• Journal of the Korea Academia-Industrial cooperation Society
• /
• v.12 no.1
• /
• pp.537-544
• /
• 2011

This work was conducted to investigate the oxidation characteristics of methane having the highest ignition temperature among the other hydrocarbon gases using transition metal catalysts. The catalyst used for methane oxidation was manganese oxide having a various oxidation number, such as MnO, $MnO_2$, $Mn_2O_3$, $Mn_3O_4$, $Mn_4O_5$. The manganese oxide(MnxOy) catalyst is impregnated on $TiO_2$, $Al_2O_3$ for methane oxidation. To enhanced both of activity and life time of catalysts, Ni and Co was used as a promoter. In this study, various co-catalysts were synthesized by using excess wet impregnation method. The effect of reaction temperature and space velocity was measured to calculate the activity of catalysts such as, activation energy of $T_{50}$, and $T_{90}$. The life time of bi-metallic manganese mixture, such as Mn-Co and Mn-Ni catalysts, were increased more 10 % than manganese oxide catalyst, but activity of those was decreased slightly.

• Microbiology and Biotechnology Letters
• /
• v.42 no.1
• /
• pp.32-40
• /
• 2014

Methane oxidation and the production potentials of ground soil (soil A) and garden soil (soil B, C, & D) in an urban school were evaluated, and the methanotrophic and methanogen communities in the soil samples were quantified using quantitative realtime PCR. The methanotrophic community in the raw soil A sample possessed a $6.1{\times}10^3$ gene copy number/g dry weight soil, whereas those in the raw soils B~D samples were $1.6-1.9{\times}10^5$ gene copy numbers/g dry weight soil. Serum bottles added with the soil samples were enriched with methane gas, and then evaluated for their methane oxidation potential. The soil A sample had a longer induction phase for methane oxidation than the other soils. However, soil A showed a similar methane oxidation potential with soils B~D after the induction phase. The methanotrophic community in the enriched soil A sample was increased by up to $2.3{\times}10^7$ gene copy numbers/g dry weight soil, which had no significantly difference compared with those in soils B~D ($1.2-2.8{\times}10^8$ gene copy numbers/g dry weight soil). Methane production showed a similar tendency to methane oxidation. The methanogens community in raw soil A ($1.7{\times}10^5$ gene copy number/g dry weight soil) was much less than those in raw soils B~D ($1.3-3.4{\times}10^7$ gene copy numbers/g dry weight soil). However, after methane gas was produced by adding starch to the soils, soil samples A~D showed $10^7$ gene copy numbers/g dry weight soil in methanogens communities. The results indicate that methanotrophic and methanogenic bacteria have coexisted in this urban school's soils. Moreover, under appropriate conditions for methane oxidation and production, methanotrophic bacteria and methanogens are increased and they have the potential for methane oxidation and production.

• Applied Chemistry for Engineering
• /
• v.16 no.5
• /
• pp.641-647
• /
• 2005

The partial oxidation of methane is one of important processes for hydrogen production. As a membrane reactor, palladium-silver (Pd-Ag) alloy membrane prepared by electroless plating technique was employed for partial oxidation of methane. The experimental variables were reaction temperature, $O_2/CH_4$ mole ratio, $CH_4$ feed rate, and $N_2$ sweep gas flow rate. The methane conversions increased with the reaction temperatures in the range of 350 to $730^{\circ}C$. The highest methane conversion and CO selectivity were obtained at the condition of $O_2/CH_4$ mole ratio of 0.5 and $730^{\circ}C$ using commercially available nickel/alumina catalyst. The Pd-Ag membrane reactor showed higher methane conversions, 10~40% higher, compared to those in a traditional reactor.

• Bulletin of the Korean Chemical Society
• /
• v.23 no.5
• /
• pp.669-673
• /
• 2002

Ni catalyst (Ni: 15 wt%) supported on precalcined SiO2 has been investigated in reforming reactions of methane to synthesis gas. The catalyst exhibited fairly good activity and stability in partial oxidation of methane (POM), whereas it deactivated in steam reforming of methane (SRM). Pulse reaction results of CH4, O2, and CH4/O2 revealed that Ni/SiO2 has high capability to dissociate methane. The results also revealed that both CH4 and O2 are activated on the surface of metallic Ni, and then surface carbon species react with adsorbed oxygen to produce CO and CO2 depending on the bond strength of the oxygen species on the catalyst surface.

