Journal of Liaoning Petrochemical University
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Simulation of the Consequence of Gas Leakage and Explosion Accident in Canteen Based on FLACS
Youzhi Wang, Ming Wu, Jin Du, Ke Gong
Abstract662)   HTML    PDF (1960KB)(389)      

According to the characteristics of the canteen, the FLACS software was used to build a three?dimensional model for a university canteen. On the basis of considering the jet direction, obstacles and other factors, the leakage and explosion of natural gas were simulated, and the diffusion process of gas cloud, the development law of explosion shock wave and temperature in a specific scene were studied. The results show that when the gas leaks vertically upward, the gas accumulates in the small booth due to the obstruction of the canteen roof. When the natural gas leaks horizontally, the volume fraction of natural gas cloud in the dining area is higher. At the initial stage of the explosion, the explosion pressure shock wave centered on the ignition point first appears, and the pressure shock wave travels outward in a circular arc. The leakage direction has little effect on the maximum over pressure generated by the explosion.The temperature distribution is greatly affected by the direction of leakage. When vertical injection is carried out, the high temperature is concentrated in the small booth. When horizontal injection is carried out, the temperature is distributed from high to low.

2022, 42 (1): 35-40. DOI: 10.3969/j.issn.1672-6952.2022.01.007
The Analysis of Pollutant Emission Concentration  Limits Based on Total Quantity Control
JIA Fengrui,JIN Dun, LI Yulin, DONG Hui, WU Ming
Abstract352)      PDF (1471KB)(187)      
The total idea for waste water controlling was described and then the emission concentration limited of the chemical oxygen demand(COD)and the ammonia nitrogen(NH3N)for the Jinsha River, the Luanhe River and Dalinghe River were calculated respectively by twodimensional water quality model. The results show that the COD emission concentration limits of the three rivers were under the current standards. However, the NH3N emission concentration limits were all closed to or above the standards; the recommended COD and NH3N emission concentration limits were no more than 60 and 15 mg/L, respectively.
2013, 33 (4): 1-3.
Influence of Insulation Failure Ratio on Safe Shutdown Time for the Hot Oil Pipeline
WANG Lei,WU Ming,JIA Feng-rui,YAO Yao, MA Yue,JIN Dun,FENG Jin-ye
Abstract442)      PDF (1006KB)(226)      
 
According to the problem of uncontrollable safe shutdown time when the insulation layer was partial failure under the specific conditions, a two-dimension, unsteady-state model of hot oil pipe was established by the finite volume method. In the model the influence of the latent heat of solidification was considered and the law of temperature drop in the hot oil pipe was compared and analyzed in five cases (i.e. no insulation failure, 1/8 insulation failure, 1/4 insulation failure, 1/2 insulation failure and complete insulation failure). Based on the above, the relative curve between the shutdown time and the average temperature of hot oil after line turndown was fitted by SPSS 18.0, and the safe shutdown time of the above five cases were determined finally. The results show that the laws of temperature drop of hot oil pipe is similar in the above five cases, and the safe shutdown time is 205, 148, 118, 99 and 74 hours. Due to the latent heat of solidification could partly make up for the heat loss, safe shutdown time of 1/2 insulation failure was only 19 hours less than 1/4 insulation failure’s.
2012, 32 (4): 55-59. DOI: 10.3696/j.issn.1672-6952.2012.04.015