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    • 21. 发明申请
    • APPARATUS FOR LIQUID TREATMENT OF PULP
    • 液体处理装置
    • WO1987006281A1
    • 1987-10-22
    • PCT/SE1987000168
    • 1987-04-01
    • SUNDS DEFIBRATOR AKTIEBOLAGLINDSTRÖM, Alf, Inge
    • SUNDS DEFIBRATOR AKTIEBOLAG
    • D21C09/06
    • D21C9/06
    • The apparatus comprises an endless perforated steel belt (1). Devices (11) for the supply of treatment liquid are located above the belt, and containers (8) for the collection of liquid are located beneath the belt. Said containers (8) extend along the entire width of the belt (1). The containers (8) are provided with outlet (9) for liquid and outlet (10) for vapours and gases, which vapour outlet (10) is connected to the bottom of the containers (8). The vapour outlet (10) communicates with an internal passageway (21), which extends upwards to the upper portion of the containers (8) above a liquid level in the containers, and a screening is provided for preventing liquid to flow from the belt down into the vapour outlet (10).
    • 该设备包括环形穿孔钢带(1)。 用于供应处理液体的装置(11)位于皮带上方,用于收集液体的容器(8)位于皮带下方。 所述容器(8)沿着带(1)的整个宽度延伸。 容器(8)设置有用于蒸气和气体的液体和出口(10)的出口(9),该蒸汽出口(10)连接到容器(8)的底部。 蒸汽出口(10)与内部通道(21)连通,内部通道(21)向上延伸到容器(8)的上部,高于容器中的液面,并且提供了一种防止液体从带状物向下流动的筛选 进入蒸汽出口(10)。
    • 25. 发明申请
    • METHOD AND APPARATUS FOR MANUFACTURING FIBRE PULP
    • 制造纤维纸浆的方法和装置
    • WO1984003313A1
    • 1984-08-30
    • PCT/SE1984000053
    • 1984-02-14
    • SUNDS DEFIBRATOR AKTIEBOLAGREINHALL, Rolf, Bertil
    • SUNDS DEFIBRATOR AKTIEBOLAG
    • D21B01/12
    • D21D1/30
    • Fibre pulp is manufactured in a refiner with opposed refining members (22, 23, 24) rotary relative to each other and enclosed in a pressure-proof refiner housing (20). Steam is separated from the fibre pulp in the refiner housing (20) at the counter-effect of centrifugal forces generated by radial wing members (40) on a rotary refining member (23, 24). The steam is led off separately from the refiner housing (20) through a steam outlet (42), which communicates with a space (41) radially inside of the wing members (40). The fibre pulp is discharged separately through a discharge device (50, 60, 70, 80, 90) while in the refiner housing the desired pressure is maintained.
    • 纤维纸浆在具有相对于彼此旋转的相对的澄清构件(22,23,24)的精磨机中制造并且封闭在耐压精炼机壳体(20)中。 在旋转精炼部件(23,24)上由径向翼部件(40)产生的离心力的反作用力使蒸汽与磨浆机壳体(20)中的纤维纸浆分离。 蒸汽通过蒸汽出口(42)与磨浆机壳体(20)分开引出,蒸汽出口(42)与翼部件(40)的径向内侧的空间(41)连通。 纤维纸浆通过排出装置(50,60,70,80,90)分开排出,同时在磨浆机壳体中保持所需的压力。