会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明授权
    • Method and apparatus for pulping with controlled heating to improve
delignification and pulp strength
    • 用控制加热制浆以提高脱木质素和纸浆强度的方法和装置
    • US5736006A
    • 1998-04-07
    • US729022
    • 1996-10-10
    • J. Robert Prough
    • J. Robert Prough
    • D21C3/00D21C1/02D21C3/02D21C3/22D21C7/06D21C1/10
    • D21C1/02D21C3/22
    • Low temperature steaming and slurrying of wood chips results in significant improvement in treatment, the chips being maintained at a temperature below 110.degree. C. (more desirably at about 105.degree. C. or less, and most desirably at about 100.degree. C. or less) until actually heated to cooking temperature. Steaming may be accomplished utilizing a vertical chip bin with one dimensional convergence and side relief or a horizontal steaming vessel, the steaming device connected to a high pressure feeder. A pump having an NPSHR less than the NPSHA may be used for drawing slurry into the high pressure feeder from the steaming device, or a pump may be disposed between the steaming device and the high pressure feeder for forcing slurry into the high pressure feeder through a conduit including a radiused elbow. The steaming is practiced at a pressure of 5 psig or less, preferably substantially atmospheric steaming is practiced. The pulp produced typically has strength properties at least about 10% greater than the pulp produced from material where it is steamed and slurried at temperatures in excess of 110.degree. C.
    • 木片的低温蒸煮和浆料化处理显着改善,芯片保持在110℃以下(更优选约105℃或更低,最优选约100℃或更低) )直到实际加热到烹调温度。 蒸汽可以利用具有一维会聚和侧面浮雕的垂直切屑仓或水平蒸汽容器来实现,蒸汽装置连接到高压进料器。 具有小于NPSHA的NPSHR的泵可以用于从蒸汽装置将浆料引入高压进料器中,或者可以在蒸汽装置和高压进料器之间设置泵,以将浆料通过一个 导管包括一个圆角的弯头。 蒸汽在5psig或更低的压力下实施,优选基本上是大气蒸汽。 生产的纸浆通常具有的强度特性比从其蒸出并在超过110℃的温度下制浆的材料产生的纸浆大至少约10%。
    • 3. 发明授权
    • Chip pumping to a digester
    • 芯片泵送到消化器
    • US5622598A
    • 1997-04-22
    • US428302
    • 1995-04-25
    • J. Robert Prough
    • J. Robert Prough
    • D21C7/06D21C7/08
    • D21C7/06
    • A system for feeding wood chips entrained in cooking liquor to a high pressure feeder connected to a continuous digester includes a vertical treatment (e.g. steaming) vessel, a metering device connected to the discharge from the steaming vessel, a generally vertical chip chute extending downwardly from the metering device, and a slurry pump having an inlet. The slurry pump pumps the slurry from an outlet thereof to a high pressure feeder low pressure inlet. In order to minimize the effect of changes in liquid volume upon the operation of the system, and to provide separate control of liquor volume and chip volume, a substantially vertical liquor tank having a top and bottom the bottom including a discharge opening above the slurry pump inlet is provided. A conduit directly connects the liquor tank discharge opening with the slurry pump inlet. A pressure isolating device may be used in the system if it is to operate at superatmospheric pressure rather than atmospheric pressure.
    • 用于将夹带在蒸煮液中的木片喂入连接到连续蒸煮器的高压进料器的系统包括垂直处理(例如蒸汽)容器,连接到来自蒸煮容器的排出口的计量装置, 计量装置和具有入口的浆料泵。 浆料泵将浆料从出口泵送到高压进料器低压入口。 为了最小化液体体积变化对系统操作的影响,并且提供对液体体积和碎屑体积的单独控制,具有顶部和底部底部的基本上垂直的液体容器包括在浆料泵上方的排出口 提供入口。 导管将液罐排放口与浆料泵入口直接连接。 如果要在超大气压力而不是大气压下运行,则可以在系统中使用压力隔离装置。
    • 4. 发明授权
    • Method of controlling pressurized ozone to a pulp delignification reactor
    • 将加压臭氧控制到纸浆脱木质反应器的方法
    • US5567274A
    • 1996-10-22
    • US275392
    • 1994-07-15
    • Erwin D. FunkKaj HenricsonStephen J. Dunn
    • Erwin D. FunkKaj HenricsonStephen J. Dunn
    • B01J4/00D21C9/10D21C9/153D21C7/12
    • D21C9/153D21C9/1026
    • A method and apparatus supply ozone containing gas under superatmospheric pressure to an ozone delignification device. The speed of a water ring compressor is controlled so that it compresses as much ozone gas per unit time at desired superatmospheric pressure as the ozone delignification unit utilizes, with essentially no excess. The ozone containing gas is fed from the water ring compressor through a separator buffer tank which levels out pressure pulses and separates cooling water from compressed ozone gas prior to the gas entering the ozone delignification unit. The gas passes through a control valve controlled by a mass flowmeter which senses the amount of cellulose pulp fed to the ozone delignification unit. The speed control of the compressor may be provided by a differential pressure controller connected across the control valve.
