公开(公告)号：US5503660A

公开(公告)日：1996-04-02

申请号：US252518

申请日：1994-06-01

申请人： Rainer Reimert ,  Karel Vydra

发明人： Rainer Reimert ,  Karel Vydra

IPC分类号： A01N43/30 ,  A01N37/50 ,  A01N43/54 ,  A01N43/60 ,  A01N43/653 ,  A01N43/84 ,  A01N47/26 ,  A01N47/38 ,  A01N55/10 ,  A01P3/00 ,  B01D45/06 ,  B01D46/30 ,  B01D50/00 ,  C10J3/84

CPC分类号： B01D46/30 ,  B01D45/06 ,  B01D50/002 ,  C10J3/84 ,  C10K1/026 ,  C10K1/20 ,  C10J2300/0956 ,  C10J2300/1223 ,  Y10S48/02

摘要： The hot raw gas, which contains slag droplets is conducted downwardly in an entrance chamber of a slag separator through a first bed of packings into a flow-deflecting space, in which the raw gas is upwardly deflected and then flows upwardly in an exit chamber through a second bed of packings to a gas outlet. The effective velocity of flow of the raw gas in the first bed is 1.5 to 10 times its effective velocity of flow in the second bed. Liquid slag is drained from the flow-deflecting space.

摘要翻译： 含有矿渣液滴的热原料气体通过第一填料床在炉渣分离器的入口室中向下进入流动偏转空间，在该空气流中，原料气体向上偏转，然后在出口室中通过 第二个填料床到气体出口。 第一床中原料气体的有效流速为其在第二床中的有效流速的1.5至10倍。 液体渣从流动偏转空间排出。

公开(公告)号：US3997655A

公开(公告)日：1976-12-14

申请号：US618192

申请日：1975-09-30

申请人： Lothar Reh ,  Karl-Heinz Dorr ,  Hugo Grimm ,  Karel Vydra

发明人： Lothar Reh ,  Karl-Heinz Dorr ,  Hugo Grimm ,  Karel Vydra

IPC分类号： C01B17/765 ,  C01B17/76

CPC分类号： C01B17/765

摘要： Gases having a high SO.sub.2 content are catalytically reacted in a contacting zone having a plurality of series-connected contacting trays. A partial stream of partly reacted gases from the contacting zone containing SO.sub.3 is admixed with the SO.sub.2 containing gas before entering the first contacting tray. The gases are subjected to interstage cooling between contacting trays. At least a portion of the partly reacted gases is passed through an absorber prior to mixing with the feed stock gas having a high SO.sub.2 content. The rate at which SO.sub.3 is absorbed is increased in dependence on the loss of catalyst activity in the contacting zones such that the conversion of SO.sub.2 to SO.sub.3 in the contacting trays remains approximately constant.

摘要翻译： 具有高SO 2含量的气体在具有多个串联连接的接触盘的接触区中催化反应。 在进入第一接触盘之前，将含有SO 3的接触区的部分反应气体的部分气体与含SO 2的气体混合。 气体在接触盘之间经历级间冷却。 在与具有高SO 2含量的原料气体混合之前，部分反应的气体的至少一部分通过吸收器。 吸收SO 3的速率依赖于接触区中催化剂活性的损失而增加，使得接触塔盘中的SO 2转化为SO 3保持近似恒定。

公开(公告)号：US4016248A

公开(公告)日：1977-04-05

申请号：US662168

申请日：1976-02-27

申请人： Karel Vydra ,  Zdenek Hubalek

发明人： Karel Vydra ,  Zdenek Hubalek

IPC分类号： C01B17/765 ,  C01B17/68 ,  C01B17/76

CPC分类号： C01B17/765

摘要： A process for the catalytic conversion of SO.sub.2 to SO.sub.3 wherein a main stream of SO.sub.2 -containing gas is branched to form a partial stream which is admixed with an oxygen-containing gas and brought to the temperature of the first contact hurdle or stage. The effluent therefrom is mixed with the remainder of the SO.sub.2 -containing gas and is fed to the second contact hurdle or stage. The oxgyen-containing gas is added in an amount sufficient to reduce the SO.sub.2 concentration so that a temperature can be used in the first stage which corresponds to the SO.sub.2 +1/2 O.sub.2 .revreaction.SO.sub.3 equilibrium.

