METHOD FOR CONTINUOUS PRODUCTION OF POLYCARBONATE

摘要

To provide a method for continuous production of a polycarbonate with safety, wherein (1) the contents of impurities in phosgene, which adversely affect a product, such as carbon tetrachloride, chloroform, etc., are decreased, and in its turn, the contents of the impurities in a polycarbonate are decreased; (2) by using a formed phosgene gas directly for an oligomer reaction step without going through a purification step, noxious phosgene is not substantially held; and preferably, (3) an apparatus is automatically stopped even at abnormal time, and noxious phosgene is detoxicated without being leaked outside the system.
Specifically, a method for continuous production of a polycarbonate including (1) a step of allowing chlorine and carbon monoxide to react with each other to continuously produce a phosgene gas; (2) a step of continuously supplying the phosgene gas continuously produced in the above-described step (1), an alkaline aqueous solution of a dihydric phenol-based compound, and an organic solvent into an oligomer reactor, to continuously produce a polycarbonate oligomer-containing reaction mixture; and (3) a step of continuously supplying the polycarbonate oligomer-containing reaction mixture produced in the above-described step (2), an alkaline aqueous solution of a dihydric phenol-based compound, and an organic solvent into a polymer reactor, to continuously produce a polycarbonate, wherein the following requirements (i) to (iii) are satisfied, is disclosed.
(i) In the step (1), chlorine and carbon monoxide are allowed to react with each other by being passed through a catalyst layer diluted with a material which is substantially inactive against carbon monoxide and chlorine, thereby controlling all of the contents of carbon tetrachloride and chloroform in the obtained phosgene gas to not more than 200 ppm by volume.
(ii) The phosgene gas continuously produced in the step (1) is used for the step (2) as it is without being purified.
(iii) At least a part of the organic solvent used in at least one of the steps (2) and (3) is purified to obtain an organic solvent having the content of each of carbon tetrachloride and chloroform of not more than 50 ppm by mass, and the organic solvent is reused as the organic solvent of at least one of the steps (2) and (3).