VERFAHREN ZUM ERZEUGEN VON POLYCARBONATEN
    1.
    发明授权
    VERFAHREN ZUM ERZEUGEN VON POLYCARBONATEN 有权
    方法制备聚碳酸酯

    公开(公告)号:EP1341837B1

    公开(公告)日:2005-10-19

    申请号:EP01998580.3

    申请日:2001-11-08

    申请人: Zimmer AG

    IPC分类号: C08G64/20 C08G64/30

    CPC分类号: C08G64/30 C08G64/205

    摘要: The invention relates to polycarbonates, obtained by reacting a monomer carbonate component with at least one diphenol or dialcohol in the presence of a transesterification catalyst. According to the invention, the melted components are mixed with the transesterification catalyst and a transesterification product is obtained that is then subjected to polycondensation. For polycondensation, the transesterification product is passed through a preliminary reactor, at least one intermediate reactor and a final reactor, said reactors being connected in series and having a shaft, on which mixing elements are attached, that is driven in a substantially horizontal manner. A melt residence time of between 5 minutes and 2 hours is maintained in the preliminary reactor and the final reactor, the temperatures in the preliminary reactor are maintained within the range of 220 to 300 DEG C and the pressure in the preliminary reactor is maintained in the range of 100 to 800 mbar and in the final reactor in the range of 0.1 to 50 mbar.

    VERFAHREN UND VORRICHTUNG ZUR KONTINUIERLICHEN HERSTELLUNG VON POLYESTERN
    3.
    发明公开
    VERFAHREN UND VORRICHTUNG ZUR KONTINUIERLICHEN HERSTELLUNG VON POLYESTERN 有权
    方法和设备聚酯连续生产

    公开(公告)号:EP1478677A1

    公开(公告)日:2004-11-24

    申请号:EP03770944.1

    申请日:2003-09-19

    申请人: Zimmer AG

    摘要: The invention relates to the continuous production of polyesters, whereby the esterification or transesterification of dicarboxylic acids or dicarboxylate diol esters is carried out in at least one reaction stage, the prepolycondensation of the esterification or transesterification product is carried out under vacuum in a reaction stage comprising a vertical tube and the polycondensation of the prepolycondensation product is carried out in at least one reaction stage. According to the invention, the prepolycondensation can be carried out in a reaction stage with simultaneous increase in the viscosity of the prepolycondensation product and lowering of the process temperature, whereby the esterification/transesterification product entering the prepolycondensation reactor, freely moving with limited heating, serially passes through firstly at least one first reaction zone formed from an annular channel, then into a second reaction zone formed in the radially outer annular channel of at least one annular channel divided into several concentric annular channels, then serially through the annular channels to the outlet and is then supplied to a third stirred reaction zone at the base of the vertical tube.

    VERFAHREN ZUR HERSTELLUNG VON POLYBUTYLENTEREPHTHALAT
    4.
    发明公开
    VERFAHREN ZUR HERSTELLUNG VON POLYBUTYLENTEREPHTHALAT 有权
    用于生产聚对苯二甲酸丁二醇

    公开(公告)号:EP1397412A1

    公开(公告)日:2004-03-17

    申请号:EP02732622.2

    申请日:2002-04-16

    申请人: Zimmer AG

    CPC分类号: C08G63/183 C08G63/85

    摘要: The invention relates to a method for the production of PBT, whereby a mixture of BDO and TPA are esterified in the presence of a catalyst solution and the esterified product polycondensed. In order to prevent the formation of deposits in the PBT, the catalyst solution contains 0.05 to 10 wt. % alkyl titanate, 85 to 99 wt. % BDO, 50 to 50000 ppm dicarboxylic acids and at most 0.5 wt. % water.

    VERFAHREN UND VORRICHTUNG ZUR KONTINUIERLICHEN HERSTELLUNG VON POLYESTERN

    公开(公告)号:EP1478677B8

    公开(公告)日:2005-08-17

    申请号:EP03770944.1

    申请日:2003-09-19

    申请人: Zimmer AG

    摘要: The invention relates to the continuous production of polyesters, whereby the esterification or transesterification of dicarboxylic acids or dicarboxylate diol esters is carried out in at least one reaction stage, the prepolycondensation of the esterification or transesterification product is carried out under vacuum in a reaction stage comprising a vertical tube and the polycondensation of the prepolycondensation product is carried out in at least one reaction stage. According to the invention, the prepolycondensation can be carried out in a reaction stage with simultaneous increase in the viscosity of the prepolycondensation product and lowering of the process temperature, whereby the esterification/transesterification product entering the prepolycondensation reactor, freely moving with limited heating, serially passes through firstly at least one first reaction zone formed from an annular channel, then into a second reaction zone formed in the radially outer annular channel of at least one annular channel divided into several concentric annular channels, then serially through the annular channels to the outlet and is then supplied to a third stirred reaction zone at the base of the vertical tube.

