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公开(公告)号：US08114190B2
公开(公告)日：2012-02-14
申请号：US12564643
申请日：2009-09-22
CPC分类号： C04B7/364 , B01D45/12 , B01D46/02 , B01D50/002 , C04B7/24 , C04B7/4423 , Y02P40/126 , Y02P40/145 , Y02W10/40
摘要： Method and system for a cement burning facility. When exhaust gas in a part of a preheater or a kiln inlet of a cement kiln is extracted, a cement material is dispersed. The dispersed amount of the cement material is adjusted to maintain the temperature of the extracted gas between 950° C. and 1,150° C. The extracted gas is cooled to at most the melting point of a chlorine compound. A solid-gas separation device adjusts classification particle size to between 15 μm and 30 μm. A dust trap removes fine powder dust with a particle size equal to or smaller than the classification particle size. The amount of fine powder dust collected by the dust trap is maintained between 50 g/m3N and 150 g/m3N, with the concentration of chlorine in the collected fine powder dust set to between 5% and 20%.
摘要翻译： 水泥燃烧设备的方法和系统。 当提取部分预热器或水泥窑的窑入口处的废气时，分散水泥材料。 调整水泥材料的分散量，以保持提取气体的温度在950℃至1150℃之间。将提取的气体冷却至至多氯化合物的熔点。 固体气体分离装置将分级粒度调整为15μm〜30μm。 除尘器除去粒度等于或小于分级粒度的细粉尘。 由集尘器收集的细粉尘的量保持在50g / m3N至150g / m3N之间，收集的细粉尘中的氯浓度设定在5％至20％之间。
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公开(公告)号：US20100083878A1
公开(公告)日：2010-04-08
申请号：US12564643
申请日：2009-09-22
CPC分类号： C04B7/364 , B01D45/12 , B01D46/02 , B01D50/002 , C04B7/24 , C04B7/4423 , Y02P40/126 , Y02P40/145 , Y02W10/40
摘要： An object of this invention is to provide an exhaust gas treatment method and system for a cement burning facility which allows the handling property of collected powder dust to be improved and which enables smooth removal of hydrogen chloride that may result from burning of organic sludge. When part of exhaust gas in a lowermost part of a preheater 3 or a kiln inlet part 2 of a cement kiln 1 is extracted to obtain extracted gas, a cement material is dispersed, and the disperse amount of the cement material is adjusted so as to maintain the temperature of the extracted gas between 950° C. and 1,150° C. The extracted gas is cooled to at most the melting point of a chlorine compound. Then, solid-gas separation device 12 adjusts a classification particle size to between 15 μm and 30 μm. Dust trap 13 collects and removes fine powder dust with a particle size equal to or smaller than the classification particle size. Thus, the amount of fine powder dust collected by the dust trap is maintained between 50 g/m3N and 150 g/m3N, with the concentration of chlorine in the collected fine powder dust set to between 5% and 20%.
摘要翻译： 本发明的目的是提供一种用于水泥燃烧设备的废气处理方法和系统，其能够改善收集的粉尘的处理性能，并且能够平滑地除去可能由有机污泥燃烧产生的氯化氢。 当提取出水泥窑1的预热器3或窑入口部2的最下部的废气的一部分而得到抽出气体时，分散水泥材料，调整水泥材料的分散量，使得 将提取气体的温度保持在950℃和1150℃之间。将提取的气体冷却至至多氯化合物的熔点。 然后，固气分离装置12将分级粒径调整为15μm〜30μm。 除尘器13收集并除去粒度等于或小于分级粒度的细粉尘。 因此，由粉尘收集器收集的细粉尘的量保持在50g / m3N至150g / m3N之间，收集的细粉尘中的氯浓度设定在5％至20％之间。
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公开(公告)号：US08038768B2
公开(公告)日：2011-10-18
申请号：US12307285
申请日：2007-12-19
申请人： Yoshiaki Komatsu , Michio Ishizaki , Haruki Miura
发明人： Yoshiaki Komatsu , Michio Ishizaki , Haruki Miura
CPC分类号： B01D53/002 , B01D2257/204 , C04B7/364 , C04B7/43 , C04B7/475 , F27B7/2033 , F27D17/004 , Y02P40/123
摘要： An exhaust gas treatment method and system of a cement burning facility, wherein a chlorine concentration of the collected fine powder dust is set in a range of 5 to 20% in such a manner that when a part of exhaust gas is extracted as extracted gas from a lowermost part of a preheater, or a kiln inlet part of a cement kiln, a cement raw material is dispersed and the temperature of the extracted gas is held in a range of 950° to 1150° C. By adjusting the dispersion amount of the cement raw material, the extracted gas is cooled to a melting point or less of a chlorine compound, and a classification particle size in a solid-gas separator is then adjusted in a range of 12 μm to 30 μm, to separate for removal and collection fine powder dust.
摘要翻译： 一种水泥燃烧设备的废气处理方法和系统，其中收集的细粉尘的氯浓度设定在5至20％的范围内，使得当废气的一部分从抽出气体中抽出时 预热器的最低部分或水泥窑的窑入口部分，分散水泥原料，将提取气体的温度保持在950〜1150℃的范围内。通过调节 水泥原料，将提取的气体冷却至氯化合物的熔点以下，然后将固体气体分离器的分级粒径调整为12μm〜30μm的范围，分离除去和收集 细粉尘
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公开(公告)号：US20110185953A1
公开(公告)日：2011-08-04
申请号：US12307285
申请日：2007-12-19
申请人： Yoshiaki Komatsu , Michio Ishizaki , Haruki Miura
发明人： Yoshiaki Komatsu , Michio Ishizaki , Haruki Miura
IPC分类号： F23J3/00
CPC分类号： B01D53/002 , B01D2257/204 , C04B7/364 , C04B7/43 , C04B7/475 , F27B7/2033 , F27D17/004 , Y02P40/123
摘要： An object of the present invention is to provide an exhaust gas treatment method and system of a cement burning facility which can be configured by general-purpose apparatuses, and which is capable of improving the handling property of collected fine powder dust and thereby realizing a stable operation without the need of maintenance. To this end, according to the present invention, the chlorine concentration of the collected fine powder dust is set in a range of 5 to 20% in such a manner that when a part of exhaust gas is extracted as extracted gas from a lowermost part of a preheater 3, or a kiln inlet part 2 of a cement kiln 1, a cement raw material is dispersed and the temperature of the extracted gas is held in a range of 950° C. to 1150° C. by adjusting the dispersion amount of the cement raw material, that after the extracted gas is cooled to a melting point or less of a chlorine compound, a classification particle size in solid-gas separation means 12 is adjusted in a range of 12 μm to 30 μm, to separate dust having the classification particle size or more, and that fine powder dust having the classification particle size or less is collected and removed from the extracted gas by dust trap means 13.
摘要翻译： 本发明的目的是提供一种能够通过通用设备构成的水泥燃烧设备的废气处理方法和系统，其能够提高收集的细粉尘的处理性能，从而实现稳定的 操作无需维护。 为此，根据本发明，收集的细粉尘的氯浓度设定在5〜20％的范围内，使得当废气的一部分从抽出气体的最下部抽出时 预热器3或水泥窑1的窑入口部2，分散水泥原料，将提取气体的温度保持在950℃〜1150℃的范围内，通过调节 水泥原料，将提取气体冷却至氯化合物的熔点以下时，将固体气体分离装置12的分级粒径调整为12μm〜30μm的范围，分离具有 分级粒径以上，并且通过除尘装置13从提取气体中收集并除去分级粒径以下的细粉尘。
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