首页|水力旋流器的底流口直径对其分离性能的影响

水力旋流器的底流口直径对其分离性能的影响

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底流口直径对旋流器的性能有着非常显著的影响。本研究采用体积法测量并计算了颗粒浓度和分离效率,在流化催化裂化(FCC)催化剂-水液固体系内考察了底流口直径对水力旋流器分离性能的影响。发现在入口浓度不同时,底流口直径对旋流器性能的影响规律不同。在低浓度体系(C 入≤10%)内,随着底流口直径的增加底流液浓度急剧减小,但溢流液浓度基本不变。在高浓度体系(C 入≥15%)内,随底流口直径的增加底流液浓度变化不大,但溢流液浓度显著降低。在本实验范围内,随着底流口直径的增加,分流比显著增加,分离效率明显增加,压降略有降低。
Influence of the Spigot Diameter of a Hydrocyclone on Its Separation Performance
The spigot diameter has a significant influence on performance of a hydrocyclone. In a cold model hydrocyclone dealing with fluid catalytic cracking (FCC) catalyst and water, the separation performance was investigated by measuring volume fraction of the particle in fluid and calculating the particle concentration and separation efficiency. It was found that the influence of the spigot diameter on the separation performance of hydrocyclone considerably varied with solid loading of the system. For the system of low solid concentration (Cinlet≤10%), with increasing the spigot diameter, solid concentration of flow out of the spigot significantly decreased, while that of flow out of the vortex finder barely changed. For the high solid loading system (Cinlet≥15%), when the spigot diameter increased solid concentration of flow out of the spigot approximately kept constant, but that of flow out of the vortex finder considerably decreased. For all solid loading employed in this work, the split ratio and separation efficiency increased, but the pressure drop of the hydrocyclone slightly decreased with the increase of spigot diameter.

hydrocyclonesplit ratioseparation efficiencypressure drop

宫振宇、张妍君、鄂承林、刘梦溪、杨斌

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中国石油大学 北京,北京 102249

中国石油化工集团公司北京燕山分公司,北京 102500

中国石油天然气集团公司中国寰球工程公司,北京 100029

中国石油天然气集团公司大港油田原油运销公司,天津 300280

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水力旋流器 分流比 分离效率 压降

2014

化学反应工程与工艺
联合化学反应工程研究所 ,中石化上海石油化工研究院

化学反应工程与工艺

CSTPCDCSCD北大核心
影响因子:0.392
ISSN:1001-7631
年,卷(期):2014.(5)
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