期刊文献+

颗粒塞阀及其操作特性的研究

Study on the Particle Plug Valve and its Operation Charateristics
在线阅读 下载PDF
导出
摘要 通过对粗聚丙烯和瓷球两种Geldart-D类颗粒漏斗-立管系统实验研究,发现在悬料操作区域内,漏斗-立管系统具有较高的抗压能力。因此,把在悬料条件下具有抗压特征的漏斗-立管系统(无机械转动部件阀门)称之为“颗粒塞阀”。颗粒塞阀的抗压下限可由下式 ()22mfgmfgmf24oomf233tsptmfmfsp300(1)()(1)d()7.0()dUUDDplDdDdemrefeef---=+ 沿立管高度积分求得;而抗压上限是由Ergun公式沿立管高度积分求得,但计算所用的气速是指此系统的漏斗中颗粒的有效重量等于气固之间作用的曳力时所对应的立管中气速。并指出了此阀可用于把颗粒从低压容器输送到高压容器的场合。 In the hopper-standpipe system, experiments were carried out to study the hung-up regime for coarse polypropylene and ceramic ball particles, which belong to Geldart-D powder. The system in the hung-up regime is named as the Particle Plug Valve because of its characteristics of high anti-pressure. The incipient condition of anti-pressure of particle plug valve could be obtained by integrating the ddpl differential equation along the height of the standpipe. However, the terminal condition could be obtained by integrating the Ergun equation along the height of the standpipe, where the gas velocity used refers to that in the standpipe when the buoyancy force exerted on the entire particle bed by fluid flowing upwards equals to the effective gravitational force of all particle in the hopper of the system. The particle plug valve can be used when the particles are conveyed from the low-pressure vessel to the high-pressure one.
出处 《高校化学工程学报》 EI CAS CSCD 北大核心 2004年第5期571-578,共8页 Journal of Chemical Engineering of Chinese Universities
关键词 颗粒塞阀 Geldart-D颗粒 流化床 漏斗-立管系统 悬料 particle plug valve geldart-D powder fluidized bed hopper-standpipe system hung-up regime
  • 相关文献

参考文献11

  • 1胡庆元,景山,王金福,金涌.粗颗粒在锥型床中的流化特性[J].高校化学工程学报,2000,14(1):12-18. 被引量:11
  • 2胡庆元,景山,王金福,金涌.粗颗粒在负压差漏斗-立管系统悬料区特性[J].高校化学工程学报,2000,14(3):251-257. 被引量:4
  • 3景山,胡庆元,王金福,金涌.漏斗-立管系统悬料区的压降计算方法[J].高校化学工程学报,2000,14(4):320-323. 被引量:1
  • 4Deiva V R, Chaouki J, Klvana D. Fluidization of cryogels in a conical column [J]. Powder Technol, 1996, 89: 179-186.
  • 5Olazar M San, Jose M J, Aguayo A T J, Arandes M, Bilbao J. Stable operation conditions for gas-solids contact regimes in conical spouted beds [J]. Ind Eng Chem Res, 1992, 31: 1784-1792.
  • 6Ergun S. Fluid flow through packed columns [J]. Chem Eng Progr, 1952, 48: 89-96.
  • 7郭天民 宋瑜 等.颗粒自由、正压差和负压差流落研究[J].化工学报,1960,2:97-97.
  • 8Knowlton T M, Hirsan I. L-Valves characterized for solids flow [J]. Hydrocarbon Processing, 1978, 3: 149-159.
  • 9Knowlton T M, Hirsan I, Leung L S. in Davidson JF, Keairns D L. (eds). Fluidization [M], Cambridge Univ Press, 1978: 128.
  • 10Li X G, Liu D L, Kwauk M. Pneumatically controlled multi-stage fluidized bed 2 [A]. Proc, Joint Meeting of Chem Eng, SIESC and AIChE [C]. Beijing: Chemical Industry Press, 1982: 382.

二级参考文献10

  • 1Bi H T,Can J Chem Eng,1997年,75卷,4期,460页
  • 2Peng Y,Chem Eng Sci,1997年,52卷,14期,2277页
  • 3Olazar M,Ind Eng Chem Res,1992年,31卷,1784页
  • 4张先润,化工机械,1976年,6卷,34页
  • 5Jing S,Powder Technol,1999年,101卷,266页
  • 6Zhang J Y,Powder Technol,1998年,97卷,109页
  • 7Peng Y,Chem Eng Set,1997年,52卷,14期,2277页
  • 8郭天明,化工学报,1960年,2卷,97页
  • 9胡庆元,景山,王金福,金涌.粗颗粒在锥型床中的流化特性[J].高校化学工程学报,2000,14(1):12-18. 被引量:11
  • 10胡庆元,景山,王金福,金涌.粗颗粒在负压差漏斗-立管系统悬料区特性[J].高校化学工程学报,2000,14(3):251-257. 被引量:4

共引文献12

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部