By using index method and multivariable analysis, a methodology of the threat and risk of natural gas (NG) and natural gas liquids (NGL) pipelines to environment will be presented by considering total infrastructure. General concepts are introduced and explained in detail.
Published in |
International Journal of Environmental Monitoring and Analysis (Volume 3, Issue 6-1)
This article belongs to the Special Issue Environmental Social Impact Assessment (ESIA) and Risk Assessment of Crude Oil and Gas Pipelines |
DOI | 10.11648/j.ijema.s.2015030601.11 |
Page(s) | 1-8 |
Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
Copyright |
Copyright © The Author(s), 2015. Published by Science Publishing Group |
Quantitative Risk Analysis, Risk Valorization, Risk Analysis of NG Pipelines, Risk Analysis of NGL Pipelines, Acceptable Risk Zones, Unacceptable Risk Zones
[1] | FEMA, Emergency Response Guidebook, 2008. |
[2] | FEMA, DOT, and EPA, Handbook of Chemical Hazards Analysis Procedures, US Environmental Protection Agency, US Department of Transportation, and the Federal Emergency Management Agency, 1989. |
[3] | United States Environmental Protection Agency (EPA), Evaluation of Dense Gas Simulation Models, Draft, EPA 450/4-90, United States Environmental Protection Agency, September 1990. |
[4] | United States Environmental Protection Agency (EPA), Risk Management Program Guidance for Offsite Consequence Analysis (OCAG), EPA 550-B-99-009, United States Environmental Protection Agency, April 1999. |
[5] | United States Environmental Protection Agency (EPA), TANKS 4.09b, Computer Program, US Environmental Protection Agency, September 1999. |
[6] | United States Department of Transportation Office of Pipeline Safety (DOT-OPS), Gas Pipeline Incident Database, 1984-200 1, and Hazardous Liquid Incident Database, 1986-2001. |
[7] | United States Department of Transportation Office of Pipeline Safety (DOT-OPS), 2000 Annual Reports for Natural Gas Transmission and Distribution Pipeline Operators. |
[8] | United States Department of Transportation, Research and Special Programs Administration, 49 CFR Part 192, [Docket No. RSPA¬00-7666; Amendment 192-95] RIN 2137-AD54, Pipeline Safety: Pipeline Integrity Management in High Consequence Areas (Gas Transmission Pipelines), ACTION: Final rule. |
[9] | U.S. Department of Commerce (US DOC), "Heat radiation from Large Pool Fires" NISTIR 6546, Fire Safety Engineering Division Building and Fire Research Laboratory, November 2000. Risk Assessment, American Institute of Chemical Engineers, New York, 1995. |
[10] | Frank Lees, Hazard Identification, Assessment and Control, Loss Prevention in the Process Industries Second Edition, 1996. |
[11] | Eltgroth, Mark W., "CHARM® Emergency Response System Technical Reference Manual," Radian Corporation, September 1995. |
[12] | Radian International, CHARM® Technical Manual, 1995. |
[13] | HSE, "The Effect of Explosions in the Process Industries," Loss Prevention Bulletin, 68:37-47, Health & Safety Executive (HSE), 1986. |
[14] | HSE, Second Report Advisory Committee Ma/or Hazards, U.K. Health and Safety Commission, Health & Safety Executive (HSE), 1979. |
[15] | W. K, Muhlbauer, Pipeline Risk Management Manual, Second Edition, Gulf Publishing Co., Houston, TX, 1996. |
[16] | W. K, Muhlbauer, Pipeline Risk Management Manual, Third Edition, Gulf Publishing Co., Houston, TX, 2004. |
[17] | Risk Assessment, American Institute of Chemical Engineers, New York, 1995. |
[18] | CCPS (Center for Chemical Process Safety),Guidelines for Fire Protection in Chemical, Petrochemical, and Hydrocarbon Processing Facilities, 2003. |
[19] | CCPS (Center for Chemical Process Safety), Guidelines for Chemical Process Quantitative Risk Analysis, 1999. |
