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Title: Model simulates pipeline, tank-storage failures

Journal Article · · Oil Gas J.; (United States)
OSTI ID:6819773

There is an important need for accurate mathematical models to predict the source rates and resulting safety impacts of accidental releases of materials from gas or liquid pipelines and from cryogenic storage tanks. Two major types of hazards can develop after a structural failure of a pipeline or hydrocarbon storage tank: a combustion hazard or a toxic chemical hazard. Both of these types of hazards can affect the safety of personnel in the vicinity of the structural failure. A flammable vapor cloud can form after a pipeline or tank fracture and, if an ignition source is present, the cloud can detonate, or explode. In the case of a crude oil or gas-pipeline failure, a toxic cloud may also develop due to the presence of hydrogen sulfide (H/sub 2/S). Even in low concentrations, inhalation of H/sub 2/S may cause physical impairment or death. The existence of these two potential hazards--a flammability hazard or a toxic chemical hazard--prompts the need to conduct safety analysis studies of facilities and transport systems that carry pressurized fluids and gases. However, the simulation modeling of the flammability or toxicity concentration limits due to the structural failure of a pipeline or storage tank is quite difficult. Complicating factors include the two-phase (gas and liquid) flow caused by a pressurized liquid pipeline break, and the gravitational settling of a cold, dense gas if a cryogenic liquid such as liquified natural gas (LNG) is spilled.

Research Organization:
Scientific Research Associates Glastonbury, CT
OSTI ID:
6819773
Journal Information:
Oil Gas J.; (United States), Vol. 81:37
Country of Publication:
United States
Language:
English