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Process for the preparation of urea, and urea and the urea solution thus prepared

机译:制备尿素的方法以及由此制备的尿素和尿素溶液

摘要

Process for the preparation of urea in which a urea synthesis solution containing carbamate and free ammonia is formed in a high-pressure part in a synthesis zone at an NH3/CO2 molar ratio of up to 4:1, a temperature of at least 175 DEG C. and the corresponding pressure, a portion of the carbamate is decomposed in a first decomposition stage at synthesis pressure or lower pressure by a stripping treatment with carbon dioxide while heat is being supplied, and the gas mixture thus obtained is at least in part condensed and the condensate and the non-condensed portion of the gas mixture, if any, are returned to the synthesis zone, a further portion of the carbamate still present is decomposed in at least two further decomposition stages and the gas mixture formed is separated, in the first of the further decomposition stages a pressure of 12-30 bar being maintained and heat being supplied and in the second of the further decomposition stages a lower pressure being maintained, and the remaining urea-containing solution is processed further by evaporation to a concentrated urea solution and, if desired, solid urea. In the first decomposition stage a portion of the urea synthesis solution is subjected to a stripping treatment with carbon dioxide while heat is being supplied, and the remaining portion of the urea synthesis solution is countercurrently contacted with carbon dioxide under adiabatic conditions. The gas mixtures obtained in both operations are at least in part condensed in a first condensation zone. The solution obtained in the treatment of the urea synthesis solution with carbon dioxide under adiabatic conditions is supplied to the first of the further decomposition stages and the stripped urea synthesis solution to the second of the further decomposition stages.
机译:制备尿素的方法,其中在合成区的高压部分以高达3∶1的NH 3 / CO 2摩尔比,至少175℃的温度形成含有氨基甲酸酯和游离氨的尿素合成溶液。在相应的压力下,一部分氨基甲酸酯在合成压力或更低的压力下在第一分解阶段中通过在供给热量的同时通过二氧化碳的汽提处理而分解,并且由此获得的气体混合物至少部分冷凝。并且将气体混合物的冷凝物和非冷凝部分(如果有的话)返回到合成区,仍然存​​在的另一部分氨基甲酸酯在至少两个另外的分解阶段中分解,并且分离形成的气体混合物,在第一个进一步的分解阶段中,保持12-30 bar的压力并提供热量;在第二个进一步的分解阶段中,保持较低的压力,并且通过蒸发至浓缩的尿素溶液和(如果需要的话)固体尿素,进一步处理包含尿素的溶液。在第一分解阶段中,一部分尿素合成溶液在供给热量的同时用二氧化碳进行汽提处理,并且剩余部分的尿素合成溶液在绝热条件下与二氧化碳逆流接触。在两个操作中获得的气体混合物在第一冷凝区中至少部分冷凝。在绝热条件下用二氧化碳处理尿素合成溶液中获得的溶液被供应到另外的分解步骤的第一阶段,汽提的尿素合成溶液被提供到分解的第二步骤的第二阶段。

著录项

  • 公开/公告号BR8603803A

    专利类型

  • 公开/公告日1987-03-17

    原文格式PDF

  • 申请/专利权人 STAMICARBON B.V.;

    申请/专利号BR19868603803

  • 发明设计人 VICTOR ELODIE ALBERT BAENENS;

    申请日1986-08-08

  • 分类号C07C126/02;

  • 国家 BR

  • 入库时间 2022-08-22 07:21:38

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