Trioxane production method wherein a side aqueous flow is deducted at a first distillation stage
    2.
    发明授权
    Trioxane production method wherein a side aqueous flow is deducted at a first distillation stage 失效
    三恶烷制备方法,其中在第一蒸馏阶段扣除侧水流

    公开(公告)号:US08530678B2

    公开(公告)日:2013-09-10

    申请号:US11665840

    申请日:2005-10-20

    IPC分类号: C07D323/06

    CPC分类号: C07D323/06

    摘要: Processes are disclosed comprising: (a) reacting an aqueous formaldehyde solution in a reactor in the presence of a suitable catalyst to obtain a reaction product mixture comprising trioxane, formaldehyde and water; (b) distilling the reaction product mixture to form a top stream comprising crude trioxane; and (c) treating the top stream in one or more additional stages to form pure trioxane; wherein an aqueous sidestream is drawn off during the distilling of the reaction mixture.

    摘要翻译: 公开的方法包括:(a)在合适的催化剂存在下使甲醛水溶液在反应器中反应,得到包含三恶烷,甲醛和水的反应产物混合物; (b)蒸馏反应产物混合物以形成包含粗三恶烷的顶流; 和(c)在一个或多个附加阶段处理顶部流以形成纯三恶烷; 其中在蒸馏反应混合物期间抽出水分流。

    Method for the Separation by Distillation of Pure Trioxane
    7.
    发明申请
    Method for the Separation by Distillation of Pure Trioxane 审中-公开
    蒸馏纯三恶烷分离方法

    公开(公告)号:US20070293688A1

    公开(公告)日:2007-12-20

    申请号:US11660530

    申请日:2005-08-18

    IPC分类号: C07D323/06

    摘要: The present invention relates to a process for distillatively removing pure trioxane from a feedstream (I) comprising trioxane in a proportion of at least 50% by weight, based on the total weight of the feedstream (I), and additionally formaldehyde and water, which comprises feeding the feedstream I and a further aqueous stream (II) which does not contain any components extraneous to the feedstream to a dividing wall column (TWK1) having a dividing wall TW which is arranged substantially perpendicularly and divides the column interior into a feed region (A1), a withdrawal reaction (B1), an upper combined column region (C1) and a lower combined column region (D1), and drawing off from the first dividing wall column (TWK1) a bottom stream (III) comprising pure trioxane and a sidestream (IV) at the withdrawal region (B1), comprising pure water.

    摘要翻译: 本发明涉及一种从基于原料流(I)的总重量至少50重量%的比例的另外的甲醛和水的含有三恶烷的原料流(I)蒸馏除去纯三恶烷的方法,以及另外的甲醛和水 包括将进料流I和不含任何与进料流无关的任何组分的另外的水流(II)进料到具有基本上垂直布置的分隔壁TW的分隔壁塔(TWK 1),并将塔内部分成进料 区域(A 1),取出反应(B 1),上部组合塔区域(C 1)和下部混合塔区域(D 1),从第一分隔壁塔(TWK 1) (III),其包含纯三恶烷和在取出区(B1))的侧流(IV),其包含纯水。

    Method for separating trioxane from a trioxane/formaldehyde/water mixture by means of pressure change rectification
    10.
    发明授权
    Method for separating trioxane from a trioxane/formaldehyde/water mixture by means of pressure change rectification 有权
    通过压力变换精馏从三恶烷/甲醛/水混合物中分离三恶烷的方法

    公开(公告)号:US07713387B2

    公开(公告)日:2010-05-11

    申请号:US10583698

    申请日:2004-12-21

    IPC分类号: B01D3/00 C07D323/06 C07C45/78

    CPC分类号: C07D323/06

    摘要: A process for removing trioxane from a use stream I of formaldehyde, trioxane and water, by a) providing a use stream I of formaldehyde as the main component and trioxane and water as the secondary components, b) mixing the use stream I with a recycle stream VII to obtain a feed stream Ia, c) distilling the use stream Ia in a first distillation stage to obtain a stream II of formaldehyde as the main component and water as the secondary component, and a stream III of trioxane as the main component and water and formaldehyde as the secondary components, d) distilling the stream III in a second distillation stage having a pressure higher than in the first distillation stage, to obtain a stream IV of trioxane and a stream V of trioxane as the main component and water and formaldehyde as the secondary components, e) distilling the stream V in a third distillation stage to obtain a stream VI of water and the recycle stream VII of trioxane as the main component and water and formaldehyde as the secondary components.

    摘要翻译: 一种从甲醛,三恶烷和水的使用流I中除去三恶烷的方法,通过以下步骤:a)提供以甲醛为主要成分的使用流I和作为第二组分的三恶烷和水,b)将使用流I与再循环 流VII以获得进料流Ia,c)在第一蒸馏阶段中蒸馏出使用流Ia以获得作为主要组分的甲醛的流II和作为第二组分的水,以及作为主要组分的三恶烷的流III和 水和甲醛作为次要组分,d)在具有高于第一蒸馏阶段的压力的第二蒸馏阶段中蒸馏料流III,得到三恶烷的流IV和三恶烷的流V作为主要成分, 甲醛作为次要组分,e)在第三蒸馏阶段中蒸馏物流V以获得水的流VI和三恶烷的再循环流VII作为主要成分,水和甲醛为t 他的次要成分。