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E-raamat: Guidelines for Combustible Dust Hazard Analysis [Wiley Online]

  • Formaat: 256 pages
  • Ilmumisaeg: 20-Jun-2017
  • Kirjastus: Wiley-AIChE
  • ISBN-10: 1119378206
  • ISBN-13: 9781119378204
Teised raamatud teemal:
  • Wiley Online
  • Hind: 144,80 €*
  • * hind, mis tagab piiramatu üheaegsete kasutajate arvuga ligipääsu piiramatuks ajaks
Guidelines for Combustible Dust Hazard AnalysisSuurem pilt
  • Formaat: 256 pages
  • Ilmumisaeg: 20-Jun-2017
  • Kirjastus: Wiley-AIChE
  • ISBN-10: 1119378206
  • ISBN-13: 9781119378204
Teised raamatud teemal:
Wiley Online e-raamatudRohkem infot Wiley Online kohta
Raamatu kodulehekülg: https://onlinelibrary.wiley.com/doi/book/10.1002/9781119378204

The book explains how to do a dust hazard assessment by using either an approach based on compliance with existing consensus standards, or by using a risk based approach.

Covered topics include background of the combustible dust fire and explosion hazard problem, a standards based approach to assessing combustible dust hazards, hazards inside dust processing equipment, hazards in dust handing buildings, a risk based approach to assessing combustible dust hazards, addressing risk issues in an existing facility, worked examples, and issues to watch out for

