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    • 1. 发明授权
    • Wet flue-gas desulfurization equipment
    • 湿式烟气脱硫设备
    • US08496742B2
    • 2013-07-30
    • US12519551
    • 2007-09-19
    • Tomoyuki KonishiTakanori NakamotoKouji MuramotoHiroyuki NosakaAtsushi KatagawaTakuro Ueda
    • Tomoyuki KonishiTakanori NakamotoKouji MuramotoHiroyuki NosakaAtsushi KatagawaTakuro Ueda
    • B01D53/14
    • B01D53/18B01D53/504B01D2257/302
    • In an absorbing tower including an absorption unit of relatively small diameter capable of absorption and removal by an absorbent slurry for exhaust gas purification and a tank unit of relatively large diameter for temporarily storing the absorbent slurry flowing down from the absorption unit, the tank unit and the absorption unit are joined together by a conical member. By disposing an entrance flue at the conical member, a distance from an upper portion of the conical member to a spray header is shortened, and a height of the absorbing tower can be reduced accordingly. By extending a front end of the entrance flue to the absorption unit into which droplets of the absorbent slurry fall, a high-temperature exhaust gas from a boiler, etc., that has passed through the entrance flue, is made to pass through a circumference of the conical member so that an inexpensive material can be used in the conical member.
    • 在具有能够通过用于排气净化的吸收剂浆料吸收除去的相对小直径的吸收单元的吸收塔和用于临时储存从吸收单元向下流动的吸收剂浆料的相对较大直径的罐单元, 吸收单元通过锥形构件连接在一起。 通过在锥形构件处设置入口烟道,缩短了从锥形构件的上部到喷雾头的距离,并且可以相应地减小吸收塔的高度。 通过将入口烟道的前端延伸到吸收剂浆液滴下的吸收单元中,使已经通过入口烟道的来自锅炉等的高温废气通过圆周 的锥形构件,使得可以在锥形构件中使用便宜的材料。
    • 2. 发明授权
    • Wet-type exhaust desulfurizing apparatus
    • 湿式排气脱硫装置
    • US08172931B2
    • 2012-05-08
    • US12441648
    • 2007-09-19
    • Takuro UedaTakanori NakamotoAtsushi KatagawaHajime OkuraHiroshi Ishizaka
    • Takuro UedaTakanori NakamotoAtsushi KatagawaHajime OkuraHiroshi Ishizaka
    • B01D47/06
    • B01D53/504B01D53/185B01D2251/404B01D2251/608B01D2257/2045B01D2257/2047
    • An absorbing tower is provided in its side wall with a gas entrance for introducing a combustion exhaust gas into the absorbing tower, and an absorbing liquid is sprayed from the nozzles of a spray header into the exhaust gas introduced to rise from the gas entrance. A trough is arranged in the side wall of the absorbing tower and above the gas entrance, and a nose having a horseshoe shape in a top plan view and extending into tower is disposed in the tower side wall portion of the gas entrance other than the portion arranging the trough and at the same or at substantially the same height as the portion of the trough. The absorbing liquid, which is sprayed from the nozzle and drops along the absorbing tower wall portion, is rescattered to the center portion of the absorbing tower excepting the entrance of the absorbing tower, so that the gas-liquid contact efficiency is improved while suppressing an increase in pressure loss, thereby to prevent the drift of the gas at the tower wall portion.
    • 吸收塔在其侧壁上设置有用于将燃烧废气引入吸收塔的气体入口,并且吸收液体从喷雾头的喷嘴喷射到从气体入口引入的废气中。 在吸收塔的侧壁和气体入口的上方布置有槽,并且在顶部平面图中具有马蹄形并延伸到塔的鼻子设置在除了部分之外的气体入口的塔侧壁部分 布置槽并且与槽的部分处于相同或基本上相同的高度。 从喷嘴喷射并沿着吸收塔壁部滴下的吸收液被除去吸收塔的入口以外的吸收塔的中心部分,从而提高气液接触效率,同时抑制气液接触效率 增加压力损失,从而防止塔壁部分处的气体漂移。
    • 3. 发明申请
    • WET-TYPE EXHAUST DESULFURIZING APPARATUS
    • 湿式脱水装置
    • US20090320687A1
    • 2009-12-31
    • US12441648
    • 2007-09-19
    • Takuro UedaTakanori NakamotoAtsushi KatagawaHajime OkuraHiroshi Ishizaka
    • Takuro UedaTakanori NakamotoAtsushi KatagawaHajime OkuraHiroshi Ishizaka
    • B01D53/18
    • B01D53/504B01D53/185B01D2251/404B01D2251/608B01D2257/2045B01D2257/2047
    • An absorbing tower is provided in its side wall with a gas entrance for introducing a combustion exhaust gas into the absorbing tower, and an absorbing liquid is sprayed from the nozzles of a spray header into the exhaust gas introduced to rise from the gas entrance. A trough is arranged in the side wall of the absorbing tower and above the gas entrance, and a nose having a horseshoe shape in a top plan view and extending into tower is disposed in the tower side wall portion of the gas entrance other than the portion arranging the trough and at the same or at substantially the same height as the portion of the trough. The absorbing liquid, which is sprayed from the nozzle and drops along the absorbing tower wall portion, is rescattered to the center portion of the absorbing tower excepting the entrance of the absorbing tower, so that the gas-liquid contact efficiency is improved while suppressing an increase in pressure loss, thereby to prevent the drift of the gas at the tower wall portion.
