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负压差斜管内催化剂颗粒流动特性的实验研究

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在规格为Φ150 mm×3 600 mm的负压差斜管-阀门实验装置上,通过测量和分析不同催化剂颗粒质量流率(G)时斜管内轴向动态压力的特征参数,进行催化裂化装置斜管内催化剂颗粒的流动特性研究.结果表明:斜管蓄压能力随Gs的增大而增大,管内依次出现稀相分层流、密相分层流和填充流;斜管内的压力分布、主频、幅值、标准偏差与流态相对应,可用于流态的量化识别;当Gs=65.96 kg/(m2·s)时,斜管内存在多流态,分别为过渡填充流、填充流、密相流;在斜管中部通入松动风,可以有效改善颗粒输送能力和斜管蓄压能力.
EXPERIMENTAL STUDY ON FLOW CHARACTERISTICS OF CATALYST PARTICLES IN INCLINED PIPE WITH NEGATIVE PRESSURE GRADIENT
On the Φ150 mm × 3 600 mm negative pressure gradient tube-valve experimental device,the characteristic parameters of the axial dynamic pressure in the inclined tube with different catalyst particle mass flow rates(Gs)were measured and analyzed,and the flow characteristics of catalyst particles in inclined tube of FCC unit were studied.The results showed that the pressure storage capacity of the inclined pipe increased with the increase of particle mass flow rate Gs and the lean phase stratified flow and dense phase stratified flow appeared successively in the pipe.The pressure distribution,dominant frequency,amplitude and pressure variance in the inclined tube correspond to the flow pattern,which could be used for quantitative identification of the flow pattern.When Gs=65.96 kg/(m2·s),there were multiple flow patterns in the inclined pipe,including transition packed-bed flow,packed-bed flow and dense phase flow.The aeration gas was injected into the middle of the inclined pipe to effectively improve the particle conveying capacity and the pressure storage capacity of the inclined pipe.

catalytic crackinginclined pipeflow patterndynamic pressureaeration gas

贺娇、彭威、刘梦溪、唐海光、魏耀东、史柯柯

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中国石油大学(北京)重质油全国重点实验室,北京 102249

中国石油大学(北京)克拉玛依校区工学院

中国石油青海油田格尔木炼油厂

催化裂化 斜管 流态 动态压力 松动风

国家重点研发计划项目中国石油大学(北京)科学基金项目克拉玛依市科技创新人才专项中国石油大学(北京)克拉玛依校区青年人才基金项目

2021YFA15013042462022QZDX00320232023hjcxrc0012XQZX20230037

2024

石油炼制与化工
中国石油化工股份有限公司石油化工科学研究院

石油炼制与化工

CSTPCD北大核心
影响因子:0.825
ISSN:1005-2399
年,卷(期):2024.55(8)