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
    • Xylanase treatment of chemical pulp
    • 木聚糖酶处理化学纸浆
    • US07368036B2
    • 2008-05-06
    • US10505815
    • 2003-03-05
    • Jeffrey S. TolanCorina Popovici
    • Jeffrey S. TolanCorina Popovici
    • D21C9/10D21C9/14
    • 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。
    • 7. 发明授权
    • Upflow reactor for enzymatic hydrolysis of cellulose
    • 用于纤维素酶水解的上流式反应器
    • US07727746B2
    • 2010-06-01
    • US11303424
    • 2005-12-16
    • Brian FoodyZiyad RahmeJeffrey S. Tolan
    • Brian FoodyZiyad RahmeJeffrey S. Tolan
    • C12P19/14
    • 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。
    • 8. 发明申请
    • RECOVERY OF VOLATILE CARBOXYLIC ACIDS BY A STRIPPER-EXTRACTOR SYSTEM
    • 通过剥离器系统恢复挥发性羧酸
    • US20120209028A1
    • 2012-08-16
    • US13392744
    • 2010-08-18
    • Jeffrey S. TolanBrian FoodyVijay Anand
    • Jeffrey S. TolanBrian FoodyVijay Anand
    • C07C51/42
    • C12F3/00C07C51/43C07C51/445Y02E50/16C07C53/08
    • A process for recovering a volatile carboxylic acid from an aqueous stream comprising same, the process comprising the steps of: (i) steam stripping the carboxylic acid from the aqueous stream, which aqueous stream is produced by a conversion process using a lignocellulosic feedstock as a substrate, the steam stripping comprising contacting the aqueous stream with steam by flowing the aqueous stream and the steam countercurrent to one another, thereby producing a vapour stream comprising vapourized carboxylic acid and steam and a stripped aqueous stream; (ii) extracting the vapourized carboxylic acid with an organic solvent by contacting the vapour stream with the organic solvent to produce (a) a stream comprising the organic solvent and the carboxylic acid and (b) the steam at least substantially depleted of the carboxylic acid, wherein the organic solvent has an atmospheric boiling point of at least about 150° C. and is insoluble in water; (iii) returning the steam from step (ii) to the steam stripping step (step i) to further strip the carboxylic acid from the aqueous stream; and (iv) separating the carboxylic acid from the organic solvent.
    • 一种从包含其的含水流中回收挥发性羧酸的方法,该方法包括以下步骤:(i)从水流中汽提汽提羧酸,该水流通过使用木质纤维素原料的转化方法生产, 蒸汽汽提包括通过使水流和蒸汽逆流地相互流动使水流与蒸汽接触,从而产生包含蒸发的羧酸和蒸汽和汽提的水流的蒸气流; (ii)通过使蒸气流与有机溶剂接触来提取挥发的羧酸,以产生(a)包含有机溶剂和羧酸的物流,和(b)至少基本上不含羧酸的蒸汽 其中所述有机溶剂的常压沸点为至少约150℃,并且不溶于水; (iii)将来自步骤(ii)的蒸汽返回到汽提步骤(步骤i),以进一步从水流中分离出羧酸; 和(iv)从有机溶剂中分离出羧酸。
    • 9. 发明申请
    • UPFLOW HYDROLYSIS REACTOR SYSTEM FOR HYDROLYZING CELLULOSE
    • 用于水解纤维素的UPFLOW水解反应器系统
    • US20100221819A1
    • 2010-09-02
    • US12762589
    • 2010-04-19
    • Brian FoodyZiyad RahmeJeffrey S. Tolan
    • Brian FoodyZiyad RahmeJeffrey S. Tolan
    • C12M1/00
    • 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。 另外,提供了包含纤维素酶和絮状物的试剂盒。
    • 10. 发明申请
    • METHOD FOR THE PRODUCTION OF GLUCOSE FROM LIGNOCELLULOSIC FEEDSTOCKS
    • 用于生产来自木糖脂原料的葡萄糖的方法
    • US20100184151A1
    • 2010-07-22
    • US12686485
    • 2010-01-13
    • Jeffrey S. TolanBrian Foody
    • Jeffrey S. TolanBrian Foody
    • C12P19/00C12P7/04
    • C12P7/10C12P19/02C12P19/14C12P2201/00Y02E50/16
    • A method for producing glucose from a lignocellulosic feedstock is provided. The method comprises pretreating the lignocellulosic feedstock with acid to produce a pretreated feedstock composition. A calcium-containing stream is provided that comprises calcium that is obtained from the lignocellulosic feedstock and a calcium carbonate-containing stream is obtained by precipitation of the calcium from the calcium-containing stream. The pH of the pretreated feedstock is adjusted with (a) the calcium carbonate-containing stream; (b) a calcium hydroxide-containing stream that is derived from said calcium carbonate-containing stream by subjecting said calcium carbonate-containing stream to calcination; or (c) a combination of the calcium carbonate-containing stream and the calcium hydroxide-containing stream. The pH adjustment results in a neutralized pretreated lignocellulosic feedstock having a pH between about 3 and about 9 and enzymatic hydrolysis of the neutralized, pretreated lignocellulosic feedstock is then conducted with cellulase enzymes to produce the glucose.
    • 提供了一种从木质纤维原料生产葡萄糖的方法。 该方法包括用酸处理木质纤维素原料以产生预处理的原料组合物。 提供含钙流,其包含从木质纤维素原料获得的钙,并且通过从含钙流中沉淀钙获得含碳酸钙的流。 用(a)含碳酸钙的料流调节预处理原料的pH; (b)通过使所述含碳酸钙的料流进行煅烧从含有所述含碳酸钙的料流中得到的含氢氧化钙的料流; 或(c)含碳酸钙的料流和含氢氧化钙的料流的组合。 pH调节导致pH为约3至约9的中和预处理木质纤维素原料,然后用纤维素酶进行中和的预处理的木质纤维素原料的酶水解以产生葡萄糖。