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    • 3. 发明授权
    • Method and arrangement for separating contaminants from liquids or vapors
    • 污染物与液体或蒸气分离的方法和装置
    • US08992729B2
    • 2015-03-31
    • US13880274
    • 2011-10-17
    • Carl-Gustav BergHeikki Jaakkola
    • Carl-Gustav BergHeikki Jaakkola
    • D21C11/00D21C11/06D21C11/10
    • D21C11/0092D21C11/06D21C11/103
    • A method and assembly for separating contaminants from liquids, such as condensates, or vapors at an evaporation plant. The contaminants are separated from liquids by stripping when bringing a contaminant-enriched liquid into direct contact with a vapor by spraying or distributing the liquid into the vapor flowing in a vapor duct or onto wall surfaces in the vapor duct thus reducing the contaminant-content of the sprayed liquid and producing a cleaner liquid. The contaminants are enriched in the vapor. From vapors contaminants are separated by absorption when bringing a contaminant-enriched vapor into direct contact with a cleaner liquid by spraying or distributing the liquid into the vapor flowing in a vapor duct or onto wall surfaces in the vapor duct thus increasing the contaminant-content of the liquid, but producing a cleaned vapor.
    • 用于在蒸发设备处分离污染物(例如冷凝物或蒸气)的方法和组件。 当通过喷射或将液体分散到蒸汽管道中蒸发的蒸汽或蒸汽管道中的壁表面上而使富含污染物的液体与蒸汽直接接触时,通过汽提将污染物从液体中分离出来,从而降低了污染物含量 喷雾液体并产生更清洁的液体。 污染物富含蒸气。 蒸气中的污染物通过吸收而分离,当将富含污染物的蒸气与清洁液体直接接触时,通过喷射或将液体分散到蒸汽管道中蒸发的蒸气或蒸汽管道中的壁表面上,从而增加污染物含量 液体,但产生清洁的蒸气。
    • 9. 发明授权
    • Flash tank steam economy improvement
    • US06524436B2
    • 2003-02-25
    • US09999483
    • 2001-12-04
    • Auvo K. KettunenMatti Lautala
    • Auvo K. KettunenMatti Lautala
    • D21C1106
    • D21C11/06
    • By the utilization of a jet ejector (such as a thermocompresser) in a cellulose chemical pulp mill, it is possible to effectively increase the utilization of steam. The volume of steam from a flash tank which flashes black liquor from a pulp digester may be increased (e.g. at least about 10%), while the volume and temperature of the liquor discharged from the flash tank are decreased and its concentration increased, by operatively connecting the jet ejector to the steam discharge from a flash tank. The jet ejector is supplied with higher pressure steam from another source which can result in a low pressure or partial vacuum condition in the flash tank. The flash tank may be a single flash tank or one of a series of flash tanks, and an ejector can be associated with at least another flash tank in the series. The hot spent cooking liquor from the digester can be cooled in a heat exchanger (for example in indirect heat exchange relationship with a fresh cooking liquor) prior to introduction in to the flash tank or series of flash tanks. Alternatively a jet ejector may be used to increase the pressure of a low pressure steam flow in a pulp mill to make it suitable for alternative uses.