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    • 1. 发明专利
    • Method for preparation of aliphatic oligocarbonate diol
    • 制备异烟酸二醇的方法
    • JP2005089464A
    • 2005-04-07
    • JP2004268724
    • 2004-09-15
    • Bayer Materialscience Agバイエル・マテリアルサイエンス・アクチェンゲゼルシャフトBayer MaterialScience AG
    • HOFACKER STEFFENBACHMANN ROLFBAECKER LOTHARWITOSSEK HERBERT
    • C07C68/06C07B61/00C07C45/64C07C45/82C07C69/96C08G64/02C08G64/30
    • C08G64/305C08G64/0208
    • PROBLEM TO BE SOLVED: To provide an improved method for preparation of aliphatic oligocarbonate diol by transesterification of dimethyl carbonate (DMC) with an aliphatic diol. SOLUTION: The invention relates to a process for preparing oligocarbonate diol, comprising a process reacting dimethyl carbonate with the diol component in the presence of a transesterification catalyst at a pressure of 3 to 6 bar and at temperatures of 100-200°C., by continuously introducing the DMC into the liquid phase of the reaction mixture and continuously removing from the reaction mixture by distillation of the methanol which forms as a gaseous methanol/DMC mixture, a process reducing the temperature of the reaction mixture on completion of the continuous metered addition of DMC, to ≤190°C, and reducing the pressure to atmospheric pressure, such that further methanol/DMC mixture is distilled off in parallel, further reducing the pressure after atmospheric pressure has been attained and, after a pressure of ≤100 mbar has been attained, introducing an inert gas stream into the reaction mixture. COPYRIGHT: (C)2005,JPO&NCIPI
    • 待解决的问题:提供通过碳酸二甲酯(DMC)与脂族二醇的酯交换制备脂肪族低聚碳酸酯二醇的改进方法。 解决方案:本发明涉及一种制备低聚碳酸酯二醇的方法,包括在酯交换催化剂存在下,在3至6巴的压力和100-200℃的温度下使碳酸二甲酯与二醇组分反应的方法 通过连续地将DMC引入反应混合物的液相,并通过蒸馏形成甲醇/ DMC混合气体的甲醇从反应混合物中连续除去,在完成反应混合物后,降低反应混合物的温度 连续计量加入DMC至≤190℃,并将压力降至大气压,使得另外甲醇/ DMC混合物平行蒸馏掉,进一步降低大气压力后的压力,压力≤ 已经达到100毫巴,将惰性气流引入反应混合物中。 版权所有(C)2005,JPO&NCIPI
    • 7. 发明专利
    • DE502004010700D1
    • 2010-03-18
    • DE502004010700
    • 2004-09-08
    • BAYER MATERIALSCIENCE AG
    • HOFACKER STEFFEN DRWITOSSEK HERBERT DRBAECKER LOTHAR
    • C07C68/06C08G64/30C07B61/00C07C45/64C07C45/82C07C68/08C07C69/96C08G64/02
    • Preparation of oligocarbonate polyol involves reacting dimethyl carbonate with a polyol component in the presence of an ytterbium compound transesterification catalyst at a pressure of atmospheric pressure to 6 bar and at 100 - 170[deg]C; and reducing the pressure and passing an inert gas stream into the reaction mixture. Preparation of oligocarbonate polyol involves (i) reacting dimethyl carbonate with a polyol component in the presence of an ytterbium compound transesterification catalyst at a pressure of atmospheric pressure to 6 bar and at a temperature of 100 - 170[deg]C; and (ii) reducing the pressure and passing an inert gas stream into the reaction mixture. The step i) involves (n >= 2) successive substeps (ia) in which (i) is 1 - n, and in each substep (ia), a pressure (P 1) of 3 - 6 bar is established in the reactor, a portion (x i) of the total amount of dimethyl carbonate is added to the liquid phase of the reaction mixture and, after a reaction time at a temperature, the methanol formed in the reaction is removed from the reaction mixture by distillation in the form of a gaseous methanol/dimethyl carbonate mixture, in the course of which the pressure is reduced, at constant temperature, from (P 1) to a pressure (P 2), and in the last substep (ib) the portion (x n) still absent from the total amount is added and the pressure (P n) at the end of the substep is atmospheric pressure.
    • 8. 发明专利
    • PREPARATION OF ALIPHATIC OLIGOCARBONATE POLYOLS
    • HK1078308A1
    • 2006-03-10
    • HK05110243
    • 2005-11-16
    • BAYER MATERIALSCIENCE AG
    • HOFACKER STEFFENWITOSSEK HERBERTBAECKER LOTHAR
    • C07C68/06C07B61/00C07C20060101C07C45/64C07C45/82C07C68/08C07C69/96C08G64/30
    • Preparation of oligocarbonate polyol involves reacting dimethyl carbonate with a polyol component in the presence of an ytterbium compound transesterification catalyst at a pressure of atmospheric pressure to 6 bar and at 100 - 170[deg]C; and reducing the pressure and passing an inert gas stream into the reaction mixture. Preparation of oligocarbonate polyol involves (i) reacting dimethyl carbonate with a polyol component in the presence of an ytterbium compound transesterification catalyst at a pressure of atmospheric pressure to 6 bar and at a temperature of 100 - 170[deg]C; and (ii) reducing the pressure and passing an inert gas stream into the reaction mixture. The step i) involves (n >= 2) successive substeps (ia) in which (i) is 1 - n, and in each substep (ia), a pressure (P 1) of 3 - 6 bar is established in the reactor, a portion (x i) of the total amount of dimethyl carbonate is added to the liquid phase of the reaction mixture and, after a reaction time at a temperature, the methanol formed in the reaction is removed from the reaction mixture by distillation in the form of a gaseous methanol/dimethyl carbonate mixture, in the course of which the pressure is reduced, at constant temperature, from (P 1) to a pressure (P 2), and in the last substep (ib) the portion (x n) still absent from the total amount is added and the pressure (P n) at the end of the substep is atmospheric pressure.
    • 10. 发明专利
    • AT456601T
    • 2010-02-15
    • AT04021317
    • 2004-09-08
    • BAYER MATERIALSCIENCE AG
    • HOFACKER STEFFENWITOSSEK HERBERTBAECKER LOTHAR
    • C07C68/06C08G64/30C07B61/00C07C45/64C07C45/82C07C68/08C07C69/96C08G64/02
    • Preparation of oligocarbonate polyol involves reacting dimethyl carbonate with a polyol component in the presence of an ytterbium compound transesterification catalyst at a pressure of atmospheric pressure to 6 bar and at 100 - 170[deg]C; and reducing the pressure and passing an inert gas stream into the reaction mixture. Preparation of oligocarbonate polyol involves (i) reacting dimethyl carbonate with a polyol component in the presence of an ytterbium compound transesterification catalyst at a pressure of atmospheric pressure to 6 bar and at a temperature of 100 - 170[deg]C; and (ii) reducing the pressure and passing an inert gas stream into the reaction mixture. The step i) involves (n >= 2) successive substeps (ia) in which (i) is 1 - n, and in each substep (ia), a pressure (P 1) of 3 - 6 bar is established in the reactor, a portion (x i) of the total amount of dimethyl carbonate is added to the liquid phase of the reaction mixture and, after a reaction time at a temperature, the methanol formed in the reaction is removed from the reaction mixture by distillation in the form of a gaseous methanol/dimethyl carbonate mixture, in the course of which the pressure is reduced, at constant temperature, from (P 1) to a pressure (P 2), and in the last substep (ib) the portion (x n) still absent from the total amount is added and the pressure (P n) at the end of the substep is atmospheric pressure.