초록

Chlorine is prepared by catalytic oxidation of a hydrogen chloride stream having a content of sulfur in elemental or bonded form of less than 100 ppm, preferably less than 50 ppm, more preferably less than 5 ppm, most preferably less than 1 ppm, based on the weight of the hydrogen chloride stream.

대표청구항 ▼

1. A process for the preparation of an isocyanate by phosgenation of an amine comprising: a) reacting carbon monoxide with chlorine to form phosgene,b) reacting an amine with phosgene to form, a crude isocyanate mixture and a gas stream containing hydrogen chloride,c) distilling the crude isocyanate

1. A process for the preparation of an isocyanate by phosgenation of an amine comprising: a) reacting carbon monoxide with chlorine to form phosgene,b) reacting an amine with phosgene to form, a crude isocyanate mixture and a gas stream containing hydrogen chloride,c) distilling the crude isocyanate mixture to purify the mixture and obtain the isocyanate and a mixture containing isocyanate and from 10 to 70 wt. % of non-vaporizable residue, based on the weight of the mixture,d) working up the mixture of isocyanate and 10 to 70 wt. % of non-vaporizable residue obtained in c) to recover isocyanate by evaporation in a kneader dryer or in residue pans or the amine by hydrolysis of the residue, and recycling at least a portion of the isocyanate obtained or of the amine obtained to the reaction in b), ande) subjecting the gas stream containing hydrogen chloride with a content of sulfur in elemental or bonded form of less than 100 ppm, based on weight of the gas stream, obtained in b) to catalytic oxidation to produce chlorine, andf) recycling at least a portion of the chlorine prepared in step e) to the preparation of phosgene in a). 2. The process of claim 1 in which in d), the isocyanate is separated from the residue in a kneader dryer or in a residue pan using bitumen having a sulfur content of <5 wt. % sulfur, based on total weight of the bitumen being employed. 3. The process of claim 1 in which in d), separation of the isocyanate from the residue is carried out in a kneader dryer or residue pans. 4. The process of claim 3 in which the gas stream containing hydrogen chloride from b) is purified to remove sulfur by absorption. 5. The process of claim 3 in which the gas stream containing hydrogen chloride from b) is purified in a guard bed. 6. The process of claim 1 in which CO and/or phosgene is freed from sulfur via an adsorption agent in a). 7. The process of claim 1 in which phosgene having a sulfur content of less than 100 ppm is generated in a). 8. The process of claim 1 in which the reaction of the amine with phosgene in b) is carried out in the gas phase.