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MELAMINE SYNTHESIS PLANT AND MELAMINE SYNTHESIS

机译:三聚氰胺合成厂和三聚氰胺合成

摘要

High pressure melamine manufacturing process starting from urea with high yields and conversion rates characterized in that it comprises the following steps: a) urea is fed to a reactor essentially containing molten melamine, which reactor operates in continuous and is kept at a temperature in the range of 360 to 420° C. under a pressure higher than 7x103 KPa and preferably 8x103 to 9x103 KPa, while a vigorous mixing is provided by evolving gases; b) liquid reaction product is recovered containing 85 to 95%, preferably 88 to 93% melamine and a gaseous phase is removed containing essentially CO2 and NH3; c) liquid phase collected in b) is continuously fed, together with fresh NH3 to a tubular reactor, in which the essentially whole volume is occupied by the liquid phase (plug flow reactor) without any mixing of the reaction product with reactant nor the intermediate products (no "back mixing"), kept at a temperature of 360 to 450° C. and under a pressure higher than 7x103 KPa for a residence time sufficient to complete the reaction; d) melamine with a high purity level is collected from the outlet of the tubular reactor.
机译:从尿素以高收率和高转化率开始的高压三聚氰胺制造工艺,其特征在于它包括以下步骤:a)将尿素进料到基本上包含熔融三聚氰胺的反应器中,该反应器连续运行并保持在该温度范围内。在高于7x103 KPa,优选为8x103至9x103 KPa的压力下,压力为360至420°C,同时通过放出的气体进行剧烈混合; b)回收包含85-95%,优选88-93%三聚氰胺的液体反应产物,并除去基本上包含CO 2和NH 3的气相; c)将b)中收集的液相与新鲜的NH3一起连续进料到管式反应器中,其中基本上整个体积都被液相占据(活塞流反应器),而反应产物与反应物或中间体之间没有任何混合产物(无“反向混合”),在360至450℃的温度下和在高于7×103 KPa的压力下保持足以完成反应的停留时间; d)从管式反应器的出口收集高纯度三聚氰胺。

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