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    • 1. 发明申请
    • Xylanase treatment of chemical pulp
    • 木聚糖酶处理化学纸浆
    • US20050150619A1
    • 2005-07-14
    • US10505815
    • 2003-03-05
    • Jeffrey TolanCorina Popovici
    • Jeffrey TolanCorina Popovici
    • D21C5/00D21C9/10D21C9/12D21C9/14
    • D21C5/005D21C9/10D21C9/1036D21C9/14
    • The present invention discloses methods of bleaching chemical pulp that use xylanase enzymes after chemical bleaching. The method comprises the steps of carrying out a chlorine dioxide stage to produce a partially bleached pulp, treating the partially bleached pulp with a xylanase enzyme, optionally in the presence of oxygen and hydrogen peroxide, in a mild extraction stage, then bleaching the pulp with a second chlorine dioxide stage. The method allows the mill to decrease the usage of sodium hydroxide or other alkali, while decreasing the use of chlorine dioxide, and possibly improving the yield and strength of the pulp, while maintaining a similar level of bleached brightness of the pulp. The pulp bleaching method of the present invention may be performed in a pulp mill as part of a complex pulp bleaching process.
    • 本发明公开了化学漂白后使用木聚糖酶的漂白化学纸浆的方法。 该方法包括以下步骤:进行二​​氧化氯阶段以产生部分漂白的纸浆,在温和萃取阶段任选在氧气和过氧化氢存在下,用木聚糖酶处理部分漂白的纸浆,然后用纸浆漂白纸浆 第二个二氧化氯阶段。 该方法允许研磨机降低氢氧化钠或其他碱的用量,同时减少二氧化氯的使用,并且可能提高纸浆的产率和强度,同时保持纸浆的漂白亮度相似水平。 本发明的纸浆漂白方法可以在纸浆厂中进行,作为复杂纸浆漂白方法的一部分。
    • 2. 发明申请
    • Upflow settling reactor for enzymatic hydrolysis of cellulose
    • 用于纤维素酶水解的上流沉降反应器
    • US20060154352A1
    • 2006-07-13
    • US11303424
    • 2005-12-16
    • Brian FoodyZiyad RahmeJeffrey Tolan
    • Brian FoodyZiyad RahmeJeffrey Tolan
    • C12P7/06C12P19/02
    • C12P19/14C12M45/09C12P19/02C12P19/04Y02E50/16Y02E50/17
    • A process for the enzymatic hydrolysis of cellulose to produce a hydrolysis product from a pre-treated cellulosic feedstock is provided. The process comprises introducing an aqueous slurry of the pre-treated cellulosic feedstock at the bottom of a hydrolysis reactor. Axial dispersion in the reactor is limited by avoiding mixing and maintaining an average slurry flow velocity of about 0.1 to about 20 feet per hour, such that the undissolved solids flow upward at a rate slower than that of the liquid. Cellulase enzymes are added to the aqueous slurry before or during the step of introducing. An aqueous stream comprising hydrolysis product and unhydrolyzed solids is removed from the hydrolysis reactor. Also provided are enzyme compositions which comprise cellulase enzymes and flocculents for use in the process. In addition, a kit comprising cellulase enzymes and flocculent is provided.
    • 提供了一种纤维素酶水解从预处理的纤维素原料产生水解产物的方法。 该方法包括在水解反应器的底部引入预处理的纤维素原料的含水浆料。 通过避免混合并保持约0.1至约20英尺/小时的平均浆料流速,使得未溶解的固体以比液体慢的速率向上流动,来限制反应器中的轴向分散。 在引入步骤之前或期间,将纤维素酶加入到含水浆料中。 从水解反应器中除去包含水解产物和未水解固体的水流。 还提供了包含用于该方法的纤维素酶和絮凝剂的酶组合物。 此外,提供了包含纤维素酶和絮状物的试剂盒。