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    • 1. 发明授权
    • Raw gas collection system
    • 原始采气系统
    • US09115437B2
    • 2015-08-25
    • US13824969
    • 2011-09-14
    • Anders Kenneth SorhuusGeir WeddeOdd Edgar Bjarno
    • Anders Kenneth SorhuusGeir WeddeOdd Edgar Bjarno
    • C25C3/22F27B14/08F27D17/00
    • C25C3/22F27B14/08F27D17/001F27D17/004Y02P10/122Y02P10/262
    • A raw gas collection system (15) for collecting raw gas from a plurality of aluminum smelting pots (4) is equipped with a plurality of branch ducts (16, 16a-d). Each branch duct (16, 16a-d) is arranged to channel a respective branch flow (32, 32a-b) of raw gas from an aluminum smelting pot (4) to a collecting duct (20a), which is common to and shared by branch ducts (16, 16a-d). Several of the branch ducts (16, 16a-d) are equipped with a combined heat transfer and flow resistance generating element (17) to remove heat from the respective branch flow (32, 32a-b) of raw gas and to balance the flow of raw gas in the raw gas collecting system (15). The combined heat transfer and flow resistance generating elements (17) reduce the need for adjusting the respective branch duct (16, 16a-d) flow volumes using dampers, thereby reducing the power required to transport the raw gas through the system.
    • 用于从多个铝冶炼罐(4)收集原料气体的原料气体收集系统(15)配备有多个分支管道(16,17a-d)。 每个分支管道(16,16a-d)被布置成将来自铝冶炼罐(4)的原料气体的相应分支流(32,32a-b)引导到收集管道(20a),该收集管道共享并共享 通过支管(16,16a-d)。 几个分支管道(16,16a-d)配备有组合的传热和流动阻力产生元件(17),以从原气体的相应分支流(32,32a-b)去除热量并平衡流量 的原料气体收集系统(15)中的原料气体。 组合的传热和流动阻力产生元件(17)减少了使用阻尼器调节各个分支管道(16,17a-d)流量的需要,从而降低了将原料气体输送通过系统所需的功率。
    • 2. 发明申请
    • RAW GAS COLLECTION SYSTEM
    • 原始气体收集系统
    • US20130199939A1
    • 2013-08-08
    • US13824969
    • 2011-09-14
    • Anders Kenneth SorhuusGeir WeddeOdd Edgar Bjarno
    • Anders Kenneth SorhuusGeir WeddeOdd Edgar Bjarno
    • C25C3/22
    • C25C3/22F27B14/08F27D17/001F27D17/004Y02P10/122Y02P10/262
    • A raw gas collection system (15) for collecting raw gas from a plurality of aluminium smelting pots (4) is equipped with a plurality of branch ducts (16, 16a-d). Each branch duct (16, 16a-d) is arranged to channel a respective branch flow (32, 32a-b) of raw gas from an aluminium smelting pot (4) to a collecting duct (20a), which is common to and shared by branch ducts (16, 16a-d). Several of the branch ducts (16, 16a-d) are equipped with a combined heat transfer and flow resistance generating element (17) to remove heat from the respective branch flow (32, 32a-b) of raw gas and to balance the flow of raw gas in the raw gas collecting system (15). The combined heat transfer and flow resistance generating elements (17) reduce the need for adjusting the respective branch duct (16, 16a-d) flow volumes using dampers, thereby reducing the power required to transport the raw gas through the system.
