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    • 1. 发明授权
    • Method for pulping sawdust
    • 制浆锯屑的方法
    • US06325888B1
    • 2001-12-04
    • US08520941
    • 1995-08-31
    • Jay J. MieleMarco MaroisR. Fred ChasseJ. Wayne ChambleeJohn D. WestonJ. Robert Prough
    • Jay J. MieleMarco MaroisR. Fred ChasseJ. Wayne ChambleeJohn D. WestonJ. Robert Prough
    • D21C102
    • Chemical cellulose pulp is made from sawdust utilizing a static down-flow retention vessel. By adding steam and cooking liquor to a flow of sawdust a heated slurry, at a cooking temperature of about 250-350° F., is produced. The heated slurry is, at superatmospheric pressure, moved downwardly in the static down-flow retention vessel while cooking temperature is maintained, for a time period of about 0.5-6 (preferably 1 to 3) hours, the slurry having a consistency of about 5-30%. At superatmospheric pressure, without significant reduction in pressure from the retention vessel, the slurry is cooled to well below cooking temperature by diffusing cooling liquid through it, as in a conventional pressure diffuser. The discharge from the retention vessel is preferably substantially solely gravity action (e.g. using a discharge with single convergence and side relief). Various mixing, diluting, thickening, steaming, and pumping devices are utilized in the system from initial steaming of the sawdust to passage into the top of the retention vessel.
    • 化学纤维素纸浆使用静态下流保留容器由锯屑制成。 通过将蒸汽和蒸煮液添加到锯屑流中,在约250-350°F的烹饪温度下产生加热的浆料。 加热的浆料在超大气压力下在静态下流保持容器中向下移动,同时保持烹饪温度约0.5-6(优选1至3)小时的时间,该浆料具有约5的稠度 -30%。 在超大气压下,没有显着降低来自保留容器的压力,如常规压力扩散器那样,将冷却液通过其冷却而将浆料冷却到远低于烹调温度。 来自保留容器的排出物优选基本上仅仅是重力作用(例如,使用具有单一收敛和侧面释放的放电)。 在系统中使用各种混合,稀释,增稠,蒸汽和泵送装置,从初始蒸发锯屑到通入保留容器的顶部。
    • 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 of minimizing transition metal ions during chemical pulping in a digester by adding chelating agent to the digester
    • 在蒸煮器中通过向蒸煮器中加入螯合剂在化学制浆过程中使过渡金属离子最小化的方法
    • US06475338B1
    • 2002-11-05
    • US08659682
    • 1996-06-05
    • Jian Er JiangKaj O. Henricson
    • Jian Er JiangKaj O. Henricson
    • D21C102
    • D21C3/22
    • The production of chemical (e.g., kraft) cellulose pulp much more suited to totally chlorine free or elemental chlorine free bleaching is produced by reducing the bleaching chemical consumability of the produced pulp. The effective alkalinity of the pulp during at least the majority of the cooking stage is maintained at about 15 g/l or above (e.g., about 18-25 g/l), expressed as sodium hydroxide, so as to reduce the charged acid groups (including hexeneuronic acids) by at least 30% (e.g., at least about 50%) compared with pulp cooked at conventional alkalinity. Instead—or in addition to—the cellulosic material which produces the pulp may be heated to a temperature (at least about 100° C., preferably at least about 130° C.) to release significant quantities of the transition metals within it, and preferably while it has this elevated temperature and a dissolved organic solids concentration of about 120 g/l or less, a chelating agent (such as EDTA) is added to combine with a significant quantity of the released transition metals to produce complexes. At least a majority of the complexes are preferably removed (e.g., using an extraction screen in a digester) before the pulp is bleached.
