초록 ▼

The present invention relates to a process for the continuous preparation of diaryl carbonates from phosgene and at least one monohydroxy compound (monophenol) in the presence of catalysts, and also the use thereof for preparing polycarbonates. The hydrogen chloride formed in the reaction is convert

The present invention relates to a process for the continuous preparation of diaryl carbonates from phosgene and at least one monohydroxy compound (monophenol) in the presence of catalysts, and also the use thereof for preparing polycarbonates. The hydrogen chloride formed in the reaction is converted by thermal oxidation into chlorine, with the chlorine being recirculated to the preparation of phosgene. In particular, the process comprises utilization of the hydrogen chloride formed for the process for preparing diphenyl carbonate (DPC process).

대표청구항 ▼

1. A process for preparing diaryl carbonate, which comprises the steps of: (a) preparing phosgene by reaction of chlorine with carbon monoxide;(b) reacting the phosgene formed in step (a) with at least one monophenol in the presence of a homogeneous metal catalyst to form at least one diaryl carbona

1. A process for preparing diaryl carbonate, which comprises the steps of: (a) preparing phosgene by reaction of chlorine with carbon monoxide;(b) reacting the phosgene formed in step (a) with at least one monophenol in the presence of a homogeneous metal catalyst to form at least one diaryl carbonate and hydrogen chloride;(c) isolating and working-up the diaryl carbonate formed in step (b);(d) isolating and optionally purifying the hydrogen chloride formed in step (b);(e) thermally oxidizing at least part of the hydrogen chloride from step (d) to chlorine by oxygen forming a gas mixture with formation of water; and(f) recirculating at least part of the chlorine prepared in step (e) to the preparation of phosgene in step (a); wherein the thermal oxidation by oxygen in step (e) is carried out using one or more catalyst, and wherein the catalyst is selected from the group consisting of titanium chloride, zirconium chloride, aluminum chloride and titanium phenoxide. 2. The process according to claim 1, further comprising 1) cooling the gas mixture formed in step (e) to condense aqueous hydrochloric acid;2) separating off the resulting aqueous solution of hydrogen chloride hydrochloric acid from the gas mixture;3) feeding at least part of the aqueous hydrochloric acid which has been separated off from the gas mixture to an electrochemical oxidation step in which at least part of the aqueous hydrochloric acid is oxidized to chlorine gas;4) optionally adding the chlorine gas obtained from the electrochemical oxidation in step 3) to the gas mixture obtained in step (e);5) removing residual amounts of water present in the gas mixture from steps 3) and (e) to give a chlorine-rich gas mixture;6) freeing the resulting chlorine-rich gas mixture from oxygen and optionally from secondary constituents. 3. The process according to claim 1, wherein the hydrogen chloride formed in step (b) is purified in step (d) by removing the phosgene by liquefaction. 4. The process according to claim 1, wherein the hydrogen chloride is purified in step (d) by freezing-out. 5. The process according to claim 2, wherein the separation of the aqueous hydrochloric acid from the gas mixture in steps 2) comprises scrubbing of the gas mixture with water or dilute hydrochloric acid. 6. The process according to claim 2, wherein the electrochemical oxidation of the aqueous hydrogen chloride solution in step 3) is carried out in an electrolysis cell in which an anode space and a cathode space are separated by an ion-exchange membrane. 7. The process according to claim 2, wherein the electrochemical oxidation of the aqueous hydrochloric acid in step 3) is carried out in an electrochemical cell in which an anode space and a cathode space are separated by a diaphragm. 8. The process according to claim 2, wherein the electrochemical oxidation of the aqueous hydrochloric acid in step 3) comprises a gas diffusion electrode as a cathode. 9. The process according to claim 8, wherein the gas diffusion electrode is operated as an oxygen-depolarized cathode. 10. The process according to claim 8, wherein the cathode comprises rhodium sulphide. 11. The process according to claim 2, wherein the hydrochloric acid is oxidized in step 3) together with alkali metal chlorides. 12. The process according to claim 2, wherein the hydrochloric acid is oxidized in step 3) together with sodium chloride, in an anodic chloralkali electrolysis. 13. The process according to claim 12, wherein a depleted alkali metal chloride solution from the chloralkali electrolysis is used as alkali metal chloride solution. 14. The process according to claim 2, wherein part of the hydrogen chloride provided for the thermal oxidation in step (e) is branched off, subjected to absorption in water or dilute hydrochloric acid to give a concentrated solution, which is combined with the aqueous hydrochloric acid from step 2) and fed to the electrochemical oxidation in step 3). 15. The process according to claim 1, wherein the chlorine is converted into phosgene as per step (a) and the resulting phosgene is used for the reaction with phenol to form diphenyl carbonate in step (b). 16. The process according to claim 1, wherein the thermal oxidation in step (e) is operated at a conversion of from 50 to 98%. 17. The process according to claim 2, wherein the gas mixture formed in the reaction in step (e) consists of chlorine and water, unreacted hydrogen chloride and oxygen, and carbon dioxide and nitrogen. 18. The process according to claim 2, wherein the thermal oxidation in step (e) is operated at a conversion of from 60 to 95%; and wherein the removal of the residual amounts of water in step 5) is carried out by scrubbing with sulphuric acid.