATING TECHNICALLY PURE 2, 4-DIISOCYANATOTOLUENE OR ISOMER MIXTURES HAYING AN INCREASED CONTENT OF 2,4-DIISO- CYANATOTOLUENE FROM ISOMER MIXTURES OF 2,4- AND 2,6-DIISOCYANATOTOLUENE Technically pure 2, 4-diisocyanatotoluene or an isomer mixture having an increased 2, 4-diisocyanato-toluene content is obtained from an isomer mixture of 2,4- and 2,6-diisocyanatotoluene. The 2,4- and 2,6diisocyanatotoluene mixture is first cooled to a temperature of from 4 to 9.degree.C and further cooled to between -2 to -6.degree.C at a rate of 0.5 to 3.degree.C per hour. The temperature of the mixture is maintained at that temperature for at least 30 minutes. Any liquid present is removed and the solid remaining is then melted. Melting is preferably carried out by heating the solid at a rate of 0.5 to 3.degree.C per hour until the remaining solid has a 2,4-diisocyanato-toluene content of at least 98%. The liquid melt is removed and the solid having the desired 2,4-diisocyanato-toluene content is then melted.
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The 2,4- and 2,6diisocyanatotoluene mixture is first cooled to a temperature of from 4 to 9.degree.C and further cooled to between -2 to -6.degree.C at a rate of 0.5 to 3.degree.C per hour. The temperature of the mixture is maintained at that temperature for at least 30 minutes. Any liquid present is removed and the solid remaining is then melted. Melting is preferably carried out by heating the solid at a rate of 0.5 to 3.degree.C per hour until the remaining solid has a 2,4-diisocyanato-toluene content of at least 98%. 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The 2,4- and 2,6diisocyanatotoluene mixture is first cooled to a temperature of from 4 to 9.degree.C and further cooled to between -2 to -6.degree.C at a rate of 0.5 to 3.degree.C per hour. The temperature of the mixture is maintained at that temperature for at least 30 minutes. Any liquid present is removed and the solid remaining is then melted. Melting is preferably carried out by heating the solid at a rate of 0.5 to 3.degree.C per hour until the remaining solid has a 2,4-diisocyanato-toluene content of at least 98%. 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The 2,4- and 2,6diisocyanatotoluene mixture is first cooled to a temperature of from 4 to 9.degree.C and further cooled to between -2 to -6.degree.C at a rate of 0.5 to 3.degree.C per hour. The temperature of the mixture is maintained at that temperature for at least 30 minutes. Any liquid present is removed and the solid remaining is then melted. Melting is preferably carried out by heating the solid at a rate of 0.5 to 3.degree.C per hour until the remaining solid has a 2,4-diisocyanato-toluene content of at least 98%. The liquid melt is removed and the solid having the desired 2,4-diisocyanato-toluene content is then melted.</abstract><edition>4</edition><oa>free_for_read</oa></addata></record>
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subjects ACYCLIC OR CARBOCYCLIC COMPOUNDS
CHEMISTRY
METALLURGY
ORGANIC CHEMISTRY
title PROCESS FOR SEPARATING TECHNICALLY PURE 2,4- DIISOCYANATOTOLUENE OR ISOMER MIXTURES HAVING AN INCREASED CONTENT OF 2,4-DIISOCYANATOTOLUENE FROM ISOMER MIXTURES OF 2,4-AND 2,6 DIISOCYANATOTOLUENE
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