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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

A process is claimed for the prodn. of urea-formaldehyde resins (I) with U:F ratio from 1:1.0 to 1:2.1 and a solids content of 58-75 wt.% (opt. contg. melamine, phenol, etc.), by concn. of a condensate soln. (II), followed opt. by reaction with urea. (II) contains 38-55 wt.% dry matter, and is conc. by thin-layer evapn. to 58-72 wt.%, with recycling of 10-60 wt.% of the prod. soln. to the thin layer evaporator. Evapn. is performed in falling-film evaporator(s) in series or in parallel, pref. in two or three stages with recycling at each stage; evaporator is operated with film thickness about 1.5 mm and dwell-time 1-10 mins., pref. with steam at 2-6 bar, and at 48-100 deg.C; recycled soln. is treated with 60-70 wt.% aq. urea soln. before re-entering the evaporator; evapn. is performed at 850-100 mbar; pref., (II) contains 40-50 wt.% dry matter, and is conc. to 60-68 wt.%.
机译:要求保护该产品的过程。 U.F比为1:1.0至1:2.1,固含量为58-75 wt。%(优选含三聚氰胺,苯酚等)的脲醛树脂(I)冷凝液(II),然后选择。通过与尿素反应。 (II)含有38-55重量%的干物质,并且是浓稠的。通过薄层蒸发。至58-72重量%,其中产品的10-60重量%的再循环。 soln。到薄层蒸发器。 va优选在降膜蒸发器中串联或并联进行。分两个或三个阶段,每个阶段进行回收;蒸发器的膜厚约1.5毫米,保压时间1-10分钟,优选。在2-6 bar和48-100摄氏度的温度下使用蒸汽;再生溶液。用60-70重量%的水溶液处理。尿素溶液重新进入蒸发器之前;逃避在850-100毫巴下进行;优选地,(II)包含40-50重量%的干物质,并且是浓的。至60-68重量%。

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