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procedures for the extraction of wiederbenutzbaren urea in urea entparaffinierungsanlagen kreislauflösungen

机译:尿素脱蜡系统中可重复利用尿素的提取程序

摘要

Process for purifying aq. urea solns., partic. for regenerating those flowing in closed circuit in a dewatering plant comprises adding, esp. to a fraction withdrawn from the circuit, ammonia to concn. of 1-10 wt.%. This soln is then held at 110-170 degrees C for 30-240 min., then excess NH3 and CO2 are eliminated, if necessary, before recycling to the dewaxing plant. Pref. NH3 added is that obtd. from a previously purified stream, esp. that liberated by expansion of the warm purified soln. Pref. absorption, purification, sepn. of CO2 and opt. excess NH3 and opt. sepn. of CO2 from NH3 are all effected in a single operative stage in a single reactor. Appts. for the process is also claimed. Condensation prods. such as biuret are destroyed and urea losses are reduced, e.g. by 50-80%.
机译:纯化水的过程尿素溶液。用于再生脱水设备中闭路流动的那些的方法包括添加,特别是。从回路中抽出一部分,氨气浓缩。 1-10重量%。然后将这种溶液在110-170摄氏度下保持30-240分钟,然后根据需要除去多余的NH3和CO2,然后再循环回脱蜡工厂。首选加入的NH3是obtd。从先前纯化的流中,特别是通过温热的纯锡膨胀而释放出来的。首选吸收,纯化,分离。的二氧化碳和选择。 NH3过量并选择。 sepn。来自NH 3的CO 2全部在单个反应器的单个操作阶段中进行。 Appts。该过程也被要求。冷凝物。例如缩二脲的销毁和尿素损失的减少,例如。 50-80%。

著录项

  • 公开/公告号DE2821995C2

    专利类型

  • 公开/公告日1986-08-14

    原文格式PDF

  • 申请/专利权人 OEMV AG WIEN AT;

    申请/专利号DE19782821995

  • 申请日1978-05-19

  • 分类号C07C126/08;C10G73/24;C07C127/01;

  • 国家 DE

  • 入库时间 2022-08-22 07:32:58

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