期刊文献+

爆破片装置泄放量计算方法探讨 被引量:7

Research of Discharge Capacity Calculation for Bursting Disc Devices
下载PDF
导出
摘要 结合ASMEⅧ-1 UG125-137及API520(2000版)等最新标准规范,参考美国CRANE公司技术文件《low of Fluids Through Valves,Fittings and Pipes》,介绍了爆破片装置泄放量的另外一种计算方法,即流体阻力系数法,并对两种方法进行了对比分析,同时给出了计算实例。 Having latest standards and specifications like ASMEⅧ-1 UG125-137 and API520(2000)considered and the technical papers like Flow of Fluids Through Valves,Fittings and Pipes from CRANE corporation referenced,the fluid resistance coefficient method for calculating discharge capacity of the bursting disc devices was introduced and compared,and a computation example was also presented.
作者 吴全龙
机构地区 华东理工大学
出处 《化工机械》 CAS 2012年第2期180-182,221,共4页 Chemical Engineering & Machinery
关键词 爆破片装置 泄放系数 流体阻力系数 泄放量 bursting disc device discharge coefficient fluid resistance coefficient discharge capacity
  • 相关文献

参考文献5

  • 1GBl50-1998,钢制压力容器[S].北京:中国标准出版社,1998.
  • 2ASMEⅧ一1.RulesforConstructionofPressureVessels[s].北京:中国石化出版社,2007.
  • 3GB567-1999,爆破片与爆破片装置[S].北京:中国标准出版社,1999.
  • 4GB/T12242-2005,压力释放装置性能试验规范[S].北京:中国标准出版料.2005.
  • 5API 520 Part 1-2000,Sizing,Selection and Installation of Pressure-Relieving Devices in Refineries[ S]. Chica-go : API Publishing Services ,2000.

共引文献1

同被引文献35

  • 1吴全龙,邱清宇.用流体阻力系数法计算爆破片泄放量[J].石油化工设备,2006,35(3):18-20. 被引量:7
  • 2李志义,喻健良.关于爆破片的泄放能力——国家专业技术标准与国际标准异同剖析[J].压力容器,1996,13(3):185-190. 被引量:7
  • 3吴全龙,邱清宇.ASME PTC 25爆破片装置流体阻力系数的测定[J].化工机械,2006,33(4):209-214. 被引量:5
  • 4符松,王亮.湍流转捩模式研究进展[J].力学进展,2007,37(3):409-416. 被引量:46
  • 5中华人民共和国国家质量监督检验检疫总局,中国标准化管理委员会.GB567-2012爆破片安全装置[s].北京:中国标准出版社,2012.
  • 6ISO. IS04126-I0 Safety devices for protection against excessive pressures-sizing of safety valves and connected inlet and outlet lines for gas/liquid two phase flow[S]. Switzerland: International Standards Organization, 2010.
  • 7Zhao Guibing. An easy method to design gas/vapor relief system with rupture disk[J]. Journal of Loss Prevention in the Process Industries, 2015, 35: 321-328.
  • 8Surt Feng, Zhang Fan, Jin Manping, et al. Vent sizing ofcumene hydroperoxide(CHP) system under fire scenario considering emergency flooding measure[J]. Journal of Loss Prevention in the Process Industries, 2014, 32: 230-237.
  • 9Raimondi L. Rigorous calculation of critical flow conditions for pressure safety devices[J]. Process Safety and Environmental Protection, 2007, 85(4): 277-288.
  • 10SchmidtJ. Sizing of nozzles, venturis, orifices, control andsafety valves for initially sub-cooled gas/liquid two-phase flow-The HNEDS method[J]. Forschlngenieurwes, 2007, 71(71): 47-58.

引证文献7

二级引证文献7

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