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    • 2. 发明授权
    • Process for the preparation of cyclopropyl alkyl ketones
    • 制备环丙基烷基酮的方法
    • US6002046A
    • 1999-12-14
    • US263876
    • 1999-03-08
    • Manfred KaufholdWolfgang KleemissUdo JegelkaMichael Korell
    • Manfred KaufholdWolfgang KleemissUdo JegelkaMichael Korell
    • C07B61/00C07C45/59C07C45/67C07C45/82C07C45/85C07C49/293C07C45/54
    • C07C45/82C07C45/676C07C45/85
    • Cyclopropyl alkyl ketones are separated from 3-acyltetrahydrofuran-2-ones by adding an alcohol, water or a water/alcohol mixture to a reaction product containing C.sub.1-4 -alkyl cyclopropyl ketone and 4,5-dihydro-2-alkylfuran by-product and an acid catalyst and reacting the by-product with the added alcohol, water of water/alcohol mixture before, during or after distilling said reaction product; and effectively separating C.sub.1 -.sub.4 -alkyl cyclopropyl ketone from reaction by-products.In the preparation of cyclopropyl alkyl ketones from 3-acyltetrahydrofuran-2-ones very reactive 4,5-dihydro-2-alkylfurans are also produced. By reacting such compounds with nucleophilic compounds, such as alcohols or water, before, during or after distillation of the reaction products, it is possible reliably to separate off the 4,5-dihydro-2-alkylfurans as high-boiling addition compounds. The offgas which is produced in the production process for cyclopropyl alkyl ketones can be simply and reliably purified by reactive washing. The byproducts, which are difficult to handle for a production process, can thus be reliably eliminated.
    • 通过向含有C 1-4 - 烷基环丙基酮和4,5-二氢-2-烷基呋喃副产物的反应产物中加入醇,水或水/醇混合物将环丙基烷基酮与3-酰基四氢呋喃-2-酮分离 和酸催化剂,在蒸馏所述反应产物之前,期间或之后使副产物与所加入的醇,水/醇混合物的水反应; 并有效地将C1-4烷基环丙基酮与反应副产物分离。 在制备3-酰基四氢呋喃-2-酮的环丙基烷基酮时,也产生非常活泼的4,5-二氢-2-烷基呋喃。 通过使这些化合物与亲核化合物如醇或水反应,在反应产物蒸馏之前,期间或之后,可以可靠地将4,5-二氢-2-烷基呋喃分离成高沸点加成化合物。 在环丙基烷基酮的生产过程中生产的废气可以通过反应性洗涤简单可靠地纯化。 因此,可以可靠地消除对生产过程难以处理的副产物。
    • 10. 发明授权
    • Process for the recovery of pure methylal from methanol-methylal mixtures
    • 从甲醇 - 甲缩醛混合物中回收纯甲缩醛的方法
    • US4385965A
    • 1983-05-31
    • US342975
    • 1982-01-26
    • Wolfgang H. E. MullerManfred Kaufhold
    • Wolfgang H. E. MullerManfred Kaufhold
    • C07C41/00C07C41/58C07C43/303C07C67/00B01D3/26
    • C07C41/58
    • In a process for recovering pure methylal from methanol-methylal mixtures, which can optionally contain still further compounds, the separation conducted in a rectification device comprising two rectifying columns. In the first rectifying column, the mixture to be separated is rectified under a pressure lower than that in the second column, into a methylal-rich, methanol-poor distillate, and into a practically methylal-free, methanol-rich sump product. The methylal-rich distillate of the first rectification is then separated in a second rectifying column, operated under a higher pressure than the first rectification column, into a compound stream containing methanol and methylal, which is then recycled to the first rectifying column, and into pure methylal as the sump product. In a specific refinement, the first rectification is preferably operated under a pressure of 1-22 bar absolute and the second rectification preferably under a pressure of 9-30 bar absolute, with the second rectification being operated under a pressure which is at least 8 bar higher than that of the first rectification.
    • 在从可以任选地含有其它化合物的甲醇 - 甲缩醛混合物中回收纯甲缩醛的方法中,在包括两个精馏塔的精馏装置中进行分离。 在第一精馏塔中,将待分离的混合物在低于第二塔的压力下进行精馏,成为富含甲缩醛的不饱和甲醇的馏出物,并进入实际上无甲醛的富含甲醇的油槽产物。 然后将第一精馏的甲缩醛馏出物在比第一精馏塔高的压力下操作的第二精馏塔中分离成含有甲醇和甲缩醛的复合物流,然后将其再循环至第一精馏塔,并进入 纯甲缩醛作为贮槽产品。 在特定的改进中,第一精馏优选在1-22巴绝对压力下操作,优选在9-30巴绝对压力下进行第二次精馏,第二次精馏在至少8巴的压力下操作 高于首次整改。