Risk Analysis of Chemical Plant Explosion Accidents Based on Bayesian Network
Abstract
:1. Introduction
2. Materials and Methods
- Activity: This node refers to some activities carried out in the chemical plant, such as running, using, transporting, and cleaning equipment. The frequency and danger of different activities in the factory are different. For example, when making chemicals, accidents are more likely to occur;
- Factory type: Due to numerous chemical industry categories, we divide them into three main categories: petrochemical, chemical fiber, and basic chemical. This is just a big category for the chemical industry, and there are many different subcategories under each category;
- Hazardous material characteristics: The characteristics of hazardous materials have a direct impact on the severity of the explosion. Some hazardous materials are flammable and explosive, toxic and harmful, or easy to vaporize. If a factory with toxic and harmful hazardous materials explodes, it will affect the health of the residents around the factory and lead to inadequate emergency response or more severe consequences;
- Material form: This node refers to the form of the material, such as gas, liquid, powder, solid. If an explosion caused by liquids or gases, hazardous materials in this state spread quickly, and the consequences may be more serious. Among them, the dust explosion is a very important type, and we classify this type into the state (3);
- Accident equipment: We use the device ontology model [30] to divide accident equipment into four main categories: heat exchange equipment, reaction equipment, fluid conveying equipment, and tower equipment. High-Pressure equipment such as a pump or compressor is the most dangerous equipment. The reaction is often carried out under high pressure or high temperature, so the reaction equipment includes rotating machinery;
- Personnel factors: this node refers to accidents caused by personnel factors. The personnel factors include operational violations, behavioral errors, and unfamiliar with the operational process;
- Equipment factors: This node refers to chemical plant explosion accidents caused by equipment factors. Based on existing literature and expert experience, equipment factors can be classified into equipment selection errors, static electricity or explosion-proof line problems, equipment aging, lack of maintenance, and equipment damage;
- Incidental event: There is a cause of explosion before the explosion, such as over-temperature and over-pressure in the equipment, material flowing out of the equipment, the material is ignited;
- Type of explosion: We classify this node into two states based on the expert experience, one is normal explosion, the other is other types of an explosion, such as a flash explosion. Normal explosions often have relatively small casualties and will not cause a series of accidents. Other types of explosions refer to a series of explosions or fires that cause more serious consequences;
- Emergency response: This node refers to the emergency mechanism, the contingency plan of the chemical plant, and the emergency plan after the explosion. We define two situations, effective response, and inadequate response;
- Property loss: We classify property loss into four levels according to the Regulations on Production Safety Accident Reporting and Investigation and Handling [31]. Property loss have four levels: less than 10 million yuan, 10–20 million yuan, 5000–100 million yuan, more than 100 million yuan;
- Casualties: Similar to property damage, casualties have four levels.
2.1. BN Construction
2.1.1. Step 1: Structure Learning
- (1)
- Use expert knowledge to obtain pair-wise influential relationships among BN nodes. We implemented the process by a questionnaire survey of four experts;
- (2)
- Compare the direct causal relationship between the two factors and establish a contiguous Boolean matrix;
- (3)
- Calculate the reachable matrix according to the adjacent Boolean matrix. This step is not required, and it is a sacrifice of computational speed for comprehensibility;
- (4)
- Partition reachable matrix into different levels to construct the influence diagram. Once the superior node is determined, it will be separated from the other nodes;
- (5)
- Draw the direct links and derive the directed acyclic graph.
2.1.2. Step 2: Parameter Learning
3. Results and Discussions
3.1. Scenario Reasoning
3.2. Sensitivity Analysis
3.2.1. The Sensitivity of Nodes in “Accident Results” and Emergency Response
3.2.2. Evaluation of the Most Severe Chemical Plant Explosion Accident
3.2.3. Impact of the Fast and Effective Emergency Response Measures
4. Conclusions
- (a)
- We analyze the process of the chemical plant explosion and propose 12 key nodes, which correspond to “Accident background,” “Cause of accident,” “Critical event,” and “Accident results.” It should be noted that in Hazard and Operability Analysis (HAZOP)and Safety Integrity Level Analysis (SIL), accident consequences are often quantified from production losses, property losses, human damage, and environmental impacts [42,43]. Chemical plant accidents have a significant impact on the environment, because of the characteristics of toxic or non-toxic chemicals, the state of gaseous or liquid chemicals, proximity to rivers or residential areas, and cause a domino effect. However, due to the limited number of historical cases we collected and the lack of environmental impact results for small and medium-sized accidents (about 95% of the total number of cases), only major accidents or particular chemical material accidents include environmental impacts. Therefore, we did not collect this information before. In the future, we will specifically collect the nodes that have the impact of the accident environment, further analyze the vital factor of the accident environment, and propose solutions;
- (b)
- We Use the Dempster-Shafer theory and the ISM-K2 algorithm to construct a Bayesian network model for chemical plant explosion accidents and the EM algorithm to learn its probability distribution;
- (c)
- Through “Forward and backward reasoning” and “Sensitivity analysis,” the scenario reasoning is carried out, various states of the nodes and severe catastrophic conditions are analyzed.
