Catalytic process for preparing bisphenol A
    5.
    发明申请
    Catalytic process for preparing bisphenol A 审中-公开
    用于制备双酚A的催化方法

    公开(公告)号:US20050177006A1

    公开(公告)日:2005-08-11

    申请号:US11043255

    申请日:2005-01-26

    IPC分类号: C07C37/20 C07C39/16

    CPC分类号: C07C37/20 C07C39/16

    摘要: The present invention relates to a process for preparing bisphenol A in which the phenol and acetone are reacted to give bisphenol A in the presence of a sulfonic acid ion-exchanger in at least one reactor, and in which the reactor, at the time when it is started up, is filled with sulfonic acid ion-exchanger with a bulk volume of 30 to 70 vol. % of the total reactor volume.

    摘要翻译: 本发明涉及一种制备双酚A的方法,其中苯酚和丙酮在至少一个反应器中在磺酸离子交换剂存在下反应得到双酚A,其中反应器在其时 启动,填充体积为30至70体积的磺酸离子交换剂。 总反应器体积的百分比。

    Production of bisphenol-A with reduced sulfur content
    9.
    发明申请
    Production of bisphenol-A with reduced sulfur content 失效
    生产具有降低硫含量的双酚A

    公开(公告)号:US20050215833A1

    公开(公告)日:2005-09-29

    申请号:US11043800

    申请日:2005-01-26

    摘要: A process for the production of bisphenol-A having low concentration of sulphur is disclosed. The process comprise a) reacting phenol with acetone in the presence of a sulfonic acid ion exchanger to form a product mixture containing water, bisphenol-A/phenol adduct, phenol and sulfurous particles, and b) filtering the product mixture to separate the sulfurous particles to obtain a purified product mixture that contains water, phenol and bisphenol-A/phenol adduct. In one embodiment of the process further comprise distilling the purified product mixture to remove the water to obtain a first material system that contains said adduct and phenol, crystallizing the adduct, and removing the phenol by filtration using a filtering apparatus to obtain crystalline adduct. In a yet additional embodiment the process comprise crystallizing the purified product mixture to obtain a second material system that contains crystalline adduct, water and phenol and removing the phenol and water by filtration using a filtering apparatus to obtain crystalline adduct.

    摘要翻译: 公开了一种生产低浓度硫的双酚A的方法。 该方法包括a)在磺酸离子交换剂存在下使苯酚与丙酮反应,形成含有水,双酚A /苯酚加成物,苯酚和亚硫酸颗粒的产物混合物,和b)过滤产物混合物以分离出亚硫酸颗粒 以获得含有水,苯酚和双酚A /苯酚加合物的纯化产物混合物。 在该方法的一个实施方案中还包括蒸馏纯化的产物混合物以除去水以获得含有所述加合物和苯酚的第一材料体系,结晶加合物,并使用过滤装置通过过滤除去苯酚以获得结晶加合物。 在另外的实施方案中,该方法包括使纯化的产物混合物结晶以获得含有结晶加合物,水和苯酚的第二材料体系,并使用过滤装置通过过滤除去苯酚和水以获得结晶加合物。

    Dewatering of circulatory flows in the production of bisphenol A
    10.
    发明申请
    Dewatering of circulatory flows in the production of bisphenol A 失效
    双酚A生产中循环流动的脱水

    公开(公告)号:US20050177007A1

    公开(公告)日:2005-08-11

    申请号:US11043275

    申请日:2005-01-26

    IPC分类号: C07C37/74 C07C37/84 C07C37/68

    摘要: A process for producing bisphenol A is disclosed. The process entails a) reacting phenol with acetone in the presence of an acidic catalyst to form a reaction mixture that includes bisphenol A and water, and b) removing water from the reaction mixture by distillation in a column to obtain a bottom product, and c) separating bisphenol-A/phenol adduct from the reaction mixture by crystallization and filtration. The bottom temperature of the column is 100 to 150° C., the overhead temperature of the column is 20 to 80° C., the absolute pressure is 50 to 300 mbar at the head of the column and 100 to 300 mbar at the bottom of the column, and wherein said (c) is carried out before or after said (b).

    摘要翻译: 公开了一种生产双酚A的方法。 该方法需要在酸性催化剂的存在下使苯酚与丙酮反应,形成包括双酚A和水的反应混合物,和b)通过在塔中蒸馏从反应混合物中除去水以得到底部产物,c )通过结晶和过滤从反应混合物中分离双酚A /苯酚加合物。 柱的底部温度为100至150℃,柱的塔顶温度为20至80℃,柱顶部的绝对压力为50至300毫巴,底部为100至300毫巴 并且其中所述(c)在所述(b)之前或之后进行。