    • 一种在超大气压下向臭氧脱木质装置供给含臭氧气体的方法和装置。 控制水环式压缩机的速度,使得它以按照臭氧脱木质装置利用的基本上没有过量的压力,按照期望的超大气压力压缩单位时间内的臭氧气体。 含臭氧气体从水环压缩机通过分离器缓冲罐供给,分离器缓冲罐排出压力脉冲,并在气体进入臭氧脱木素装置之前将冷却水与压缩的臭氧气体分离。 气体通过由质量流​​量计控制的控制阀,该质量流量计感测供给到臭氧脱木质单元的纤维素纸浆的量。 压缩机的速度控制可以由连接在控制阀上的差压控制器提供。
    • 5. 发明授权
    • Two stage pressure diffuser
    • 两级压力扩散器
    • US5567262A
    • 1996-10-22
    • US685400
    • 1991-04-16
    • Joseph PhillipsJohn Weston
    • Joseph PhillipsJohn Weston
    • D21C9/02D21C7/00D21C9/04D21D1/40
    • D21D1/40D21C7/00D21C9/04
    • A multi-stage pressure diffuser is provided for treating paper pulp or similar comminuted cellulosic fibrous material. Two different subvolumes are defined within the annular screen of the pressure diffuser by a tubular baffle hung from adjacent the top of the vessel, and a transverse wall near the middle of the vessel. Wash liquid is introduced into the top stage, extracted liquid passes through the bottom of the baffle, and is removed through a liquid outlet at the top of the vessel. That removed liquid is then reintroduced into the bottom stage as wash liquid, and the extracted liquid from the bottom stage is discharged from the vessel at the bottom. The screen assembly may be blanked at the area of the transverse wall dividing the subvolumes from each other, in order to minimize the possibility of mixing of the extraction flows in the different stages.
    • 提供了用于处理纸浆或类似粉碎的纤维素纤维材料的多级压力扩散器。 两个不同的子体积通过从容器的顶部悬挂的管状挡板和靠近容器中部的横向壁限定在压力扩散器的环形屏幕内。 洗涤液体被引入顶部,提取液体通过挡板的底部,并通过容器顶部的液体出口去除。 然后将去除的液体作为洗涤液重新引入底部,并且从底部的提取液体从底部的容器排出。 屏幕组件可以在分隔子体积的横壁的区域处被冲切,以便最小化在不同阶段中的提取流的混合的可能性。
    • 6. 发明授权
    • Chip bin with steaming control and a gas vent containing a vacuum and
pressure relief device
    • 具有蒸汽控制的切屑仓和包含真空和压力释放装置的排气口
    • US5547546A
    • 1996-08-20
    • US317801
    • 1994-10-04
    • J. Robert ProughJoseph R. Phillips
    • J. Robert ProughJoseph R. Phillips
    • D21B1/02D21C7/06D21C7/12
    • D21C7/12D21B1/021D21C7/06
    • A chip bin for wood chips in a continuous digester system includes internal steaming that is controlled in response to both the interior temperature across the level of chips in the bin, and the level of chips in the bin, so as to substantially prevent cool, non-condensible gas-laden chips from accumulating at the top of the chip column in the bin, and to substantially prevent steam blow-through. The temperature probe used in the chip bin has a temperature sensing portion with a length of about ten to twenty feet instead of the conventional five foot length, and extends across the level of the chips to a position about five feet below the level of chips. Control of steam added to the bin is provided utilizing a controller which controls the position of one or more valves in one or more steam conduits, each valve having multiple open positions and a closed position. A vacuum and pressure relief device is disposed in a non-condensible gases vent from the bin which minimizes the potential for gross gas flow variations across it. The relief device includes a solid interior peripheral portion of the vent, a gate mounted for pivotal movement by a pivot shaft, and a casing which is a cylindrical sector (having a sector angle of about 30.degree.-60.degree.) in which the gate pivots. The casing is mounted in the solid interior peripheral portion and a brush seal is provided between the gate and the cylindrical sector casing.
