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Deflagration of premixed methane–air in a large scale detonation tube

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TLDR
In this paper, a detonation tube (30m long) was facilitated at the University of Newcastle to cover the knowledge gap in terms of boosting flame deflagration of low methane concentrations.
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This article is published in Process Safety and Environmental Protection.The article was published on 2017-07-01 and is currently open access. It has received 44 citations till now. The article focuses on the topics: Deflagration & Premixed flame.

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Investigation on the overpressure of methane-air mixture gas explosions in straight large-scale tunnels

TL;DR: In this article, the authors used the computational fluid dynamics (CFD) code of Flame Accelerator Simulator (FLACS) to investigate the overpressure of methane-air explosions in straight large-scale tunnels.
Journal ArticleDOI

Impact of suspended coal dusts on methane deflagration properties in a large-scale straight duct.

TL;DR: The results revealed that the presence of the coal dust enhanced the turbulence in the front flame and the pressure wave and flame velocities were both increased when a 10gm-3 coal dust concentration coexisted with a 9.5% methane concentration in the deflagration.
Journal ArticleDOI

Experimental study of overpressure evolution laws and flame propagation characteristics after methane explosion in transversal pipe networks

TL;DR: Wang et al. as mentioned in this paper established a transversal pipe network methane explosion experimental system and experimentally studied the explosive pressure wave propagation laws of premixed gases of three different methane concentrations (8, 9.5, and 11%).
Journal ArticleDOI

Gas explosions of methane-air mixtures in a large-scale tube

TL;DR: In this article, 12 batches of premixed methane-air mixture explosion tests were conducted in a 30m long testing tube with section dimensions of 0.8m × 0.4m.
Journal ArticleDOI

Flame Deflagration In Side-on Vented Detonation Tubes: a Large Scale Study

TL;DR: It is proved the existence of a significant correlation between the fire and explosion driving parameters such as pressure rise and flame propagation velocity with the vent location, and the effectiveness of side-on venting on methane flame deflagration in large scale operations has not been clearly addressed.
References
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Journal ArticleDOI

Gas explosion handbook

TL;DR: In this article, a brief introduction to gas explosion safety is given, based on current knowledge of the subject and on experience in applying this knowledge to practical problems in the industry, including cloud formation, gas explosions, blast waves and structural response.
Journal ArticleDOI

Major accidents in process industries and an analysis of causes and consequences

TL;DR: In this paper, the authors briefly recapitulates some of the major accidents in chemical process industries which occurred during 1926-1997 and revealed that vapour cloud explosion (VCE) poses the greatest risk of damage.
Journal ArticleDOI

Flammability of methane, propane, and hydrogen gases

TL;DR: In this article, the results of flammability studies for methane, propane, hydrogen, and deuterium gases in air conducted by the Pittsburgh Research Laboratory were reported, which illustrate the complications associated with buoyancy, turbulence, selective diffusion, and ignitor strength versus chamber size.
Journal ArticleDOI

The critical tube diameter for detonation failure in hydrocarbon-air mixtures☆

TL;DR: In this paper, the critical tube diameters dc for the successful transformation of a planar to a spherical detonation have been measured in nine gaseous fuels (CH4, C2H2, C 2H4, c2H6, C3H8, C4H10, MAPP and H2) in stoichiometric fuel-oxygen mixtures diluted with nitrogen at atmospheric initial pressure.
Journal ArticleDOI

Loss prevention in the process industries

TL;DR: In this article, the authors propose a method for measuring the performance of a single node in a set of images.ING and INDEXING, e.g., this article.
Related Papers (5)
Frequently Asked Questions (15)
Q1. How many photodiodes were located along the length of the tube?

There were 33 pressure transducers and 33 photodiodes located along the length of the tube with three pressure transducers and three photodiodes located at the middle of each section. 

In the case of low methane concentration (i.e 1.25% and 2.5%), the reading of dynamic pressures were over driven by the initial explosion in the firstsection. 

The flame intensity signal of the first section ranged between 1.5 V to 3 V. Regardless, the methane concentration in the RS, exempting the 9.5% scenario, caused the flame intensity signal in the first section to reach about 4.5 V. 

A detailed record of methane flame deflagration velocity is not only required to determine the pressure impulse and explosion development, but also to design an effective flame mitigation system. 

The flame velocity at 5% methane concentration, however, when increasing the RS length from 12 m to 25 m, significantly accelerated the flame velocity from 70 m.s-1 to about 83 m.s-1. 

The maximum dynamic pressure recorded was 2.56 bar at a 9.5% concentration for a 12 m RS length and the maximum side on pressure was higher than the side on pressure in all the other results. 

the pressure wave declined gradually to 0.4 bar, where the pressure wave profile behaved in a typical way to the observed methane explosion at the 3 m RS length (see Figure 9). 

The flame velocity helps to estimate the distance and time required between the flame detectors and the location where the flame mitigation acts. 

The explosion characteristics, pressure wave and flame velocities were investigated for a wide range of methane-air mixtures (1.25%, 2.5%, 5%, 7.5%, 10% and 15%). 

They also noticed that the position of the ignitor plays an important role on the flame speed and pressure profile, where the maximum pressure was recorded when the ignitors were in the middle of the tube. 

The maximum pressure wave velocity was 310 m.s-1 for methane stoichiometric concentration at 9.5 m, and the minimum pressure wave velocity was 25 m.s-1 at 5% methane concentration for the 3 m RS (see Figure 10). 

As the flame velocity in the early stage is relatively low due to the low burning rate, a slow pressure wave velocity was generated. 

The detonation tube used in this study consisted of eleven sections with a diameter of 0.5 m, a total length of 30 m, and a 6 m silencer attached at the end of the tube to reduce the noise of the explosions (see Figure 1). 

Each circulation system consisted of a blower (the volumetric flow rates for the first and second circulation blowers were 720 litre/min and 1900 litre/min, respectively). 

At a stoichiometric methane concentration (see Figure 12 (a)), the peak velocity was achieved at 17.5 m before the flame velocity began to decline.