    • 吸收塔在其侧壁上设置有用于将燃烧废气引入吸收塔的气体入口,并且吸收液体从喷雾头的喷嘴喷射到从气体入口引入的废气中。 在吸收塔的侧壁和气体入口的上方布置有槽,并且在顶部平面图中具有马蹄形并延伸到塔的鼻子设置在除了部分之外的气体入口的塔侧壁部分 布置槽并且与槽的部分处于相同或基本上相同的高度。 从喷嘴喷射并沿着吸收塔壁部滴下的吸收液被除去吸收塔的入口以外的吸收塔的中心部分,从而提高气液接触效率,同时抑制气液接触效率 增加压力损失,从而防止塔壁部分处的气体漂移。
    • 8. 发明授权
    • Wet flue-gas desulfurization apparatus and method of wet flue-gas desulfurization
    • 湿式烟气脱硫装置及湿式烟气脱硫方法
    • US07731926B2
    • 2010-06-08
    • US12092787
    • 2006-09-20
    • Naoki OdaTakanori NakamotoHiroyuki Nosaka
    • Naoki OdaTakanori NakamotoHiroyuki Nosaka
    • B01D53/50B01D53/77
    • B01D53/504
    • Flue gas of boiler is introduced through gas inlet part of flue-gas desulfurization apparatus, and absorbent liquid sprayed from spray nozzle is trapped in recirculation tank. There, agitation is performed by oxidation agitator to thereby oxidize SO2 absorbed from the flue gas into gypsum. In the tank, oxidation air is fed from posterior air pipe and anterior air pipe behind and ahead of liquid propulsion by the propeller. Thus, even when the amount of oxidation air must be increased in accordance with an increase of boiler load, the oxidation efficiency can be enhanced without increasing the number of agitators. Then the apparatus with which even when the amount of oxidation air fed to the liquid trapping section is increased, highly efficient oxidation can be performed without increasing the number of agitators installed and the operating cost.
    • 锅炉烟气通过烟气脱硫装置的进气部分引入,喷嘴吸收液体被吸入回流罐。 在那里,通过氧化搅拌器进行搅拌,从而将从废气吸收的SO 2氧化成石膏。 在坦克中,氧化空气从后空气管道和前空气管道通过螺旋桨进入液体推进器的后面和前面。 因此,即使必须根据锅炉负荷的增加来增加氧化空气的量,可以提高氧化效率而不增加搅拌器的数量。 然后即使当供给到液体捕获部分的氧化空气的量增加时,也可以进行高效氧化,而不增加安装的搅拌器的数量和操作成本。
    • 10. 发明申请
    • WET FLUE-GAS DESULFURIZATION APPARATUS AND METHOD OF WET FLUE-GAS DESULFURIZATION
    • 湿气脱硫装置和湿气脱硫方法
    • US20090263305A1
    • 2009-10-22
    • US12092787
    • 2006-09-20
    • Naoki OdaTakanori NakamotoHiroyuki Nosaka
    • Naoki OdaTakanori NakamotoHiroyuki Nosaka
    • B01D53/50B01D53/34
    • B01D53/504
    • Exhaust (Flue) gas of boiler is introduced through gas inlet part (port) (2) of flue-gas desulfurization apparatus (system), and absorbent liquid sprayed from spray nozzle (5) of absorbent liquid spray section (4) is trapped (stored) in liquid trapping (recirculation tank) section (7). There, agitation is performed by means of propeller (11) of oxidation agitator (8) to thereby oxidize SO2 absorbed from the exhaust (flue) gas into gypsum. In the liquid trapping section (7), oxidation air is fed from posterior air pipe (10) and anterior air pipe (13) behind and ahead of liquid propulsion (to the rear and front of a liquid discharge) by the propeller (11). Thus, even when the amount of oxidation air must be increased in accordance with an increase of boiler load, the oxidation efficiency can be enhanced without increasing of the number of agitators. Accordingly, there can be provided a wet flue-gas desulfurization apparatus (system) and method with which even when the amount of oxidation air fed to the liquid trapping section is increased, highly efficient oxidation can be performed without increasing the number of agitators installed and the operating cost.
    • 锅炉排气(烟气)通过烟道气脱硫装置(系统)的气体入口部分(2)引入,吸收液喷雾部分(4)的喷嘴(5)喷射的吸收剂液体被捕获( 储存)在液体捕集(再循环罐)部分(7)中。 在那里,通过氧化搅拌器(8)的螺旋桨(11)进行搅拌,从而将从废气(烟道)气体吸收的SO 2氧化成石膏。 在液体捕集部分(7)中,螺旋桨(11)从后空气管道(10)和前空气管道(13)向液体推进(在液体排放物的后部和前部)的前方和前方供给氧化空气, 。 因此,即使根据锅炉负荷的增加必须增加氧化空气的量,也可以在不增加搅拌器的数量的情况下提高氧化效率。 因此,可以提供一种湿式烟道气脱硫装置(系统)和方法,即使在供给到液体捕集部的氧化空气量增加的情况下也能够进行高效氧化,而不会增加安装的搅拌器的数量, 经营成本。