- (1)
- Effective emergency response plays a vital role in reducing property loss and casualties. The most severe accidents are directly related to untimely emergency response. It should be noted that the structure of the network has a great impact on the sensitivity results. Since the node is closer to the casualty and property loss nodes, it has a stronger influence;
- (2)
- In chemical plant explosion accidents, different equipment and different equipment problems will affect the final emergency response, property loss, and casualties. More critical, equipment factors have a more significant impact than personnel factors. However, personnel factors are the key causes of accidents in all stages of the hazardous chemicals industry chain. From a longer time perspective, equipment factors are also caused by management factors [44]. At the same time, equipment defects of human defects will eventually lead to accidents [45];
- (3)
- The type of chemical plant and ongoing work have a less impact on the final casualties. The effects of different explosions are also not apparent, but different hazardous materials have a significant impact. The impact of different explosion causes is even higher, such as the damage caused by loss of containment is higher than other types of hazards;
- (4)
- In the prevention of chemical plant explosions, there are many kinds of prevention methods, such as safety management of equipment, employee safety operation training, and quick and effective emergency response. Among these methods, equipment safety management and personnel safety training are more important and useful. This also shows that passive security measures (safety management of equipment) are more robust than active security measures (emergency response) [46]. Hamza also proposed in the literature, to improve the safety of the process, the training focus on human factors is important [47], but an effective emergency response can minimize casualties and property loss. Engineering measures to prevent chemical plant explosions in advance are also critical, including the design of hazardous area classifications or ensuring separation distances to minimize damage. Reference [48] mandates EU member states to consider the domino effect and land use planning. Reference [15] combined the results of the risk analysis with the Analytic Hierarchical Process to design an optimal layout in which the level of on-site and off-site risks will be minimized in major accidents. When a domino scenario occurs, the engineering measure can reduce hazards and determine the number of installations in danger and set the corresponding best emergency strategy for different units. Furthermore, in emergencies, the fire protection team can intervene according to the best plan planned [49].
Author Contributions
Funding
Conflicts of Interest
References
- Zerrouki, H.; Smadi, H. Bayesian belief network used in the chemical and process industry: A review and application. J. Fail. Anal. Prev. 2017, 17, 159–165. [Google Scholar] [CrossRef]
- Zhang, N.; Shen, S.L.; Zhou, A.N.; Chen, J. A brief report on the March 21, 2019 explosions at a chemical factory in Xiangshui, China. Process Saf. Prog. 2019, 38, e12060. [Google Scholar] [CrossRef]
- Babrauskas, V. The ammonium nitrate explosion at West, Texas: A disaster that could have been avoided. Fire Mater. 2018, 42, 164–172. [Google Scholar] [CrossRef]
- Li, Y.; Liu, Z.; Jia, J. Statistic analysis of chemical enterprises accidents occurring in China during 2006~2015. Appl. Chem. Ind. 2017, 46, 1620–1623. [Google Scholar]
- Liu, R. Research of Accident Analysis and Prediction of Chemical Manufacturers. Master’s Thesis, North University of China, Taiyuan, China, 2015. [Google Scholar]
- Reniers, L.G.L. Multi-Plant Safety and Security Management in the Chemical and Process Industries; (RENIERS:MULTIPLANT SAFETY O-BK) || Appendix B: The IESLA Instrument; John Wiley & Sons, Inc.: Hoboken, NJ, USA, 2010; pp. 251–260. [Google Scholar] [CrossRef]
- Wang, J.; Fan, Y.; Gao, Y. Analysis of causes of accidents in chemical industry based on HFACS model. China Saf. Sci. J. 2018, 28, 81–86. [Google Scholar]
- Liu, J.; Li, L. Suggestion on accident analysis and fire safety management of chemical industry park. Fire Sci. Technol. 2014, 33, 1343–1347. [Google Scholar]
