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    • 4. 发明授权
    • Continuous process for making ethanol
    • 连续制造乙醇的方法
    • US5837506A
    • 1998-11-17
    • US916742
    • 1997-08-19
    • Lee R. LyndColin R. South
    • Lee R. LyndColin R. South
    • C12P7/10
    • C12P7/10Y02E50/16
    • An improved continuous process for producing ethanol from cellulosic materials employs an intermittently agitated, perpetually fed, solids retaining reactor vessel. Cellulosic substrate, catalysts and fermentation agents are introduced into a reaction vessel to form a slurry. The slurry is agitated for a first selected time interval under conditions sufficient to initiate and maintain a fermentation reaction and then allowed to settle during a second selected time interval. At the end of the second selected time interval an ethanol-containing effluent is removed from the vessel. Thereafter, additional cellulosic material, catalysts and fermentation agents are added to the reactor vessel. This operating cycle is repeated virtually perpetually to effect the ethanol production. It can be implemented using a single bioreactor or a cascade of bioreactors.
    • 用于从纤维素材料生产乙醇的改进的连续方法采用间歇搅动的,永久进料的固体保留反应器容器。 将纤维素底物,催化剂和发酵剂引入反应容器中以形成浆料。 在足以启动和维持发酵反应的条件下将浆料搅拌第一选定的时间间隔,然后在第二选定的时间间隔内使其沉降。 在第二选择的时间间隔结束时,从容器中除去含乙醇的流出物。 此后,将另外的纤维素材料,催化剂和发酵剂加入到反应器容器中。 这种操作周期几乎永久地重复,以实现乙醇生产。 它可以使用单个生物反应器或级联的生物反应器来实现。
    • 5. 发明授权
    • Continuous process for ethanol production from lignocellulosic materials
without mechanical agitation
    • 不经机械搅拌从木质纤维素材料生产乙醇的连续方法
    • US5258293A
    • 1993-11-02
    • US695516
    • 1991-05-03
    • Lee R. LyndDavid A. HogsettGisbert Spieles
    • Lee R. LyndDavid A. HogsettGisbert Spieles
    • C12P7/10C12P7/14
    • C12P7/14C12P7/10Y02E50/16Y10S435/813
    • An improved and highly productive method of continuously producing ethanol from lignocellulosic substrates is provided. The method involves providing a suitable microbial system within a reaction vessel and adding fermentable substrate to the reactor to form a reaction mixture. The fermentation reaction is allowed to proceed while a quiescent state is maintained within the reactor. During the fermentation, soluble substrate is differentially retained relative to the feed slurry and reaction biocatalysts are retained and internally recycled within the system. Further, while fermenting substrate is retained within the system, it forms a stratified zone within the reactor such that the concentration of actively fermenting substrate is highest at upper portions of the reaction zone and is lowest, near zero, at a lower portion of the reaction zone. Insoluble, fully reacted substrate may be withdrawn from a region near the bottom of the reactor.
    • 提供了一种从木质纤维素基质连续生产乙醇的改进和高效的方法。 该方法包括在反应容器内提供合适的微生物系统,并向反应器中加入可发酵底物以形成反应混合物。 允许发酵反应进行,同时在反应器内保持静止状态。 在发酵期间,可溶性底物相对于进料浆液差异保留,反应生物催化剂被保留并在系统内部再循环。 此外,当发酵底物保留在体系内时,其在反应器内形成分层区域,使得主动发酵底物的浓度在反应区的上部处最高,并且在反应的较低部分处最低,接近零 区。 可以从反应器底部附近的区域取出不溶的完全反应的底物。