    • 通过减少所产生的纸浆的漂白化学品消耗能力,生产更适合于完全无氯或无元素无氯漂白的化学(例如牛皮纸)纤维素纸浆。 在烹饪阶段的至少大部分期间纸浆的有效碱度保持在约15g / l或更高(例如约18-25g / l),以氢氧化钠表示,以便减少带电的酸基团 (包括己烯醛酸)与常规碱度煮熟的纸浆相比至少30%(例如至少约50%)。 或者除了生产纸浆的纤维素材料之外,还可以加热到至少约100℃,优选至少约130℃的温度以释放大量的过渡金属,以及 优选当其具有这种升高的温度和约120g / l或更低的溶解有机固体浓度时,加入螯合剂(例如EDTA)以与大量释放的过渡金属组合以产生络合物。 在纸浆漂白之前,至少大部分复合物优选被除去(例如,在蒸煮器中使用提取筛网)。
    • 4. 发明授权
    • Pretreatment of chips before cooking
    • 烹饪前预处理薯片
    • US06248208B1
    • 2001-06-19
    • US08460723
    • 1995-06-02
    • Kaj O. HenricsonAki Hannu VilpponenHannu Olavi RamarkAuvo Kimmo KettunenC. Bertil Stromberg
    • Kaj O. HenricsonAki Hannu VilpponenHannu Olavi RamarkAuvo Kimmo KettunenC. Bertil Stromberg
    • D21C102
    • D21C1/06
    • The strength properties of chemical cellulose pulp (particularly kraft pulp) are improved by substituting a cold impregnation soak for conventional impregnation procedures. After steaming, wood chips are soaked in an alkaline liquid at a temperature of about 80-110° C. (preferably 80-100° C., or alternatively 90-105° C.) for between one-half-72 hours (typically about 2-4 hours) at a pressure of about 0-15 bar (preferably about 1-5 bar), to dissolve at least about 8% of the wood (preferably about 10-20%) and at least about 15% of the lignin. The alkaline liquid used preferably contains sulfide (e.g. black liquor, green liquor, white liquor, or mixtures thereof), but almost any alkaline liquid having an alkali concentration of about 1.0 mole of NaOH/liter or less (typically about 0.75 m/l or less) is suitable. The wood chips are then raised to a cooking temperature of about 145-180° C. and cooked to produce the cellulose chemical pulp. There may be an intermediate step, between soaking and raising the cooking temperature, of heating the wood chips to a temperature of about 110-150° C. (preferably about 120-140° C.) for about 10-90 minutes (preferably about 10-30 minutes). Alternatively or additionally the majority of the dissolved lignin (and/or other solids) may be removed before raising the wood chips to cooking temperature. The system for treating the wood chips need only include a low pressure soaking vessel (with an associated pump or other transfer device) in addition to conventional equipment.
    • 化学纤维素纸浆(特别是牛皮纸浆)的强度性能通过用常规浸渍方法的冷浸渍浸渍来改善。 蒸汽之后,将木屑浸入碱性液体中,温度约为80-110℃(优选80-100℃,或90-105℃)浸渍半个小时之间(通常为 约2-4小时),在约0-15巴(优选约1-5巴)的压力下溶解至少约8%的木材(优选约10-20%)和至少约15% 木质素。 使用的碱性液体优选含有硫化物(例如黑液,绿液,白液或其混合物),但几乎任何碱性浓度为约1.0摩尔NaOH /升或更低(通常约0.75米2 /升)或 少)适合。 然后将木屑升至约145-180℃的烹饪温度,并煮熟以生产纤维素化学纸浆。 在浸泡和提高烹饪温度之间可以有一个中间步骤,将木片加热至约110-150℃(优选约120-140℃)的温度约10-90分钟(优选约为 10-30分钟)。 或者或另外,在将木屑升高至烹饪温度之前,可以除去大部分溶解的木质素(和/或其它固体)。 用于处理木片的系统除了常规设备之外仅需要包括低压均热容器(具有相关联的泵或其它转移装置)。
    • 5. 发明授权
    • Effluent shower for pulp washer
    • 洗浆机出水淋浴
    • US06502434B1
    • 2003-01-07
    • US09688530
    • 2000-10-16
    • Klaus Doelle
    • Klaus Doelle
    • D21C102
    • D21C9/06Y10S239/12
    • A washer for washing a fiber suspension includes a porous surface traveling in a running direction and having a width in a direction transverse to the running direction. The porous surface is configured for carrying the fiber suspension thereon. A shower includes a pipe extending parallel to the width of the porous surface. The pipe has a sidewall with a longitudinally extending slot therein. The shower further includes a pair of lips connected to the pipe. The lips are positioned immediately adjacent to and on opposite sides of the slot, thereby defining a slot nozzle with a discharge gap. The lips are movable toward and away from each other to adjust the size of the discharge gap.
