|
化工过程本质安全化技术研究进展
|
Abstract:
本文分析了化工过程本质安全化技术的研究背景,总结了化工过程本质安全的概念和本质安全化技术的主要设计原则,对五类本质安全指数评价方法和本质安全的换热网络优化设计的研究进展进行详细综述,指出了各本质安全指数评价方法的优缺点。结合评价方法探讨了本质安全化设计原则在化工生产实践中的应用,也就是本质安全的换热网络优化设计。同时指出本质安全原则与换热网络集成方式以及建立求解本质安全换热网络同步优化的数学模型是该技术的关键,可作为未来的研究方向。
This paper introduces the research background of inherent safety technology in chemical process, introduces the concept of inherent safety of chemical process and the main design principles of inherent safety technology, summarizes the research progress of five types of inherent safety index evaluation methods and the optimization design of heat exchanger network of inherent safety, and points out the advantages and disadvantages of each inherent safety index evaluation method. This paper focuses on the application of inherently safe design principle in chemical production practice, that is, the optimization design of inherently safe heat exchanger network. At the same time, it is pointed out that the integration of inherent safety principle and heat exchanger network and the establishment of mathematical model for solving the synchronous optimization of inherently safe heat exchanger network are the key points of this technology, which can be used as the research direction in the future.
[1] | 王杭州, 邱彤, 陈炳珍, 等. 本质安全化的化工过程设计方法研究进展[J]. 化学反应工程与工艺, 2014, 30(3): 254-261. |
[2] | 赵劲松. 化工过程安全[M]. 北京: 化学工业出版社, 2015: 1-7. |
[3] | 闫海报, 张如君. 化工过程的本质安全化设计策略分析[J]. 化工设计通讯, 2019, 11(45): 186-190. |
[4] | Kletz, T.A. (1978) What You Don’t Have, Can’t Leak. Chemical Industry, 10, 287-292. |
[5] | Kletz, T.A. (2003) Inherently Safer Design—Its Scope and Future. Process Safety and Environmental Protection, 81, 401-405. https://doi.org/10.1205/095758203770866566 |
[6] | 葛春涛. 化工过程本质安全原理及应用的研究进展[J]. 化工技术与开发, 2014, 43(10): 26-30. |
[7] | 张帆, 徐伟, 石宁. 化工过程中的本质安全化设计技术研究进展[J]. 安全、健康和环境, 2015, 15(1): 1-4. |
[8] | Hendershot, D.C. (2006) An Overview of Inherently Safer Design. Process Safety Progress, 25, 98-107.
https://doi.org/10.1002/prs.10121 |
[9] | 陈炳珍. 面向本质安全的化工过程设计研究进展[C]//王静康. 中国工程院化工、冶金与材料工学部第七届学术会议论文集. 北京: 化学工业出版社, 2009: 24-28. |
[10] | 叶昊天, 董以宁, 许爽, 等. 考虑本质安全的换热网络多目标优化[J]. 化工学报, 2019, 70(7): 2584-2593. |
[11] | Koller, G., Fischer, U., Hungerbuhler, K., et al. (2000) Assessing Safety, Health and Environmental Impact Early during Process Development. Industrial & Engineering Chemistry Research, 39, 960-972.
https://doi.org/10.1021/ie990669i |
[12] | Rogers, R., Verwoerd, I.M., Bots, T., et al. (2004) How to Integrate She in Process Development and Plant Design. Chemical Engineering, 43, 497-499. |
[13] | Leong, C.T. and Shariff, A.M. (2008) Inherent Safety Index Module (ISIM) to Assess Inherent Safety Level during Preliminary Design Stage. Process Safety and Environmental Protection, 86, 113-119.
https://doi.org/10.1016/j.psep.2007.10.016 |
[14] | Leong, C.T. and Shariff, A.M. (2009) Process Route Index (PRI) to Assess Level Explosiveness for Inherent Safety Quantification. Journal of Loss Prevention in the Process Industries, 22, 216-221.
https://doi.org/10.1016/j.jlp.2008.12.008 |
[15] | Shariff, A.M., Leong, C.T., Zaini, D., et al. (2012) Using Process Stream Index (PSI) to Assess Inherent Safety Level during Preliminary Design Stage. Safety Science, 50, 1098-1103. https://doi.org/10.1016/j.ssci.2011.11.015 |
[16] | Gentile, M., Rogers, W.J., Mannan, M.S., et al. (2003) Develop-ment of a Fuzzy Logic-Based Inherent Safety Index. Process Safety and Environmental Protection, 81, 444-456. https://doi.org/10.1205/095758203770866610 |
[17] | Srinivasan, R. and Nhan, N.T. (2008) A Statistical Approach for Evaluating Inherent Benignness of Chemical Process Routes in Early Design Stages. Process Safety and Environment Protection, 86, 163-174.