- Kao, C.S.; Hu, K.H. Acrylic reactor runaway and explosion accident analysis. J. Loss Prev. Process Ind. 2002, 15, 213–222. [Google Scholar] [CrossRef]
- De Rademaeker, E.; Suter, G.; Pasman, H.J.; Fabiano, B. A review of the past, present and future of the European loss prevention and safety promotion in the process industries. Process Saf. Environ. Prot. 2014, 92, 280–291. [Google Scholar] [CrossRef]
- Huang, L.; Cai, G.; Yuan, H.; Chen, J. A hybrid approach for identifying the structure of a Bayesian network model. Expert Syst. Appl. 2019, 131, 308–320. [Google Scholar] [CrossRef]
- Husmeier, D. Introduction to Learning Bayesian Networks from Data; Springer: London, UK, 2005; pp. 17–57. [Google Scholar]
- Khakzad, N. Application of dynamic Bayesian network to risk analysis of domino effects in chemical infrastructures. Reliab. Eng. Syst. Saf. 2015, 138, 263–272. [Google Scholar] [CrossRef]
- Khakzad, N.; Yu, H.; Paltrinieri, N.; Khan, F. Reactive Approaches of Probability Update Based on Bayesian Methods. Dyn. Risk Anal. Chem. Pet. Ind. 2016, 51–61. [Google Scholar] [CrossRef]
- Khakzad, N.; Reniers, G. Risk-based design of process plants with regard to domino effects and land use planning. J. Hazard. Mater. 2015, 299, 289–297. [Google Scholar] [CrossRef] [PubMed]
- Villa, V.; Paltrinieri, N.; Khan, F.; Cozzani, V. Towards dynamic risk analysis: A review of the risk assessment approach and its limitations in the chemical process industry. Saf. Sci. 2016, 89, 77–93. [Google Scholar] [CrossRef]
- Lee, K.; Park, I.; Yoon, B. An approach for R&D partner selection in alliances between large companies, and small and medium enterprises (SMEs): Application of bayesian network and patent analysis. Sustainability 2016, 8, 18. [Google Scholar]
- Ghasemi, F.; Sari, M.H.M.; Yousefi, V.; Falsafi, R.; Tamosaitiene, J. Project portfolio risk identification and analysis, considering project risk interactions and using bayesian networks. Sustainability 2018, 10, 1609. [Google Scholar] [CrossRef] [Green Version]
- Chu, Z.; Wang, W.; Wang, B.; Zhuang, J. Research on factors influencing municipal household solid waste separate collection: Bayesian belief networks. Sustainability 2016, 8, 152. [Google Scholar] [CrossRef] [Green Version]
- Tang, Z.; Li, Y.; Hu, X.; Wu, H. Risk analysis of urban dirty bomb attacking based on bayesian network. Sustainability 2019, 11, 306. [Google Scholar] [CrossRef] [Green Version]
- Francis, R.A.; Guikema, S.D.; Henneman, L. Bayesian Belief Networks for predicting drinking water distribution system pipe breaks. Reliab. Eng. Syst. Saf. 2014, 130, 1–11. [Google Scholar] [CrossRef]
- Wu, J.; Xu, S.; Zhou, R.; Qin, Y. Scenario analysis of mine water inrush hazard using Bayesian networks. Saf. Sci. 2016, 89, 239. [Google Scholar] [CrossRef]
- Yuan, Z.; Khakzad, N.; Khan, F.; Amyotte, P. Risk analysis of dust explosion scenarios using Bayesian networks. Risk Anal. 2015, 35, 278–291. [Google Scholar] [CrossRef]
- Wu, J.S.; Hu, Z.Q.; Chen, J.Y.; Li, Z. Risk assessment of underground subway stations to fire disasters using bayesian network. Sustainability 2018, 10, 21. [Google Scholar] [CrossRef] [Green Version]
- Zhang, C.; Wu, J.S.; Hu, X.F.; Ni, S.J. A probabilistic analysis model of oil pipeline accidents based on an integrated Event-Evolution-Bayesian (EEB) model. Process Saf. Environ. Prot. 2018, 117, 694–703. [Google Scholar] [CrossRef]
- Warfield, J.N. Developing interconnection matrices in structural modeling. IEEE Trans. Syst. Man Cybern. 1974, 81–87. [Google Scholar] [CrossRef] [Green Version]
- Cooper, G.F.; Herskovits, E. A Bayesian method for the induction of probabilistic networks from data. Mach. Learn. 1992, 9, 309–347. [Google Scholar] [CrossRef]
- Heckerman, D.; Geiger, D.; Chickering, D.M. Learning Bayesian networks: The combination of knowledge and statistical data. Mach. Learn. 1995, 20, 197–243. [Google Scholar] [CrossRef] [Green Version]
- Liu, S.; Wan, F.; Yang, Y. Weiming, model of chemical domain device ontology constructing. J. East China Univ. Sci. Technol. 2017, 43, 404–410. [Google Scholar]
- BayesFusion GeNIe Modeler User Manuel. Available online: http://support.bayesfusion.com/docs/genie.pdf (accessed on 20 October 2019).
