0D model of microwave discharge in water with barbotage of methane through the discharge zone

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A microwave discharge inside of a methane bubble in boiling water is modeled in a 0D approximation taking into account the change in the size of the plasma bubble. The process of quenching the reaction products after the bubble detaches from the electrode surface is also simulated. The working pressure is 1 atm. It is shown that the main reaction products are H2, CO2, and CO. The ratio of CO2 and CO concentrations depends on the ratio of the initial flows of water vapor and methane. The calculated concentrations of the main decomposition products of methane and water are in good agreement with experimental data.

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Yu. Lebedev

Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences

编辑信件的主要联系方式.
Email: lebedev@ips.ac.ru
俄罗斯联邦, Moscow

T. Batukaev

Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences

Email: lebedev@ips.ac.ru
俄罗斯联邦, Moscow

I. Bilera

Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences

Email: lebedev@ips.ac.ru
俄罗斯联邦, Moscow

A. Tatarinov

Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences

Email: lebedev@ips.ac.ru
俄罗斯联邦, Moscow

A. Titov

Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences

Email: lebedev@ips.ac.ru
俄罗斯联邦, Moscow

I. Epstein

Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences

Email: lebedev@ips.ac.ru
俄罗斯联邦, Moscow

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2. Fig. 1. Scheme of plasma bubble formation in water. Arrows inside the central tube-antenna show the supply of methane. Arrows outside the tube-antenna show microwaves. A bubble with plasma is located at the end of the central electrode-antenna. The bubbles that emerge are outside the discharge zone; they contain products of chemical reactions that occur during the hardening process.

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3. Fig. 2. Evolution of a bubble in a zero-dimensional model: 1 – bubble at the initial moment, 2 – bubble at the moment of separation, 3 – bubble ascent.

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4. Fig. 3. Dependence of the gas temperature in the bubble on time for different values ​​of M at P = 200 W, F CH 4 = 50 ml/min: 1 – M = 0.5; 2 – M = 3, 3 – M = 5.

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5. Fig. 4. Evolution of the plasma bubble size: 1 – M = 0.5; 2 – M = 3, 3 – M = 5. P = 200 W, F CH 4 = 50 ml/min.

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6. Fig. 5. Evolution of the average reduced field: 1 – M = 0.5; 2 – M = 3, 3 – M = 5. P = 200 W, F CH 4 = 50 ml/min.

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7. Fig. 6. Concentrations of the main charged particles before the bubble detaches from the antenna: 1 – electrons; 2 – sum of concentrations of negative ions, 3 – sum of concentrations of positive ions. M = 3, P = 200 W, F CH 4 = 50 ml/min.

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8. Fig. 7. Concentrations of the main neutral particles before the bubble detaches from the antenna for different values ​​of M: M = 0.5 (a); M = 3 (b), M = 5 (c); 1 – H 2 O, 2 – CH 4, 3 – H 2, 4 – CO 2, 5 – CO. P = 200 W, F CH 4 = 50 ml/min.

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9. Fig. 8. Scheme of formation of CO from methane and water vapor.

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10. Fig. 9. Rate of the main processes of formation and destruction of CO: M = 0.5 (a); 1 – HCO + H 2 O = H + H 2 + + CO; 2 – H + HCCO = CH 2 + CO; 3 – CO + OH = = CO 2 + H; 4 – O 1 (D) + CO → CO 2 ; M = 5 (b); 1 – HCO + H 2 O = H + H 2 + CO; 2 – H + HCO = H 2 + + CO; 3 – CO + OH = CO 2 + H; 4 – O – + CO → CO 2 + + e ; P = 200 W.

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11. Fig. 10. Total rate of formation and decay of CO 2: 1 – M = 0.5; 2 – M = 3, 3 – M = 5. P = 200 W, F CH 4 = 50 ml/min.

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12. Fig. 11. Quenching speed depending on time; M = 3; P = 200 W, F CH 4 = 50 ml/min.

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13. Fig. 12. Decomposition products of methane and water vapor depending on the methane flow. 1, 2, 3 – mole fractions of H2, CO and CO2, respectively, experiment; 1 ′, 2 ′, 3 ′ – mole fractions of H2, CO and CO2, calculation (ml/min, P = 200 W).

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