https://doi.org/10.1016/j.psep.2007.10.011 |
[18] | Khan, F.I. and Amyotte, P.R. (2004) Integrated Inherent Safety Index (I2SI): A Tool for Inherent Safety Evaluation. Process Safety Progress, 23, 136-148. https://doi.org/10.1002/prs.10015 |
[19] | Gupta, J.P. and Edwards, D.W. (2003) A Simple Graphical Method for Measurement of Inherent Safety. Journal of Hazardous Materials, 104, 15-30. https://doi.org/10.1016/S0304-3894(03)00231-0 |
[20] | 石晓伟, 王达. 化工过程模糊安全评价及其在过程开发中的应用[J]. 广州化工, 2015, 43(22): 242-244. |
[21] | 余金栉. 不同化工过程本质安全评价方法的比较与分析[J]. 石化技术, 2018, 25(10): 304. |
[22] | 都健, 杨坡, 刘琳琳, 等. 带有热储罐的间歇过程换热网络综合[J]. 化工学报, 2013, 64(12): 4325-4329. |
[23] | 肖武, 史朝霞, 姜晓滨, 等. 考虑管壳式换热器强化的换热网络综合研究进展[J]. 化工进展, 2018, 4(37): 1267-1275. |
[24] | 霍兆义, 尹洪超, 赵亮, 等. 国内换热网络综合方法研究进展与展望[J]. 化工进展, 2012, 31(4): 726-731. |
[25] | 孔令启, 张晓荷, 李玉刚, 等. 间歇化工过程热集成研究发展[J]. 化工进展, 2020, 39(10): 3849-3858. |
[26] | Chan, I., Alwi, S.R.W., Hassim, M.H., et al. (2014) Heat Exchanger Network Design Considering Inherent Safety. Energy Procedia, 61, 2649-2473. https://doi.org/10.1016/j.egypro.2014.12.025 |
[27] | Liu, X., Klemesa, J.J., Varbanov, P.S., et al. (2015) Safety Issue Consideration for Direct and Indirect Heat Transfer on Total Sites. Chemical Engineering, 45, 457-459. |
[28] | Zaini, D., Pasha, M. and Kaura, S. (2016) Inherently Safe Heat Exchanger Network Design by Consequence Based Analysis. Pro-cedia Engineering, 148, 908-915. https://doi.org/10.1016/j.proeng.2016.06.500 |
[29] | Pasha, M., Zaini, D. and Shariff, A.M. (2017) Inherently Safer Design for Heat Exchanger Network. Journal of Loss Prevention in the Process Industries, 48, 55-70. https://doi.org/10.1016/j.jlp.2017.04.002 |
[30] | 李宝红, 李继文. 采用换热器负荷图指导换热网络改造的新方法[J]. 化工学报, 2020, 71(3): 1288-1296. |
[31] | Jung, S., Ng, D., Laird, C.D., et al. (2010) A New Approach for Facility Siting Using Mapping Risks on a Plant Grid Area and Optimization. Journal of Loss Prevention in the Process Industries, 23, 824-830.
https://doi.org/10.1016/j.jlp.2010.06.001 |
[32] | Jung, S., Ng, D., Lee, J.H., et al. (2010) An Approach for Risk Re-duction Based on Optimizing the Facility Layout and Siting in Toxic Gas Release Scenarios. Journal of Loss Prevention in the Process Industries, 23, 139-148.
https://doi.org/10.1016/j.jlp.2009.06.012 |
[33] | Diaz-Ovalle, C., Vazquez-Roman, R. and Mannan, M.S. (2010) An Approach to Solve the Facility Layout Problem Based on the Worst-Case Scenario. Journal of Loss Prevention in the Process Industries, 23, 385-392.
https://doi.org/10.1016/j.jlp.2010.01.004 |
[34] | Vazquez-Roman, R., Lee, J.H., Jung, S., et al. (2010) Optimal Facil-ity Layout under Toxic Release in Process Facilities: A Stochastic Approach. Computers & Chemical Engineering, 34, 122-133.
https://doi.org/10.1016/j.compchemeng.2009.08.001 |
[35] | Inchaurregui-Mendez, J.A., Vazquez-Roman, R., Ponce-Ortega, J.M., et al. (2016) Optimal Safe Layouts with Heat Exchanger Networks Synthesis Having Isothermal Process Streams. Chemical Engineering, 48, 27-29. |
[36] | Nemet, A., Klemes, J.J., Moon, I., et al. (2015) Safety Analy-sis Embedded in Total Site Synthesis. Chemical Engineering, 45, 47-48. |
[37] | Nemet, A., Klemes, J.J., Moon, I., et al. (2015) Synthesis of Safer Heat Exchanger Networks. Chemical Engineering Transactions, 56, 1885-1890. |
[38] | Nemet, A., Klemes, J.J., Kravanja, Z., et al. (2017) Heat Exchanger Networks Synthesis Considering Risk Assessment for Entire Network Lifetime. Chemical Engineering Transaction, 57, 307-312. |
[39] | Nemet, A., Klemes, J.J., Kravanja, Z., et al. (2017) Process Synthesis with Simultaneously Inherent Safety. Chemical Engineering Transaction, 61, 374-379. |
[40] | 吕俊峰, 肖武, 王开锋, 等. 换热网络多目标优化算法研究进展[J]. 化工进展, 2016, 35(2): 352-357. |