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    • 1. 发明申请
    • METHOD FOR SEPARATING GASEOUS POLLUTANTS FROM HOT PROCESS GASES
    • 从热过程气体中分离气体污染物的方法
    • WO1996016722A1
    • 1996-06-06
    • PCT/SE1995001403
    • 1995-11-24
    • ABB FLÄKT ABÅHMAN, StefanBRINGFORS, Nils
    • ABB FLÄKT AB
    • B01D53/81
    • B01D53/508B01D53/81
    • Hot process gases are passed through a contact reactor (10), in which a particulate absorbent material, which is reactive with gaseous pollutants in the gases, is introduced into the gases to convert the gaseous pollutants into separable dust. The process gases are then passed through a dust separator (5). The major part of the dust separated in the dust separator (5) is passed to a mixer (11), in which it is mixed and moistened, whereupon it is recirculated as absorbent material by being introduced, together with fresh absorbent, into the process gases. Burnt lime is added as fresh absorbent. The dust is kept so long in the mixer and recirculated so many times that the total residence time of the burnt lime in the mixer in moistened state is sufficiently long for the burnt lime to react substantially completely with water supplied to the mixer and form slaked lime.
    • 热处理气体通过接触反应器(10),其中与气体中的气态污染物反应的颗粒状吸收材料被引入到气体中以将气态污染物转化成可分离的灰尘。 然后将工艺气体通过灰尘分离器(5)。 在灰尘分离器(5)中分离的灰尘的主要部分被送入混合器(11),在混合器(11)中混合并润湿,随后将其与新鲜吸收剂一起引入到该过程中作为吸收材料再循环 气体。 添加生石灰作为新鲜吸收剂。 灰尘在搅拌机中保持如此长时间,再循环多次,使润湿状态下混合器中生石灰的总停留时间足够长,以使生石灰与供给混合器的水基本完全反应,并形成熟石灰 。
    • 3. 发明申请
    • OXIDATION PROCESS
    • 氧化工艺
    • WO1994029003A1
    • 1994-12-22
    • PCT/SE1994000489
    • 1994-05-25
    • ABB FLÄKT ABBRINGFORS, Nils
    • ABB FLÄKT AB
    • B01D53/34
    • C01F11/464B01D53/502C01P2004/61
    • A process for oxidizing a sulphite-ion-containing and/or hydrogen-sulphite-ion-containing aqueous solution in the presence of lime, preferably in wet flue-gas desulphurisation. In the process, lime, preferably calcium carbonate, is added to at least a part of the aqueous solution, and this part of the solution is then contacted with an oxygen-containing gas, such as air, before any precipitation of calcium sulphite has occurred. The oxygen-containing gas should be blown into the solution within 1 min of the addition of lime, preferably within 30 s, and most preferred within 5 s. It is further preferred that the solution be vigorously agitated, e.g. by means of a stirrer or a pump, when the process is implemented. The added lime should have a minimal particle size, and the average particle size preferably should not exceed about 30 mu m. It is preferred that the process be implemented at a temperature of about 40-60 DEG C.
    • 一种在石灰存在下氧化含亚硫酸根离子和/或含亚硫酸氢离子的水溶液的方法,优选在湿式烟道气脱硫中。 在此过程中,将石灰,优选碳酸钙加入到至少一部分水溶液中,然后在发生亚硫酸钙沉淀之前,将该部分溶液与含氧气体如空气接触, 。 在加入石灰的1分钟内,优选在30秒内,最好在5秒内将含氧气体吹入溶液中。 进一步优选的是剧烈搅拌溶液。 通过搅拌器或泵,当实施该过程时。 添加的石灰应具有最小的粒度,平均粒径优选不超过约30μm。 该方法优选在约40-60℃的温度下进行。
    • 4. 发明申请
    • METHOD AND DEVICE FOR SEPARATING GASEOUS POLLUTANTS FROM HOT PROCESS GASES BY ABSORPTION AND A MIXER FOR MOISTENING PARTICULATE DUST
    • 用于通过吸收从热过程气体分离气体污染物的方法和装置以及用于搅拌颗粒剂的混合器
    • WO2004026443A1
    • 2004-04-01
    • PCT/SE2003/001453
    • 2003-09-17
    • ALSTOM (SWITZERLAND) LTD.ÅHMAN, StefanBRINGFORS, Nils
    • ÅHMAN, StefanBRINGFORS, Nils
    • B01D53/50
    • B01F3/1271B01D53/508B01F3/1228B01F7/00908B01F7/022B01F15/00863B01F15/063
    • In a method of separating gaseous pollutants from hot process gases, the process gases are passed through a contact reactor (22), in which an absorbent material in a moistened state is introduced to convert the gaseous pollutants into separable dust. The dust is separated in a dust separator (10). The separated dust is cooled in a first step by being brought into direct contact with a cooling fluid. In a second step, the cooled dust is mixed with a gas containing water vapour, said gas having a saturation temperature that is higher than the temperature of the cooled dust. The dust moistened by condensation of the water vapour is introduced into the contact reactor (22) to be mixed with the process gases. A mixer (24) for moistening of absorbent material has a first end (26) and a second end (28) and is divided into two zones. A first zone is a cooling zone (68) located at the first end (26). A second zone is a moistening zone (80) located at the second end (28).