• Bulletin of the Korean Chemical Society
• /
• v.25 no.4
• /
• pp.573-576
• /
• 2004

• Journal of the Korean Applied Science and Technology
• /
• v.31 no.3
• /
• pp.446-452
• /
• 2014

Methanol was directly produced by the partial oxidation of methane with four-component mixed oxide catalysts. Four-component(Mo-Bi-Cr-Si) mixed oxide catalysts were prepared by the co-precipitation and sol-gel methods. The catalyst prepared by the sol-gel method showed about eleven times higher surface area than that prepared by the co-precipitation method. From the $O_2$-TPD experiment of the prepared catalysts, it was proven that there exists two types of oxygen species, and the oxygen species that participates in the partial oxidation reaction is the lattice oxygen desorbing around $750^{\circ}C$. The optimum reaction condition for methanol production was $420^{\circ}C$, 50 bar, flow rate of 115 mL/min, and $CH_4/O_2$ ratio of 10/1.5, providing methane conversion and methanol selectivity of 3.2 and 26.7%, respectively.

• Transactions of the Korean hydrogen and new energy society
• /
• v.20 no.4
• /
• pp.337-343
• /
• 2009

Noncatalytic partial oxidation of methane for producing synthesis gas was studied in a lab-scale experimental apparatus. Partial oxidation developed for high-temperature, fuel-rich combustion and it is exothermic process. but Steam reforming and Caron reforming is highly endothermic process to need much energy. Noncatalytic partial oxidation of methane is affected by temperature and equivalent ratio, so we studied effect about composition of synthesis gas at lab scale reactor. We used electronic heater to control the temperature of reactor. The quality of synthesis gas is improved and reduced heat value to require at Noncatalytic partial oxidation because the reacting temperature is lower at oxy condition.

• Applied Chemistry for Engineering
• /
• v.35 no.2
• /
• pp.79-84
• /
• 2024

Methane is an abundant and renewable hydrocarbon, but it causes global warming as a greenhouse gas. Therefore, methods to convert methane into useful chemicals or energy sources are needed. Methanol is a simple and abundant chemical that can be synthesized by the partial oxidation of methane. Methanol can be used as a chemical feedstock or a transportation fuel, as well as a fuel for low-temperature fuel cells. However, the electrochemical oxidation of methanol is a complex and multi-step reaction. To understand and optimize this reaction, new electrocatalysts and reaction mechanisms are required. This review discusses the methanol oxidation reaction mechanism, recent research trends, and future research directions.

• Journal of the Korean Applied Science and Technology
• /
• v.27 no.1
• /
• pp.29-36
• /
• 2010

The effects of La addition to Ni/$CeO_2$ methane partial oxidation catalysts were investigated. Catalysts were prepared by the impregnation and urea methods. In the preparation of catalysts, La content was changed from 1 wt% to 3wt%. Catalysts that contain 2wt% La showed the highest methane conversion of about 80% and CO selectivity of 84% and $H_2$ selectivity of 70%. This result may be stemmed from that, when La content is 2wt%, a fluorite oxide-type structure is well formed and carbon deposition is also decreased. Among the catalysts, 2.5wt% Ni/Ce(La)Ox showed the highest catalytic activity. From the experiment of changing reaction temperature with 2.5wt% Ni/Ce(La)Ox catalyst, it was found that the optimum reaction temperature is $750^{\circ}C$ and at this temperature methane conversion was about 90%, CO and $H_2$ selectivities were 94 and 80%, respectively.

• Journal of Energy Engineering
• /
• v.8 no.2
• /
• pp.256-264
• /
• 1999

The performance of the Pt-B/cordierite catalysts (2 wt%) Pt, 70 wt% Alumina, 28 wt%) Ceria and Zirconia, B: base metal) loaded with 6∼12 wt% Mn, Cu, V, Co, Cr and Ba, respectively was studied for partial oxidation of methane reaction and compared with that of Ni loaded catalyst. As a results, it was found that Ba, Co, Cr as well as Ni loaded catalysts showed higher activity for methane partial oxidation of methane than the Mn, Cu and V loaded catalyst. But it was known that catalysts having good activity for methane showed the good activity for coke formation, too. A XRD analysis of the catalyst before and after the reaction using 5 wt% Ni/Al$_2$O$_3$) showed that there were three Ni phases. In these results, it was found that methane oxidation reaction occulted at the front of the catalyst bed consisted of NiAl$_2$O$_4$and NiO and reforming reaction occurred at the rear part of the catalyst bed consisted of reduced Ni.