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process for the production of lagerstabilen, liquid urea formaldehyde leimharzen.

机译:生产过程中的液态啤酒脲甲醛leimharzen。

摘要

The resins (I), with molar ratio U:F 1:1.0-1:2.1 and solids content 58-75 wt.% on total wt. (I) are prepd. by 1) thin layer-evaporating UF precondensate with solids content 38-55 wt.% on wt. (I) to solids content 58-72 wt.% 2) returning 10-60 wt.% prod. to thin layer-evapn. 3) adding aq. U soln. then 4) flash-evaporating prod. directly (i.e., within interval so short that no substantial reaction occurs between U added in 3) and condensate). Opt. UF precondensate is also prepd. with melamine and/or phenol, opt. as precondensates with HCHO. Interval between 3) and 4) is 0.5-5, partic. 1.8-2.5, seconds. Thin layer evapn. is effected in one or more consecutive or parallel stages, partic. in 2 or 3 stages with prod. being returned in each stage. Average film thickness in falling film evaporator(s) is about 1.5 mm, average residence time is 1-10 minutes. Thin film evapn. is carried out with steam at 2-6 bar. Soln. is evaporated at 48-100 deg.C. Mixing is provided between 3) and 4). U soln. in 3) is 60-72 wt.%. Returned part of soln. is treated with 60-72 wt.% soln. of U before again subjecting to thin layer evapn.
机译:树脂(I)的摩尔比U∶F为1∶1.0-1∶2.1,固体含量为总重量的58-75重量%。 (一)准备。通过1)薄层蒸发的UF预冷凝物,其固体含量为38-55重量%。 (I)至固体含量58-72重量%2)返回10-60重量%的产品。薄层蒸发。 3)添加水U soln。然后4)闪蒸产品。直接(即在很短的间隔内,以至于3中添加的U之间不会发生实质性反应)和冷凝物。选择。 UF预冷凝液也可制备。选择含三聚氰胺和/或苯酚。作为HCHO的预缩合物。 3)和4)之间的间隔为0.5-5(以偶数表示)。 1.8-2.5秒薄层蒸发。分阶段进行一个或多个连续或并行阶段。在2或3阶段使用prod。在每个阶段被归还。降膜蒸发器的平均膜厚约为1.5毫米,平均停留时间为1-10分钟。薄膜蒸发。用2-6 bar的蒸汽进行。索恩在48-100℃蒸发。在3)和4)之间提供混合。 U soln。 3)中的含量为60-72重量%。返回部分soln。用60-72wt。%的sol处理。在再次经受薄层蒸发之前的U的值。

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