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granulation process of urea with an acid scrubbing system and the subsequent integration of ammonium salt in urea granules

机译:酸洗涤系统制粒尿素的过程以及随后将铵盐整合到尿素颗粒中

摘要

urea granulation process with an acid scrubbing system and the subsequent integration of ammonium salt in urea granules. the invention relates to a urea granulation process with a purification system including several residual streams for removing dust and ammonia from the exhaust gas of a urea granulation unit comprising a urea granulator (1), a stage of urea granulator scrubber dust (2), a granulator scrubber acid stage (3), product coolers (5), a product cooler deputy dust stage (4), an evaporation unit (6), and a condenser unit (7). In this way, a first stream of fresh air (8), passing through a first sequence of process steps, is sent to the urea granulator (1), through which the air charged with dust and ammonia (9) is removed from the granulator (1) and transported in a granulator scrubber dust stage (2), followed by a granulator scrubber acid stage (2), followed by a granulator scrubber acid stage (3), this stage in that the air loaded with ammonia (12) is contacted with an acid in the liquid phase (22) and the ammonia is purified from this air by the generation of an ammonium salt. a second stream of fresh air (15), passing through a second sequence of process steps, is used to cool the product removed from the sand granulator (1), by means of which said cooling is carried out in product coolers (5 ), in this way the said air is heated, and later it is transported to a dust stage of the product cooler debugger (4). the clean exhaust gas (13) taken from the acid stage of the granulator scrubber (3), and the clean exhaust gas (18) taken from the dust cooler stage of the product cooler (4), are released into the atmosphere ( 19). therefore, the purification system is passed, which in itself is a complete closed system, and totally separated from urea synthesis, by means of which the ammonium salt solution stream (23) of the acid stage of the purifier is granulator (3), is fed into said dust stage of the product cooler debugger (4), whereby the ammonia from the air stream charged with dust (17) leaving the product coolers (5) is removed, and the liquid substance released (24) from the dust stage of the product cooler scrubber (4) and the liquid substance released (11) from the dust stage of the granulator scrubber (2) are sent to the evaporation unit (6). the vapor stream (29) of the evaporation unit (6), which contains ammonia is supplied in the condenser unit (7), which releases a liquid process condenser (30), and said liquid process condensate (30) is supplied with concentrated liquid substance (28) from the evaporation unit (6), containing urea and ammonium salt, and a melt of urea (26) from a synthesis unit (27) are transported in the urea granulator (1), separately . in this way, the ammonium salt contained in the concentrated liquid substance stream (28) is integrated into the granulated urea product.
机译:尿素制粒过程,采用酸洗系统,随后将铵盐整合到尿素颗粒中。本发明涉及具有纯化系统的尿素制粒方法,该纯化系统包括用于从包括尿素制粒机(1),尿素制粒机洗涤器粉尘级(2)的尿素制粒机的废气制粒单元的废气中除去灰尘和氨的残余流。制粒器洗涤器酸级(3),产品冷却器(5),产品冷却器副粉尘级(4),蒸发单元(6)和冷凝器单元(7)。以此方式,经过第一顺序的工艺步骤的第一新鲜空气流(8)被送到尿素造粒机(1),通过该尿素造粒机(1),从该造粒机中去除了充有灰尘和氨的空气(9)。 (1)并在制粒机洗涤器除尘阶段(2)中运输,然后在制粒机洗涤器酸阶段(2),然后在制粒机洗涤器酸阶段(3)中运输,该阶段的过程是在装有氨气的空气中(12)在液相(22)中与酸接触,氨通过生成铵盐从空气中纯化出来。经过第二步工艺步骤的第二股新鲜空气流(15)用于冷却从制砂机(1)中取出的产品,并在产品冷却器(5)中进行冷却;以这种方式,将所述空气加热,然后将其输送到产品冷却器调试器(4)的除尘级。从制粒机洗涤器(3)的酸性阶段获得的清洁废气(13)和从产品冷却器(4)的粉尘冷却器阶段获得的清洁废气(18)释放到大气(19)中。因此,必须通过纯化系统,该系统本身是一个完整的封闭系统,并且与尿素合成完全分离,通过该系统可以将纯化器酸性阶段的铵盐溶液流(23)作为制粒机(3)。将其送入产品冷却器调试器(4)的所述粉尘级,从而去除了充有灰尘(17)的气流离开产品冷却器(5)的氨,并从粉尘级(24)释放了液体物质(24)。产品冷却器洗涤器(4)和从制粒机洗涤器(2)的粉尘阶段释放的液体物质(11)被送至蒸发单元(6)。在冷凝器单元(7)中供应包含氨的蒸发单元(6)的蒸气流(29),其释放出液体工艺冷凝器(30),并且向所述液体工艺冷凝液(30)供应浓缩液。来自蒸发单元(6)的含有尿素和铵盐的物质(28)和来自合成单元(27)的尿素熔体(26)分别在尿素造粒机(1)中运输。以这种方式,将浓缩的液体物质流(28)中包含的铵盐整合到粒状尿素产物中。

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