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    • 2. 发明申请
    • METHOD FOR PRODUCING A COARSE-GRAINED AMMONIUM SULFATE PRODUCT VIA CRYSTALLIZATION AND INSTALLATION FOR OPERATING THE METHOD
    • 通过结晶化和安装方法生产粗粒度硫酸亚铁产品的方法
    • US20130230446A1
    • 2013-09-05
    • US13780297
    • 2013-02-28
    • GEA MESSO GMBH
    • Guenter HofmannHolger LeptienJohannes Widua
    • B01D9/00
    • B01D9/0036B01D9/0022B01D9/0031B01D9/0059C01C1/248
    • Method for the production of a coarse-grained ammonium sulphate product by crystallization and installation for carrying out the method. A method for the continuous production of a coarse-grained ammonium sulphate product from an ammonium sulphate solution in a crystallizer operates in accordance with the DTB principle and has an internal suspension circuit and a clarifying zone, from which a clarified partial flow of solution is constantly drawn off into an external circuit, is heated in a heat exchanger so as to dissolve the solids contained therein and is then guided back as a clear solution into the lower region of the crystallizer. In order to ensure production of a product crystallizate with a grain coarseness which is practically constant over time, a fine crystal suspension flow may be drawn off from the clarifying zone as a further partial flow and guided back into the internal circuit of the crystallization stage without any previous dissolution of the solid proportion contained therein.
    • 通过结晶和安装来实施该方法生产粗粒度硫酸铵产品的方法。 在结晶器中从硫酸铵溶液连续生产粗粒度硫酸铵产品的方法根据DTB原理进行操作,并且具有内部悬浮电路和澄清区,澄清的部分溶液流从其中恒定地 被排出到外部回路中,在热交换器中被加热以便溶解其中所含的固体,然后作为透明溶液被引导回到结晶器的下部区域。 为了确保产生晶粒粗糙度随着时间的推移实际上恒定的晶粒细化物,可以将澄清区域中的细晶体悬浮液流作为另外的部分流动而被引回到结晶阶段的内部回路而没有 任何先前溶解的固体比例都包含在其中。
    • 4. 发明授权
    • Method and device for continuously producing a crystallite having a constant particle size distribution
    • 用于连续生产具有恒定粒度分布的微晶的方法和装置
    • US08486158B2
    • 2013-07-16
    • US12993694
    • 2009-06-10
    • Reinhard ScholzGünter Hofmann
    • Reinhard ScholzGünter Hofmann
    • B01D9/00
    • C01C1/242B01D9/0022B01D9/0036B01D9/0063C01C1/248C01P2004/51
    • The invention proposes a method and a device for continuously producing a crystallite, wherein a metered amount of seed crystals is fed continuously to the internal solution circuit of a crystallizer, in particular a DTB crystallizer, through a crystallization seed line from a seed generator preferably designed as a flash crystallizer. The amount of seed crystals fed is controlled by an electronic control system as a function of a measured value determined by a sensor, said value being representative of the particle size distribution of the crystallites in the solution in the internal circuit in the crystallizer. By way of a line, the seed generator receives a partial stream of the external solution circuit of the crystallizer, said external circuit being routed through a line. Excess fine crystalline suspension can be fed back to the external circuit from the seed generator by way of a return line.
    • 本发明提出了一种用于连续生产微晶的方法和装置,其中将一定数量的晶种连续地送入结晶器,特别是DTB结晶器的内部溶液回路,通过晶种生长线从种子发生器中优选设计 作为闪光结晶器。 通过电子控制系统控制晶种的量作为由传感器确定的测量值的函数,所述值代表结晶器内部电路中的溶液中的微晶的粒度分布。 通过线路,种子发生器接收结晶器的外部溶液电路的部分流,所述外部电路通过线路。 过多的细晶悬浮液可以通过回流线从种子发生器反馈到外部电路。
    • 5. 发明申请
    • METHOD AND DEVICE FOR CONTINUOUSLY PRODUCING A CRYSTALLITE HAVING A CONSTANT PARTICLE SIZE DISTRIBUTION
    • 用于连续生产具有恒定颗粒尺寸分布的晶体的方法和装置
    • US20110061205A1
    • 2011-03-17
    • US12993694
    • 2009-06-10
    • Reinhard ScholzGünter Hofmann
    • Reinhard ScholzGünter Hofmann
    • B01D9/02
    • C01C1/242B01D9/0022B01D9/0036B01D9/0063C01C1/248C01P2004/51
    • The invention proposes a method and a device for continuously producing a crystallite, wherein a metered amount of seed crystals is fed continuously to the internal solution circuit of a crystallizer, in particular a DTB crystallizer, through a crystallization seed line from a seed generator preferably designed as a flash crystallizer. The amount of seed crystals fed is controlled by an electronic control system as a function of a measured value determined by a sensor, said value being representative of the particle size distribution of the crystallites in the solution in the internal circuit in the crystallizer. By way of a line, the seed generator receives a partial stream of the external solution circuit of the crystallizer, said external circuit being routed through a line. Excess fine crystalline suspension can be fed back to the external circuit from the seed generator by way of a return line.
