Combustion of double gas hydrate

An experimental study on double hydrate dissociation in the presence of air velocity u0 was performed. Forced convection increases the dissociation rate. The experimental curve for the time of the combustion beginning was obtained. During the dissociation of a complex gas hydrate, two typical decay modes can be distinguished. To increase the combustion efficiency of gas hydrate fuel, the most optimal air velocity corresponds to the range of 0.75-1.25 m/s. The increase in the velocity u0 over 3.5 m/s leads to the cessation of fuel combustion.

[1]  S. Misyura,et al.  Dissociation of various gas hydrates (methane hydrate, double gas hydrates of methane-propane and methane-isopropanol) during combustion: Assessing the combustion efficiency , 2020 .

[2]  S. Misyura,et al.  Comparing the dissociation kinetics of various gas hydrates during combustion: Assessment of key factors to improve combustion efficiency , 2020 .

[3]  Galina S. Nyashina,et al.  Gas Hydrate Combustion in Five Method of Combustion Organization , 2020, Entropy.

[4]  S. Misyura,et al.  Developing the environmentally friendly technologies of combustion of gas hydrates. Reducing harmful emissions during combustion. , 2020, Environmental pollution.

[5]  A. Meleshkin,et al.  Hydrate Formation in Water Foam Volume , 2020 .

[6]  A. Meleshkin,et al.  Effect of Surfactants on Synthesis of Gas Hydrates , 2020 .

[7]  X. Xing,et al.  Effect of the water on the flame characteristics of methane hydrate combustion , 2020 .

[8]  S. Misyura The crystallization behavior of the aqueous solution of CaCl2 salt in a drop and a layer , 2020, Scientific Reports.

[9]  S. Misyura Non-isothermal evaporation and heat transfer of the salt solution layer on a structured wall in the presence of corrosion , 2020 .

[10]  X. Xing,et al.  Effects of the diameter and the initial center temperature on the combustion characteristics of methane hydrate spheres , 2020 .

[11]  I. Donskoy,et al.  Ways to improve the efficiency of carbon dioxide utilization and gas hydrate storage at low temperatures , 2019 .

[12]  V. Morozov,et al.  The influence of the surface microtexture on wettability properties and drop evaporation , 2019, Surface and Coatings Technology.

[13]  S. Misyura,et al.  Non-stationary combustion of natural and artificial methane hydrate at heterogeneous dissociation , 2019, Energy.

[14]  V. Morozov,et al.  Marangoni flow and free convection during crystallization of a salt solution droplet , 2019, Colloids and Surfaces A: Physicochemical and Engineering Aspects.

[15]  M. Khasanov,et al.  Mathematical model of injection of liquid carbon dioxide in a reservoir saturated with methane and its hydrate , 2019, International Journal of Heat and Mass Transfer.

[16]  S. Misyura The influence of convection on heat transfer in a water layer on a heated structured wall , 2019, International Communications in Heat and Mass Transfer.

[17]  R. Volkov,et al.  Interaction of two drops at different temperatures: The role of thermocapillary convection and surfactant , 2018, Colloids and Surfaces A: Physicochemical and Engineering Aspects.

[18]  S. Misyura The influence of characteristic scales of convection on non-isothermal evaporation of a thin liquid layer , 2018, Scientific Reports.

[19]  N. Musakaev,et al.  The mathematical model of the gas hydrate deposit development in permafrost , 2018 .

[20]  S. Misyura The Anomalously High Rate of Crystallization, Controlled by Crystal Forms under the Conditions of a Limited Liquid Volume , 2018 .

[21]  S. Misyura Wall effect on heat transfer crisis , 2016 .

[22]  S. Misyura High temperature nonisothermal desorption in a water–salt droplet , 2015 .

[23]  V. Nakoryakov,et al.  Boiling crisis in droplets of ethanol water solution on the heating surface , 2013 .

[24]  V. P. Lebedev,et al.  Effects of flow turbulence on film cooling efficiency , 1995 .