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    • 2. 发明授权
    • Method for heating pulps
    • 纸浆加热方法
    • US06491787B2
    • 2002-12-10
    • US09509474
    • 2000-03-28
    • Kari PeltonenReijo VesalaVesa Vikman
    • Kari PeltonenReijo VesalaVesa Vikman
    • D21C102
    • D21C9/007D21C9/10
    • A method and apparatus for heating cellulose pulp with steam are provided. Low-pressure (e.g. 3-5 bar (abs.)) steam is supplied into the pulp flowing as a plug flow in such a way that in the flow direction of the pulp, before supplying the low-pressure steam, the pulp is pressurized so that the pulp pressure at the point of the steam introduction is lower than the pressure of the available steam. After the steam is introduced the pulp is mixed with a pressure-raising mixer (such as a fluidizing centrifugal pump) to divide the steam evenly into the pulp and/or to equalize the temperature of the pulp.
    • 提供了一种用蒸汽加热纤维素纸浆的方法和装置。 将低压(例如3-5巴(绝对))蒸汽供应到作为塞子流动的纸浆中,使得在纸浆的流动方向上,在供给低压蒸汽之前,将纸浆加压 使得蒸汽引入点处的纸浆压力低于可用蒸汽的压力。 在引入蒸汽之后,将纸浆与升压混合器(例如流化离心泵)混合以将蒸汽均匀地分配到纸浆中和/或使纸浆的温度相等。
    • 3. 发明授权
    • Method and apparatus for mixing gaseous chemical to fiber suspension
    • 将气态化学品与纤维悬浮液混合的方法和设备
    • US5791778A
    • 1998-08-11
    • US767524
    • 1996-12-16
    • Matti ManninenKari PeltonenReijo Vesala
    • Matti ManninenKari PeltonenReijo Vesala
    • D21C9/153B01F3/04B01F7/00B01F7/04D21C9/10B01F5/04
    • D21C9/153B01F3/0446B01F7/0075B01F7/048D21C9/10B01F2003/04886B01F2003/0495
    • A method and apparatus allow large volumes of gas (at least about 10% by volume) to be mixed into a cellulosic fiber suspension having a consistency of about 8-25%. The mixing of ozone containing gas into the suspension is particularly desirable. The suspension is passed into the inlet of a mixer, gas is introduced into the mixer, and the gas and fiber suspension are homogenized by fluidizing the gas and suspension. The flow of suspension through the mixer is throttled so that the effect of the fluctuation and pressure between the inlet and outlet is minimized, and the homogeneously mixed gas and fiber suspension mixture is discharged from mixer outlet. The mixer may have a premixing zone in which the gas and suspension are fluidized to the floc level and the gas is evenly distributed throughout the suspension, then a homogenization zone in which the fiber suspension is fluidized to fiber or microfloc level and the gas is brought into contact with each fiber or microfloc, and then a maintenance zone in which the fluidization level is maintained high enough to prevent the generation of gas bubbles and the separation of gas from the suspension.
    • 一种方法和装置允许将大体积的气体(至少约10体积%)混合到具有约8-25%的稠度的纤维素纤维悬浮液中。 将含臭氧气体混入悬浮液是特别理想的。 将悬浮液送入混合器的入口,将气体引入混合器中,并通过使气体和悬浮液流化使气体和纤维悬浮液均化。 通过混合器的悬浮液的流动被节流,使得入口和出口之间的波动和压力的影响最小化,并且均匀混合的气体和纤维悬浮液混合物从混合器出口排出。 混合器可以具有预混合区域,其中气体和悬浮液被流化到絮状物水平并且气体均匀分布在整个悬浮液中,然后是均匀化区域,其中纤维悬浮液被流化为纤维或微环境水平并且气体被带入 与每个纤维或微团接触,然后是维持区,其中流化水平保持足够高以防止产生气泡和气体与悬浮液分离。
    • 5. 发明申请
    • APPARATUS FOR DISTRIBUTING A PULP FLOW
    • 用于分配纸浆流量的装置
    • US20090071619A1
    • 2009-03-19
    • US11912260
    • 2006-04-21
    • Kari PeltonenJanne Vehmaa
    • Kari PeltonenJanne Vehmaa
    • D21F1/06
    • D21F1/06
    • An apparatus for distributing a pulp flow, said apparatus including: a valve body connected to an inlet conduit and an outlet conduit for the pulp flow and provided with a closing member for opening and closing the valve to regulate the pulp flow; a distribution member arranged in a direction the pulp flow and downstream of the closing member, said distribution member distributing the pulp flow into at least two partial flows, and at least two channels wherein each channel receives a respective one of the two partial flows, wherein said channels are connected to the valve body or to the outlet conduit from the valve.
