Process for producing yeast cells
    1.
    发明授权
    Process for producing yeast cells 失效
    生产酵母细胞的方法

    公开(公告)号:US4033821A

    公开(公告)日:1977-07-05

    申请号:US675551

    申请日:1976-04-09

    IPC分类号: C12N1/32 C12C11/08 C12B1/00

    CPC分类号: C12N1/32 Y10S435/938

    摘要: A process for producing yeast cells by culturing in a culture liquor containing methanol and/or ethanol as main carbon sources a yeast belonging to the species Pichia aganobii and capable of assimilating methanol and/or ethanol, and separating the cells of said yeast from the culture liquor.

    摘要翻译: 通过在含有甲醇和/或乙醇作为主要碳源的培养液中培养属于毕赤酵母属的酵母并能够同化甲醇和/或乙醇并将所述酵母的细胞与培养物分离的酵母细胞的生产方法 酒。

    Cultivation of micro-organisms on hydrocarbons

    公开(公告)号:US3713976A

    公开(公告)日:1973-01-30

    申请号:US3713976D

    申请日:1971-06-21

    发明人: BUNTING P LEATHEN W

    IPC分类号: C12N1/26 C12P21/00 C12C11/08

    摘要: Protein concentrates are obtained in a process which includes: 1. Cultivating a hydrocarbon-consuming micro-organism in the presence of an aqueous nutrient medium, a hydrocarbon and a gas containing free oxygen; 2. CONTACTING THE CULTIVATED MICRO-ORGANISM FROM (1.) AT A TEMPERATURE BELOW THAT WHICH SUPPORTS ACTIVE FERMENTATION OF THE MICRO-ORGANISM WITH A GAS CONTAINING FREE OXYGEN IN THE PRESENCE OF AN AQUEOUS NUTRIENT MEDIUM CONTAINING A THIOSULFATE COMPOUND, E.G., SODIUM THIOSULFATE, AND A GAS CONTAINING FREE OXYGEN IN THE ABSENCE OF ADDED HYDROCARBON; AND 3. RECOVERING FROM (2.) A MICRO-ORGANISM HAVING (A) A PROTEIN CONTENT GREATER THAN THAT OF THE MICRO-ORGANISM OBTAINED IN (1.) AND (B) A SULFUR-CONTAINING AMINO ACID, E.G., CYSTINE AND METHIONINE, CONTENT GREATER THAN THAT OF THE MICRO-ORGANISM OBTAINED IN (1.).

    Continuous fermentation process
    5.
    发明授权
    Continuous fermentation process 失效
    连续发酵过程

    公开(公告)号:US3940492A

    公开(公告)日:1976-02-24

    申请号:US483007

    申请日:1974-06-25

    摘要: Wort is continuously supplied to a circuit including an elongated closed channel and through which micro-organisms are fed. After fermentation has taken place in the circuit, the mixture of wort and micro-organisms is centrifuged to separate it into fermented wort, a living cell mass and impurities, these three components being separately discharged from the centrifuge. The separate discharges of fermented wort and living cell mass are continuous, and the latter discharge includes an excess of living cells formed in the circuit, an amount of cell mass corresponding to this excess being discharged from the circuit.

    摘要翻译: 麦芽汁连续供应到包括细长的封闭通道的电路中,通过微生物进料。 在回路中发酵后,将麦芽汁和微生物的混合物离心分离成发酵麦芽汁,活细胞块和杂质,这三个组分分别从离心机中排出。 发酵麦芽汁和活细胞块的单独排放是连续的,后者的排放包括在回路中形成的过量的活细胞,相当于该余量的细胞块数量从回路排出。

    Preparation of alcohol or alcoholic beverages
    7.
    发明授权
    Preparation of alcohol or alcoholic beverages 失效
    酒精或酒精饮料的制备

    公开(公告)号:US4092434A

    公开(公告)日:1978-05-30

    申请号:US632254

    申请日:1975-11-17

    CPC分类号: C12G3/12 C12P7/06 Y02E50/17

    摘要: Alcohol or an alcoholic beverage is produced by a process wherein a mash of cereal grains and liquefying enzymes is cooked at a temperature of from 75.degree. C to 85.degree. C which is lower than the temperature of maximum viscosity for the mash and which is higher than the sterilization temperature of undesirable microorganisms in the mash which grow during fermentation with yeast. After cooking, the mash is cooled, saccharifying enzymes are added, the resultant mash is fermented with yeast to produce alcohol and the alcohol is distilled.

    摘要翻译: 酒精或酒精饮料通过以下方法生产:其中谷物和液化酶的糊状物在75℃至85℃的温度下烹饪,该温度低于糊状物的最大粘度的温度,并且高于 在用酵母发酵过程中生长的糊状物中不希望的微生物的灭菌温度。 烹饪后,将糊状物冷却,加入糖化酶,用酵母发酵所得的糊状物以产生醇,并蒸馏出醇。

    Process for cultivating micro-organisms in the presence of hydrocarbons
    10.
    发明授权
    Process for cultivating micro-organisms in the presence of hydrocarbons 失效
    在碳氢化合物存在下生成微量有机物的方法

    公开(公告)号:US3698998A

    公开(公告)日:1972-10-17

    申请号:US3698998D

    申请日:1969-05-13

    CPC分类号: C12N1/02 C12N1/00 C12N1/26

    摘要: IN THE CULTIVATION OF MICRO-ORGANISMS, A LIQUID HYDROCARBON FEEDSTOCK IS EMPLOYED CONTAINING AT LEAST 70% BY WEIGHT OF LINEAR PARAFFINIC HYDROCARBONS. THE GROWING STEP IS CONDUCTED IN THE PRESENCE OF A GAS-CONTAINING MOLECULAR OXYGEN AND WITH A NUTRIENT AQUEOUS MEDIUM CONTAINING; (A) ASSIMILABLE NITROGEN AND PHOSPHORUS; (B) OLIGOELEMENTS SUCH AS TRACE AMOUNTS OF COPPER, COBALT, IRON, MOLYBDENUM AND MANGANESE COMPOUNDS; (C) GROWTH FACTORS SUCH AS YEAST, ETC.; AND (D) ESSENTIAL MINERAL ELEMENTS SUCH AS POTASSIUM, AMMONIUM AND MAGNESIUM IONS. THE MICRO-ORGANISMS ARE THEN RECOVERED FROM AT LEAST THE MAJOR PART OF UNCONVERTED HYDROCARBONS, PREFERABLY BY DECANTATION, AND THEN SUBJECTED TO A MATURATION STEP IN AN AQUEOUS MEDIUM SIMILAR TO THE NUTRITIVE AQUEOUS MEDIUM, BUT DEPRIVED OF AT LEAST ONE OF THE ESSENTIAL MINERAL ELEMENTS.