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    • 66. 发明授权
    • Process for producing urea
    • 生产尿素的方法
    • US5597454A
    • 1997-01-28
    • US418089
    • 1995-04-06
    • Jing M. Lee
    • Jing M. Lee
    • B01D3/34B01D3/38C07C273/04B01D3/00C07C273/16
    • B01D3/34B01D3/38C07C273/04Y02P20/124Y02P20/57
    • A urea production process combining lower pressure urea concentration and carbamate recovery steps into a single non-vacuum operation. Following high pressure stripping wherein a bulk of unreacted carbamate is recovered from the reaction effluent, remaining carbamate is stripped by heated air at atmospheric pressure wherein urea is concurrently concentrated without the use of vacuum evaporators. Weak carbamate solution subsequently formed is stripped of water (and residual urea is hydrolyzed) using air and steam at a medium pressure single tower hydrolyzer/stripper to obtain a concentrated carbamate stream suitable for recycle to the reactor. The process employs heat integration for enhanced energy efficiency and produces a good quality aqueous condensate suitable for direct use as boiler feed water. Thus the aqueous condensate produced requires no additional cooling and ammonia treatment. The process employs simplified and reduced process unit operation to eliminate equipment for cost reduction.
    • 将低压尿素浓度和氨基甲酸酯回收步骤组合成单一非真空操作的尿素生产方法。 在高压汽提之后,从反应流出物中回收大量未反应的氨基甲酸酯,剩余的氨基甲酸酯在大气压下被加热的空气汽提,其中尿素同时浓缩而不使用真空蒸发器。 使用空气和蒸汽在中压单塔水解器/汽提器上将随后形成的弱氨基甲酸酯溶液除去水(和残留的尿素水解),得到适于再循环至反应器的浓氨基甲酸酯流。 该方法采用热集成来提高能源效率,并产生适合直接用作锅炉给水的优质水凝胶。 因此,产生的水凝胶不需要额外的冷却和氨处理。 该过程采用简化和简化的过程单元操作,以消除设备降低成本。
    • 70. 发明授权
    • Methods for removing biuret from urea by adsorption
    • 通过吸附从尿素中除去缩二脲的方法
    • US4701555A
    • 1987-10-20
    • US753692
    • 1985-07-10
    • Donald C. YoungJames A. Green, II
    • Donald C. YoungJames A. Green, II
    • C07C273/16C07C127/24C07C126/08
    • C07C273/16
    • The biuret content of biuret-containing urea is reduced by contacting a solution or melt of biuret-containing urea with a polar adsorbent under conditions sufficient to remove at least a portion of biuret from the urea. The resulting biuret-containing adsorbent can be regenerated for further use by contact with a polar desorbent under conditions sufficient to desorb at least a portion of the biuret contained on the adsorbent. Optionally, biuret can be recovered by recovering the biuret-containing desorbent, and biuret concentration in the desorbent can be increased by recycling the biuret-containing desorbent into contact with biuret-containing adsorbents, and biuret can be recovered from the desorbent by low temperature crystallization.
    • 通过在足以从尿素除去至少一部分缩二脲的条件下使含缩二脲的脲与极性吸附剂的溶液或熔体接触来降低缩二脲含脲的缩二脲含量。 所得到的含缩二脲合金的吸附剂可以在足以解吸吸附剂上所含的至少一部分缩二脲的条件下与极性解吸剂接触来再生再进一步使用。 任选地,可以通过回收含缩二脲的解吸剂来回收缩二脲,并且可以通过将含缩二脲的解吸剂再循环到与含缩二脲的吸附剂接触来提高解吸剂中的缩二脲浓度,并且可以通过低温结晶从解吸剂中回收缩二脲 。