- Report on Production Safety Accident and Regulations of Investigation and Treatment, Council, S. (Ed.) Beijing, China, 2007.
- Hu, C. Research overview on bayesian network. J. Hefei Univ. 2013, 23, 33–40. [Google Scholar]
- Zhou, Z.; Shen, G.; Zhu, X. Application of bayesian network in intelligence prediction. Inf. Sci. 2014, 32, 3–8. [Google Scholar]
- Banuls, V.A.; Turoff, M.; Roxanne Hiltz, S. Collaborative scenario modeling in emergency management through cross-impact. Technol. Forecast. Soc. Chang. 2013, 80, 1756–1774. [Google Scholar] [CrossRef]
- Dempster, A.P. Upper and lower probabilities induced by a multivalued mapping. Ann. Math. Stat. 1967, 38, 325–339. [Google Scholar] [CrossRef]
- Dempster, A.P.; Laird, N.M.; Rubin, D.B. Maximum likelihood from incomplete data Via the EM algorithm. J. R. Stat. Soc. Ser. B Methodol. 1977, 39, 1–38. [Google Scholar]
- Al-Ajlan, A. The comparison between forward and backward chaining. Int. J. Mach. Learn. Comput. 2015, 5, 106–113. [Google Scholar] [CrossRef] [Green Version]
- Nadkarni, S.; Shenoy, P.P. A Bayesian network approach to making inferences in causal maps. Eur. J. Oper. Res. 2001, 128, 479–498. [Google Scholar] [CrossRef] [Green Version]
- Ismail, M.A.; Sadiq, R.; Soleymani, H.R.; Tesfamariam, S. Developing a road performance index using a Bayesian belief network model. J. Frankl. Inst. Eng. Appl. Math. 2011, 348, 2539–2555. [Google Scholar] [CrossRef]
- Khan, F.I.; Abbasi, S.A. Techniques and methodologies for risk analysis in chemical process industries. J. Loss Prev. Process Ind. 1998, 11, 261–277. [Google Scholar] [CrossRef]
- Khakzad, N.; Reniers, G. Application of bayesian network and multi-criteria decision analysis to risk-based design of chemical plants. In 15th International Symposium on Loss Prevention and Safety Promotion; DeRademacher, E., Schmelzer, P., Eds.; Italian Association of Chemical Engineering-AIDIC: Freiburg, Germany, 2016; Volume 48, pp. 223–228. [Google Scholar]
- Khan, F.I.; Haddara, M. Risk-based maintenance (RBM): A new approach for process plant inspection and maintenance. Process Saf. Prog. 2004, 23, 252–265. [Google Scholar] [CrossRef]
- Johansen, I.L.; Rausand, M. Risk metrics: Interpretation and choice. In Proceedings of the 2012 IEEE International Conference on Industrial Engineering and Engineering Management, Hong Kong, China, 10–13 December 2012; pp. 1914–1918. [Google Scholar]
- Zhang, H.; Liu, W. Hazardous chemical accidents causation characteristics of china: A statistical investigation. Ind. Saf. Environ. Prot. 2012, 5. [Google Scholar]
- Liang, C. Causation Analysis of Hazardous Chemical Explosion Based on Bayesian Network-The Case of Production Explosions. Master’s Thesis, Beijing University Of Chemical Technology, Beijing, China, 2016. [Google Scholar]
- Ji, J.; Tong, Q.; Khan, F.; Dadashzadeh, M.; Abbassi, R. Risk-based domino effect analysis for fire and explosion accidents considering uncertainty in processing facilities. Ind. Eng. Chem. Res. 2018, 57, 3990–4006. [Google Scholar] [CrossRef]
- Zerrouki, H.; Tamrabet, A. Safety and risk analysis of an operational heater using bayesian network. J. Fail. Anal. Prev. 2015, 15, 657–661. [Google Scholar] [CrossRef]
- Christou, M.; Gyenes, Z.; Struckl, M. Risk assessment in support to land-use planning in Europe: Towards more consistent decisions? J. Loss Prev. Process Ind. 2011, 24, 219–226. [Google Scholar] [CrossRef]
