Furnace for the direct reduction of iron oxides
    81.
    发明授权
    Furnace for the direct reduction of iron oxides 失效
    炉直接还原氧化铁

    公开(公告)号:US06342179B1

    公开(公告)日:2002-01-29

    申请号:US09653283

    申请日:2000-08-31

    IPC分类号: C21B708

    摘要: Gravitational type furnace for the direct reduction of mineral iron comprising a median reaction zone (14) in which the reactions to reduce the mineral iron occur, means (12, 13) to feed the mineral iron to said reaction zone (14), distribution means (16, 17, 18) to introduce reducing gas into said reaction zone (14), discharge means (15) to discharge the reduced metal iron, and an intake device (20) for the reducing gas, said intake device (20) being positioned in correspondence with a chamber (21) situated above said reaction zone (14), a toroidal grid (22) being arranged in said chamber (21).

    摘要翻译: 用于直接还原矿物铁的重力式炉,包括其中发生减少矿物铁的反应的中间反应区(14),将矿铁进料到所述反应区(14)的装置(12,13),分配装置 (16,17,18),以将还原气体引入所述反应区(14),排出装置(15)以排出还原的金属铁和用于还原气体的进气装置(20),所述进气装置(20)是 位于与位于所述反应区(14)上方的腔室(21)相对应的环形栅极(22),布置在所述腔室(21)中。

    Arrangement and process for the reduction of metal-oxide-bearing material
    82.
    发明授权
    Arrangement and process for the reduction of metal-oxide-bearing material 失效
    用于还原含金属氧化物的材料的布置和工艺

    公开(公告)号:US06221126B1

    公开(公告)日:2001-04-24

    申请号:US09205439

    申请日:1998-12-04

    IPC分类号: C21B1302

    摘要: Arrangement for the reduction of metal-oxide-bearing material, particularly of, iron ore, with a reduction vessel in which the metal-oxide-bearing material is reduced in counterflow with reduction gas and which is provided with an inlet for metal-oxide-bearing material, an inlet for reduction gas, an outlet for off-gas and an outlet for reduced material, a vessel for metal-oxide-bearing material, which is connected with the reduction vessel by means of a line and a first supply line for a sealing gas which serves to seal the reduction vessel against the vessel, which first supply line is provided at the connecting line between the vessel and the reduction vessel, characterized in that at least one additional supply line for a sealing gas is provided at the connecting line, which additional supply line is located between the first supply line and the vessel.

    摘要翻译: 用于还原金属氧化物的材料,特别是铁矿石的还原容器,其中含有金属氧化物的材料与还原气体相反地减少并且具有用于金属氧化物的材料的入口, 轴承材料,还原气体入口,废气出口和还原材料出口,用于金属氧化物轴承材料的容器,其通过线路与还原容器连接,第一供应管线用于 密封气体,其用于将所述还原容器密封在所述容器上,所述第一供应管线设置在所述容器和所述还原容器之间的连接管线处,其特征在于,在所述连接处设置至少一个用于密封气体的附加供应管线 该附加供应管线位于第一供应管线和容器之间。

    Shaft furnace for direct reduction of oxides
    84.
    发明授权
    Shaft furnace for direct reduction of oxides 失效
    用于直接还原氧化物的炉膛

    公开(公告)号:US5702246A

    公开(公告)日:1997-12-30

    申请号:US603922

    申请日:1996-02-22

    申请人: Oscar G. Dam

    发明人: Oscar G. Dam

    摘要: A shaft furnace for reduction of oxides includes a shaft member having an oxide inlet and defining a pre-heating and pre-reducing zone downstream of the oxide inlet, a reducing zone downstream of the pre-heating and pre-reducing zone a transition zone downstream of the reducing zone, and a discharge zone downstream of the transition zone; and a gas reforming zone associated with the shaft member for reforming a methane-containing gas into a reformed gas and for introducing the reformed gas into the reducing zone whereby oxides in the reducing zone are reduced by the reformed gas.

    摘要翻译: 用于还原氧化物的竖炉包括具有氧化物入口并且在氧化物入口下游限定预加热和预还原区的轴构件,在预热和预还原区下游的还原区,过渡区下游 的减压区,以及过渡区下游的排放区; 以及与所述轴构件相关联的气体重整区,用于将含甲烷的气体重整成重整气体,并将重整气体引入还原区,由此还原区中的氧化物被重整气体还原。

    Process and device for manufacturing cement clinker
    86.
    发明授权
    Process and device for manufacturing cement clinker 失效
    制造水泥熟料的工艺和装置

    公开(公告)号:US4367095A

    公开(公告)日:1983-01-04

    申请号:US226993

    申请日:1981-01-21

    申请人: Gerald Namy

    发明人: Gerald Namy

    CPC分类号: C04B7/44 F27B1/005 Y02P40/121

    摘要: A process and apparatus for manufacturing cement clinker in which pellets of raw material containing the necessary components for manufacturing the clinker are introduced into an apparatus where the pellets flow under gravity, successively through a preheating zone, a clinkering zone using a fluidized bed and a cooling zone. The pellets contain an amount of comminuted carbon determined so that its combustion produces an amount of heat within each pellet sufficient to carry out decarbonation of the material, taking into account the heat introduced by the hot gases passing upwardly through the apparatus. Decarbonation is completed at the base of the preheating zone and the pellets enter the clinkering zone at a temperature which is close to the clinkering temperature. Additional heat is supplied through burners within the clinkering zone.

