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    • 1. 发明授权
    • Wet method of preparing fiberboard products in a substantially closed
and balanced white water system
    • 在基本上封闭和平衡的白水系统中制备纤维板产品的湿法
    • US4221630A
    • 1980-09-09
    • US898385
    • 1978-04-20
    • Stig D. SelanderKarl N. Cederquist
    • Stig D. SelanderKarl N. Cederquist
    • D21F11/00D21F1/00D21F1/66D21F11/04D21C9/18
    • D21F11/04D21F1/66
    • A method of making fiberboard using a substantially closed white water system. One or more layers of separately prepared surface pulp is applied to a layer of base pulp at the wet sheet forming stage. Lignocellulose chips in a pressure-sealed defibrating zone under generation of steam. The steam is separated at the discharge end of the defibrating zone under atmospheric pressure. The atmospheric steam is utilized to presteam the raw chips. The presteamed chips are thereafter dewatered to a moisture content coordinated to the energy demand of the defibrating treatment and the desired generation of steam prior to entering the defibrating zone. The water removed at the dewatering stage is collected for use in preparing the surface layer pulp suspension. A small portion of the base pulp to be used for the surface layer pulp is diverted to a refiner and diluted with water. The major portion of the base pulp is diluted with white water drained off and recycled from the base layer wet sheet forming stage to form a base layer suspension, which suspension is then transported by the white water to the wet sheet forming stage, where the white water and recycled to the base layer suspension stage to form a new base layer suspension. The diverted portion of the base pulp is further diluted with white water recycled from the surface layer forming stage to form a surface layer suspension.A portion of the white water recycled from the wet sheet forming stage to the base layer suspension stage is heated by a portion of the steam separated at the discharge end of the defibrating zone to drive off surplus white water to maintain a constant volume of white water.
    • 使用基本封闭的白水系统制造纤维板的方法。 在湿片形成阶段将一层或多层单独制备的表面纸浆施加到基纸层上。 生成蒸汽的压力密封解纤带中的木质纤维素片。 在大气压下,在除颤区的排出端分离蒸汽。 大气蒸汽用于预先生产原料。 然后将预先冷却的芯片脱水至在进行解纤带之前与解纤处理的能量需求协调的水分含量和所需的蒸汽产生量。 在脱水阶段除去的水被收集用于制备表层纸浆悬浮液。 将用于表层纸浆的一小部分基础纸浆转移至精制机并用水稀释。 基浆的主要部分用排出的白水稀释,并从基层湿片形成阶段再循环,形成基层悬浮液,然后将该悬浮液通过白水输送到湿片形成阶段,其中白色 水并再循环到基层悬浮液阶段以形成新的基层悬浮液。 用从表面层形成阶段再循环的白水进一步稀释基础纸浆的转向部分以形成表面层悬浮液。 从湿片形成阶段再循环到基层悬浮阶段的白水的一部分被在解纤带排放端分离的一部分蒸汽加热,以驱除多余的白水以保持恒定体积的白水 。
    • 2. 发明授权
    • Method for wet combustion of organic material
    • 有机材料湿法燃烧方法
    • US4604957A
    • 1986-08-12
    • US703257
    • 1985-02-20
    • Karl N. Cederquist
    • Karl N. Cederquist
    • D21C11/14F23G7/04
    • D21C11/14
    • The wet method of combusting organic material dispersed in a liquid comprising waste liquor from wood pulping processes in which the organic material is oxidized by contact with air or other oxygenating gases at a temperature ranging between 180.degree. C. and 340.degree. C. and a correspondingly superatmospheric pressure. The combustion of oxygenation is carried out in two steps: namely, a first step in which the organic material is partially oxidized so that the major portion of the organic substances is converted into carbon dioxide and water, and a minor portion is converted to water-soluble low-molecular fatty acids resistant to oxidation; in a second oxidizing step, the residual oxygen-resistant fatty acids are combusted in the presence of a substantial excess of oxygen-enriched air or other molecular-oxygenating gas so as to liberate the total heat of combustion of the organic material and to impart to the resultant gaseous mixture of effluents a molecular oxygen content sufficient to achieve the partial oxidation in the first step.
    • 燃烧分散在包含来自木材制浆过程的废液的液体中的有机材料的湿法,其中有机材料通过与空气或其它氧化气体在180℃至340℃的温度范围内接触而被氧化,并相应地 超大气压。 氧合的燃烧分两步进行:即第一步骤,其中有机材料被部分氧化,使得主要部分的有机物质转化为二氧化碳和水,少量部分转化为水溶性, 耐氧化的可溶性低分子脂肪酸; 在第二氧化步骤中,残留的耐氧脂肪酸在大量过量的富氧空气或其它分子氧化气体的存在下燃烧,以释放有机材料的总燃烧热量并赋予 所得到的流出物气体混合物的分子氧含量足以在第一步中实现部分氧化。