    • 一种用于分配纸浆流的装置,所述装置包括:连接到入口管道的阀体和用于纸浆流的出口管道,并且设置有用于打开和关闭阀门以调节纸浆流量的关闭构件; 分配构件,其布置在纸浆流动方向和封闭构件的下游,所述分配构件将纸浆流分配到至少两个部分流中,以及至少两个通道,其中每个通道接收两个部分流中的相应一个,其中 所述通道从阀门连接到阀体或出口导管。
    • 6. 发明授权
    • Method and apparatus for separating gas from a gaseous material
    • 从气态物质中分离气体的方法和装置
    • US6071331A
    • 2000-06-06
    • US456699
    • 1995-06-01
    • Toivo NiskanenKari Peltonen
    • Toivo NiskanenKari Peltonen
    • B01D19/00D21C7/08D21D5/26
    • D21C7/08B01D19/0052D21D5/26
    • Gas is separated from fluent material, particularly a liquid or a cellulose fiber suspension having a consistency of about 8-18%, utilizing a closed separation apparatus having a spiral housing with a central axis, a fluent material inlet channel, a fluent material outlet, and a gas outlet. A pressure differential is maintained between the inlet channel and the spiral housing, and the pressure differential is converted to kinetic energy of the fluent material by causing the fluent material to flow through one or more spiral flow paths through the inlet channel toward the spiral housing. In the spiral housing a rotor is rotated to impart a strong centrifugal force to the fluent material to cause gas to separate and collect adjacent the central axis of the spiral housing, from which the gas is removed. The strong centrifugal force caused by the rotating rotor discharges the fluent material through the outlet. The spiral flow paths rotate with the rotor in the spiral housing.
    • 气体与流动材料特别是具有约8-18%稠度的液体或纤维素纤维悬浮液分离,利用具有中心轴线的螺旋壳体的密闭分离装置,流动材料入口通道,流体物质出口, 和气体出口。 在入口通道和螺旋壳体之间保持压差,并且通过使流动材料流过穿过入口通道的一个或多个螺旋流动路径朝向螺旋壳体,将压差转换成流动材料的动能。 在螺旋壳体中,旋转转子以向流动材料施加强大的离心力,以使气体在螺旋壳体的中心轴线附近分离和收集,气体从该外壳中除去。 旋转转子产生的强力离心力通过出口排出流体物质。 螺旋流动路径随着转子旋转在螺旋壳体中。
    • 7. 发明申请
    • APPARATUS FOR MIXING A SUBSTANCE INTO A MEDIUM
    • 将物质与中等浓度混合的装置
    • US20130199746A1
    • 2013-08-08
    • US13577204
    • 2011-02-04
    • Kari PeltonenArto LaukkanenTimo PerttulaJanne Vehmaa
    • Kari PeltonenArto LaukkanenTimo PerttulaJanne Vehmaa
    • D21F1/00
    • D21F1/00B01F5/0451B01F5/0463B01F5/0646B01F5/0652B01F5/0682B01F5/0688B01F15/0201B01F15/0261
    • The invention relates to an apparatus for mixing a gaseous or liquid substance into fiber suspension. The apparatus includes a tubular body, which defines a space that forms a flow channel for the suspension, in which body an inlet and an outlet for the suspension are arranged so that the suspension flows through the flow channel mainly in the axial direction. Further the apparatus comprises a feed member that extends into the flow channel transversely against the flow direction of the suspension and has a cylindrical wall provided with openings for leading the substance from the feed member into the flow channel. At least one protrusion is arranged on the inner surface of the tubular body in the region the feed member. A throttling member is arranged in the flow channel downstream of the feed member in the flow direction of the suspension, and a mixing chamber is formed in the flow channel between the feed member and the throttling member.
