Method of manufacturing polycarbonates
A technology of polycarbonate and carbonic diester, applied in the field of polycarbonate production, can solve the problem that the polymerization rate is not completely satisfactory
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Embodiment 1、10、33
[0157] The equipment for polycarbonate polymerization includes on the stirring tank to mix raw materials, two pre-polymerization tanks and two horizontal polymerization tanks. device such as figure 1 shown in . The conditions for each reaction are shown in Table 1 below.
[0158] Pressure (Torr)
temperature(℃)
average dwell time
(Hour)
Atmospheric pressure (nitrogen atmosphere)
160
2
Pre-polymerization tank I
100
230
1
Pre-polymerization tank II
20
270
0.5
Horizontal polymerization tank I
2
305
0.5
Horizontal polymerization tank II
0.5
305
0.5
[0159] The molten bisphenol A is directly connected to the bisphenol A production device through the pipe (supply rate, 36.0kg / hr); after distillation, the molten diphenyl carbonate is directly added through the pipe (the supply rate, 34.7kg / hr); an...
Embodiment 2~9
[0162] Working examples 2~9, comparative examples 1~9
[0163] Polycarbonate was also produced by a method similar to Working Example 1, but using a different type and / or different amount of catalyst. The results are presented in Table 2.
[0164] catalyst
Embodiment 20
[0170] The device for polycarbonate polymerization is equipped with a stirring tank for mixing raw materials, two pre-polymerization tanks and two horizontal polymerization tanks. Various reaction conditions are given below.
[0171] Pressure (Torr)
[0172] The amount of phenolic solution of 0.5% sodium hydroxide added was adjusted so that the alkalinity shown corresponded to the amount shown in Table 5, expressed as NaOH per mole of bisphenol A produced in the bisphenol A production plant, directly from the tube Pumped molten bisphenol A (feeding rate: 36.0kg / hr), molten diphenyl carbonate pumped directly from the pipe after distillation (feeding rate: 35.5kg / hr), and decomposed at 100~300℃ The phenolic solution of the catalyst was continuously supplied in the amounts shown in Table 5 to a stirred tank maintained at the temperature given above. Next, the phenolic solution of the alkali metal phosphite catalyst of the specified amount is continuously supplied to ...
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