[20] | CCPS (Center for Chemical Process Safety), Guidelines for Evaluating the Characteristics of Vapor Cloud Explosions, Flash Fires, and BLEVES, American Institute of Chemical Engineers, New York, 1994. |
[21] | CCPS (Center for Chemical Process Safety), Guidelines for Evaluating Process Plant Buildings for External Explosions and Fires, American Institute of Chemical Engineers, New York, New York, 1996. |
[22] | CCPS (Center for Chemical Process Safety), Guidelines for Chemical Process Quantitative Risk Analysis, American Institute of Chemical Engineers, New York, New York, 1989. |
[23] | CCPS (Center for Chemical Process Safety), Guidelines for Hazard Evaluation Procedures, American Institute of Chemical Engineers, New York, 1992. |
[24] | Greenwood, B., L. Seeley, and J. Spouge, "Risk Criteria for Use in Quantitative Risk Analysis," in CCPS, International Conference and Workshop on Risk Analysis and Process Safety, October 21¬24, 1997, Atlanta, Georgia, American Institute of Chemical Engineers, New York, New York, 1997, pp. 29-40. |
[25] | McAllister, E. W. (ed), Pipeline Rules of Thumb Handbook, Gulf Publishing Co., Houston, Texas, 1993, pp. 497-501. |
[26] | John B. Cornwell and William E. Martinsen, Quantitative Risk Analysis of the Wahsatch Gas Gathering Pipeline System, Houston, Texas, 1994. |
[27] | Huseyin Murat Cekirge. Qualitative Risk of Gas Pipelines. American Journal of Energy Engineering. Vol. 3, No.3, 2015, pp. 53-56. doi: 10.11648/j.ajee.20150303.14 |
APA Style
Huseyin Murat Cekirge. (2015). Quantitative Risk Analysis for Gas (NG and NGL) Pipelines. International Journal of Environmental Monitoring and Analysis, 3(6-1), 1-8. https://doi.org/10.11648/j.ijema.s.2015030601.11
ACS Style
Huseyin Murat Cekirge. Quantitative Risk Analysis for Gas (NG and NGL) Pipelines. Int. J. Environ. Monit. Anal. 2015, 3(6-1), 1-8. doi: 10.11648/j.ijema.s.2015030601.11
AMA Style
Huseyin Murat Cekirge. Quantitative Risk Analysis for Gas (NG and NGL) Pipelines. Int J Environ Monit Anal. 2015;3(6-1):1-8. doi: 10.11648/j.ijema.s.2015030601.11
@article{10.11648/j.ijema.s.2015030601.11, author = {Huseyin Murat Cekirge}, title = {Quantitative Risk Analysis for Gas (NG and NGL) Pipelines}, journal = {International Journal of Environmental Monitoring and Analysis}, volume = {3}, number = {6-1}, pages = {1-8}, doi = {10.11648/j.ijema.s.2015030601.11}, url = {https://doi.org/10.11648/j.ijema.s.2015030601.11}, eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ijema.s.2015030601.11}, abstract = {By using index method and multivariable analysis, a methodology of the threat and risk of natural gas (NG) and natural gas liquids (NGL) pipelines to environment will be presented by considering total infrastructure. General concepts are introduced and explained in detail.}, year = {2015} }
TY - JOUR T1 - Quantitative Risk Analysis for Gas (NG and NGL) Pipelines AU - Huseyin Murat Cekirge Y1 - 2015/10/16 PY - 2015 N1 - https://doi.org/10.11648/j.ijema.s.2015030601.11 DO - 10.11648/j.ijema.s.2015030601.11 T2 - International Journal of Environmental Monitoring and Analysis JF - International Journal of Environmental Monitoring and Analysis JO - International Journal of Environmental Monitoring and Analysis SP - 1 EP - 8 PB - Science Publishing Group SN - 2328-7667 UR - https://doi.org/10.11648/j.ijema.s.2015030601.11 AB - By using index method and multivariable analysis, a methodology of the threat and risk of natural gas (NG) and natural gas liquids (NGL) pipelines to environment will be presented by considering total infrastructure. General concepts are introduced and explained in detail. VL - 3 IS - 6-1 ER -