- Khakzad, N. Which fire to extinguish first? A risk-informed approach to emergency response in oil terminals. Risk Anal. 2018, 38, 1444–1454. [Google Scholar] [CrossRef] [PubMed] [Green Version]
Nodes Type | Nodes (BN Variables) | States of Bayesian Nodes |
---|---|---|
Accident background | Activity | (1) Use or run; (2) Transport; (3) Overhaul or clean |
Factory type | (1) Petrochemical; (2) Chemical fiber; (3) Basic chemical | |
Hazardous material characteristics | (1) Inflammable and explosive or easy to vaporize; (2) Highly corrosive; (3) Poisonous and harmful | |
Material form | (1) Gas or gas-liquid mixing; (2) Liquid; (3) Powder, dust, particles or solid | |
Accident equipment | (1) Heat exchange equipment or tower equipment; (2) Reaction equipment; (3) Transportation equipment | |
Cause of accident | Personnel factors | (1) Operation violation or an unfamiliarity with the operation process; (2) Behavioral error; (3) Other personal reasons |
Equipment factors | (1) Device selection error; (2) Static electricity or explosion-proof line problems; (3) Equipment aging and lack of maintenance; (4) Equipment damage | |
Critical event | Incidental event | (1) Overpressure and over-temperature; (2) Reaction and catalysis; (3) Loss of containment; (4) Ignition |
Type of explosion | (1) Normal explosion; (2) Other types of explosion | |
Emergency response | (1) Effective response; (2) Inadequate response | |
Accident results | Property loss | (1) Less than 10 million yuan; (2) 10–50 million yuan; (3) 50–100 million yuan; (4) More than 100 million yuan |
Casualties | (1) Less than three deaths (3–10 injuries); (2) 3–10 deaths (10–50 injuries); (3) 10–30 deaths (50–100 injuries); (4) More than 30 deaths (More than 100 injuries) |
L1 | L2 | L3 | L4 | K1 | K2 | K3 | K4 | |
---|---|---|---|---|---|---|---|---|
Value | 0–3 | 3–10 | 10–30 | 30–100 | 0–10 | 10–50 | 50–100 | 100–500 |
Probability | 0.8 | 0.15 | 0.04 | 0.01 | 0.68 | 0.03 | 0.02 | 0.00 |
Max | 6 deaths | 10.3 million yuan | ||||||
Average | 4 deaths | 5.8 million yuan | ||||||
Min | 2 deaths | 5 million yuan |
Case | Bayesian Nodes | Description |
---|---|---|
A1 | A.Activity | Activity = ‘Use or run’ |
A2 | A.Activity | Activity = ‘Transport’ |
A3 | A.Activity | Activity = ‘Overhaul or clean’ |
B1 | B.Factory type | Factory type = ‘Petrochemical’ |
B2 | B.Factory type | Factory type = ‘Chemical fiber’ |
B3 | B.Factory type | Factory type = ‘Basic chemical’ |
C1 | C.Hazardous material characteristics | Hazardous material characteristics = ‘Inflammable and explosive or easy to vaporize’ |
C2 | C.Hazardous material characteristics | Hazardous material characteristics = ‘Highly corrosive‘ |
C3 | C.Hazardous material characteristics | Hazardous material characteristics = ‘Poisonous and harmful’ |
D1 | D.Material form | Material form = ‘Gas or gas-liquid mixing’ |
D2 | D.Material form | Material form = ‘Liquid’ |
D3 | D.Material form | Material form = ‘Powder or particles or solid’ |
E1 | E.Accident equipment | Accident equipment = ‘Heat exchange equipment or tower equipment’ |
E2 | E.Accident equipment | Accident equipment = ‘Reaction equipment’ |
E3 | E.Accident equipment | Accident equipment = ‘Transportation equipment’ |
F1 | F.Personnel factors | Personnel factors = ‘Operation violation or not familiar with the operation process’ |
F2 | F.Personnel factors | Personnel factors = ‘Behavioral error’ |