    • 用于洗涤纤维悬浮液的洗衣机包括在运行方向上行进且在横向于运行方向的方向上具有宽度的多孔表面。 多孔表面构造成用于在其上承载纤维悬浮液。 淋浴器包括平行于多孔表面的宽度延伸的管道。 该管具有其中具有纵向延伸槽的侧壁。 淋浴器还包括一对连接到管道上的嘴唇。 嘴唇定位成紧邻槽的相对侧并且在狭槽的相对侧上,从而限定具有放电间隙的缝隙喷嘴。 嘴唇可以彼此移动并远离,以调整放电间隙的尺寸。
    • 6. 发明授权
    • Apparatus for cleaning a suspension, preferably a fiber mass suspension
    • 用于清洁悬浮液,优选纤维悬浮液的装置
    • US06182478B2
    • 2001-02-06
    • US09524344
    • 2000-03-13
    • Jouko HautalaJukka HeimonenVeli-Matti RajalaIsmo Hourula
    • Jouko HautalaJukka HeimonenVeli-Matti RajalaIsmo Hourula
    • D21C102
    • B03D1/26B03D1/1412B03D1/1493B03D1/16B03D1/242D21B1/325D21C5/02D21F1/70Y02W30/646Y02W30/648
    • An apparatus for cleaning a fiber mass suspension, the apparatus comprising a receptacle and an inlet channel and an outlet channel for feeding the suspension into and for discharging it from the receptacle. In addition, the apparatus comprises air feed means for feeding air into the lower portion of the receptacle. The apparatus comprises at least one partition wall dividing the receptacle into spaces in such a way that the suspension may flow between the spaces at the lower portion and the upper portion of the partition wall, respectively. The air feeding means are positioned to feed air into one aeration space, whereby the air separates impurities from the suspension and makes the suspension flow on different sides of the partition wall upwards and downwards, respectively, so that a spiral flow is created around the partition wall from the inlet channel into the outlet channel.
    • 一种用于清洁纤维悬浮液的装置,该装置包括一个容器和一个入口通道以及一个出口通道,用于将悬浮液输送到容器中并将其从容器中排出。 此外,该装置包括用于将空气进入容器的下部的空气供给装置。 该装置包括至少一个分隔壁,该分隔壁将容器分成空间,使得悬架可以分别在分隔壁的下部和上部的空间之间流动。 空气供给装置被定位成将空气输送到一个通风空间中,由此空气将杂质与悬浮液分离,并使悬浮液分别在分隔壁的不同侧面上下流动,从而在隔板周围产生螺旋流 墙壁从入口通道进入出口通道。
    • 7. 发明授权
    • Method for treatment of loose material
    • 处理松散物料的方法
    • US06572734B2
    • 2003-06-03
    • US10226409
    • 2002-08-23
    • Jack T. Baker
    • Jack T. Baker
    • D21C102
    • D21C7/06D21C7/14
    • A pre-treatment device for wood chips for pulping comprises a tube through which the wood chips fall into a digester. Steam is injected into the tube through rings of nozzles, which are angled circumferentially to impart a rotary and turbulent motion to the falling chips. Some nozzles are angled downwardly to encourage the chips to flow freely through the tube, some are horizontal to encourage a longer dwell time near the nozzles. Digesting liquor is also sprayed onto the chips from spray nozzles after the first ring of steam nozzles. The heat and steam expel air and other non-condensable gases and volatiles from the chips, allowing them to absorb the liquor. At the bottom of the tube, the chips are propelled down and outwards by jets of higher-pressure steam, spreading and packing them into the digester.
    • 用于制浆的木屑的预处理装置包括木屑落入蒸煮器中的管。 蒸汽通过喷嘴环注入到管中,这些喷嘴圆周地成角度,以向落下的碎片施加旋转和湍流运动。 一些喷嘴向下倾斜以促使切屑自由地流过管,有些喷嘴是水平的,以便在喷嘴附近促进更长的停留时间。 在蒸汽喷嘴的第一环之后,消化液也从喷嘴喷射到碎片上。 热和蒸汽排出空气和其他不可冷凝的气体和来自碎屑的挥发物,允许它们吸收液体。 在管的底部,芯片通过高压蒸汽喷射向下和向外推进,并将其包装并进入蒸煮器。