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    • 7. 发明申请
    • PROCESS AND APPARATUS FOR PRODUCING AMMONIUM SULFATE CRYSTALS
    • 生产硫酸汞晶体的方法和装置
    • US20160159657A1
    • 2016-06-09
    • US14899579
    • 2014-06-20
    • CAP III B.V.
    • Johan Thomas TingeGeert EkkelenkampRobert Geertman
    • C01C1/24B01D9/00
    • C01C1/24B01D9/0022B01D9/0031B01D9/004B01D9/0063B01D2009/0086C01C1/248C07C249/08C07C2601/14C07D201/04C07D201/16C07C251/44
    • The present invention provides a continuous process for producing ammonium sulfate crystals, wherein said process comprises: (a) feeding to a first group of crystallization sections, which crystallization sections are heat integrated in series, a first aqueous ammonium sulfate solution that contains one or more impurities; (b) feeding to a second group of crystallization sections, which crystallization sections are heat integrated in series, a second aqueous ammonium sulfate solution that contains one or more impurities; (c) crystallizing ammonium sulfate crystals in each crystallization section respectively from each of said solutions of ammonium sulfate that contain one or more impurities; (d) purging a fraction of the ammonium sulfate solution that contains one or more impurities from each of said crystallization sections; and (e) discharging ammonium sulfate crystals from each crystallization section, characterized in that: (i) both the first group of crystallization sections and the second group of crystallization sections are together heat integrated in one series of crystallization sections; wherein the first group of crystallization sections operates at higher temperature than the second group of crystallization sections; and (ii) the composition of the first aqueous ammonium sulfate solution that contains one or more impurities is different to the composition of the second aqueous ammonium sulfate solution that contains one or more impurities. Further provided is apparatus suitable for producing ammonium sulfate crystals.
    • 本发明提供了一种用于生产硫酸铵晶体的连续方法,其中所述方法包括:(a)将第一组结晶部分进料到该第一组结晶部分,该结晶部分是串联的热积分法,第一组硫酸铵水溶液含有一种或多种 杂质; (b)将第二组结晶部分进料到该第二组结晶部分,该结晶部分串联加热一体化,含有一种或多种杂质的第二硫酸铵溶液; (c)分别从含有一种或多种杂质的所述硫酸铵溶液中分别在每个结晶段中结晶硫酸铵晶体; (d)从每个所述结晶部分清洗含有一种或多种杂质的硫酸铵溶液的一部分; 和(e)从每个结晶部分排出硫酸铵晶体,其特征在于:(i)第一组结晶部分和第二组结晶部分一起热集成在一系列结晶部分中; 其中所述第一组结晶段在比所述第二组结晶段更高的温度下操作; 和(ii)含有一种或多种杂质的第一硫酸铵水溶液的组成与含有一种或多种杂质的第二硫酸铵水溶液的组成不同。 还提供了适用于生产硫酸铵晶体的装置。
    • 8. 发明申请
    • PROCESS FOR INITIATING AN AMMONIUM SULFATE CRYSTALLIZATION PROCESS
    • 开发硫酸铵结晶过程的方法
    • US20150224421A1
    • 2015-08-13
    • US14424639
    • 2013-08-28
    • DSM IP ASSETS B.V.
    • Geert EkkelenkampJohan Thomas TingePieter Vonk
    • B01D9/00C01C1/248C01C1/24
    • B01D9/0018B01D9/0031B01D9/0036B01D2009/0086C01C1/24C01C1/248C01P2004/60C05C3/00
    • A continuous process for producing crystal-line ammonium sulfate, said process comprising a start-up operation followed by a steady-state operation, wherein the start-up operation comprises: i) in a crystallizer, evaporating solvent from an approximately saturated ammonium sulfate solution; ii) replacing evaporated solvent with further approximately proximately saturated ammonium sulfate solution; iii) introducing to the crystallizer seed crystals of ammonium sulfate; iv) continuing to evaporate solvent, until a desired degree of supersaturation is reached; and v) recovering crystalline ammonium sulfate from ammonium sulfate solution in a recovery unit, and the steady-state operation comprises: vi) continuously feeding approximately saturated ammonium sulfate solution into the crystallizer and continuously withdrawing ammonium sulfate crystals from the crystallizer, such that the total combined volume of ammonium sulfate solution and ammonium sulfate crystals within the crystallizer remains constant; and vii) recovering crystalline ammonium sulfate from ammonium sulfate solution in a recovery unit, characterized in that the degree of supersaturation in the crystallizer during the start-up operation is maintained between 1.2% and the point at which primary nucleation occurs; and apparatus suitable for carrying out the process.
    • 一种用于生产结晶线型硫酸铵的连续方法,所述方法包括启动操作,随后进行稳态操作,其中启动操作包括:i)在结晶器中,从约饱和的硫酸铵溶液蒸发溶剂 ; ii)用另外的近似饱和的硫酸铵溶液代替蒸发的溶剂; iii)将结晶器引入硫酸铵晶种; iv)继续蒸发溶剂,直到达到所需的过饱和度; 和v)在回收单元中从硫酸铵溶液中回收结晶硫酸铵,并且稳态操作包括:vi)将大约饱和的硫酸铵溶液连续地进料到结晶器中并连续地从结晶器中取出硫酸铵晶体,使得总计 结晶器中硫酸铵溶液和硫酸铵晶体的组合体积保持不变; 和vii)在回收单元中从硫酸铵溶液中回收结晶硫酸铵,其特征在于,启动操作期间结晶器中的过饱和度保持在1.2%和初始成核出现点之间; 以及适于执行该过程的装置。