Flame Propagation and Lean-Limit Extinction Within Stratified Mixtures Involving a Diluent Gas

1992 ◽  
Vol 114 (3) ◽  
pp. 216-220
Author(s):  
G. A. Karim ◽  
V. Panlilio

Flame propagation within confined, stratified gaseous environments were investigated experimentally. The diluents nitrogen and helium were used in turn to overlay initially combustible methane-air or hydrogen-air mixtures. Gas stratification was achieved by allowing the two initially homogeneous gases to interdiffuse for a certain period of time at constant temperature and pressure within a long, vertical, smooth, closed, circular tube. Upward flame propagation was examined following spark ignition while the tube was closed at the top but open at the bottom. Near-extinction flame speeds, lower than those predicted according to Davies and Taylor (1950), were obtained with helium dilution. Moreover, estimated reactant concentrations at the observed location of flame extinction indicated, in specific instances, that mixture stratification appears to slightly enhance locally the lean flammability limit. Nonuniform, stratified combustible gaseous mixtures and flame propagation within such mixtures are found in many situations, including in numerous technical applications, as well as in various potentially hazardous circumstances. The leakage of a fuel from storage tanks or pipelines, the formation of layered combustible mixtures within rooms, corridors, or elevator shafts of buildings, the formation of gas pockets in coal mine galleries, and the inerting of flammable mixtures through diluent gas addition are some examples. Some relevant information about the stratification process and the flame propagation characteristics in these specific circumstances has already been reported in the literature by Bakke and Leach (1962), James and Purdy (1962), Girard et al. (1979), Karim and Lam (1986) and Karim et al. (1987). This investigation considers some aspects of flame propagation and mass transfer within confined, stratified gaseous environment. The diluents nitrogen and helium were used in turn to overlay initially combustible methane-air or hydrogen-air mixtures. Mixture stratification was produced by permitting the two initially homogeneous gaseous systems to interdiffuse at constant temperature within a long, vertical, smooth, closed, circular tube. Only upward flame propagation was examined, as this mode is expected to involve the widest flammability limits and the fastest propagation for both homogeneous and stratified methane-air mixtures when confined in tubes (Liebman et al., 1971).

2002 ◽  
Vol 37 (6) ◽  
pp. 549-568 ◽  
Author(s):  
Yu.N. Shebeko ◽  
W. Fan ◽  
I.A. Bolodian ◽  
V.Yu. Navzenya

Divergent views on the fundamental cause of flammability limits suggest insufficient knowledge of the mechanism of flame failure. Direct and schlieren photography have been applied to a study of flame failure in tubes at the fuel-lean limit of flammability. Results show that a bubble of hot exhaust gas rises in contact with upward propagating flames and continues to rise even after the visible flame has failed. Downward propagating flames show no evidence of such a mechanism . Comparison with fluid dynamical calculations shows that the exhaust bubble and attached flame rise in accordance with a relation involving only the tube diameter and the local gravitational acceleration. It is deduced that the bubble plays a major part in assisting the stability of a rising flame, hence accounting for the difference between flammability limits for upward and downward propagation. Further discussion suggests that this mechanism itself causes flammability limits as conventionally defined and shows how limits for different fuels are related. The final conclusion is that the limit of flammability, as commonly measured, is not a fundamental combustion parameter of a fuel.


The present paper is an account of a simple relative method of obtaining the thermal conductivity of a gas or a gaseous mixture to within 1 % for the complete range of gas conductivities. This is followed by an application of the method to deuterium gas. The principle of the apparatus to be described is similar to that upon which the so-called “conductivity meters” (e.g. the katharometer of G. A. Shakespeare, 1916-17) is based, but only in so far as both depend for their action on a transfer of heat from a heated wire through a surrounding gas. In the author’s apparatus this transfer takes place by conduction only but in the “conductivity meters” it takes place partly by conduction and partly by convection. The term “conductivity meter”, often applied to this and similar instruments, is misleading, for they do not and cannot measure the thermal conductivity of a gas or gaseous mixture. Calibrated empirically in terms of gaseous mixtures of known composition they are used industrially in the investigation of composition of other mixtures. Generally these industrial meters employ two similar fine metal filaments of considerable resistance (often 10-20 Ω ) connected in series and placed in the adjacent arms of a Wheatstone bridge. They are mounted in some form of cell designed for working at a constant temperature and either wire can be surrounded by any selected gas or mixture.


1991 ◽  
Vol 3 ◽  
pp. 875-883 ◽  
Author(s):  
G. Makhviladze ◽  
V. Melikhov ◽  
V. Rabinkov

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