F3 | F.Personnel factors | Personnel factors = ‘Other personal reasons’ |
G1 | G.Equipment factors | Equipment factors = ‘Device selection error’ |
G2 | G.Equipment factors | Equipment factors = ‘Static electricity or line explosion-proof problems’ |
G3 | G.Equipment factors | Equipment factors = ‘Equipment aging and lack of maintenance’ |
G4 | G.Equipment factors | Equipment factors = ‘Equipment damage’ |
H1 | H.Incidental event | Incidental event = ‘Overpressure and over-temperature’ |
H2 | H.Incidental event | Incidental event = ‘Reaction and catalysis’ |
H3 | H.Incidental event | Incidental event = ‘Loss of containment’ |
H4 | H.Incidental event | Incidental event = ‘Ignition’ |
I1 | I.Type of explosion | Type of explosion = ‘Normal explosion’ |
I2 | I.Type of explosion | Type of explosion = ‘Other types of explosion’ |
J1 | J.Emergency response | Emergency response = ‘Effective response’ |
J2 | J.Emergency response | Emergency response = ‘Inadequate response’ |
K1 | K.Property loss | Property loss = ‘Less than 10 million yuan’ |
K2 | K.Property loss | Property loss = ‘10–50 million yuan’ |
K3 | K.Property loss | Property loss = ‘50–100 million yuan’ |
K4 | K.Property loss | Property loss = ‘More than 100 million yuan’ |
L1 | L.Casualties | Casualties = ‘0–3 deaths (3–10 injuries)’ |
L2 | L.Casualties | Casualties = ‘3–10 deaths (10–50 injuries)’ |
L3 | L.Casualties | Casualties = ‘10–30 deaths (50–100 injuries)’ |
L4 | L.Casualties | Casualties = ‘More than 30 deaths (More than 100 injuries)’ |
Bayesian Nodes | State of Bayesian Nodes | Estimated Probabilities | ||||||||
---|---|---|---|---|---|---|---|---|---|---|
A1B1 | A1B2 | A1B3 | A2B1 | A2B2 | A2B3 | A3B1 | A3B2 | A3B3 | ||
J.Emergency response | J1 | 0.630 | 0.636 | 0.635 | 0.605 | 0.608 | 0.611 | 0.627 | 0.607 | 0.637 |
J2 | 0.370 | 0.364 | 0.365 | 0.395 | 0.392 | 0.389 | 0.373 | 0.393 | 0.363 | |
K.Property loss | K1 | 0.720 | 0.722 | 0.722 | 0.717 | 0.717 | 0.718 | 0.720 | 0.717 | 0.721 |
K2 | 0.247 | 0.247 | 0.247 | 0.251 | 0.250 | 0.250 | 0.248 | 0.251 | 0.246 | |
K3 | 0.030 | 0.029 | 0.029 | 0.029 | 0.029 | 0.029 | 0.030 | 0.029 | 0.030 | |
K4 | 0.003 | 0.002 | 0.002 | 0.003 | 0.003 | 0.003 | 0.003 | 0.003 | 0.003 | |
L.Casualties | L1 | 0.822 | 0.822 | 0.822 | 0.819 | 0.819 | 0.819 | 0.820 | 0.819 | 0.821 |
L2 | 0.136 | 0.136 | 0.136 | 0.137 | 0.137 | 0.137 | 0.136 | 0.137 | 0.136 | |
L3 | 0.036 | 0.036 | 0.036 | 0.037 | 0.037 | 0.037 | 0.036 | 0.037 | 0.036 | |
L4 | 0.007 | 0.006 | 0.007 | 0.008 | 0.008 | 0.007 | 0.007 | 0.008 | 0.007 |
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Share and Cite
Zhu, R.; Li, X.; Hu, X.; Hu, D. Risk Analysis of Chemical Plant Explosion Accidents Based on Bayesian Network. Sustainability 2020, 12, 137. https://doi.org/10.3390/su12010137
Zhu R, Li X, Hu X, Hu D. Risk Analysis of Chemical Plant Explosion Accidents Based on Bayesian Network. Sustainability. 2020; 12(1):137. https://doi.org/10.3390/su12010137
Chicago/Turabian StyleZhu, Rongchen, Xin Li, Xiaofeng Hu, and Deshui Hu. 2020. "Risk Analysis of Chemical Plant Explosion Accidents Based on Bayesian Network" Sustainability 12, no. 1: 137. https://doi.org/10.3390/su12010137
APA StyleZhu, R., Li, X., Hu, X., & Hu, D. (2020). Risk Analysis of Chemical Plant Explosion Accidents Based on Bayesian Network. Sustainability, 12(1), 137. https://doi.org/10.3390/su12010137