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作 者:付小苏[1] 张颂红[1] 刘炳炎[1] 姚克俭[1]
机构地区:[1]绿色化学合成技术国家重点实验室培育基地浙江工业大学化学工程与材料学院,浙江杭州310032
出 处:《石油化工》2011年第7期775-779,共5页Petrochemical Technology
基 金:中国石油化工股份有限公司资助项目(302004);浙江省科技计划项目(2009C31045)
摘 要:在内径600mm的有机玻璃塔内,以空气-水为物系,研究了圆形固定阀塔板和条形固定阀塔板的流体力学性能;在内径600mm的不锈钢塔内,以正庚烷-环己烷为物系,研究了两种塔板的传质性能。实验结果表明,圆形固定阀塔板的板压降比条形固定阀塔板高约40%,与F1浮阀塔板相当;相对于条形固定阀塔板,圆形固定阀塔板上积液点气速更低,液泛点气速更高,操作弹性更大;圆形固定阀塔板气液接触更合理,传质效率更高;圆形固定阀塔板开孔率更高,可达到25%,鼓泡更均匀。圆形固定阀塔板具有高效、大通量、高弹性、抗堵等特点,适宜在石油化工领域中应用。Hydrodynamics of an air-water system in standing-valve trays or elongated standing-valve .trays a 600 mm ID organic glass column with round was studied, and mass transfer behavior of n- heptane-cyclohexane system in a 600 nun ID stainless steel column with the two kinds of trays separately was investigated. The tray pressure drop of the round standing-valve trays was 40% higher than that of the elongated standing-valve trays, similar to that of F1 valve trays. Compared with the elongated standing-valve trays, the round standing-valve trays had low effusion point gas velocity, high flooding point gas velocity, high operating flexibility, reasonable gas-liquid contact and high mass transfer efficiency. And the round standing-valve trays had larger percentage of open area (about 25% ) and more uniform bubbling than the elongated standing-valve trays.
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