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    • 1. 发明申请
    • METHOD AND DEVICE FOR STRIPPING AMMONIA FROM LIQUIDS
    • WO2004012840A3
    • 2004-02-12
    • PCT/DK2003/000520
    • 2003-08-01
    • GREEN FARM ENERGY A/SBONDE, Torben, A.
    • BONDE, Torben, A.
    • B01D3/38
    • The present invention in a first aspect provides a method and a system for stripping volatile compounds such as ammonia from e.g. fermentation liquids. Part of the ammonia is stripped form the liquid in a stripper system comprising a shunt through which liquid such as e.g. fermentation medium comprising a biomass can be diverted in the form of a side stream in liquid contact with a main fermentor(s). The stripper system is connected to an evaporator. In the evaporator aqueous liquid is heated at a pressure below atmospheric pressure whereby vapour is developed at a temperature below 100°C. The vapour from the evaporator is directed to the liquid medium comprising ammonia and this results in ammonia being stripped from the liquid and transferred to the vapour phase. The vapour phase is condensed in first condenser at a low pressure, e.g. a pressure well below 1 bar, and the liquid thus obtained is further treated in a stripper unit at a higher pressure, such as e.g. a pressure at or above 1 bar, to obtain a more concentrated solution of ammonia. When stripped for at least part of the ammonia the liquid initially obtained from the biogas reactor and diverted to the shunt can be returned to the reactor.
    • 2. 发明申请
    • METHOD AND DEVICE FOR STRIPPING AMMONIA FROM LIQUIDS
    • 用于从液体中去除氨的方法和装置
    • WO2004012840A2
    • 2004-02-12
    • PCT/DK0300520
    • 2003-08-01
    • GREEN FARM ENERGY ASBONDE TORBEN A
    • BONDE TORBEN A
    • B01D3/34C02F1/20C02F1/44C02F1/52B01D3/38C02F1/58
    • C02F1/20B01D3/346C02F1/441C02F1/444C02F1/5236C02F2101/16C02F2103/20C02F2303/12C12M21/04C12M23/36C12M47/18Y02E50/343
    • The present invention in a first aspect provides a method and a system for stripping volatile compounds such as ammonia from e.g. fermentation liquids. Part of the ammonia is stripped form the liquid in a stripper system comprising a shunt through which liquid such as e.g. fermentation medium comprising a biomass can be diverted in the form of a side stream in liquid contact with a main fermentor(s). The stripper system is connected to an evaporator. In the evaporator aqueous liquid is heated at a pressure below atmospheric pressure whereby vapour is developed at a temperature below 100°C. The vapour from the evaporator is directed to the liquid medium comprising ammonia and this results in ammonia being stripped from the liquid and transferred to the vapour phase. The vapour phase is condensed in first condenser at a low pressure, e.g. a pressure well below 1 bar, and the liquid thus obtained is further treated in a stripper unit at a higher pressure, such as e.g. a pressure at or above 1 bar, to obtain a more concentrated solution of ammonia. When stripped for at least part of the ammonia the liquid initially obtained from the biogas reactor and diverted to the shunt can be returned to the reactor.
    • 本发明的第一方面提供了用于从例如乙醇中汽提挥发性化合物如氨的方法和系统。 发酵液。 部分氨在包含分流器的汽提系统中从液体中汽提出来, 包含生物质的发酵培养基可以以与主发酵罐液体接触的侧流形式转向。 汽提塔系统连接到蒸发器。 在蒸发器中,含水液体在低于大气压的压力下加热,由此在低于100℃的温度下形成蒸气。 来自蒸发器的蒸汽被引导至包含氨的液体介质,这导致氨从液体中汽提并转移至汽相。 汽相在第一冷凝器中在低压下冷凝, 压力远低于1巴,并且由此获得的液体在更高压力下的汽提单元中进一步处理,例如, 压力等于或高于1巴,以获得更浓的氨溶液。 当汽提至少一部分氨时,最初从沼气反应器获得并转移到分流器的液体可返回反应器。