    摘要翻译: 本发明涉及聚酯的连续生产,其中二羧酸或二羧酸酯二醇酯的酯化或酯交换在至少一个反应阶段中进行,酯化或酯交换产物的预缩聚在真空下在包括 垂直管并且预聚缩合产物的缩聚在至少一个反应阶段中进行。 根据本发明,预聚缩合可以在反应阶段进行,同时提高预缩聚产物的粘度和降低工艺温度,由此进入预聚缩合反应器的酯化/酯交换产物随着有限加热自由移动, 首先穿过由环形通道形成的至少一个第一反应区,然后穿入形成在至少一个环形通道的径向外部环形通道中的第二反应区,所述至少一个环形通道被分成多个同心环形通道,然后依次通过环形通道到达出口 然后供应到垂直管底部的第三搅拌反应区。

    VERFAHREN ZUR KONTINUIERLICHEN HERSTELLUNG VON POLYESTERN ODER COPOLYESTERN
    7.
    发明授权
    VERFAHREN ZUR KONTINUIERLICHEN HERSTELLUNG VON POLYESTERN ODER COPOLYESTERN 有权
    PROCESS聚酯或共连续生产

    公开(公告)号:EP1345980B1

    公开(公告)日:2005-05-25

    申请号:EP01271410.1

    申请日:2001-11-27

    申请人: Zimmer AG

    CPC分类号: B01D3/14 C08G63/78

    摘要: The invention relates to a method for the production of polyesters or copolyesters, wherein continuos esterification of dicarboxylic acid esters and diols or continuos interesterification of dicarboxylic acid esters with diols is carried out in n reaction pressure levels connected one after the other, wherein the pressure in the first reaction pressure level, which is higher relative to the other reaction pressure levels, drops successively from one reaction pressure level to the other, the vapor flows of the individual reaction pressure levels are jointly rectified in a rectifying column and the diol components falling to the bottom of the rectifying column are fed back again at least to the first reaction level. In order to reduce the degree of complication of said process, at least the last reaction pressure level has a negative pressure, the pressure in the rectifying column is higher than the pressure in the last reaction pressure level and the vapors coming out of the last reaction pressure level are compressed to the pressure prevailing in the rectifying column.

    VERFAHREN UND VORRICHTUNG ZUR KONTINUIERLICHEN HERSTELLUNG VON POLYESTERN
    8.
    发明授权
    VERFAHREN UND VORRICHTUNG ZUR KONTINUIERLICHEN HERSTELLUNG VON POLYESTERN 有权
    方法和设备聚酯连续生产

    公开(公告)号:EP1478677B1

    公开(公告)日:2005-03-23

    申请号:EP03770944.1

    申请日:2003-09-19

    申请人: Zimmer AG

    摘要: The invention relates to the continuous production of polyesters, whereby the esterification or transesterification of dicarboxylic acids or dicarboxylate diol esters is carried out in at least one reaction stage, the prepolycondensation of the esterification or transesterification product is carried out under vacuum in a reaction stage comprising a vertical tube and the polycondensation of the prepolycondensation product is carried out in at least one reaction stage. According to the invention, the prepolycondensation can be carried out in a reaction stage with simultaneous increase in the viscosity of the prepolycondensation product and lowering of the process temperature, whereby the esterification/transesterification product entering the prepolycondensation reactor, freely moving with limited heating, serially passes through firstly at least one first reaction zone formed from an annular channel, then into a second reaction zone formed in the radially outer annular channel of at least one annular channel divided into several concentric annular channels, then serially through the annular channels to the outlet and is then supplied to a third stirred reaction zone at the base of the vertical tube.

    VERFAHREN ZUR HERSTELLUNG VON POLYBUTYLENTEREPHTHALAT
    9.
    发明授权
    VERFAHREN ZUR HERSTELLUNG VON POLYBUTYLENTEREPHTHALAT 有权
    用于生产聚对苯二甲酸丁二醇

    公开(公告)号:EP1397412B1

    公开(公告)日:2005-04-20

    申请号:EP02732622.2

    申请日:2002-04-16

    申请人: Zimmer AG

    CPC分类号: C08G63/183 C08G63/85

    摘要: The invention relates to a method for the production of PBT, whereby a mixture of BDO and TPA are esterified in the presence of a catalyst solution and the esterified product polycondensed. In order to prevent the formation of deposits in the PBT, the catalyst solution contains 0.05 to 10 wt. % alkyl titanate, 85 to 99 wt. % BDO, 50 to 50000 ppm dicarboxylic acids and at most 0.5 wt. % water.

    VERFAHREN ZUR KONTINUIERLICHEN HERSTELLUNG VON POLYESTERN ODER COPOLYESTERN
    10.
    发明公开
    VERFAHREN ZUR KONTINUIERLICHEN HERSTELLUNG VON POLYESTERN ODER COPOLYESTERN 有权
    PROCESS聚酯或共连续生产

    公开(公告)号:EP1345980A1

    公开(公告)日:2003-09-24

    申请号:EP01271410.1

    申请日:2001-11-27

    申请人: Zimmer AG

    CPC分类号: B01D3/14 C08G63/78

    摘要: The invention relates to a method for the production of polyesters or copolyesters, wherein continuos esterification of dicarboxylic acid esters and diols or continuos interesterification of dicarboxylic acid esters with diols is carried out in n reaction pressure levels connected one after the other, wherein the pressure in the first reaction pressure level, which is higher relative to the other reaction pressure levels, drops successively from one reaction pressure level to the other, the vapor flows of the individual reaction pressure levels are jointly rectified in a rectifying column and the diol components falling to the bottom of the rectifying column are fed back again at least to the first reaction level. In order to reduce the degree of complication of said process, at least the last reaction pressure level has a negative pressure, the pressure in the rectifying column is higher than the pressure in the last reaction pressure level and the vapors coming out of the last reaction pressure level are compressed to the pressure prevailing in the rectifying column.