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    • 5. 发明授权
    • Process for liquefying starch
    • 液化淀粉的方法
    • US4734365A
    • 1988-03-29
    • US795779
    • 1985-11-07
    • Ryooichi HagaMasahiko IshidaMasako Katsurayama
    • Ryooichi HagaMasahiko IshidaMasako Katsurayama
    • C12N9/28C12P19/14C12R1/145
    • C12N9/2417C12P19/14Y10S435/842
    • This invention relates to a process for liquefying starch. More particularly it relates to an appropriate process for liquefying starch by using a thermostable .alpha.-amylase which has an optimum working pH range in an acidic region and a low calcium requirement.This invention provides a process for liquefying starch by using a calcium-requiring, thermostable .alpha.-amylase which requires a calcium concentration of 10 .mu.m or below under a thermostable condition.In the process of the present invention, it is unnecessary to add a calcium salt in liquefying starch and the starch slurry can be reacted while remaining acidic without neutralization, so that the load at the desalting step of the product can be significantly relieved.
    • 本发明涉及一种液化淀粉的方法。 更具体地说,涉及通过使用在酸性区域具有最佳工作pH范围和低钙需求的热稳定性α-淀粉酶来液化淀粉的合适方法。 本发明提供了一种通过使用需要钙的热稳定性α-淀粉酶来液化淀粉的方法,该淀粉酶在热稳定条件下需要10微米或更低的钙浓度。 在本发明的方法中,不需要在液化淀粉中添加钙盐,淀粉浆料可以在保持酸性而不中和的同时反应,从而可以显着减轻产品脱盐步骤的负荷。
    • 8. 发明授权
    • Anaerobic digestion process for organic wastes
    • 有机废物厌氧消化过程
    • US4491522A
    • 1985-01-01
    • US551730
    • 1983-11-15
    • Masahiko IshidaRyoichi HagaTadashi IshibashiYoji Odawara
    • Masahiko IshidaRyoichi HagaTadashi IshibashiYoji Odawara
    • B09B3/00C02F3/28C02F3/30C02F11/04
    • C02F3/28C02F3/30Y02E50/343Y10S435/801
    • The present invention relates to an anaerobic digestion process for organic wastes with a high efficiency and an improved recovery rate of methane.This process comprises the following steps: (1) anaerobically digesting organic wastes under simultaneous presence of facultative anaerobic bacteria and obligatory anaerobic bacteria, (2) separating the anaerobically digested slurry obtained from the step (1) into a liquor fraction containing the two groups of bacteria and an undecomposed solid fraction, (3) mixing the liquor fraction obtained from the step (2) with the surplus activated sludge slurry produced by anaerobically treating organic waste water, under anaerobic condition, (4) separating the mixed slurry obtained from the step (3) into a solid fraction containing the surplus activated sludge which has absorbed the two groups of bacteria and a liquor fraction, and recycling back the solid fraction obtained from the step (4) as the sources of the two groups of bacteria and nitrogen to the step (1).
    • 本发明涉及一种具有高效率和提高甲烷回收率的有机废物的厌氧消化方法。 该方法包括以下步骤:(1)在兼性厌氧菌和强制性厌氧菌同时存在下厌氧消化有机废物,(2)将由步骤(1)获得的厌氧消化浆液分离成含有两组 细菌和未分解的固体部分,(3)将在步骤(2)中获得的液体馏分与在厌氧条件下厌氧处理有机废水产生的剩余活性污泥浆混合,(4)将从步骤 (3)成为含有吸收了两组细菌和液体馏分的剩余活性污泥的固体成分,将从步骤(4)获得的固体成分作为两组细菌和氮源的来源循环回到 步骤(1)。