    摘要翻译: 一种用于制造水泥熟料的方法和装置,其中将含有用于制造熟料的必需组分的原料颗粒引入到颗粒在重力作用下依次通过预热区,使用流化床的熟料区和冷却 区。 颗粒含有一定量的粉碎碳,使其燃烧在每个颗粒内产生足以进行材料脱碳的热量,同时考虑到向上通过设备的热气体引入的热量。 在预热区的底部完成脱碳化,颗粒在接近熟化温度的温度下进入熟料区。 通过烧结区内的燃烧器提供额外的热量。

    Process for calcining limestone
    87.
    发明授权
    Process for calcining limestone 失效
    煅烧石灰石的工艺

    公开(公告)号:US4031183A

    公开(公告)日:1977-06-21

    申请号:US658576

    申请日:1976-02-17

    摘要: A process and apparatus for burning limestone to produce calcined lime in which limestone is burned continuously in a vertical kiln provided with a plurality of fuel injectors which permit pulsed introduction of fuel so as to ensure a lamellar flow of fuel through the kiln and a controlled release of heat.

    摘要翻译: 一种用于燃烧石灰石以生产煅烧石灰的方法和装置,其中石灰石在设置有多个燃料喷射器的立式窑中连续燃烧,其允许脉冲引入燃料,以确保燃料通过窑的片层流动和受控释放 的热量。

    Process and apparatus for firing and sintering of granular material
    88.
    发明授权
    Process and apparatus for firing and sintering of granular material 失效
    烧结和烧结颗粒材料的方法和装置

    公开(公告)号:US4025293A

    公开(公告)日:1977-05-24

    申请号:US621781

    申请日:1975-10-14

    申请人: Karl Beckenbach

    发明人: Karl Beckenbach

    CPC分类号: C04B2/12 F27B1/005

    摘要: A process for the firing and sintering of granular material in a gas or oil heated shaft furnace is disclosed in which the material, fed from the top of the furnace passes downwards successively through an entry zone, a preheating zone, a firing zone in which burners are disposed around the furnace wall, and a cooling zone, and in which the feeding of the material at the top of the furnace is so effected that a central depression is maintained in the upper surface of the material in the entry zone, said surface sloping downwardly from the periphery of the entry zone into the central depression, so that segregation of the material occurs automatically, the coarser pieces of material rolling into the central depression, whereby a column of the coarser material is maintained along the vertical axis of the furnace. The feeding of the material at the top of the furnace is effected by means of a charging bell over which the material to be fed to the furnace is discharged, the material being guided by the charging bell to the periphery of the entry zone and then rolling into the central depression below the charging bell.

    摘要翻译: 公开了一种用于燃气或油加热竖炉中的颗粒材料的烧制和烧结的方法,其中从炉顶进料的材料依次通过入口区,预热区,燃烧区 设置在炉壁周围,并且冷却区,其中在炉顶部的材料的供给如此受到影响,使得在进入区中的材料的上表面中保持中心凹陷,所述表面倾斜 从入口区域的周边向下到中心凹陷处,使得材料的偏析自动发生,较粗的材料块滚动到中心凹陷中,由此沿着炉的垂直轴线保持较粗的材料的柱。 炉子顶部的材料进料是通过一个加料钟来进行的,待加料到炉子的材料将在其上被排放,材料由加料钟引导到入口区的周边,然后轧制 进入充电钟下方的中央凹陷。

    Apparatus for and method of manufacturing white portland cement clinker
    90.
    发明授权
    Apparatus for and method of manufacturing white portland cement clinker 失效
    制造白蛋白水泥夹克的方法和方法

