TY - JOUR
T1 - Influential factors of vented explosion position on maximum explosion overpressure of methane-air mixture explosion in single spherical container and linked vessels
AU - Zhang, Kai
AU - Wang, Zhirong
AU - Chen, Zhen
AU - Jiang, Fengwei
AU - Wang, Supan
N1 - Publisher Copyright:
© 2017 American Institute of Chemical Engineers
PY - 2018/6
Y1 - 2018/6
N2 - An explosion venting system is established to examine the influencing factors of the vented explosion position for a single vessel, a single vessel connected by pipes and two vessels connected by pipes during the explosion venting process of a methane-air mixture. Relative to a single vessel, it is shown that the maximum explosion venting pressure of the lateral vented explosion does not appear to vary greatly from that of a top vented explosion. It appears that as the volume of the spherical vessel increases, the maximum pressure increases. The maximum overpressure for an explosion venting on the top and side does not vary for either a large or small vessel connected by pipes. However, as the maximum explosion overpressure in the pipe increases, the maximum explosion overpressure peak occurs at the end of the pipe, and the explosion flame that propagates in the pipe accelerates and enlarges. Compared with an airtight explosion, an explosion venting on the top and side of a single vessel is more effective for both a large and small vessel connected by pipes. The pressure in the vessel and pipe appears to fluctuate and produces multiple peaks in the explosion venting process. Ignition in a large vessel is more dangerous than ignition in a small vessel under an airtight condition for two vessels connected by pipes. Regardless of the ignition position in the large or small vessel, the explosion venting effect in the small vessel is better than that in the large vessel.
AB - An explosion venting system is established to examine the influencing factors of the vented explosion position for a single vessel, a single vessel connected by pipes and two vessels connected by pipes during the explosion venting process of a methane-air mixture. Relative to a single vessel, it is shown that the maximum explosion venting pressure of the lateral vented explosion does not appear to vary greatly from that of a top vented explosion. It appears that as the volume of the spherical vessel increases, the maximum pressure increases. The maximum overpressure for an explosion venting on the top and side does not vary for either a large or small vessel connected by pipes. However, as the maximum explosion overpressure in the pipe increases, the maximum explosion overpressure peak occurs at the end of the pipe, and the explosion flame that propagates in the pipe accelerates and enlarges. Compared with an airtight explosion, an explosion venting on the top and side of a single vessel is more effective for both a large and small vessel connected by pipes. The pressure in the vessel and pipe appears to fluctuate and produces multiple peaks in the explosion venting process. Ignition in a large vessel is more dangerous than ignition in a small vessel under an airtight condition for two vessels connected by pipes. Regardless of the ignition position in the large or small vessel, the explosion venting effect in the small vessel is better than that in the large vessel.
KW - connected container
KW - gas explosion venting
KW - maximum explosion overpressure
KW - single spherical container
KW - vented explosion position
UR - http://www.scopus.com/inward/record.url?scp=85047845598&partnerID=8YFLogxK
U2 - 10.1002/prs.11940
DO - 10.1002/prs.11940
M3 - 文章
AN - SCOPUS:85047845598
SN - 1066-8527
VL - 37
SP - 248
EP - 255
JO - Process Safety Progress
JF - Process Safety Progress
IS - 2
ER -