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    • 21. 发明授权
    • Method for separating lactones from a mixture containing lactones
    • 从含有内酯的混合物中分离内酯的方法
    • US3953472A
    • 1976-04-27
    • US451564
    • 1974-03-15
    • Yutaka FujitaToru SawakiTadahisa SasanoMasao Sada
    • Yutaka FujitaToru SawakiTadahisa SasanoMasao Sada
    • C07D313/04C07C51/44C07D307/33C07D309/30C07D315/00C07D307/12
    • C07D315/00C07C51/44
    • Lactones are separated from a mixture of (a) at least one member selected from the group consisting of hydroxy acids wherein the OH group and the COOH group are bonded through 3 or 4 carbon atoms, lactones derived therefrom, lower polymers of said hydroxy acids and/or said lactones and esters of said hydroxy acids and/or said lactones and (b) at least one member selected from the group consisting of hydroxy acids wherein the OH group and the COOH group are bonded through 5 carbon atoms, lactones derived therefrom, lower polymers of said hydroxy acids and/or said lactones and esters of said hydroxy acids and/or said lactones, by heating said mixture in the presence of one or more monovalent or bivalent aliphatic or alicyclic alcohols under the conditions so as to remove the lactones from said (a) by distillation.
    • 将内酯与(a)选自羟基酸,其中OH基和COOH基通过3或4个碳原子键合的至少一种成分,由其衍生的内酯,所述羟基酸的低级聚合物和 /或所述羟基酸和/或所述内酯的所述内酯和酯,和(b)选自羟基酸中的至少一种,其中OH基和COOH基通过5个碳原子连接,由其衍生的内酯, 所述羟基酸和/或所述内酯和所述羟基酸和/或所述内酯的酯的低级聚合物通过在一种或多种一价或二价脂族或脂环族醇的存在下在条件下加热所述混合物以除去内酯 从(a)通过蒸馏。
    • 26. 发明授权
    • Process for production of aromatic polycarbonate resin and molded article of aromatic polycarbonate resin
    • 芳香族聚碳酸酯树脂的制造方法和芳香族聚碳酸酯树脂的成型体
    • US06472496B2
    • 2002-10-29
    • US09840144
    • 2001-04-24
    • Kyosuke MatsumotoMasasi SimonaruToru SawakiKatsushi SasakiMasahiro MurakamiYoshiki Matsuoka
    • Kyosuke MatsumotoMasasi SimonaruToru SawakiKatsushi SasakiMasahiro MurakamiYoshiki Matsuoka
    • C08G6400
    • C08G64/307
    • An aromatic polycarbonate resin is produced under the conditions that the flow velocity of the reaction mixture in a pipe through which a molten reaction mixture passes is a specific value or over, the viscosity-average molecular weight of the reaction mixture is 1,000 or more, the sum of the average retention times of the reaction mixture is not longer than 3 hours, the wall temperature of the pipe through which a molten reaction mixture passes is set to be higher than the temperature of the reaction mixture in the pipe, the catalyst deactivation agent is added within 2 hours after the completion of the melt polycondensation reaction, the filtration is carried out by using a filter having a specific retained particle size under a specific pressure difference, specific treated amount of the aromatic polycarbonate resin per unit area of the filter and a ratio of W (flow quantity of filtered polymer)×1,000/A (maximum area of the polymer path in the filtration vessel) falling within a specific range, etc.
    • 在熔融反应混合物通过的管中的反应混合物的流速为特定值以上的条件下制造芳香族聚碳酸酯树脂,反应混合物的粘均分子量为1000以上 反应混合物的平均保留时间的总和不超过3小时,熔融反应混合物通过的管的壁温设定为高于管中的反应混合物的温度,催化剂失活剂 在熔融缩聚反应完成后2小时内加入,过滤通过使用具有特定保留粒径的特定压力差的过滤器,每单位面积过滤器的芳族聚碳酸酯树脂的特定处理量, 过滤聚合物的流量(以过滤聚合物的流量计)×1,000 / A(过滤容器内的聚合物路径的最大面积) 特点范围等
    • 28. 发明授权
    • Process for producing polycarbonate resin
    • 生产聚碳酸酯树脂的方法
    • US06252036B1
    • 2001-06-26
    • US09402835
    • 1999-10-13
    • Kazuki HatonoHiroaki KanekoToru SawakiKatsushi Sasaki
    • Kazuki HatonoHiroaki KanekoToru SawakiKatsushi Sasaki
    • C08G6378
    • C08G64/14C08G64/307
    • The purpose of this invention is to produce a stabilized terminal-blocked polycarbonate resin with a limited number of the terminal hydroxy groups having excellent thermal stability, color stability and hydrolysis resistance by an industrially advantageous method using a terminal blocking agent. In the production of a polycarbonate by the melt-polycondensation of an aromatic dihydroxy compound with an aromatic carbonic acid diester in the presence of a polycondensation catalyst, a terminal blocking agent expressed by the following formula (1) [in the formula, R1 is chlorine atom, methoxycarbonyl group or ethoxycarbonyl group; R2 is an alkyl group having a carbon number of 1 to 30, an alkoxy group having a carbon number of 1 to 30, an aryl group having a carbon number of 6 to 30 or an aryloxy group having a carbon number of 6-30] is added after the melt-polycondensation to the system in an amount of 0.3 to 4 mol-equivalent based on the hydroxy terminal group amount of the polycarbonate at 200 to 350° C. under a pressure of 1,013 hPa (760 mmHg) or below for 0.1 second or longer and, thereafter, a stabilizer is added and kneaded into the system at 200 to 350° C. under a pressure of 1.333×105 hPa (105 mmHg) or below for 0.1 second or longer.
    • 本发明的目的是通过使用端基封端剂的工业上有利的方法制备具有有限数目的末端羟基的稳定的封端聚碳酸酯树脂,其具有优异的热稳定性,颜色稳定性和耐水解性。 在通过芳族二羟基化合物与芳香族碳酸二酯在缩聚催化剂存在下的熔融缩聚反应制造聚碳酸酯时,由下式(1)表示的封端剂[式中,R1为氯原子 原子,甲氧基羰基或乙氧基羰基; R 2为碳数为1〜30的烷基,碳数为1〜30的烷氧基,碳数为6〜30的芳基或碳原子数为6〜30的芳氧基] 在对于体系进行熔融缩聚之后,相对于聚碳酸酯的羟基端基量为200〜350℃,在1013hPa(760mmHg)以下的压力下,以0.3〜4mol当量的量进行熔融缩聚, 0.1秒以上,然后在1.333×105hPa(105mmHg)以下0.1秒以上的压力下,在200〜350℃下加入稳定剂并捏合到体系中。