    • 在将气体污染物与热处理气体分离的方法中,工艺气体通过接触反应器(22),其中引入湿润状态的吸收材料以将气态污染物转化成可分离的粉尘。 灰尘在灰尘分离器(10)中分离。 分离的灰尘通过与冷却流体直接接触而在第一步骤中冷却。 在第二步骤中,将冷却的灰尘与含有水蒸气的气体混合,所述气体的饱和温度高于冷却的粉尘的温度。 通过水蒸汽冷凝润湿的灰尘被引入到接触反应器(22)中以与工艺气体混合。 用于润湿吸收材料的混合器(24)具有第一端(26)和第二端(28),并被分成两个区域。 第一区域是位于第一端(26)处的冷却区(68)。 第二区域是位于第二端(28)处的润湿区(80)。
    • 5. 发明申请
    • APPARATUS FOR CLEANING GAS
    • 清洁气体的装置
    • WO1994008700A1
    • 1994-04-28
    • PCT/SE1993000810
    • 1993-10-06
    • ABB FLÄKT ABBRINGFORS, Nils
    • ABB FLÄKT AB
    • B01D53/34
    • B05B7/066B01D53/504B05B7/0466B05B7/0807
    • A nozzle (12a, 12b, 12c) for atomizing a liquid, optionally containing suspended dry matter, by means of compressed gas, comprises, an inlet (32b) for liquid, an inlet (31b) for compressed gas, and an outlet (41) for gas mixed with finely divided liquid, as well as an intermediate mixing space (51). The inlet (31b) for compressed gas is adapted to give the gas a substantially rectilinear path through the mixing space (51). The inlet (32b) for the liquid is separated from the mixing space (51) by a partition (32) having a plurality of first holes (38) for introducing the liquid into the mixing space (51) in a direction substantially perpendicular to the main flow direction of the gas in the mixing space (51). The mixing space (51) is defined downstream by a wall (35) having a plurality of second holes (39). An inlet device (11a, 11b, 11c) comprising the inlet (31b) for compressed gas and the inlet (32b) for liquid consists of two concentric tubes (31, 32). The inlet (32b) for liquid consists of the inner tube (32). The inlet (31b) for compressed gas consists of the annular conduit (31b) between the concentric tubes (31, 32). The inner tube (32) is closed in the axial direction downstream of the first holes (38) provided for introducing the liquid into the mixing space (51). A convergent channel (57) connects the mixing space (51) to the outlet (41).