    • 本发明涉及一种用于将气态或液态物质混合成纤维悬浮液的装置。 该装置包括管状体,其限定形成用于悬架的流动通道的空间,其中主体布置有用于悬架的入口和出口,使得悬架主要沿轴向流过流动通道。 此外,该装置包括进料构件,其横向于悬挂液流动方向延伸到流动通道中,并且具有设置有用于将物质从进料构件引导到流动通道中的开口的圆柱形壁。 在进给构件的区域中,至少一个突出部布置在管状体的内表面上。 节流部件沿着悬架的流动方向布置在进料构件下游的流动通道中,并且在进料构件和节流构件之间的流动通道中形成混合室。
    • 8. 发明授权
    • Method and apparatus for mixing a first medium to a second medium and a
bleaching process applying said method
    • 用于将第一介质混合到第二介质的方法和装置以及应用所述方法的漂白方法
    • US5536368A
    • 1996-07-16
    • US211793
    • 1994-05-02
    • Mika P. MakelaToivo NiskanenKari Peltonen
    • Mika P. MakelaToivo NiskanenKari Peltonen
    • B01F3/04B01F7/00D21C9/10D21C9/153
    • B01F7/008B01F3/04468B01F3/04531D21C9/10D21C9/153B01F2003/04709
    • The present invention relates to a mixing of gas into a medium. The method and apparatus in accordance with the present invention are especially applicable in the bleaching plants of the wood processing industry for mixing gaseous bleaching chemicals into pulp and to bleaching process of pulp, in which the mixing method and apparatus in accordance with the present invention are applied. An excellent application is mixing ozone-containing gas into a fiber suspension flowing in a pipe line and an ozone bleaching process. The previously known methods and apparatuses have not been able to mix satisfactorily large volumes of gas, about 50% of the total volume of the flow, into the medium flow. In the method in accordance with the present invention the mixing is carried out in a strong shear force field efficiently and uniformly, whereafter the fiber network of the medium is allowed to form rapidly and in a controlled manner so that gas is not allowed to separate in the flow as bubbles, but remains in the plug flow in the fiber network.
    • PCT No.PCT / FI92 / 00276 Sec。 371日期:1994年5月2日 102(e)日期1994年5月2日PCT提交1992年10月16日PCT公布。 公开号WO93 / 07961 日期:1993年04月29日。本发明涉及将气体混合到介质中。 根据本发明的方法和装置特别适用于木材加工工业用于将气体漂白化学品混入纸浆中的漂白设备和纸浆漂白工艺,其中根据本发明的混合方法和设备是 应用。 将含臭氧的气体混合到在管线中流动的纤维悬浮液和臭氧漂白过程中的一个很好的应用。 以前已知的方法和装置不能将令人满意的大体积的气体(流体的总体积的约50%)混合到介质流中。 在根据本发明的方法中,混合在有力和均匀的强剪切力场中进行,之后允许介质的纤维网络以受控的方式快速形成,使得不允许气体分离 流动作为气泡,但保留在光纤网络中的插头流中。
    • 9. 发明授权
    • Method and apparatus for separating gas from a gaseous material
    • 从气态物质中分离气体的方法和装置
    • US5462585A
    • 1995-10-31
    • US182036
    • 1994-01-14
    • Toivo NiskanenKari Peltonen
    • Toivo NiskanenKari Peltonen
    • B01D19/00D21C7/08D21D5/26
    • D21C7/08B01D19/0052D21D5/26
    • Gas is separated from fluent material, particularly a liquid or a cellulose fiber suspension having a consistency of about 8-18%, utilizing a closed separation apparatus having a spiral housing with a central axis, a fluent material inlet channel, a fluent material outlet, and a gas outlet. A pressure differential is maintained between the inlet channel and the spiral housing, and the pressure differential is converted to kinetic energy of the fluent material by causing the fluent material to flow through one or more spiral flow paths through the inlet channel toward the spiral housing. In the spiral housing a rotor is rotated to impart a strong centrifugal force to the fluent material to cause gas to separate and collect adjacent the central axis of the spiral housing, from which the gas is removed. The strong centrifugal force caused by the rotating rotor discharges the fluent material through the outlet. The spiral flow paths may be stationary or may rotate with the rotor in the spiral housing.