    • 用于连续蒸煮器系统中的木片的碎片箱包括内部蒸汽,其响应于箱中的切屑水平的内部温度以及料仓中的切屑水平而被控制,以便基本上防止冷却, 可靠的气体填充芯片积聚在料斗中的芯片柱的顶部,并且基本上防止蒸汽吹过。 在芯片仓中使用的温度探测器具有温度感测部分,其长度大约为十到二十英尺,而不是传统的五英尺长度,并且延伸跨越芯片的水平到比芯片级别大约五英尺的位置。 通过控制一个或多个蒸汽导管中的一个或多个阀的位置,每个阀具有多个打开位置和关闭位置的控制器来提供加到箱中的蒸汽的控制。 真空和压力释放装置设置在不可冷凝的气体排放口中,从而最小化跨越其的总气体流量变化的可能性。 排气装置包括通气口的实心内周部分,安装用于通过枢轴枢转运动的门和作为门枢转的圆柱形部分(具有约30°-60°的扇形角)的壳体 。 壳体安装在实心内周部分中,并且在门和圆柱形扇形外壳之间设置有刷密封件。
    • 10. 发明授权
    • Method of controlling the pressure of a continuous digester using an
extraction-dilution
    • 使用萃取 - 稀释法控制连续蒸煮器的压力的方法
    • US5824188A
    • 1998-10-20
    • US712977
    • 1996-09-12
    • J. Robert ProughBruno S. MarcocciaRichard O. LaaksoCarl L. Luhrmann
    • J. Robert ProughBruno S. MarcocciaRichard O. LaaksoCarl L. Luhrmann
    • D21C3/02D21C3/22D21C3/24D21C7/00D21C7/12D21C7/14D21C9/02D21C11/00D21C11/04
    • D21C3/224D21C11/0021D21C11/04D21C3/02D21C3/24D21C7/00D21C7/12D21C7/14D21C9/02
    • The sulfide ion concentration and sulfidity of kraft cooking liquor during kraft cooking of cellulose pulp is selectively increased. After treatment in a first treatment zone in which impregnation or kraft cooking takes place using a kraft cooking liquor having a first sulfide ion concentration and sulfidity, black liquor is extracted from the material, liquid is withdrawn from the material and dilution liquid is added to the withdrawn liquid and the withdrawn liquid with dilution liquid is reintroduced. In a second treatment zone after the first zone a second kraft cooking liquor is introduced having a second sulfide ion concentration and sulfidity greater than the first sulfide ion concentration and sulfidity (typically by about 20-50%), including by manipulating controlling the flow rate of extraction and the flow rates of withdrawal of liquid and addition of dilution liquid. The pressure of the continuous digester is controlled in a unique manner that avoids disruptions to the column of pulp continuously moving downwardly in the digester, anywhere in the digester, but particularly avoids non-uniform, unstable material in the countercurrent washing zone. The pressure is controlled by withdrawing liquid from, and introducing liquor into, the digester at at least one additional extraction-dilution loop aside from the main extraction of the digester and the wash dilution liquid introduction mechanism below the wash screens. Pressure can also be maintained (e.g. at about 130-170 psi) by also controlling the amount of wash dilution liquor, and by varying the extraction flow.
    • 纤维素纸浆硫酸盐蒸煮时硫酸盐蒸煮液的硫化物离子浓度和硫化物有选择地增加。 在使用具有第一硫化物离子浓度和硫化物的硫酸盐蒸煮液进行浸渍或硫酸盐蒸煮的第一处理区域中处理之后,从该材料中提取黑液,从该物质中取出液体并将稀释液加入到 取出的液体和用稀释液体排出的液体被重新引入。 在第一区域之后的第二处理区域中,引入第二硫酸盐蒸煮液,其具有大于第一硫化物离子浓度和硫化物浓度的硫化物的第二硫离子浓度和硫化物(通常为约20-50%),包括通过控制流速 的提取液和液体的提取流量以及稀释液的添加量。 以独特的方式控制连续蒸煮器的压力,避免在蒸煮器中的任何地方在蒸煮器中连续向下移动的纸浆柱的中断,但是特别地避免了逆流洗涤区域中不均匀的不稳定的材料。 除了从洗涤屏幕下面的蒸煮器和洗涤稀释液引入机构的主要提取之外,在至少一个额外的提取 - 稀释回路中,从蒸煮器中抽出液体并将其引入到蒸煮器中来控制压力。 还可以通过控制洗涤稀释液的量以及通过改变提取流量来保持压力(例如约130-170psi)。