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
    • 9. 发明申请
    • BLEACHING PULP WITH PEROXIDE AT SUPERATMOSPHERIC PRESSURE AND IN MULTIPLE STAGES
    • 在超级压力和多个阶段过氧化氢漂白浆
    • WO1996023929A1
    • 1996-08-08
    • PCT/FI1995000138
    • 1995-03-14
    • A. AHLSTROM CORPORATIONHENRICSON, KajGREENWOOD, BrianSVEDIN, BjörnPIKKA, Olavi
    • A. AHLSTROM CORPORATION
    • D21C09/16
    • D21C9/163
    • Cellulose pulp is bleached with peroxide under superatmospheric pressure in two (or more) stages, with removal of oxygen and reaction gases from the pulp between the stages, About 5-20 Kg/admt hydrogen peroxide is intimately mixed with the pulp and then introduced into a first pressurized vessel in which the pressure is between about 5-15 bar and the temperature between about 80-120 DEG C. Bleaching takes place in the first vessel for about 15-60 minutes while oxygen and reaction gases are formed, and then at least 20 % of (and preferably subtantially all of) the oxygen and reaction gases are removed from the pulp before complete consumption of all of the peroxide. Then the pulp is preferably introduced into a second vessel, additional peroxide, alkali, and steam can be added, and peroxide bleaching continues at a pressure of about 1.1-10 bar and at a temperature of about 90-120 DEG C for between about 30-200 minutes, during which oxygen and reaction gases are formed anew. The majority of the newly formed oxygen and reaction gases -- in fact subtantially all of them -- are separated out, typically upon discharge of the pulp from the second vessel.
    • 纤维素纸浆在两个(或多个)阶段的超大气压下用过氧化物漂白,除去来自阶段之间的纸浆的氧气和反应气体,约5-20Kg / adm过氧化氢与纸浆密切混合,然后引入 第一加压容器,其中压力在约5-15巴之间,温度在约80-120℃之间。漂白在第一容器中发生约15-60分钟,同时形成氧气和反应气体,然后在 在完全消耗所有过氧化物之前,至少20%(并且优选地是全部)氧和反应气体从纸浆中除去。 然后将纸浆优选引入第二容器中,可以加入额外的过氧化物,碱和蒸汽,并且过氧化物漂白在约1.1-10巴的压力和约90-120℃的温度下继续进行约30 -200分钟,在此期间重新形成氧气和反应气体。 大多数新形成的氧和反应气体 - 实际上基本上都是它们 - 被分离出来,通常在从第二容器排出纸浆时。
    • 10. 发明申请
    • PEROXIDE BLEACHING PROCESS FOR CELLULOSIC AND LIGNOCELLULOSIC MATERIAL
    • 过氧化物漂白过程用于纤维和纤维素材料
    • WO1996001920A1
    • 1996-01-25
    • PCT/US1995008137
    • 1995-06-29
    • INGERSOLL-RAND COMPANYPULP AND PAPER RESEARCH INSTITUTE OF CANADA
    • INGERSOLL-RAND COMPANYPULP AND PAPER RESEARCH INSTITUTE OF CANADASHACKFORD, Lewis, D.MILLER, William, J.ROY, Brian, P.VAN LIEROP, BarbaraBERRY, Richard, M.
    • D21C09/16
    • D21C9/1026D21C9/1057D21C9/163
    • A method for bleaching cellulosic and lignocellulosic pulp using hydrogen peroxide as a bleaching reagent, utilizes a two-step reaction, viz. a short high temperature step at a pressure sufficient to suppress boiling and a longer atmospheric pressure reduced temperature step to consume a substantial portion of the hydrogen peroxide remaining after the short phase. The method includes the steps of introducing pulp (15), at a consistency of 10 %-18 %, to a mixer (100) in which the pulp is heated to a temperature above 100 DEG C; adding sufficient sodium hydroxide to bring the pulp to a pH of 8.5; adding sufficient hydrogen peroxide (36) to equal from about 0.5 %-5.0 %, by weight, of the pulp; passing the pulp through a pressurized reactor column (400) at a rate providing a reaction time in the column of between 1 and 30 minutes; and depositing the pulp in a reaction tower and allowing the reaction to proceed for 1-5 hours until a substantial portion of the residual hydrogen peroxide has been consumed. It may be desirable to introduce the pulp to a mixer and add alkali to reactivate residual hydrogen peroxide by bringing the pulp to a pH of at least 9 between bleaching steps.
    • 使用过氧化氢作为漂白剂漂白纤维素和木质纤维素纸浆的方法采用两步反应,即, 在足以抑制沸腾的压力下的短的高温步骤和较长的大气压降低温度步骤以消耗在短相后残留的大部分过氧化氢。 该方法包括将纸浆(15)以10%-18%的浓度引入到其中将纸浆加热至高于100℃的混合器(100)的步骤; 加入足够的氢氧化钠使纸浆的pH值达到8.5; 加入足量的过氧化氢(36)至浆料重量的约0.5%-5.0%; 使纸浆通过加压反应器塔(400),其速率为提供柱在1至30分钟之间的反应时间; 并将纸浆沉积在反应塔中,并允许反应进行1-5小时,直到大部分残余过氧化氢消耗。 可能需要将纸浆引入混合器中,并通过在漂白步骤之间使纸浆达到至少9的pH来添加碱以再活化剩余的过氧化氢。