IP Library Granted Patent US 7,999,056
Granted Patent B2
US 7,999,056 · App. 12/375,136 · Granted Aug 16, 2011

Continuous production method and production apparatus of aromatic polycarbonate

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Quick Facts
Patent No.
US 7,999,056
App. No.
12/375,136
Granted
Aug 16, 2011
Kind
B2
Abstract

The object of the present invention is to provide a method of producing plural kinds of aromatic polycarbonates by a melt process without changeover loss and quality deterioration. The present invention relates to a production method of an aromatic polycarbonate, comprising supplying a molten mixture of raw materials of an aromatic dihydroxy compound and/or a carbonic diester prepared in the absence of an ester exchange catalyst to polycondensation steps of two lines each equipped with three vertical reactors connected in series and one horizontal reactor, and at the same time, continuously conducting polycondensation reaction in the presence of an ester exchange catalyst.

Claims (19)

1. A continuous production method of an aromatic polycarbonate, comprising:

preparing a molten mixture of raw materials comprising an aromatic dihydroxy compound and a carbonic diester in the absence of an ester exchange catalyst; and

polycondensing the molten mixture of the raw materials in the presence of an ester exchange catalyst in a plurality of reactors provided in plural lines to produce at least one aromatic polycarbonate by melt polycondensation with an ester exchange reaction between the aromatic dihydroxy compound and the carbonic diester,

wherein the molten mixture of the raw materials is polycondensed in the plural lines per one line of preparation of the molten mixture.

2. The continuous production method of an aromatic polycarbonate as claimed in claim 1 , further comprising adding at least one selected from the group consisting of an aromatic dihydroxy compound, a carbonic diester, an ester exchange catalyst, an end terminator, an additive and a thermoplastic resin to the molten mixture of the raw materials while being prepared or thereafter.

3. The continuous production method of an aromatic polycarbonate as claimed in claim 1 , wherein plural kinds of aromatic polycarbonate are produced by polycondensing the molten mixture of the raw materials in the plural lines.

4. The continuous production method of an aromatic polycarbonate as claimed in claim 1 , further comprising:

filtering at least one material selected from the group consisting of an aromatic dihydroxy compound, a carbonic diester, an ester exchange catalyst, an end terminator, an additive and a thermoplastic resin; and

subsequently adding a filtered material to the molten mixture of the raw materials while being prepared or thereafter.

5. The continuous production method of an aromatic polycarbonate as claimed in claim 1 , further comprising:

filtering carbonic diester; and

adding a filtered carbonic diester to the molten mixture of the raw materials or thereafter in an amount such that a molar ratio of carbonic diester to aromatic dihydroxy compound in the raw materials is from 1.0 to 1.3,

wherein the molten mixture of the raw materials that comprises the filtered carbonic diester is polycondensed by solution polycondensation in the presence of an ester exchange catalyst.

6. A production apparatus of an aromatic polycarbonate, comprising:

at least one melt mixing tank configured to prepare a molten mixture of raw materials comprising an aromatic dihydroxy compound and a carbonic diester in the absence of an ester exchange catalyst; and

polycondensation reactors provided in at least two lines per one line of the at least one melt mixing tank, the polycondensation reactors being configured to continuously polycondensate the molten mixture of the raw materials prepared in the at least one melt mixing tank, in the presence of an ester exchange catalyst.

7. The production apparatus of an aromatic polycarbonate as claimed in claim 6 , wherein the polycondensation reactors comprise:

a plurality of vertical reactors connected in series; and

at least one horizontal reactor positioned downstream of the vertical reactors.

Assignments (2)
CHANGE OF NAME Recorded Sep 5, 2017
From: MITSUBISHI RAYON CO., LTD.
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 043750/0834 →
MERGER Recorded Sep 4, 2017
From: MITSUBISHI CHEMICAL CORPORATION
To: MITSUBISHI RAYON CO., LTD.
Reel/Frame 043750/0207 →