Experimental investigation of flame propagation characteristics in the in-line crimped-ribbon flame arrester

作     者：SUN ShaoChen DING ChunHui HU XiYu LIU Gang YE Chen BI MingShu 

作者机构：School of Chemical Machinery Dalian University of Technology Dalian 116024 China Shenyang Institute of Special Equipment Inspection and Research Shenyang 110179 China 

出 版 物：《Science China(Technological Sciences)》 (中国科学（技术科学英文版）)

年 卷 期：2017年第60卷第5期

页      面：678-691页

核心收录：

学科分类：0810[工学-信息与通信工程] 03[法学] 08[工学] 0837[工学-安全科学与工程] 0805[工学-材料科学与工程（可授工学、理学学位）] 0838[工学-公安技术] 0702[理学-物理学] 0812[工学-计算机科学与技术（可授工学、理学学位）] 0306[法学-公安学] 

基　　金：supported by General Administration of Quality Supervision,Inspection and Quarantine of China Scientific Project(Grant No.2011QK083) Shenyang Science and Technology Project(Grant No.F14-048-2-00) 

主　　题：deflagration flame crimped-ribbon flame arrester explosion pressure flame speed flammable gas concentration 

摘      要：An experimental system that consisted of gas mixing equipment, a sensor detection system, a data acquisition device, and an electric spark ignition device was set up to investigate fuel/air deflagration flame propagation and quenching processes through a crimped-ribbon flame arrester in an enclosed horizontal pipe. Deflagration suppression experiments showed that when the concentration of flammable gas was close to the stoichiometric ratio, the evolution processes of explosion pressure for the propane-air and ethylene-air premixed gases in the pipe diameter （DN32-DN400） were similar and could be divided into four stages： isobaric combustion, slow pressure rise, quick pressure rise, and pressure oscillation. However, the explosion duration of the hydrogen-air premixed gas was relatively short, and the peak explosion pressure was high. The pressure rose quickly after the isobaric combustion stage. Therefore, the process can be divided into three stages in the pipe diameter （DN15-DN150）. Deflagration speed results indicated that the propane-air flame speed initially increased and eventually decreased along with increases in the pipe diameter （DN32-DN400）; however, the ethylene-air flame speed gradually increased with the increase of the pipe diameter （DNS0-DN400）. No notable pattern of change in the hydrogen-air flame speed was observed in the pipe diameter （DN15-DN150）. The maximum propane-air flame speed occurred at 5% concentration. The maximum flame speed for ethylene-air and hydrogen-air happened when the mixture was close to stoichiometric ratio. Under the conditions of the same size of experimental tube configuration and the same ignition distance but different pipe lengths, or the same pipe length but different ignition distances, experimental results showed that the flame arrester successfully stopped the flames at high flame speed and low explosion pressure, but failed at low flame speed and high explosion pressure.