    公开(公告)号:US3615080A

    公开(公告)日:1971-10-26

    申请号:US3615080D

    申请日:1969-12-18

    IPC分类号: C04B7/44 C04B7/43 F27B1/00

    CPC分类号: F27B1/005 C04B7/43

    摘要: AN APPARATUS FOR AND METHOD OF MANUFACTURING WHITE PORTLAND CEMENT CLINKER ARE DISCLOSED. THE APPARATUS HAS A REACTOR PROVIDED WITH A REACTOR BED ADAPTED TO RECEIVE AND PROCESS WHITE PORTLAND CEMENT CLINKER RAW MATERIAL. THE REACTOR HAS A HEATING AND DRYING ZONE FOR REMOVING THE WATER FROM THE RAW MATERIAL, A CALCINING ADJACENT THE HEATING AND DRYING ZONE FOR CALCINING THE CALCAREOUS PORTION OF RAW MATERIAL, A REACTION ZONE ADJACENT THE CALCINING ZONE FOR CLINKERING THE RAW MATERIAL, A GAS DISTRIBUTION ZONE ADJACENT THE REACTION ZONE FOR RECEIVING A HEATING AND REDUCING FLUID HAVING A PRESSURE SUFFICIENT TO TRAVERSE THE REACTION ZONE, THE CALCINING ZONE AND THE HEATING AND DRYING ZONE WITH A RESIDUAL REMAINING PRESSURE, AND A GAS SEAL ZONE ADJACENT THE GAS DISTRIBUTION ZONE. A DIVIDER IN THE GAS SEAL ZONE SPLIT THE FLOW OF THE SINTERED RAW MATERIAL INTO TWO CHANNELS. EACH CHANNEL HAS A CONSTRICTED PASSAGE IN THE DIRECTION OF THE FLOW OF THE SINTERED RAW MATERIAL TO PRODUCE A PRESSURE DROP THROUGH THE GAS SEAL ZONE GREATER THAN THE PRESSURE IN THE HEATING AND REDUCING FLUID. A COOLING ZONE OF THE REACTOR ADJACENT THE GAS SEALING ZONE COOLS THE SINTERED RAW MATERIAL. A COOLING PLENUM IN THE COOLING ZONE IS CONNECTED TO THE HEATING AND DRYING ZONE AND HAS A FIRST LOUVER WHICH DEFINES WITH AN EXIT LOUVER THE COOLING ZONE, THUS RETAINING THE SINTERED RAW MATERIAL IN THE COOLING ZONE WHILE EMITTING THE HEATING AND REDUCING FLUID FROM SUCH COOLING ZONE. A DISCHARGE MEANS IN DISCHARGE ZONE OF THE REACTOR DISCHARGES THE SINTERED MATERIAL WHILE SEALING THE DISCHARGE ZONE FROM THE ATMOSPHERE. THE METHOD INCLUDES THE STEPS OF: (A) RECEIVING THE RAW MATERIAL IN THE REACTOR BED OF THE REACTOR, (B) PASSING THE RAW MATERIAL THROUGH A HEATING AND DRYING ZONE TO REMOVE THE WATER FROM THE RAW MATERIAL, (C) PASSING THE DRIED RAW MATERIAL THROUGH A CALCINING ZONE ADJACENT THE HEATING AND DRYING ZONE TO CALCINE THE CALCAREOUS PORTION OF THE RAW MATERIAL, (D) PASSING THE REACTED RAW MATERIAL THROUGH A GAS DISTRIBUTION ZONE ADJACENT THE REACTION ZONE TO RECEIVE A HEATING AND REDUCING FLUID PRODUCED FROM A FLUID FUEL BURNED IN A DEFICIENCY OF OXYGEN-BEARING GAS AND HAVING A PRESSURE SUFFICIENT TO TRAVERSE THE REACTION ZONE, THE CALCINING ZONE AND THE HEATING AND DRYING ZONE WITH A RESIDUAL REMAINING PRESSURE, (E) PASSING THE RAW MATERIAL THROUGH A GAS SEALING ZONE ADJACENT THE GAS DISTRIBUTION ZONE, (F) SPLITTING THE FLOW OF THE SINTERED RAW MATERIAL IN THE GAS SEAL ZONE INTO TWO CHANNELS, EACH CHANNEL HAVING A CONSTRICTED PASSAGE IN THE DIRECTION OF THE FLOW OF THE RAW MATERIAL TO PRODUCE A PRESSURE DROP THROUGH SUCH GAS SEAL ZONE GREATER THAN THE ORIGINAL PRESSURE IN SUCH HEATING AND REDUCING FLUID, (G) PASSING THE SINTERED RAW MATERIAL THROUGH A COOLING ZONE ADJACENT THE GAS SEAL ZONE TO COOL THE SINTERED RAW MATERIAL UNDER REDUCING CONDITIONS, (H) RECEIVING THE HEATING AND REDUCING FLUID AT THE RESIDUAL REMAINING PRESSURE IN A COOLING PLENUM IN THE COOLING ZONE, (I) RETAINING THE RAW MATERIAL IN THE COOLING ZONE WHILE EMITTING THE HEATING AND REDUCING FLUID FROM THE COOLING PLENUM INTO THE COOLING ZONE, (J) RETAINING THE RAW MATERIAL IN THE COOLING ZONE WHILE EMITTING THE HEATING AND REDUCING FLUID FROM THE COOLING ZONE THROUGH AN EXIT LOUVER, (K) PASSING THE SINTERED RAW MATERIAL THROUGH A DISCHARGE ZONE ADJACENT THE COOLING ZONE, AND (L) DISCHARGING THE RAW MATERIAL WHILE SEALING THE DISCHARGE ZONE FROM THE ATMOSPHERE.