    • 用于从多个铝冶炼罐(4)收集原料气体的原料气体收集系统(15)配备有多个分支管道(16,17a-d)。 每个分支管道(16,16a-d)被布置成将来自铝冶炼罐(4)的原料气体的相应分支流(32,32a-b)引导到收集管道(20a),该收集管道共享并共享 通过支管(16,16a-d)。 几个分支管道(16,16a-d)配备有组合的传热和流动阻力产生元件(17),以从原气体的相应分支流(32,32a-b)去除热量并平衡流量 的原料气体收集系统(15)中的原料气体。 组合的传热和流动阻力产生元件(17)减少了使用阻尼器调节各个分支管道(16,17a-d)流量的需要,从而降低了将原料气体输送通过系统所需的功率。
    • 3. 发明授权
    • Pot heat exchanger
    • 锅式换热器
    • US09360145B2
    • 2016-06-07
    • US13824950
    • 2011-09-01
    • Anders Kenneth SorhuusGeir WeddeOdd Edgar Bjarno
    • Anders Kenneth SorhuusGeir WeddeOdd Edgar Bjarno
    • C25C3/22F16L53/00F27B14/08F27D17/00F28D7/16F28D21/00F28F9/02F28F13/08F28F19/00
    • C25C3/22C25C3/06C25C3/24C25C7/06F16L53/00F27B14/08F27D17/001F27D17/002F27D17/004F28D7/1615F28D7/1653F28D21/0003F28F9/0282F28F13/08F28F19/00Y02P10/262Y10T137/6416
    • A raw gas collection system for collecting raw gas from a plurality of aluminum smelting pots is equipped with a plurality of branch ducts (28d), each of which is arranged to channel a respective branch flow (38d) of raw gas from an aluminum smelting pot to a collection duct (26A), which is common to and shared by the branch ducts (28d). Each of said branch ducts (28d) is, near an outlet (52d) thereof, equipped with a curved section (50d) for aligning the branch flow (38d) with a flow direction of raw gas (27A) already present in the common collection duct (26A), and a constriction (54d) for accelerating the branch flow (38d) through the branch duct outlet (52d) into the common collection duct (26A). Furthermore, each of said branch ducts (28d) is equipped with a heat exchanger (40d) for removing heat from the respective branch flow (38d) of raw gas. The combined flow resistance of the constriction (54d) and the heat exchanger (40d) reduces the need for adjusting the respective branch flows (28d) using dampers, thereby reducing the power required to transport the raw gas.
    • 用于从多个铝冶炼罐收集原料气体的原料气体收集系统装备有多个分支管道(28d),每个分支管道(28d)布置成将来自铝冶炼罐的原料气体的相应分支流(38d) 到由分支管道(28d)共同并共享的收集管道(26A)。 所述分支管道(28d)中的每一个在其出口(52d)的附近都具有弯曲部分(50d),该弯曲部分用于使分支流(38d)与已经存在于公共集合体中的原料气体(27A)的流动方向对齐 (26A)和用于将分支流(38d)通过分支管道出口(52d)加速到共同收集管道(26A)中的收缩部(54d)。 此外,每个所述分支管道(28d)配备有用于从原料气体的各个分支流(38d)除去热量的热交换器(40d)。 收缩部(54d)和热交换器(40d)的组合流动阻力减少了使用阻尼器调节各个分支流(28d)的需要,从而降低了输送原料气体所需的功率。
    • 4. 发明申请
    • POT HEAT EXCHANGER
    • 锅热交换器
    • US20130213494A1
    • 2013-08-22
    • US13824950
    • 2011-09-01
    • Anders Kenneth SorhuusGeir WeddeOdd Edgar Bjarno
    • Anders Kenneth SorhuusGeir WeddeOdd Edgar Bjarno
    • F16L53/00
    • C25C3/22C25C3/06C25C3/24C25C7/06F16L53/00F27B14/08F27D17/001F27D17/002F27D17/004F28D7/1615F28D7/1653F28D21/0003F28F9/0282F28F13/08F28F19/00Y02P10/262Y10T137/6416
    • A raw gas collection system for collecting raw gas from a plurality of aluminium smelting pots is equipped with a plurality of branch ducts (28d), each of which is arranged to channel a respective branch flow (38d) of raw gas from an aluminium smelting pot to a collection duct (26A), which is common to and shared by the branch ducts (28d). Each of said branch ducts (28d) is, near an outlet (52d) thereof, equipped with a curved section (50d) for aligning the branch flow (38d) with a flow direction of raw gas (27A) already present in the common collection duct (26A), and a constriction (54d) for accelerating the branch flow (38d) through the branch duct outlet (52d) into the common collection duct (26A). Furthermore, each of said branch ducts (28d) is equipped with a heat exchanger (40d) for removing heat from the respective branch flow (38d) of raw gas. The combined flow resistance of the constriction (54d) and the heat exchanger (40d) reduces the need for adjusting the respective branch flows (28d) using dampers, thereby reducing the power required to transport the raw gas.