    • 用于通过压缩气体雾化任选地含有悬浮干物质的液体的喷嘴(12a,12b,12c)包括:用于液体的入口(32b),用于压缩气体的入口(31b)和出口(41 )和与中间混合空间(51)混合的气体。 用于压缩气体的入口(31b)适于使气体通过混合空间(51)的基本上直线的路径。 用于液体的入口(32b)通过具有多个第一孔(38)的分隔件(32)与混合空间(51)分开,用于将液体沿基本垂直于 气体在混合空间(51)中的主流动方向。 混合空间(51)由具有多个第二孔(39)的壁(35)限定在下游。 包括用于压缩气体的入口(31b)和用于液体的入口(32b)的入口装置(11a,11b,11c)由两个同心管(31,32)组成。 用于液体的入口(32b)由内管(32)组成。 用于压缩气体的入口(31b)由在同心管(31,32)之间的环形导管(31b)组成。 内管(32)在用于将液体引入混合空间(51)中的第一孔(38)的下游沿轴向封闭。 收敛通道(57)将混合空间(51)连接到出口(41)。
    • 6. 发明申请
    • DEVICE FOR DISCHARGING AND DISTRIBUTING AN ABSORBENT MATERIAL IN A FLUE GAS DUCT
    • 用于排放和分配烟气中的吸收材料的装置
    • WO1997037747A1
    • 1997-10-16
    • PCT/SE1997000444
    • 1997-03-17
    • ABB FLÄKT ABÅHMAN, StefanBRINGFORS, NilsJOHANSSON, Lars-Erik
    • ABB FLÄKT AB
    • B01D53/81
    • B01D53/508B01D53/83
    • In a vertical flue gas duct (10), in which flue gases containing gaseous pollutants are to be conducted upwards, a discharging and distributing device is arranged. The device is adapted to discharge and distribute a particulate absorbent material which is reactive with the gaseous pollutants in the flue gases and which, during cleaning of the flue gases, is to be introduced into these gases in moistened state in order to convert the gaseous pollutants to separable dust. The device comprises at least one distributing plate (35) which extends obliquely downwards in the flue gas duct (10) and which is adapted to receive on its upper side moistened absorbent material and which has two well-defined side edges converging obliquely downwards seen in the direction of inclination.
    • 在其中将含有气态污染物的烟道气向上导入的立式烟气管道(10)中,布置有排放和分配装置。 该装置适于排放和分布与废气中的气态污染物反应的颗粒状吸收材料,并且在烟道气的清洁期间,将其以湿润状态引入这些气体中以便将气态污染物 可分离的灰尘。 该装置包括至少一个分配板(35),其在烟道气管道(10)中向下倾斜延伸,并且适于在其上侧容纳润湿的吸收材料,并且具有两个明确限定的侧边缘,其倾斜向下收敛 倾向的方向
    • 7. 发明申请
    • METHOD AND APPARATUS FOR CLEANING FLUE GAS
    • 清洁气体的方法和装置
    • WO1991008042A1
    • 1991-06-13
    • PCT/SE1990000766
    • 1990-11-23
    • ABB FLÄKT AKTIEBOLAGBRINGFORS, NilsJOHANSSON, Lars-ErikÅHMAN, Stefan
    • ABB FLÄKT AKTIEBOLAG
    • B01D53/34
    • B01D53/508F23J15/003
    • In a method and an apparatus for cleaning a process gas, such as flue gas, of gaseous pollutants, such as sulphur dioxide, the gas is contacted in a space (5) with a particulate absorbent, such as lime, which is reactive with said gaseous pollutants, for conversion of said pollutants into separable, particulate pollutants. First the particles of the absorbent are dispersed by means of a means (20) in a carrier gas, such as air, said means communicating with at least one Venturi device (6) positioned in said space (5) and having a convergent inlet portion, at least one intake opening arranged downstream of the inlet portion and an outlet portion. Then the carrier gas and the particles dispersed therein are accelerated in said inlet portion and are at high velocity by means of said intake opening contacted with a pressurised flow of liquid, such as water, which is finely divided on the surface of said particles, before the particles are supplied to the process gas by means of said outlet portion.
    • 在用于清洁气态污染物(例如二氧化硫)的工艺气体(例如烟道气)的方法和装置中,气体在空间(5)中与颗粒状吸收剂例如石灰接触,所述颗粒吸收剂可与所述 气态污染物,用于将所述污染物转化为可分离的颗粒污染物。 首先,吸收剂的颗粒通过在诸如空气的载气中的装置(20)分散,所述装置与位于所述空间(5)中的至少一个文丘里装置(6)连通并且具有会聚进口部分 ,至少一个进气口布置在入口部分的下游和出口部分。 然后,载体气体和分散在其中的颗粒在所述入口部分被加速,并且通过所述吸入开口在与所述颗粒的表面上被细分的加压的液体流如水接触的高速下被加速 通过所述出口部分将颗粒供给到处理气体。