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    • 1. 发明申请
    • Fabric Filter With Fluidised Dust-Bed, and a Method of Maintaining It
    • 带流化床的织物过滤器及其维护方法
    • US20090266234A1
    • 2009-10-29
    • US12084924
    • 2006-12-12
    • Stefan AhmanNils Bringfors
    • Stefan AhmanNils Bringfors
    • B01D35/12B01D46/02B01D46/46B01D46/48
    • B01D46/04B01D46/0013B01D46/002B01D46/0058B01D46/48
    • A fabric filter (1) has at least a first compartment (2) and a second compartment (4). A hopper (42) is adapted for fluidisation of dust collected in the compartments (2, 4) to form a bed (52) of fluidised dust. A partition wall (62) is located between the compartments (2, 4) to separate them from each other. A passage (68) is formed at a lower end (66) of the partition wall (62) such that fluidised dust may pass through said passage (68). The partition wall (62) is arranged to extend into the bed (52) of fluidised dust for forming a seal (74) even when one of the compartments (2, 4) has been shut off. When shutting off a compartment (4) the inlets and outlets to that compartment (4) are closed and the dust in the hopper (42) is fluidised to provide a seal (74) between the compartments (2, 4).
    • 织物过滤器(1)至少具有第一隔室(2)和第二隔室(4)。 料斗(42)适于使收集在隔室(2,4)中的灰尘流化,以形成流化灰尘的床(52)。 分隔壁(62)位于隔室(2,4)之间,以将它们彼此分开。 在分隔壁(62)的下端(66)处形成通道(68),使得流化灰尘可以通过所述通道(68)。 分隔壁(62)被布置成即使当隔室(2,4)中的一个已经被切断时,其也延伸到流化灰尘的床(52)中以形成密封件(74)。 当关闭隔室(4)时,关闭该隔间(4)的入口和出口,并且将料斗(42)中的灰尘流化以在隔间(2,4)之间提供密封件(74)。
    • 2. 发明授权
    • Fabric filter with fluidised dust-bed, and a method of maintaining it
    • 带流化床的织物过滤器及其维护方法
    • US07972399B2
    • 2011-07-05
    • US12084924
    • 2006-12-12
    • Stefan AhmanNils Bringfors
    • Stefan AhmanNils Bringfors
    • B01D46/02B01D46/44
    • B01D46/04B01D46/0013B01D46/002B01D46/0058B01D46/48
    • A fabric filter (1) has at least a first compartment (2) and a second compartment (4). A hopper (42) is adapted for fluidisation of dust collected in the compartments (2, 4) to form a bed (52) of fluidised dust. A partition wall (62) is located between the compartments (2, 4) to separate them from each other. A passage (68) is formed at a lower end (66) of the partition wall (62) such that fluidised dust may pass through said passage (68). The partition wall (62) is arranged to extend into the bed (52) of fluidised dust for forming a seal (74) even when one of the compartments (2, 4) has been shut off. When shutting off a compartment (4) the inlets and outlets to that compartment (4) are closed and the dust in the hopper (42) is fluidised to provide a seal (74) between the compartments (2, 4).
    • 织物过滤器(1)至少具有第一隔室(2)和第二隔室(4)。 料斗(42)适于使收集在隔室(2,4)中的灰尘流化,以形成流化灰尘的床(52)。 分隔壁(62)位于隔室(2,4)之间,以将它们彼此分开。 在分隔壁(62)的下端(66)处形成通道(68),使得流化灰尘可以通过所述通道(68)。 分隔壁(62)被布置成即使当隔室(2,4)中的一个已经被切断时,其也延伸到流化灰尘的床(52)中以形成密封件(74)。 当关闭隔室(4)时,关闭该隔间(4)的入口和出口,并且将料斗(42)中的灰尘流化以在隔间(2,4)之间提供密封件(74)。
    • 3. 发明授权
    • Method and device for separating gaseous pollutants from hot process gases by absorption and a mixer for moistening particulate dust
    • 通过吸收将气态污染物与热过程气体分离的方法和装置,以及用于润湿颗粒物的混合器
    • US07387662B2
    • 2008-06-17
    • US10527877
    • 2003-09-17
    • Stefan AhmanNils Bringfors
    • Stefan AhmanNils Bringfors
    • B01D53/50B01D53/83
    • 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)。
    • 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
    • 通过吸收将气态污染物与热过程气体分离的方法和装置,以及用于润湿颗粒物的混合器
    • US20050244317A1
    • 2005-11-03
    • US10527877
    • 2003-09-17
    • Stefan AhmanNils Bringfors
    • Stefan AhmanNils Bringfors
    • B01D53/50B01F3/12B01F7/00B01F7/02B01F15/00B01F15/06C01F3/00
    • 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)。