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    • 1. 发明申请
    • RECOVERY OF VOLATILE CARBOXYLIC ACIDS BY A STRIPPER- EXTRACTOR SYSTEM
    • 剥离 - 萃取系统回收挥发性羧酸
    • WO2011022811A8
    • 2011-04-21
    • PCT/CA2010001272
    • 2010-08-18
    • IOGEN ENERGY CORPTOLAN JEFFREY SFOODY BRIANANAND VIJAY
    • TOLAN JEFFREY SFOODY BRIANANAND VIJAY
    • C07C51/44B01D3/00B01D11/04C12F3/00C12P7/10C12P7/40
    • 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.
    • 从包含它的含水物流中回收挥发性羧酸的方法,所述方法包括以下步骤:(i)从含水物流中汽提羧酸,所述含水物流通过转化过程产生,所述转化过程使用木质纤维素原料作为 所述蒸汽汽提包括使所述含水物流与所述蒸汽接触,使所述含水物流和所述蒸汽彼此逆流流动,从而产生包含汽化的羧酸和蒸汽以及汽提的含水物流的蒸汽物流; (ii)通过使蒸气流与有机溶剂接触,用有机溶剂萃取汽化的羧酸,以产生(a)包含有机溶剂和羧酸的物流和(b)至少基本上贫化的羧酸 其中所述有机溶剂的常压沸点为至少约150℃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)以进一步从含水物流中汽提羧酸; 和(iv)从有机溶剂中分离羧酸。
    • 2. 发明申请
    • UPFLOW SETTLING REACTOR FOR ENZYMATIC HYDROLYSIS OF CELLULOSE
    • 用于纤维素酶促水解的UPFLOW SETLING REACTOR
    • WO2006063467A8
    • 2006-10-05
    • PCT/CA2005001922
    • 2005-12-16
    • IOGEN ENERGY CORPFOODY BRIANRAHME ZIYADTOLAN JEFFREY S
    • FOODY BRIANRAHME ZIYADTOLAN JEFFREY S
    • C12P19/14C12P7/10C12P19/02C12P19/12
    • C12P19/14C12M45/09C12P19/02C12P19/04Y02E50/16Y02E50/17
    • A process for the enzymatic hydrolysis of cellulose to produce a hydrolysis product from a pre­treated 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。