DEVICE AND pH CALCULATION METHOD
    8.
    发明公开
    DEVICE AND pH CALCULATION METHOD 有权
    VORRICHTUNG UND PH-BERECHNUNGSVERFAHREN

    公开(公告)号:EP3214440A4

    公开(公告)日:2017-10-04

    申请号:EP16764572

    申请日:2016-02-05

    Abstract: A human load of regularly measuring a pH of a position 4 meters from a discharge point during a term of a commissioning of a ship with a scrubber apparatus is reduced. Provided is an apparatus provided inside a ship having a scrubber, including a first pH measuring instrument which measures a pH value of washing water discharged from the scrubber to outboard, a second pH measuring instrument which measures a pH value of washing water supplied from outboard to the scrubber, and a calculating unit which calculates a pH value of water at a predetermined position outboard, based on a dilution ratio which shows a ratio by which the washing water discharged to outboard is diluted at the predetermined position outboard, the pH value measured by the first pH measuring instrument, and the pH value measured by the second pH measuring instrument.

    Abstract translation: 减少了在具有涤气器装置的船舶试运行期间定期测量距卸货点4米的位置的pH值的人类负荷。 提供一种设置在具有洗涤器的船舶内部的设备,该设备包括:第一pH测量仪器,其测量从洗涤器向外部排出的洗涤水的pH值;第二pH测量仪器,其测量从外部供给到洗涤器的洗涤水的pH值 所述洗涤器和计算单元,所述计算单元基于表示排出到外侧的洗涤水在所述外侧的所述预定位置被稀释的比例的稀释比来计算外侧预定位置处的水的pH值, 第一个pH测量仪,以及第二个pH测量仪测量的pH值。

    CO2 RECOVERY DEVICE AND CO2 RECOVERY METHOD
    10.
    发明公开
    CO2 RECOVERY DEVICE AND CO2 RECOVERY METHOD 审中-公开
    二氧化碳回收设备和二氧化碳回收过程

    公开(公告)号:EP3150270A1

    公开(公告)日:2017-04-05

    申请号:EP15818919.1

    申请日:2015-06-19

    Abstract: Provided are a CO 2 recovery unit and a CO 2 recovery method which enable stable operation to continue even if an operation condition has changed. This CO 2 recovery unit (1) is equipped with: a CO 2 -absorber (14) that causes CO 2 included in flue gas (11A) to be absorbed into a CO 2 -absorbing solution (13); a CO 2 -regenerator (15) which regenerates the CO 2 -absorbing solution (13) by heating; and a CO 2 recovery amount control unit (111) which calculates a computed target value for the CO 2 recovery amount and a computed target value for the CO 2 recovery rate on the basis of a set value for the CO 2 recovery rate, actual measured values of the CO 2 concentration, gas flow rate, and temperature of the flue gas (11A), and maximum values for the CO 2 recovery amounts in the CO 2 -absorber (14) and the CO 2 -regenerator (15). On the basis of the set value for the CO 2 recovery rate or the computed target value for the CO 2 recovery rate, the CO 2 recovery amount control unit (111) controls: the amount of the CO 2 -absorbing solution (13) supplied to the CO 2 -absorber (14); the amount of the CO 2 -absorbing solution (13) supplied to the CO 2 -regenerator (15); and the amount of saturated steam (S) supplied to a regeneration heater (31) of the CO 2 -regenerator (15).

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