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    • 2. 发明申请
    • REFINING ELEMENT
    • 精炼元素
    • WO1997023291A1
    • 1997-07-03
    • PCT/SE1996001594
    • 1996-12-04
    • SUNDS DEFIBRATOR INDUSTRIES ABVIRVING, NilsBERGQUIST, PeterHAWÉN, Anders
    • SUNDS DEFIBRATOR INDUSTRIES AB
    • B02C07/12
    • D21D1/306B02C2/10B02C7/12D21D1/22
    • Refining element intended for a refiner with flat or conical opposed refining surfaces, which are rotary relative to each other for working and refining lignocellulosic material during its passage through a refiner gap (15, 35) between the opposed refining surfaces from an inlet portion with smaller diameter to an outlet portion with greater diameter. The refining element (19, 39) is formed with a refining surface with bars (20) and intermediate grooves (21) which extend over the entire refining element. The bars (20) in the inlet portion of the refining element (19) form an angle of 50-85 DEG with the radius or generatrix of the refining surface. The angle decreases along the surface of the refining element (19, 39) so that the bars (20) in the outlet portion form an angle between -25 DEG and +25 DEG with the radius or generatrix. The bars (20) in the inlet portion are located at a greater mutual distance than in the outlet portion.
    • 用于具有平坦或圆锥形相对的精炼表面的精炼元件,其相对于彼此旋转,用于在木质纤维素材料通过相对的精炼表面之间的精炼机间隙(15,35)期间从具有较小的入口部分 直径到具有更大直径的出口部分。 精制元件(19,39)形成有具有在整个精炼元件上延伸的杆(20)和中间槽(21)的精磨表面。 精炼元件(19)的入口部分中的杆(20)与精磨表面的半径或母线形成50-85°的角度。 角度沿着精磨元件(19,39)的表面减小,使得出口部分中的杆(20)与半径或母线形成-25度和+25度之间的角度。 入口部分中的杆(20)位于比出口部分更大的相互距离处。
    • 4. 发明申请
    • METHOD OF PURIFYING WASTE WATER
    • 净化废水的方法
    • WO1995012549A1
    • 1995-05-11
    • PCT/SE1994000990
    • 1994-10-20
    • SUNDS DEFIBRATOR INDUSTRIES ABSÄFSTRÖM, ChristerLUNDGREN, Göran
    • SUNDS DEFIBRATOR INDUSTRIES AB
    • C02F01/10
    • D21F1/66B01D5/0054C02F1/10
    • A method of purifying and recovering waste water from a fiberboard manufacturing process. The waste water is supplied to an evaporator (11), in which steam from a steam generator (12) is used as heating medium for evaporating the waste water and concentrating impurities. These impurities are thereafter separated mechanically from the evaporator (11). The steam generated in the evaporator (11) is used in a steam converter (14) for restoring the heating medium used in the evaporator (11) from condensate to steam phase. The condensate formed in the steam converter (14) is purified from solved substances in a purifying unit (15). The condensate thus purified is used as feed water in the steam generator (12), from which steam is supplied to the evaporator (11).
    • 从纤维板制造工艺中净化和回收废水的方法。 将废水供应到蒸发器(11),其中来自蒸汽发生器(12)的蒸汽用作用于蒸发废水和浓缩杂质的加热介质。 然后这些杂质与蒸发器(11)机械分离。 在蒸发器(11)中产生的蒸汽用于蒸汽转化器(14),用于将蒸发器(11)中使用的加热介质从冷凝水恢复到蒸汽相。 在蒸汽转化器(14)中形成的冷凝物从纯化单元(15)中的溶解物质中纯化。 如此净化的冷凝物被用作蒸汽发生器(12)中的给水,从蒸汽发生器(12)向蒸发器(11)供应蒸汽。
    • 9. 发明申请
    • A METHOD OF SEPARATING METAL IONS FROM PULP
    • 从PULP分离金属离子的方法
    • WO1995012710A1
    • 1995-05-11
    • PCT/SE1994000930
    • 1994-10-06
    • SUNDS DEFIBRATOR INDUSTRIES ABGERMGÅRD, Ulf
    • SUNDS DEFIBRATOR INDUSTRIES AB
    • D21C09/10
    • D21C9/1042D21C9/1005
    • A method of separating metal ions from pulp of lignocellulose-containing material. A main flow (1) of the pulp is treated with chelating agent (12) and washed (3) prior to the bleaching (5) of the pulp with hydroperoxide or ozone. Process water (4) washed out at the washing (3) and containing metal ions is mixed with pulp, which is not lateron to be bleached with hydroperoxide or ozone at pH above 7, whereby the metal ions substantially are bound to this pulp. Thereafter a liquid phase (9, 17) substantially free of metal ions is washed out of this pulp. Thereafter pH in this pulp is lowered to below 3 whereby the main part of the metal ions is released from the pulp and washed out.
    • 从含木素纤维素材料的纸浆中分离金属离子的方法。 纸浆的主流(1)用螯合剂(12)处理,并在用过氧化氢或臭氧漂洗(5)纸浆之前洗涤(3)。 将洗涤剂(3)洗涤并含有金属离子的处理水(4)与pH值高于7的氢过氧化物或臭氧漂白的纸浆混合,由此金属离子基本上与该纸浆结合。 此后,从该纸浆中洗出基本上不含金属离子的液相(9,17)。 此后,该纸浆中的pH降低至3以下,由此金属离子的主要部分从纸浆中释放出来并被洗掉。