摘要翻译： 用于将SO 2催化转化为SO 3的方法，其中含SO 2的气体的主流被分支以形成与含氧气体混合并达到第一接触障碍物或阶段的温度的部分物流。 将其流出物与剩余的含SO 2的气体混合并进料到第二接触障碍物或级。 添加含氧气体的量足以降低SO 2浓度，使得可以在对应于SO 2 + 1 / 2O 2→SO 3平衡的第一阶段中使用温度。

公开(公告)号：US4144051A

公开(公告)日：1979-03-13

申请号：US823856

申请日：1977-08-11

申请人： Martin Rahn ,  Lothar Reh ,  Bernd Thone ,  Karel Vydra

发明人： Martin Rahn ,  Lothar Reh ,  Bernd Thone ,  Karel Vydra

IPC分类号： C22B1/02 ,  C22B1/10 ,  C22B5/14 ,  F27B15/00 ,  C21B1/02

CPC分类号： C22B1/10 ,  C22B5/14

摘要： A process for thermally treating fine-grained solids with high-oxygen gases at temperatures at which the solids can form molten and gaseous reaction products comprises carrying out the thermal treatment in a cyclone chamber and thereafter conducting the gases from the cyclone chamber into a horizontal or vertical cooling chamber. The process can be used for the roasting of sulfide ores, ore concentrates and other metallurgical intermediate products. The outlet of the cyclone chamber through which the gases are removed lies approximately along the axis and cooling is carried out in the cooling chamber such that the molten droplets contained in the gas stream entering the latter are cooled in free flight below their solidification point in the gas, i.e., do not contact the walls of the cooling chamber until they are solidified at least along their surfaces.

摘要翻译： 在固体可以形成熔融和气态反应产物的温度下用高氧气热处理细粒固体的方法包括在旋风室中进行热处理，然后将来自旋风室的气体导入水平或 垂直冷却室。 该工艺可用于焙烧硫化矿石，精矿和其他冶金中间体产品。 除去气体的旋风室的出口大致沿着轴线，并且在冷却室中进行冷却，使得包含在进入其中的气流中的熔融液体在自由飞行中冷却，使其低于其凝固点的温度 气体，即不要与冷却室的壁接触，直到它们至少沿其表面固化。

公开(公告)号：US3950493A

公开(公告)日：1976-04-13

申请号：US508443

申请日：1974-09-23

申请人： Karl-Heinz Dorr ,  Lothar Reh ,  Hugo Grimm ,  Karel Vydra

发明人： Karl-Heinz Dorr ,  Lothar Reh ,  Hugo Grimm ,  Karel Vydra

IPC分类号： B01D53/50 ,  B01D53/77 ,  C01B17/74 ,  C01B17/80 ,  B01D53/34

CPC分类号： C01B17/806 ,  Y10S261/54

摘要： A process for removing sulfur trioxide from gases wherein the sulfur trioxide-containing gas is treated with sulfuric acid in a Venturi absorber, the sulfur-trioxide laden sulfuric acid is passed in indirect heat exchange with a cooling fluid within the widening outlet of the absorber and the sulfur trioxide-laden sulfuric acid is separated from the gas phase.

摘要翻译： 一种从气体中除去三氧化硫的方法，其中在文氏管吸收器中用硫酸处理含三氧化硫的气体，将含硫三氧化硫的硫酸与吸收器加宽出口内的冷却流体进行间接热交换， 将含三氧化硫的硫酸与气相分离。

公开(公告)号：US5215042A

公开(公告)日：1993-06-01

申请号：US645379

申请日：1991-01-18

申请人： Hans Beisswenger ,  Rainer Reimer ,  Karel Vydra

发明人： Hans Beisswenger ,  Rainer Reimer ,  Karel Vydra

IPC分类号： F23C10/18 ,  B01J8/38 ,  F22B31/00 ,  F23C10/02 ,  F23C10/10

CPC分类号： F23C10/10 ,  B01J8/386 ,  B01J8/388 ,  F22B31/003 ,  F23C2206/101

摘要： A reactor for combusting fine-grained solid fuels in a circulating fluidized bed contains a combustion chamber, which is provided with lines which open in the lower portion of that chamber and serve to feed primary air, secondary air and solid fuel. The fluidized bed combustion chamber is divided into compartments by at least one partition provided in the upper portion of the fluidized bed combustion chamber. Each compartment communicates through a passage with at least one solids separator, which is connected to means for recycling solids and communicates with the compartment through a passage.

