化学反应工程与工艺
化學反應工程與工藝
화학반응공정여공예
CHEMICAL REACTION ENGINEERING AND TECHNOLOGY
2015年
2期
97-105,163
,共10页
李睿%王德武%张少峰%赵立军%吴广恒
李睿%王德武%張少峰%趙立軍%吳廣恆
리예%왕덕무%장소봉%조립군%오엄항
提升管%出口结构%局部固含率分布%气力输送%快速流态化
提升管%齣口結構%跼部固含率分佈%氣力輸送%快速流態化
제승관%출구결구%국부고함솔분포%기력수송%쾌속류태화
riser%exit structure%distribution of local solid hold-up%pneumatic transport%fast fluidization
在一套组合约束型提升管冷态实验装置上,研究了气力输送和快速流态化两种流型下,出口段局部固含率分布规律及不同操作条件对固含率的影响。结果表明:局部固含率径向分布整体上呈中心小、边壁大的分布特征,并随分布器开孔率和表观气速的降低而增大,随上部流化床层压降和颗粒循环强度的降低而减小;在快速流态化操作下,局部固含率曲线分布形式与常规提升管类似,而在气力输送状态下,临近出口区域局部固含率最大值通常不出现在边壁处,其位置随表观气速和分布器开孔率增加以及颗粒循环强度和上部流化床层压降降低而远离边壁;两种流型下局部固含率径向分布的均匀性均随表观气速及分布器开孔率的增加而升高,随颗粒循环强度及流化床层压降的增加而降低。
在一套組閤約束型提升管冷態實驗裝置上,研究瞭氣力輸送和快速流態化兩種流型下,齣口段跼部固含率分佈規律及不同操作條件對固含率的影響。結果錶明:跼部固含率徑嚮分佈整體上呈中心小、邊壁大的分佈特徵,併隨分佈器開孔率和錶觀氣速的降低而增大,隨上部流化床層壓降和顆粒循環彊度的降低而減小;在快速流態化操作下,跼部固含率麯線分佈形式與常規提升管類似,而在氣力輸送狀態下,臨近齣口區域跼部固含率最大值通常不齣現在邊壁處,其位置隨錶觀氣速和分佈器開孔率增加以及顆粒循環彊度和上部流化床層壓降降低而遠離邊壁;兩種流型下跼部固含率徑嚮分佈的均勻性均隨錶觀氣速及分佈器開孔率的增加而升高,隨顆粒循環彊度及流化床層壓降的增加而降低。
재일투조합약속형제승관랭태실험장치상,연구료기력수송화쾌속류태화량충류형하,출구단국부고함솔분포규률급불동조작조건대고함솔적영향。결과표명:국부고함솔경향분포정체상정중심소、변벽대적분포특정,병수분포기개공솔화표관기속적강저이증대,수상부류화상층압강화과립순배강도적강저이감소;재쾌속류태화조작하,국부고함솔곡선분포형식여상규제승관유사,이재기력수송상태하,림근출구구역국부고함솔최대치통상불출현재변벽처,기위치수표관기속화분포기개공솔증가이급과립순배강도화상부류화상층압강강저이원리변벽;량충류형하국부고함솔경향분포적균균성균수표관기속급분포기개공솔적증가이승고,수과립순배강도급류화상층압강적증가이강저。
A cold model of riser with combined restraint was established to study the distribution of local solid hold-up in exit area and the effect of different operating conditions under pneumatic transport and fast fluidization flowing regimes. Experimental results showed that the radial distribution of local solid hold-up was lower in the center region and higher in the wall region. The local solids hold-up increased with the decrease of superficial gas velocity and distributor opening rate, decreased with the decrease of solid flux and upper fluidized bed pressure drop. Under fast fluidization operating conditions, the distribution form of local solid hold-up was similar to that in the conventional riser. Under pneumatic transport operating conditions, the maximum local solid hold-up in exit area didn’t usually appear in the wall region. The maximum position was away from the wall with the increase of superficial gas velocity and distributor opening rate, the decrease of solid flux and upper fluidized bed pressure drop. Under the two flowing regimes, the radial uniformity of local solid hold-up increased with the increase of superficial gas velocity and distributor opening rate, decreased with the increase of solid flux and upper fluidized bed pressure drop.