Granulation of urea products
    1.
    发明专利

    公开(公告)号:AU2016291068A1

    公开(公告)日:2018-01-25

    申请号:AU2016291068

    申请日:2016-07-06

    Applicant: STAMICARBON

    Abstract: Disclosed is a method of making a granulate of a urea product comprising urea and a salt, such as urea ammonium sulfate, having a high content of the salt. The high content is such as to provide an amount of the salt above the limit of solubility of the salt in urea. The granulate of the invention is characterized by having a smooth surface, which, e.g. in the event of urea ammonium sulfate, is not normally the case for granulate having the aforementioned high ammonium sulfate content. According to the invention this is realized by dividing the feed liquids to granulation. This division is based on non-final granulation liquids of a sufficiently high content of the salt, and a final granulation liquid (determining the surface) having a salt content of below the solubility limit of the salt, or no salt at all. E.g. in the event of urea ammonium sulfate, the non-final granulation liquids possibly are a slurry of urea and more than 20 wt.% of ammonium sulfate. The final granulation liquid then has 0-20 wt.% of ammonium sulfate, i.e. below the solubility limit.

    Removal of dust in urea finishing

    公开(公告)号:AU2014284776B2

    公开(公告)日:2018-01-18

    申请号:AU2014284776

    申请日:2014-07-04

    Applicant: STAMICARBON

    Abstract: Disclosed is a method for the removal of urea dust from the off- gas of a finishing section (1) of a urea production plant, the method comprises subjecting the off-gas to quenching with water (06) so as to produce quenched off-gas, and subjecting the quenched off-gas to scrubbing using at least one venturi scrubber (11). As a result, a lower pressure drop over the scrubber is attained, and a more efficient growth of urea particles, facilitating the removal thereof.

    REMOVAL OF DUST IN UREA FINISHING

    公开(公告)号:CA2917304A1

    公开(公告)日:2015-01-08

    申请号:CA2917304

    申请日:2014-07-04

    Applicant: STAMICARBON

    Abstract: Disclosed is a method for the removal of urea dust from the off- gas of a finishing section (1) of a urea production plant, the method comprises subjecting the off-gas to quenching with water (06) so as to produce quenched off-gas, and subjecting the quenched off-gas to scrubbing using at least one venturi scrubber (11). As a result, a lower pressure drop over the scrubber is attained, and a more efficient growth of urea particles, facilitating the removal thereof.

    REMOVAL OF DUST IN UREA FINISHING

    公开(公告)号:CA2917304C

    公开(公告)日:2020-09-15

    申请号:CA2917304

    申请日:2014-07-04

    Applicant: STAMICARBON

    Abstract: Disclosed is a method for the removal of urea dust from the off- gas of a finishing section (1) of a urea production plant, the method comprises subjecting the off-gas to quenching with water (06) so as to produce quenched off-gas, and subjecting the quenched off-gas to scrubbing using at least one venturi scrubber (11). As a result, a lower pressure drop over the scrubber is attained, and a more efficient growth of urea particles, facilitating the removal thereof.

    Granulation of urea products
    8.
    发明专利

    公开(公告)号:AU2016291068B2

    公开(公告)日:2019-11-28

    申请号:AU2016291068

    申请日:2016-07-06

    Applicant: STAMICARBON

    Abstract: Disclosed is a method of making a granulate of a urea product comprising urea and a salt, such as urea ammonium sulfate, having a high content of the salt. The high content is such as to provide an amount of the salt above the limit of solubility of the salt in urea. The granulate of the invention is characterized by having a smooth surface, which, e.g. in the event of urea ammonium sulfate, is not normally the case for granulate having the aforementioned high ammonium sulfate content. According to the invention this is realized by dividing the feed liquids to granulation. This division is based on non-final granulation liquids of a sufficiently high content of the salt, and a final granulation liquid (determining the surface) having a salt content of below the solubility limit of the salt, or no salt at all. E.g. in the event of urea ammonium sulfate, the non-final granulation liquids possibly are a slurry of urea and more than 20 wt.% of ammonium sulfate. The final granulation liquid then has 0-20 wt.% of ammonium sulfate, i.e. below the solubility limit.

    УДАЛЕНИЕ ПЫЛИ ПРИ ДОВОДКЕ КАРБАМИДА

    公开(公告)号:EA030594B1

    公开(公告)日:2018-08-31

    申请号:EA201690164

    申请日:2014-07-04

    Applicant: STAMICARBON

    Abstract: Раскрытспособудаленияпыликарбамидаизотходящегогазадоводочнойсекции (1) установкипопроизводствукарбамида, причемспособвключаетвыполнениегашенияотходящегогазаводой (06) сполучениемгашеногоотходящегогазаи выполнениеочисткигашеногоотходящегогазаприпомощипоменьшеймереодногоскруббераВентури (11). Врезультатеэтогодостигаетсяменьшеепадениедавлениянаскруббереи болееэффективныйростчастицкарбамида, чтоупрощаетихудаление.

    GRANULATION OF UREA PRODUCTS
    10.
    发明专利

    公开(公告)号:CA2991280A1

    公开(公告)日:2017-01-12

    申请号:CA2991280

    申请日:2016-07-06

    Applicant: STAMICARBON

    Abstract: Disclosed is a method of making a granulate of a urea product comprising urea and a salt, such as urea ammonium sulfate, having a high content of the salt. The high content is such as to provide an amount of the salt above the limit of solubility of the salt in urea. The granulate of the invention is characterized by having a smooth surface, which, e.g. in the event of urea ammonium sulfate, is not normally the case for granulate having the aforementioned high ammonium sulfate content. According to the invention this is realized by dividing the feed liquids to granulation. This division is based on non-final granulation liquids of a sufficiently high content of the salt, and a final granulation liquid (determining the surface) having a salt content of below the solubility limit of the salt, or no salt at all. E.g. in the event of urea ammonium sulfate, the non-final granulation liquids possibly are a slurry of urea and more than 20 wt.% of ammonium sulfate. The final granulation liquid then has 0-20 wt.% of ammonium sulfate, i.e. below the solubility limit.

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