List Of Tables
xiii
List Of Figures
xv
Acronyms And Abbreviations xvii
Glossary xix
Acknowledgments xxiv
Preface xxvii
1 Introduction
1(4)
1.1 Purpose of Book
1(1)
1.2 Book Road Map
2(2)
1.3 References
4(1)
2 Background
5(20)
2.1 Nature of the Dust Fire and Explosion Problem
5(5)
2.1.1 Dust Explosion Statistics
5(1)
2.1.2 Case Study: Hoeganaes Corporation
5(5)
Findings and Lessons
10(1)
2.2 Requirements for Dust Fires and Explosions
11(4)
2.2.1 Layer Fire
12(1)
2.2.2 Flash Fires and Explosions
12(3)
2.3 Combustibility and Explosivity Parameters
15(6)
2.3.1 Explosibility Screening Test
15(3)
2.3.2 Deflagration Index, Kst (bar-m/sec)
18(1)
2.3.3 Maximum Pressure, Pmax (Bar)
18(1)
2.3.4 Minimum Explosible Concentration, MEC (g/m3)
19(1)
2.3.5 Minimum Ignition Energy, MIE (mJoules, mJ)
19(1)
2.3.6 Minimum Auto Ignition Temperature, Cloud, MAIT (°C)
20(1)
2.3.7 Layer Ignition Temperature, LIT (°C)
20(1)
2.3.8 Limiting Oxygen Concentration, LOC (vol% O2)
20(1)
2.3.9 Volume Resistivity (Ohm-m)
20(1)
2.4 Comparison to Combustible Vapors
21(1)
2.5 Effect of Parameters
22(1)
2.6 Summary
22(1)
2.7 References
23(2)
3 The Hazards Within - Dust Inside Equipment
25(20)
3.1 Methods of Prevention, Protection, Mitigation
25(5)
3.1.1 Ignition Control
26(2)
3.1.2 Inerting/Oxidant Control
28(1)
3.1.3 Combustible Concentration Control
28(1)
3.1.4 Deflagration Venting
28(1)
3.1.5 Deflagration Suppression
29(1)
3.1.6 Containment
29(1)
3.1.7 Deflagration Isolation
30(1)
3.2 Issues
30(12)
3.2.1 Air/Material Separators
32(2)
3.2.2 Size Reduction Equipment (grinders, mills, etc.)
34(1)
3.2.3 Dryers
35(1)
3.2.4 Silos/Hoppers
36(1)
3.2.5 Portable Containers
37(1)
3.2.6 Conveyors
38(3)
3.2.7 Blenders/Mixers
41(1)
3.2.8 Feeding into Vessels Having Flammable Vapor Atmospheres
41(1)
3.3 Summary
42(1)
3.4 References
42(3)
4 Hazards of Dust External to Equipment
45(10)
4.1 Case Study -- Imperial Sugar
45(3)
4.2 Issues Inside a Room or Building
48(1)
4.3 Methods of Prevention and Protection
49(3)
4.3.1 Control of Dust Deposits Outside of Equipment
49(3)
4.3.2 Ignition Control
52(1)
4.3.3 Damage Limiting Construction
52(1)
4.4 Summary
52(1)
4.5 References
53(2)
5 Traditional Approach to Hazard Assessment and Control
55(14)
5.1 Introduction
55(1)
5.1.1 Process Safety Information (PSI)
55(1)
5.1.2 Competent Team
56(1)
5.2 Steps to the Traditional Approach
56(11)
5.2.1 Step 1 - Is a combustible dust involved?
57(1)
5.2.2 Step 2 - Determine Which Standards Apply
58(4)
5.2.3 Step 3 - Determine Where Fire/Explosion Hazards Exist
62(1)
5.2.4 Step 4 - Review Unit Operation vs. Standard Requirements for Prevention and Mitigation of Fires/Explosions
63(2)
5.2.5 Step 5 - Make Recommendations
65(1)
5.2.6 Step 6 - Document the DHA
65(1)
5.2.7 Step 7 - Implement the Recommendations
66(1)
5.3 Summary
67(1)
5.4 References
68(1)
6 Risk-based Approach to Dust Hazard Analysis
69(18)
6.1 Introduction
69(1)
6.2 Technique for a Risk-based DHA
70(12)
6.2.1 Step 1: Identify Failure Scenarios
70(1)
6.2.2 Step 2: Evaluate the Consequences
70(3)
6.2.3 Step 3: Are the Consequences Tolerable?
73(1)
6.2.4 Step 4: Estimate Likelihood and Risk
73(5)
6.2.5 Step 5: Is the Risk Tolerable
78(2)
6.2.6 Step 6: Recommend and Evaluate Solutions
80(1)
6.2.7 Step 7: Is the Mitigated Risk Tolerable?
81(1)
6.2.8 Step 8: Document Results
81(1)
6.3 DHA Risk Assessment, Additional Requirements
82(1)
6.3.1 DHA Leader Competency
83(1)
6.3.2 Documentation
83(1)
6.4 Managing Change and Updating Risk Assessment
83(1)
6.5 Summary
83(1)
6.6 References
84(3)
7 Special Considerations: Combustible Dust Issues in Existing Facilities
87(8)
7.1 Introduction
87(1)
7.2 Existing Facilities and Combustible Dusts
87(5)
7.2.1 Potential Issues
87(4)
7.2.2 Issues Impact
91(1)
7.2.3 Precautions
92(1)
7.3 Summary
92(1)
7.4 References
93(2)
8 Worked Examples
95(96)
8.1 Introduction
95(1)
8.2 Example 1
95(74)
8.2.1 Process Description - Example 1
95(1)
8.2.2 Traditional DHA - Example 1
95(17)
8.2.3 Risk-based DHA - Example 1
112(55)
8.2.4 Comparison of Traditional vs. Risk-based Approach - Example 1
167(2)
8.3 Example 2
169(8)
8.3.1 Process Description 2
169(2)
8.3.2 Traditional DHA
171(2)
8.3.3 Risk-based DHA
173(3)
8.3.4 Comparison of Traditional vs. Risk-based Approach - Example 2
176(1)
8.4 Example 3
177(11)
8.4.1 Process Description - Example 3
177(2)
8.4.2 Traditional DHA - Example 3
179(2)
8.4.3 Risk-based DHA - Example 3
181(7)
8.5 Summary
188(1)
8.6 References
188(3)
Appendix A Regulations and Codes
191(6)
A.1 Regulations
191(1)
A.1.1 U.S.
191(1)
A.1.2 International
191(1)
A.2 Codes
192(5)
References
195(2)
Appendix B Additional Resources
197(4)
B.1 Books
197(1)
B.2 U.S. Chemical Safety Board Reports
197(1)
B.3 Journal Articles
198(1)
B.4 Other
199(2)
Appendix C Data for Risk-based DHA
201(10)
C.1 Probability Assessment of Process Unit Fire or Dust Explosion
201(8)
C.1.1 Initiating Event Frequencies
204(1)
C.1.2 Ignition Probabilities
205(2)
C.1.3 Protection Layer PFDs
207(2)
C.2 References
209(2)
Appendix D Good Practices
211(8)
D.1 Self Assessment
211(2)
D.2 Housekeeping
213(4)
D.2.1 Combustible Dust Housekeeping Inspection Checklist
215(2)
D.3 Explosion Protection Methods
217(2)
Appendix E DHA Roadmap
219(4)
Notes for Figure E.1
221(2)
Index 223
Since 1985, the Center for Chemical Process Safety (CCPS) has been the global leader in developing and disseminating information on process safety management and technology. CCPS, an industry technology alliance of the American Institute of Chemical Engineers (AIChE), has published over 100 books in its process safety guidelines and process safety concepts series, and over 100 training modules through its Safety in Chemical Engineering Education (SACHE) series.
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