    • 用于从多个铝冶炼罐收集原料气体的原料气体收集系统装备有多个分支管道(28d),每个分支管道(28d)布置成将来自铝冶炼罐的原料气体的相应分支流(38d) 到由分支管道(28d)共同并共享的收集管道(26A)。 所述分支管道(28d)中的每一个在其出口(52d)的附近都具有弯曲部分(50d),该弯曲部分用于使分支流(38d)与已经存在于公共集合体中的原料气体(27A)的流动方向对齐 (26A)和用于将分支流(38d)通过分支管道出口(52d)加速到共同收集管道(26A)中的收缩部(54d)。 此外,每个所述分支管道(28d)配备有用于从原料气体的各个分支流(38d)除去热量的热交换器(40d)。 收缩部(54d)和热交换器(40d)的组合流动阻力减少了使用阻尼器调节各个分支流(28d)的需要,从而降低了输送原料气体所需的功率。
    • 6. 发明授权
    • Screening device and method of screening
    • 筛选装置及筛选方法
    • US09033155B2
    • 2015-05-19
    • US13807763
    • 2011-06-28
    • Anders Kenneth Sorhuus
    • Anders Kenneth Sorhuus
    • B07B9/00B07B1/00B03B4/06B07B1/04B07B4/08
    • B07B1/00B03B4/06B07B1/04B07B4/08
    • A screening device (1) comprises a first compartment (3) for receiving solid particulate material, a second compartment (5) for receiving screened particulates from said first compartment (3), a perforated wall (7) separating the first (3) and second (5) compartments from each other for screening the solid particulate material into at least two particulate size-dependent fractions, and a gas permeable layer (21) for fluidization of particulates in said first compartment (3). The first compartment (3) is provided with a solid particulate material inlet (9) located at a first end (22) of screening device (1), and a particulate material outlet (11) located at a second end (24) of screening device (1), with perforated wall (7) extending from first end (22) to second end (24) of screening device (1), enabling simultaneous transport and screening of at least a portion of said solid particulate material.
    • 筛选装置(1)包括用于接收固体颗粒材料的第一隔室(3),用于接收来自所述第一隔室(3)的筛选微粒的第二隔室(5),将第一隔室(3)和 用于将固体颗粒材料筛选成至少两个颗粒尺寸依赖级分的第二(5)隔室和用于使所述第一隔室(3)中的颗粒流态化的气体渗透层(21)。 第一隔室(3)设置有位于筛选装置(1)的第一端(22)处的固体颗粒材料入口(9)和位于筛选的第二端(24)处的颗粒材料出口(11) 装置(1)具有从筛网装置(1)的第一端(22)延伸到第二端(24)的穿孔壁(7),能够同时输送和筛选至少一部分固体颗粒材料。
    • 8. 发明申请
    • SCREENING DEVICE AND METHOD OF SCREENING
    • 筛选装置和筛选方法
    • US20130206649A1
    • 2013-08-15
    • US13807763
    • 2011-06-28
    • Anders Kenneth Sorhuus
    • Anders Kenneth Sorhuus
    • B07B1/00
    • B07B1/00B03B4/06B07B1/04B07B4/08
    • A screening device (1) comprises a first compartment (3) for receiving solid particulate material, a second compartment (5) for receiving screened particulates from said first compartment (3), a perforated wall (7) separating the first (3) and second (5) compartments from each other for screening the solid particulate material into at least two particulate size-dependent N fractions, and a gas permeable layer (21) for fluidization of particulates in said first compartment (3). The first compartment (3) is provided with a solid particulate material inlet (9) located at a first end (22) of screening device (1), and a particulate material outlet (11) located at a second end (24) of screening device (1), with perforated wall (7) extending from first end (22) to second end (24) of screening device (1), enabling simultaneous transport and screening of at least a portion of said solid particulate material.
    • 筛选装置(1)包括用于接收固体颗粒材料的第一隔室(3),用于接收来自所述第一隔室(3)的筛选微粒的第二隔室(5),将第一隔室(3)和 用于将固体颗粒材料筛选成至少两种颗粒尺寸依赖性N级分的第二(5)隔室和用于使所述第一隔室(3)中的颗粒流化的气体渗透层(21)。 第一隔室(3)设置有位于筛选装置(1)的第一端(22)处的固体颗粒材料入口(9)和位于筛选的第二端(24)处的颗粒材料出口(11) 装置(1)具有从筛网装置(1)的第一端(22)延伸到第二端(24)的穿孔壁(7),能够同时输送和筛选至少一部分固体颗粒材料。