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含碱条件下的双氧水反应失控与安全泄放特性 被引量:2

Runaway reaction and safety relief characteristics of hydrogen peroxide under alkali conditions
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摘要 利用泄放小试实验装置,研究了双氧水在含碱条件下的热失控特性和泄放条件对安全泄压规律的影响,分别考察了密闭条件下双氧水浓度、碱液浓度和搅拌速率对双氧水分解特性的影响,也考察了不同泄放条件下双氧水的泄放特点。实验结果表明:双氧水浓度和碱液浓度越高,搅拌不均匀,会增加双氧水热失控危险。泄放口径越大,泄放效率越高,在工艺条件允许的情况下,应尽量放大泄放口径;高泄放压力可以提高泄放效率,同时保留较充裕的工艺操作空间,但是过高的泄放压力可能导致体系积聚的能量无法及时泄出。 By using the vent simulation test device of bench scale, the influence of thermal runaway characteristics and relief conditions of hydrogen peroxide under alkali conditions on safety venting law was studied.The influences of hydrogen perox- ide concentration, alkali concentration, and stirring speed on hydrogen peroxide decomposition characteristics under the con- dition of enclosed test environment were investigated respectively, and venting characteristics of hydrogen peroxide under dif- ferent relief conditions were also discussed,The experimental results showed that the higher concentrations of hydrogen per- oxide and alkali, and uneven stirring will increase the risk of thermal runaway of hydrogen peroxide.The larger is the vent aperture,the higher is the vent effficiency.Therefore,if the process conditions allow,the vent aperture should be enlarged as big as possible.Higher vent pressure was also good for improving the vent efficiency and retain enough room for operation. However, the extra-high vent pressure may cause the accumulated energy could not release timely.
出处 《无机盐工业》 CAS 北大核心 2015年第10期69-73,共5页 Inorganic Chemicals Industry
关键词 双氧水 反应失控 泄放特性 hydrogen peroxide runaway reaction blowdown characteristics
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参考文献9

  • 1Fauske H K.Generalized vent sizing monogram for runaway chemi- cal reactions [ J ].Plant/Operations Progress, 1984,3 (4) : 213-215.
  • 2Fisher H G,Forrest H S ,Grossel S S ,et al.Emergency relief system design using DIERS technology :The Design Institute for Emergency Relief Systems (DIERS) project manual [ M ].New York : Wiley - AIChE, 2010.
  • 3Fauske H K.Revisiting DIERS' two-phase methodology for reactive systems twenty years later [J ].Process Safety Progress, 2006,25 (3) : 180-188.
  • 4Fauske H K.Properly size vents for non-reactive and reactive chemi- cals [ J ].Chemical Engineering Progress, 2000,96 (2) : 17-29.
  • 5Noronha J ,Torres A.Why DIERS technology should be used in risk assessment : Call for a 1999 worldwide benchmarking survey on var- ious risk reduction methods used [ J ].Process Safety Progress, 1999, 18(2) : 115-120.
  • 6王利明,王淑兰,丁信伟,朱永江.两相流模型在泄放面积计算中的应用[J].石油化工设备,2005,34(3):47-50. 被引量:8
  • 7周建东,李志义.化学反应失控的紧急泄放[J].化学工业与工程技术,1999,20(3):5-10. 被引量:4
  • 8蒋慧灵,钱新明,傅智敏.反应性液体紧急泄放面积设计进展[J].安全与环境学报,2004,4(2):86-89. 被引量:5
  • 9刘显凡,孟庭宇,喻健良,谢传欣.基于VSP2进行热失控反应泄放装置安全可靠性分析与评估[J].高校化学工程学报,2010,24(6):1046-1051. 被引量:11

二级参考文献23

  • 1岳伟挺,张宏建.基于空隙率的油气两相流流量测量的研究[J].高校化学工程学报,2005,19(3):303-308. 被引量:10
  • 2王利明,王淑兰,丁信伟,朱永江.两相流模型在泄放面积计算中的应用[J].石油化工设备,2005,34(3):47-50. 被引量:8
  • 3黄思才 刘国际.化学反应工程[M].北京:化学工业出版社,1996..
  • 4ZHOU Jian-dong(周建东).Emergency Relief of Runaway Reaction(化学反应失控紧急泄放研究)[D].Dalian(大连):Dalian University of Technology(大连理工大学),2000.
  • 5Melhem G A.Advanced ERS design using computer simulation[C] // International Symposium on Runaway Reaction and Pressure Relief Design.New York:AIChE,1995:502-566.
  • 6Etchells J,Wilday J.Workbook for Chemical Reactor Relief System Sizing[M].London (United Kingdom):HSE,1998.
  • 7Leung J C.Simplified vent sizing methods incorporating two-phase flow[C]// International Symposium on Runaway Reactions and Pressure Relief Design.New York:AIChE,1995:200-236.
  • 8Fauske H K.Flashing flows-some practical guidelines for emergency releases[J].Plant/Operations Progress,1985,4(3):132-134.
  • 9LI Zhi-yi(李志义),YU Jian-liang(喻健良).Rupture Disc Technique and Application (爆破片技术及应用)[M].Beijing(北京):Chemical Industry Press(化学工业出版社),2006.
  • 10Fisher F G,Forrest H S,Grossel S S,et al.Emergency Relief System Design Using DIERS Technology[M].New York:Wiley-AIChE,1992.

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