PROCESS AND PLANT FOR AMMONIA-UREA PRODUCTION
    4.
    发明授权
    PROCESS AND PLANT FOR AMMONIA-UREA PRODUCTION 有权
    方法和系统合成氨 - 尿素生产

    公开(公告)号:EP2688840B1

    公开(公告)日:2014-12-17

    申请号:EP12702846.2

    申请日:2012-02-10

    Applicant: CASALE SA

    CPC classification number: C07C273/10 C01C1/0488 Y02P20/52 C07C275/02

    Abstract: A process for ammonia-urea production where: liquid ammonia produced in an ammonia section is fed to a urea section directly at the ammonia synthesis pressure, and where the liquid ammonia is purified at high pressure with the steps of: cooling the liquid ammonia (20) obtaining a cooled liquid ammonia stream (21), separating a gaseous fraction (22) comprising hydrogen and nitrogen from said cooled liquid ammonia, obtaining purified liquid ammonia (23) at a high pressure, and reheating said purified liquid ammonia (23) after separation of said gaseous fraction, obtaining a reheated purified ammonia (24) having a temperature suitable for feeding to the urea synthesis process. The application also deals with an ammonia-urea plant comprising an ammonia cooler, a liquid-gas separator and an ammonia re-heater and with a method for revamping existing ammonia-urea plants.

    METHOD FOR REVAMPING A HIGH PRESSURE MELAMINE PLANT

    公开(公告)号:EP3416953A1

    公开(公告)日:2018-12-26

    申请号:EP17701154.1

    申请日:2017-01-25

    Applicant: Casale SA

    Abstract: A high pressure melamine plant comprising a synthesis section and a melamine purification section, wherein the synthesis section provides a first melamine-containing stream (6), and said melamine purification section comprises: a quencher (2) receiving said first melamine-containing stream (6) from the synthesis section; a stripper (3) fed with a second melamine-containing stream (7) from said quencher (2), wherein purified melamine (11) is collected and vapours (10) are extracted; a heat exchanger (12), wherein said vapours (10) are condensed providing a condensed stream (14); an absorber (4) fed with said condensed stream (14) providing an aqueous solution (15) comprising ammonia and carbon dioxide, at least a portion (15b) of said aqueous solution being exported from the purification section (200) of the plant.

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