2016
DOI: 10.1021/acs.energyfuels.6b00366
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Experimental Study of Minimum Ignition Energy of Methane–Air Mixtures at Low Temperatures and Elevated Pressures

Abstract: Previous research results show that, at the top of the distillation column of the liquefied process of oxygen-bearing coal-bed methane (CBM), an explosion hazard may happen. The minimum ignition energy (MIE) of combustible gas reflects the sensitivity of the explosion. Although MIE has been experimentally and theoretically studied at normal or elevated temperatures, there are no relevant data aimed at the environment (low temperature and high pressure) which exists at the top of the distillation column. Theref… Show more

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Cited by 20 publications
(6 citation statements)
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(50 reference statements)
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“…With the increasing emphasis on environmental protection and demand for energy and the increasing shortage of traditional energy such as oil, the development and utilization of LNG and oxygen-bearing coal-bed methane show significant economic and social benefits. However, in the LNG storage and oxygen-bearing coal-bed methane liquefied production, the methane concentration in the gas phase may be within the flammability limits, causing a potential explosion hazard and resulting in significant economic losses and casualties. Regardless of the combustion caused by LNG leakage or low-temperature liquefaction of oxygen-bearing coal-bed methane, there is a common ground: the initial temperature of the combustion is cryogen (typically lower than 150 K). Under low-temperature conditions, the combustion characteristics and mechanism are bound to be very different from those at room temperature, and there is a lack of research on gas combustion at low initial temperature.…”
Section: Introductionmentioning
confidence: 99%
“…With the increasing emphasis on environmental protection and demand for energy and the increasing shortage of traditional energy such as oil, the development and utilization of LNG and oxygen-bearing coal-bed methane show significant economic and social benefits. However, in the LNG storage and oxygen-bearing coal-bed methane liquefied production, the methane concentration in the gas phase may be within the flammability limits, causing a potential explosion hazard and resulting in significant economic losses and casualties. Regardless of the combustion caused by LNG leakage or low-temperature liquefaction of oxygen-bearing coal-bed methane, there is a common ground: the initial temperature of the combustion is cryogen (typically lower than 150 K). Under low-temperature conditions, the combustion characteristics and mechanism are bound to be very different from those at room temperature, and there is a lack of research on gas combustion at low initial temperature.…”
Section: Introductionmentioning
confidence: 99%
“…The electrode is placed on the flange at the beginning of the pipe network system, and an ignition energy of 10 J is selected as the starting energy for the experiments. 33 The explosion suppression device is a self-designed rectangular cavity, and its physical picture is shown in Figure 2 . The dimensions of the cavity (length × width × height) mentioned in the experiments include 500 mm × 300 mm × 200 mm, 500 mm × 500 mm × 200 mm, and 500 mm × 800 mm × 200 mm.…”
Section: Experimental Setup and Methodsmentioning
confidence: 99%
“…The vessel is placed in a constant temperature drying oven. A tungsten wire coil with a diameter of 1.2 mm powered by a 24 V and 400 W direct current source is used to ignite the gas, which can exceed the minimum ignition energy of methane under high temperatures and high pressures. The Ignition tungsten is placed at one end of the container and connected to the external through sealed stainless steel electrodes. The experimental results obtained for methane at atmospheric conditions can be compared with the literature data that were obtained using different ignition criteria, shape and size of the explosion vessels, and the ignition type, as shown in Table .…”
Section: Methodsmentioning
confidence: 99%