    • PCT No.PCT / FI92 / 00216 Sec。 371日期1994年1月14日 102(e)日期1994年1月14日PCT提交1992年7月15日PCT公布。 公开号WO93 / 01875 日期:1993年2月4日。使用具有中心轴的螺旋壳体的封闭分离装置,流动材料入口(流体材料入口),流体材料,特别是具有约8-18%稠度的液体或纤维素纤维悬浮液 通道,流畅的材料出口和气体出口。 在入口通道和螺旋壳体之间保持压差,并且通过使流动材料流过穿过入口通道的一个或多个螺旋流动路径朝向螺旋壳体,压差被转换成流动材料的动能。 在螺旋壳体中,旋转转子以向流动材料施加强大的离心力,以使气体在螺旋壳体的中心轴线附近分离和收集,气体从该外壳中除去。 旋转转子产生的强力离心力通过出口排出流体物质。 螺旋流动路径可以是静止的或者可以随着转子旋转在螺旋壳体中。
    • 10. 发明授权
    • Apparatus for mixing a substance into a medium
    • 用于将物质混合到介质中的装置
    • US08721840B2
    • 2014-05-13
    • US13577204
    • 2011-02-04
    • Kari PeltonenArto LaukkanenTimo PerttulaJanne Vehmaa
    • Kari PeltonenArto LaukkanenTimo PerttulaJanne Vehmaa
    • D21F1/00
    • D21F1/00B01F5/0451B01F5/0463B01F5/0646B01F5/0652B01F5/0682B01F5/0688B01F15/0201B01F15/0261
    • The invention relates to an apparatus for mixing a gaseous or liquid substance into fiber suspension. The apparatus includes a tubular body, which defines a space that forms a flow channel for the suspension, in which body an inlet and an outlet for the suspension are arranged so that the suspension flows through the flow channel mainly in the axial direction. Further the apparatus comprises a feed member that extends into the flow channel transversely against the flow direction of the suspension and has a cylindrical wall provided with openings for leading the substance from the feed member into the flow channel. At least one protrusion is arranged on the inner surface of the tubular body in the region the feed member. A throttling member is arranged in the flow channel downstream of the feed member in the flow direction of the suspension, and a mixing chamber is formed in the flow channel between the feed member and the throttling member.
    • 本发明涉及一种用于将气态或液态物质混合成纤维悬浮液的装置。 该装置包括管状体,其限定形成用于悬架的流动通道的空间,其中主体布置有用于悬架的入口和出口,使得悬架主要沿轴向流过流动通道。 此外,该装置包括进料构件,其横向于悬挂液流动方向延伸到流动通道中,并且具有设置有用于将物质从进料构件引导到流动通道中的开口的圆柱形壁。 在进给构件的区域中,至少一个突出部布置在管状体的内表面上。 节流部件沿着悬架的流动方向布置在进料构件下游的流动通道中,并且在进料构件和节流构件之间的流动通道中形成混合室。