CHLORINE BYPASS FACILITY, CEMENT CLINKER PRODUCTION DEVICE, CEMENT CLINKER PRODUCTION METHOD, OPERATION METHOD OF CHLORINE BYPASS FACILITY AND WASTE TREATMENT METHOD
To provide a technique capable of transporting coarse powder and enhancing a freedom degree of an installation position of a classification part.SOLUTION: A chlorine bypass facility 90 comprises: an extraction hole 21A for extracting a kiln exhaust gas, from a furnace tail 52 of a cement kiln 50, a...
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Zusammenfassung: | To provide a technique capable of transporting coarse powder and enhancing a freedom degree of an installation position of a classification part.SOLUTION: A chlorine bypass facility 90 comprises: an extraction hole 21A for extracting a kiln exhaust gas, from a furnace tail 52 of a cement kiln 50, a rising duct 42 or a space therebetween; a classifying part 22 for separating coarse powder of raw material dust from the extracted gas extracted through the extraction hole 21A, and acquiring a derivation gas having a temperature of 770°C or greater and including fine powder of the raw material dust; and a mixing part 30 for mixing, coarse powder separated by the classifying part 22 and moisture-containing waste W.SELECTED DRAWING: Figure 1
【課題】粗粉を運搬可能とし、分級部の設置位置の自由度を高めることが可能な技術を提供する。【解決手段】塩素バイパス設備90は、セメントキルン50の窯尻52、ライジングダクト42またはこれらの間からキルン排ガスを抽気する抽気口21Aと、抽気口21Aから抽気された抽気ガスから原料ダストの粗粉を分離し、原料ダストの微粉を含む770℃以上の温度を有する導出ガスを得る分級部22と、分級部22で分離された粗粉と、含水廃棄物Wとを混合する混合部30と、を有する。【選択図】図1 |
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