Back to results
US 2019/0241501 A1Published application
Process for hydrogenating toluenediamine (tda) tar
AssigneeBASF SE
InventorsArmin LANGE DE OLIVEIRA, Ines LOTTENBURGER, Christian BECHTOLD, Thomas HEIDEMANN
Life of this patent
Estimating the term…
Abstract
Process for hydrogenating toluenediamine (TDA) tar containing TDA and high boilers relative to TDA, including the step of contacting the toluenediamine tar with a heterogeneous hydrogenation catalyst comprising at least one metal selected from the group consisting of Ni, Co, Ru, Pd, Pt on at least one catalyst support selected from the group consisting of carbon, TiO2 and ZrO2, and with hydrogen under hydrogenating conditions.
Claims15
1:
- A process for hydrogenating toluenediamine (TDA) tar containing TDA and high boilers relative to TDA, the process comprising:
- contacting the toluenediamine tar with a heterogeneous hydrogenation catalyst comprising at least one metal selected from the group consisting of Ni, Co, Ru, Pd, Pt on at least one catalyst support selected from the group consisting of carbon, TiO2 and ZrO2, and with hydrogen under hydrogenating conditions.
2:
- The process according to claim 1, wherein the catalyst comprises Ni, Ni and Pt, Ru, Pd, or Pt on a ZrO2 or an active carbon catalyst support.
3:
- The process according to claim 1, wherein an amount of Ru, Pd, Pt or mixtures thereof, based on the heterogeneous hydrogenation catalyst, is 1 to 7 wt %.
4:
- The process according to claim 1, wherein an amount of Ni, Co or mixture thereof, based on the heterogeneous hydrogenation catalyst, is 0.5 to 70 wt %.
5:
- The process according to claim 1, wherein the heterogeneous hydrogenation catalyst is Ni/ZrO2, Ru/ZrO2, Pd/C, Pt/C or Pt/Ni/C.
6:
- The process according to claim 1, which is carried out in suspension or in a fixed bed.
7:
- The process according to claim 1, which is carried out as a continuous operation or batchwise.
8:
- The process according to claim 1, which is carried out at a temperature of from 120 to 270° C.
9:
- The process according to claim 1, which is carried out at a hydrogen pressure of from 60 to 300 bar.
10:
- The process according to claim 1, wherein the zirconium oxide support material is present in monoclinic, tetragonal, cubic or amorphous phase or in a mixed phase of these modifications.
11:
- The process according to claim 1, wherein the zirconium oxide support material has a BET surface area of from 30 to 300 m2/g a pore volume of from 0.1 to 1 cm3/g and a tamped density of from 500 to 2000 kg/m3.
12:
- The process according to claim 1, wherein upon hydrogenation, part of the high boilers are transformed into mid-boilers or low boilers having a lower boiling point than the high boilers.
13:
- The process according to claim 1, wherein part of the toluenediamine (TDA) tar containing TDA and high boilers relative to TDA are converted into methylcyclohexylamine (MCA) and/or methylcyclohexyldiamine (MCDA).
14:
- The process according to claim 1, wherein the toluenediamine tar is diluted with an organic solvent or diluent inert to the hydrogenation before performing the hydrogenation.
(canceled)
Dependencies are inferred from the claim text.