摘要翻译： 用于在循环流化床中燃烧细粒状固体燃料的反应器包含燃烧室，该燃烧室设置有在该室的下部开口并用于输送一次空气，二次空气和固体燃料的管线。 流化床燃烧室由设置在流化床燃烧室上部的至少一个隔板分成隔室。 每个隔室通过通道与至少一个固体分离器连通，固体分离器连接到用于再循环固体的装置，并通过通道与隔室连通。

公开(公告)号：US4200454A

公开(公告)日：1980-04-29

申请号：US892259

申请日：1978-03-31

申请人： Carl-August Maelzer ,  Martin Rahn ,  Lothar Reh ,  Bernd Thone ,  Karel Vydra ,  David Rice

发明人： Carl-August Maelzer ,  Martin Rahn ,  Lothar Reh ,  Bernd Thone ,  Karel Vydra ,  David Rice

IPC分类号： C22B1/10 ,  C22B5/14 ,  C22B13/02 ,  C22B19/04 ,  C22B19/14 ,  C22B19/20

CPC分类号： C22B5/14 ,  C22B1/10 ,  C22B13/02 ,  C22B19/14 ,  Y02P10/122 ,  Y02P10/126 ,  Y02P10/212

摘要： Zinc and, if desired, lead are volatilized from a metallurgical material such as a finely divided oxidic ore, ore concentrate or another metallurgical intermediate. The volatilization of the zinc is carried out at a temperature above 1300.degree. C. in a cyclone chamber which has an axis that is substantially horizontal, i.e. is inclined to the horizontal at an angle of 0.degree. to 15.degree.. Carbon dioxide is removed from the gas leaving the zinc condensing stage and the high carbon monoxide gas thus obtained is recycled to the cyclone chamber or at another point ahead of the condensation stage.

摘要翻译： 锌，如果需要，铅从冶金材料如细碎的氧化矿石，矿石浓缩物或另一种冶金中间体挥发。 在高于1300℃的温度下，在具有基本上水平的轴的旋风室中进行锌的挥发，即以0°至15°的角度倾斜于水平。 从离开锌冷凝阶段的气体中除去二氧化碳，将由此获得的高一氧化碳气体再循环至旋风室或冷凝阶段前的另一个位置。

公开(公告)号：US4108634A

公开(公告)日：1978-08-22

申请号：US823858

申请日：1977-08-11

申请人： Martin Rahn ,  Lothar Reh ,  Bernd Thone ,  Karel Vydra

发明人： Martin Rahn ,  Lothar Reh ,  Bernd Thone ,  Karel Vydra

IPC分类号： C22B5/08 ,  B01J6/00 ,  B01J10/00 ,  B01J19/00 ,  C01B13/16 ,  C01B13/20 ,  C01B17/04 ,  C01B25/12 ,  C01B25/41 ,  C01G9/02 ,  C10J3/46 ,  C22B1/10 ,  C22B5/14 ,  F27B15/00 ,  C21B15/00

CPC分类号： C22B1/10 ,  B01J10/005 ,  C01B13/16 ,  C01B13/20 ,  C01B17/0491 ,  C01B25/12 ,  C01B25/41 ,  C01G9/02 ,  C10J3/466 ,  C10J3/506 ,  C10J3/76 ,  C10J3/84 ,  C22B5/14 ,  C01P2004/61 ,  C10J2300/0906 ,  C10J2300/0959 ,  C10J2300/0976

摘要： A process for thermally treating fine-grained solids with high-oxygen gases at temperatures at which the solids can form molten and gaseous reaction products comprises carrying out the thermal treatment at least in part in a cyclone chamber. The solids, high-oxygen gases and, if desired, an energy carrier (usually a carbon-containing solid, liquid or gas) are mixed to form a suspension at a temperature below the reaction temperature. The suspension is fed to a vertical combustion path (tube) and reacts therein to form another suspension of primarily molten particles which is admitted to the cyclone chamber. Reactants are added to the gas phase within a core-flow region of the cyclone chamber and/or immediately after the discharge of gas therefrom to a cooling chamber.

摘要翻译： 在固体可以形成熔融和气态反应产物的温度下用高氧气热处理细粒固体的方法包括至少部分地在旋风室中进行热处理。 如果需要，固体，高氧气体和能量载体（通常为含碳固体，液体或气体）混合以在低于反应温度的温度下形成悬浮液。 将悬浮液供给到垂直燃烧路径（管）并在其中反应以形成进入旋风室的主要熔融颗粒的另一悬浮液。 将反应物加入旋流室的核心流动区域内的气相和/或其后的气体排出到冷却室之后。