Separating toluene diisocyanate and/or higher boiling solvents from distillation residues of the toluene diisocyanate manufacture using a fluidized bed

Claim 2

A process for the separation of toluene diisocyanates and/or higher boiling solvents from distillation residues obtained during the reaction of toluene diamine with phosgene in the presence of solvents and subsequent distillation of the reaction solution comprising treating the distillation residues in a fluidized bed at temperatues of 140° C. to 280° C.

Claim 3

The process of claim 1 wherein void fractions ε L of 0.4 to 0.75 are employed.

Claim 4

The process of claim 1 wherein solid material, of an average particle size of 0.5 micron to 5000 microns is initially placed into a fluidized bed vessel.

Claim 5

The process of claim 1 wherein feeding the fluidizing gas is done at an initial flow velocity of 0.1 meter per second to 2 meters per second at 20° C. and 760 mmHg.

Claim 6

The process of claim 1 comprising recycling nitrogen as the fluidizing gas.

Claim 7

The process of claim 1 comprising injecting the distillation residue by a two-product jet into the fluidized bed and injecting an atomized gas into the fluidized bed with a supply pressure of 1.5 bars to 10 bars.

Claim 8

The process of claim 1 comprising preheating fluidizing gas for energy to evaporate the desired product or products in the fluidized bed.

Claim 9

The process of claim 1 comprising introducing energy for evaporating the desired product or product mixture in the fluidized bed via the wall of the fluidized bed vessel and/or through heat exchange surfaces installed in the fluidized bed.

Claim 10

A process for the separation of toluene diisocyanates and/or higher boiling solvents from distillation residues obtained during the reaction of toluene diamine with phosgene in the presence of solvents and subsequent distillation of the reaction solution comprising establishing a fluidizing bed by placing an initial material of an average particle size of 0.5 micron to 5000 microns into a fluidized bed reactor; feeding a fluidizing gas to establish a specified void fraction of 0.4 to 0.75, at a velocity of 0.1 meter per second to 2 meters per second at normal conditions of 20° C. and 760 mmHg and which said fluidizing gas is recycling nitrogen; injecting the distillation residue containing a desired product by a two-product jet into the fluidized bed and injecting the atomizing gas into the fluidized bed with a supply pressure of 1.5 bars to 10 bars.

Claim 11

A process for the separation of toluene diisocyanates and/or higher boiling solvents from distillation residues obtained during the reaction of toluene diamine with phosgene in the presence of solvents and subsequent distillation of the reaction solution comprising establishing a fluidizing bed by placing an initial material of an average particle size of 0.5 micron to 5000 microns into a fluidized bed reactor; feeding a fluidizing gas to establish a specified void fraction of 0.4 to 0.75, at a velocity of 0.1 meter per second to 2 meters per second at normal conditions of 20° C. and 760 mmHg and which said fluidizing gas is recycling nitrogen; injecting the distillation residue containing a desired product by a two-product jet into the fluidized bed and injecting the atomizing gas into the fluidized bed with a supply pressure of 1.5 bars to 10 bars.