期刊文献+

过硫酸铵胶囊破胶剂的自加速分解温度和自反应过程研究 被引量:3

Study on the self-accelerating decomposition temperature and self-reaction process of encapsulated ammonium persulfate gel breaker
下载PDF
导出
摘要 为评价过硫酸铵胶囊破胶剂在运输中的自反应危险性,按照联合国《关于危险货物运输的建议书——试验与标准手册》中的H 2方法,采用绝热杜瓦量热仪对过硫酸铵胶囊破胶剂进行绝热储存试验,并计算了该物质在3种典型包装下的自加速分解温度。结果表明,分解反应分为2步,其活化能接近,这2步反应实质上是同一反应,即最初反应进行到一定阶段后由于接触面上的反应物消耗和产物积累而停止,而温度升高又引起包覆的聚合物软化,增大了反应物接触面和产物的扩散速度,从而使反应重新开始。研究表明,该物质的包装件不应划入联合国规定的4.1项危险品中的自反应性物质。 The present paper is aimed to introduce our study results on the self-accelerating decomposition temperature and self-reaction process of encapsulated ammonium persulfate gel breaker. As is known, since the hazardous self-reactive explosion of encapsulated ammonium persulfate gel breaker in the process of transportation has often aroused great concern in industrial and transportation practice, the study on how to solve the problem has become a hot topic in recent years. Thus, in this paper, we have first of all introduced and analyzed a few methods for the decomposition temperature (SADT) testing. Next, we have introduced the UN H.2 method in UN "Recommendation on transport of dangerous goods-manual of test and criteria", which has often been chosen to test the encapsulated ammonium persulfate gel breaker's SADT. In proceeding with our study, we have prepared an instrument calibration test by sodium chloride. In addition, we have also worked out the heat loss rate curve of the Dewar container and the heating curve of the gel breaker through examination. By using the heat loss curve per unit mass of three UN packagings for solid stated in the manual of the gel breaker' s SADT treating, it is possible to work out the temperatures of the gel breaker' s SADT in three packagings-1G (50 L), 4G (50 L) and 1G (110 L), which are 90 ℃ , 90 ℃ , and 85 ℃ respectively. The above resuits show that the gel breaker in the all three packages should not be classified as self-reactive substances by UN RTDG-model regulations. Furthermore, there were two kinds of reactions with onset temperatures of about 40 ℃ and 80 ℃ in the decomposition process. The activating energies can also be worked out after the simplified kinetic data treatment, and the final results of the two reactions are very close, which shows the two reactions are essentially the same. Therefore, if the first decomposition reaction ends up due to consumption of the reactants and accumulation of products on the contact surface, it will restart at a higher temperature, since high temperature would soften capsulate polymers, enlarge the contact surface of the reactants again, and speed the diffusion of the products.
出处 《安全与环境学报》 CAS CSCD 北大核心 2010年第3期147-150,共4页 Journal of Safety and Environment
关键词 安全科学技术基础学科 自加速分解温度 自反应性 热危害 过硫酸铵胶囊破胶剂 反应动力学 绝热杜瓦量热仪 basic disciplines of safety science and technology SADT self-reactivity thermal hazard encapsulatedammonium persulfate gel breaker reaction kinetics adiabatic Dewar calorimeter
  • 相关文献

参考文献8

  • 1LIANG Zhiqi(梁志齐).Micro-capsule technology and application(微胶囊技术及其应用)[M].Beijing:China Light Industry Press,1999.
  • 2张文胜.新型压裂液破胶剂的研究与应用[J].钻井液与完井液,2002,19(4):10-12. 被引量:19
  • 3United Nations.Recommendation on transport of dangerous goods-model regulations[M].15th ed.New York and Geneva:United Nations Publications,2007.
  • 4United Nations.Recommendation on transport of dangerous goods-manual of test and criteria[M].4th ed.New York and Geneva:United Nations Publications,2003.
  • 5SUN Jinhua(孙金华),DING Hui(丁辉).Thermal hazard assessment for chemicals(化学物质热危险性评价)[M].Beijing:Science Press,2005:158161.
  • 6BARIN I.Thermochemical data of pure substances Vol.2 (纯物质热化学数据手册(下卷))[M].CHENG Nailiang(程乃良),NIU Sitong(牛四通),XU Guiying(徐桂英),trans.Beijing:Science Press,2003:1118.
  • 7STOESSEL F.Thermal safety of chemical processes-risk assessment and process design[M].Weinheim:Wiley-VCH,2008:50-52.
  • 8孙金华,陆守香,孙占辉.自反应性化学物质的热危险性评价方法[J].中国安全科学学报,2003,13(4):44-47. 被引量:47

二级参考文献13

  • 1埃克诺米德斯MJ 诺尔蒂KG 等.油藏增产措施[M].北京:石油工业出版社,1991.574-577.
  • 2Whitmore, M. W., Wilberforce, J. K.. Use of the accelerating rate calorimeter and the thermal activity monitor to estimate stability temperature, J. Loss Prey., 1993, 6(2) :95-- 101.
  • 3Fisher, H. G. , Goetz, D. D.. Determination of self-accelerating decomposition temperatures for self-reactive substances. J.Loss Prev. , 1993, 6(3) : 183-- 193.
  • 4Sun J, H. , Li, Y. F. Hasegawa, K.. A study of self-accelerating decomposition temperature (SADT) Using reaction calorimetry. J. Loss Prev. , 2001, 14(5) :331--336.
  • 5Li, Y. F., Hasegawa, K.. On the thermal decomposition mechanism of self-reaction materials and the evaluating method for their SADTs, 9th International symposium on loss prevention and safety promotion in the process industries, Spain,1998: 555 -- 569.
  • 6United Nations. Recommendations on the transport of dangerous goods, manual of tests and criteria 3rd revised edn., 1999.
  • 7吉德利JL.水力压裂技术新进展[M].北京:石油工业出版社,1995.600-622.
  • 8采油化学.石油大学出版社
  • 9SPE 19433
  • 10SPE 24300

共引文献64

同被引文献22

引证文献3

二级引证文献2

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