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    • 46. 发明申请
    • CONTINUOUS HEATING FURNACE
    • 连续加热炉
    • US20160018161A1
    • 2016-01-21
    • US14867370
    • 2015-09-28
    • IHI Corporation
    • Kimiyoshi SATOH
    • F27B9/06F27B9/36
    • F27B9/068A21B1/14A21B1/48F27B9/20F27B9/24F27B9/243F27B9/36F27D17/00F27D99/0035F27D2099/0045Y02P60/83
    • A continuous heating furnace includes a furnace main body, a conveyance unit configured to convey a baking object W in the furnace main body, a plurality of heating sections heated by combustion, each having a first radiation surface configured to be heated by combustion and transfers heat to the baking object conveyed by the conveyance unit and arranged in the conveyance direction of the baking object in the furnace main body, and a cooling preheater having a second radiation surface configured to receive radiant heat from the baking object when being opposite to the baking object conveyed by the conveyance unit and a gas flow path configured to preheat a gas used for combustion in the heating section by the heat from the second radiation surface.
    • 连续加热炉包括炉主体,输送单元,其被配置为输送炉主体中的烘焙对象W;多个加热部,通过燃烧加热,每个加热部分具有构造成通过燃烧加热并传递热量的第一辐射面 涉及由输送单元输送并沿炉主体的焙烤物体的输送方向配置的烘焙对象,以及具有第二辐射面的冷却预热器,该第二辐射面配置为当与烘焙对象相对时从烘烤对象接收辐射热 由输送单元输送的气体流路和配置为通过来自第二辐射面的热量来预热加热区域中用于燃烧的气体的气体流路。
    • 50. 发明申请
    • TREATMENT DEVICE AND TREATMENT METHOD FOR CHLORINE BYPASS DUST
    • 氯离子除尘处理装置及处理方法
    • US20130192497A1
    • 2013-08-01
    • US13806297
    • 2011-06-08
    • Junichi TerasakiKenzaburou Kondou
    • Junichi TerasakiKenzaburou Kondou
    • C04B7/60F27D17/00
    • C04B7/60B01D53/508B01D53/62B01D53/86B09B3/0025C04B7/436F27D17/00Y02P10/283
    • In accordance with the present invention, there is provided a treat chlorine bypass dust while preventing increases in chemical cost and concentrations of heavy metals in clinker, and ensuring stability in quality of cement. In a chlorine bypass facility 1 extracting a part G of combustion gas, while cooling it, from a kiln exhaust gas passage, which runs from an inlet end of a cement kiln to a bottom cyclone, and recovering a high chlorine concentration chlorine bypass dust D5 from the extracted gas G1, a slurry S containing chlorine bypass dust and SO2 gas or/and CO2 gas are contacted with each other to obtain solid content. The slurry containing chlorine bypass dust and an exhaust gas from the chlorine bypass facility or/and the exhaust gas from the cement kiln can be contacted with each other, and the solid content can be fed to a cement finishing process, which allows cement with low CaO and Ca(OH)2 contents and with stable property such as setting time to be produced.
    • 根据本发明,提供一种治疗氯旁路粉尘,同时防止熟料中化学成本和重金属浓度的增加,并确保水泥质量的稳定性。 在氯旁路设备1中,在从水泥窑的入口端到底部旋风分离器的窑尾废气通道中冷却时,提取燃烧气体G,并且回收高氯浓度氯旁路粉尘D5 从提取气体G1中将含有氯旁路粉尘和SO 2气体或/和CO 2气体的浆料S彼此接触以获得固体含量。 含有氯旁路粉尘和来自氯旁路设备的废气和/或来自水泥窑的废气的浆料可以彼此接触,并且可以将固体成分进料到水泥整理过程中,这使得水泥具有低的 CaO和Ca(OH)2含量,并具有稳定的性能,例如凝固时间。