    • 本发明提出了一种用于连续生产微晶的方法和装置,其中将一定数量的晶种连续地送入结晶器,特别是DTB结晶器的内部溶液回路,通过晶种生长线从种子发生器中优选设计 作为闪光结晶器。 通过电子控制系统控制晶种的量作为由传感器确定的测量值的函数,所述值代表结晶器内部电路中的溶液中的微晶的粒度分布。 通过线路,种子发生器接收结晶器的外部溶液电路的部分流,所述外部电路通过线路。 过多的细晶悬浮液可以通过回流线从种子发生器反馈到外部电路。
    • 6. 发明授权
    • Method and facility for producing a coarse-grained ammonium sulfate product by crystallization
    • 用于通过结晶生产粗粒度硫酸铵产品的方法和用于执行该方法的设备
    • US07942939B2
    • 2011-05-17
    • US12863661
    • 2009-01-23
    • Günter HofmannReinhard Scholz
    • Günter HofmannReinhard Scholz
    • B01D9/00
    • C05C3/005B01D9/0022B01D9/0036B01D9/0063C01C1/248
    • A method and installation for the production of a coarse-grained ammonium sulfate product by crystallization includes firstly generating a crystal having a grain smaller than the desired grain size in a pre-crystallizer and withdrawing a suspension therefrom, from which the fine crystal was previously separated in a classification connecting piece. This suspension, which contains medium-sized grain, is then conducted with a proportion of undersaturated mother liquor, which is sufficient for further crystal growth, into a DTB product crystallizer and crystallized therein to a desired grain size. The heating of the product crystallizer is performed by the heat contained in the vapors of the pre-crystallization. The pre-crystallization may also operate according to the DTB principle, wherein the mother liquor needed for crystallization is supplied in the form of separately admixed concentrated sulfuric acid and ammonia into the external solution loop of the pre-crystallizer. The reaction heat released in this case may be sufficient for the operation of the entire process.
    • 用于通过结晶生产粗粒度硫酸铵产品的方法和装置包括首先在预结晶器中产生晶粒小于预结晶器中的所需晶粒尺寸的晶体并从其中取出悬浮液,预先分离出细晶体 在分类连接件中。 然后将含有中等粒度的这种悬浮液用一定比例的足够进一步晶体生长的不饱和母液进入DTB产物结晶器中并在其中结晶至所需的晶粒尺寸。 产物结晶器的加热通过预结晶蒸汽中所含的热量进行。 预结晶也可以根据DTB原理操作,其中结晶所需的母液以单独混合的浓硫酸和氨的形式供应到预结晶器的外溶液环中。 在这种情况下释放的反应热可能对于整个过程的操作是足够的。
    • 7. 发明申请
    • METHOD FOR PRODUCING A COARSE-GRAINED AMMONIUM SULFATE PRODUCT BY CRYSTALLIZATION AND FACILITY FOR PERFORMING THE METHOD
    • 通过结晶和生产粗糙度硫酸铵产品的方法,用于实施方法
    • US20110038781A1
    • 2011-02-17
    • US12863661
    • 2009-01-23
    • Günter HofmannReinhard Scholz
    • Günter HofmannReinhard Scholz
    • C01B21/086B01D9/00
    • C05C3/005B01D9/0022B01D9/0036B01D9/0063C01C1/248
    • A method and installation for the production of a coarse-grained ammonium sulfate product by crystallization includes firstly generating a crystal having a grain smaller than the desired grain size in a pre-crystallizer and withdrawing a suspension therefrom, from which the fine crystal was previously separated in a classification connecting piece. This suspension, which contains medium-sized grain, is then conducted with a proportion of undersaturated mother liquor, which is sufficient for further crystal growth, into a DTB product crystallizer and crystallized therein to a desired grain size. The heating of the product crystallizer is performed by the heat contained in the vapors of the pre-crystallization. The pre-crystallization may also operate according to the DTB principle, wherein the mother liquor needed for crystallization is supplied in the form of separately admixed concentrated sulfuric acid and ammonia into the external solution loop of the pre-crystallizer. The reaction heat released in this case may be sufficient for the operation of the entire process.
    • 用于通过结晶生产粗粒度硫酸铵产品的方法和装置包括首先在预结晶器中产生晶粒小于预结晶器中的所需晶粒尺寸的晶体并从其中取出悬浮液,预先分离出细晶体 在分类连接件中。 然后将含有中等粒度的这种悬浮液用一定比例的足够进一步晶体生长的不饱和母液进入DTB产物结晶器中并在其中结晶至所需的晶粒尺寸。 产物结晶器的加热通过预结晶蒸汽中所含的热量进行。 预结晶也可以根据DTB原理操作,其中结晶所需的母液以单独混合的浓硫酸和氨的形式供应到预结晶器的外溶液环中。 在这种情况下释放的反应热可能对于整个过程的操作是足够的。