VERFAHREN ZUM VERHINDERN VON STREUSTRÖMEN IN PERIPHEREN ANLAGENTEILEN IN EINER ELEKTROLYSE ZUM GEWINNEN VON METALLEN
    1.
    发明公开
    VERFAHREN ZUM VERHINDERN VON STREUSTRÖMEN IN PERIPHEREN ANLAGENTEILEN IN EINER ELEKTROLYSE ZUM GEWINNEN VON METALLEN 有权
    方法防止外围系统组件杂散电流IN A电解OBTAINING METALS

    公开(公告)号:EP1230439A1

    公开(公告)日:2002-08-14

    申请号:EP00941961.5

    申请日:2000-05-19

    申请人: Outokumpu Oyj

    IPC分类号: C25C7/06

    CPC分类号: C25C7/00 C25C1/00

    摘要: The electrolyte is guided from a reservoir (6) to an electrolysis area through at least one supply line (4). Said electrolysis area is provided with anodes and cathodes and at least one electrical direct voltage source. Used electrolyte is at least partially guided back from the electrolysis area to the reservoir through at least one discharge line (9). A bridge section of line (12) containing electrolyte exists between a first contact point (A) in the supply line electrolyte and a second contact point (B) in the discharge line electrolyte. The ohmic resistance (R1) of the electrolyte in the bridge section of line (12) between the first and second contact point is at most 10 % of the ohmic resistance (R2) that is present between the first and second contact points in the electrolyte flowing through the reservoir. The quantity of electrolyte that flows through the bridge section of line per unit of time is at most 5 % of the quantity of electrolyte flowing in the supply line in the area of the first contact point.

    PLATE-TYPE HEAT EXCHANGER WITH ANODIC CORROSION PROTECTION
    3.
    发明公开
    PLATE-TYPE HEAT EXCHANGER WITH ANODIC CORROSION PROTECTION 有权
    与阳极KORROSIONSSCHUTZ板式换热器

    公开(公告)号:EP1395788A1

    公开(公告)日:2004-03-10

    申请号:EP02743118.8

    申请日:2002-05-28

    申请人: Outokumpu Oyj

    IPC分类号: F28F19/00 C23F13/00

    CPC分类号: F28F19/004 C23F13/005

    摘要: To protect a plate-type heat exchanger (1) against corrosion due to the attack of sulfuric acid, it is proposed in accordance with the invention that the region through which flows sulfuric acid has at least one metal cathode (16, 17) and one reference electrode (27), that at least half the metal plates (7) have an electric contact (23) which is connected with the anode (21) of an electric d.c. voltage source of variable electric voltage, that the metal cathode (16, 17) likewise is electrically connected with the d.c. voltage source, and that the d.c. voltage source belongs to a potentiostat (20) which is electrically connected with the reference electrode (27).

    PLATE-TYPE HEAT EXCHANGER WITH ANODIC CORROSION PROTECTION
    6.
    发明授权
    PLATE-TYPE HEAT EXCHANGER WITH ANODIC CORROSION PROTECTION 有权
    与阳极KORROSIONSSCHUTZ板式换热器

    公开(公告)号:EP1395788B1

    公开(公告)日:2005-12-14

    申请号:EP02743118.8

    申请日:2002-05-28

    申请人: Outokumpu Oyj

    IPC分类号: F28F19/00 C23F13/00

    CPC分类号: F28F19/004 C23F13/005

    摘要: To protect a plate-type heat exchanger (1) against corrosion due to the attack of sulfuric acid, it is proposed in accordance with the invention that the region through which flows sulfuric acid has at least one metal cathode (16, 17) and one reference electrode (27), that at least half the metal plates (7) have an electric contact (23) which is connected with the anode (21) of an electric d.c. voltage source of variable electric voltage, that the metal cathode (16, 17) likewise is electrically connected with the d.c. voltage source, and that the d.c. voltage source belongs to a potentiostat (20) which is electrically connected with the reference electrode (27).

    VERFAHREN ZUM VERHINDERN VON STREUSTRÖMEN IN PERIPHEREN ANLAGENTEILEN IN EINER ELEKTROLYSE ZUM GEWINNEN VON METALLEN
    7.
    发明授权
    VERFAHREN ZUM VERHINDERN VON STREUSTRÖMEN IN PERIPHEREN ANLAGENTEILEN IN EINER ELEKTROLYSE ZUM GEWINNEN VON METALLEN 有权
    方法防止外围系统组件杂散电流IN A电解OBTAINING METALS

    公开(公告)号:EP1230439B1

    公开(公告)日:2003-07-16

    申请号:EP00941961.5

    申请日:2000-05-19

    申请人: Outokumpu Oyj

    IPC分类号: C25C7/06

    CPC分类号: C25C7/00 C25C1/00

    摘要: The electrolyte is guided from a reservoir (6) to an electrolysis area through at least one supply line (4). Said electrolysis area is provided with anodes and cathodes and at least one electrical direct voltage source. Used electrolyte is at least partially guided back from the electrolysis area to the reservoir through at least one discharge line (9). A bridge section of line (12) containing electrolyte exists between a first contact point (A) in the supply line electrolyte and a second contact point (B) in the discharge line electrolyte. The ohmic resistance (R1) of the electrolyte in the bridge section of line (12) between the first and second contact point is at most 10 % of the ohmic resistance (R2) that is present between the first and second contact points in the electrolyte flowing through the reservoir. The quantity of electrolyte that flows through the bridge section of line per unit of time is at most 5 % of the quantity of electrolyte flowing in the supply line in the area of the first contact point.