• Journal of Environmental Science International
• /
• v.12 no.12
• /
• pp.1255-1260
• /
• 2003

Plasma-photocatalytic oxidation process was applied in the decomposition of Triethylamine(TEA) and Methyl ethyl ketone(MEK). Plasma reactor was made entirely of pyrex glass and consists of 24mm inner diameter, 1,800mm length and discharge electrode of 0.4mm stainless steel. And initial concentrations of TEA and MEK for plasma-photocatalytic oxidation are 100 ppm. Odor gas samples were taken by gas-tight syringe from a glass sampling bulb which was located at reactor inlet and outlet, and TEA and MEK were determined by GC-FID. For plasma process, the decomposition efficiency of TEA and MEK were evaluated by varying different flowrates and decomposition efficiency of TEA and MEK increased considerably with decreasing treatment flowrates. For photocatalytic oxidation process, also the decomposition efficiency of TEA and MEK increased considerably with decreasing treatment flowrates. The decomposition efficiency of MEK was 57.8％, 34.2％, 18.8％ respectively and the decomposition efficiency of TEA was reached all 100％. This result is higher than that of plasma process only, From this study, the results indicate that plasma-photocatalytic oxidation process is ideal for treatment of TEA and MEK.

• Journal of Environmental Science International
• /
• v.16 no.10
• /
• pp.1197-1202
• /
• 2007

Adsorption experiments of binary mixed gases composed of acetone/methylethylketone (MEK), MEK/benzene, MEK/toluene, and benzene/toluene were carried out on activated carbon fixed-bed. The variations of equilibrium adsorption capacity according to type and fraction of binary gas were investigated. In case of binary gases composed of acetone/MEK and benzene/toluene, equilibrium adsorption capacities of MEK and toluene were increased according to the increase of fraction of MEK and toluene, but equilibrium adsorption capacities of acetone and benzene were decreased. In case of binary gases composed of MEK/benzene and MEK/toluene, equilibrium adsorption capacities of benzene and toluene were increased according to the increase of fraction of benzene and toluene, but equilibrium adsorption capacities of MEK was decreased.

• Journal of environmental and Sanitary engineering
• /
• v.14 no.2
• /
• pp.113-119
• /
• 1999

In this study, the incineration of MEK and toluene was studied on a Pt supported alumina catalyst at temperature range from 200 to $350^{\circ}C$. An approach based on the Mars-van Krevelen rate model was used to explain the results. The object of this study was to study the kinetic behavior of the platinum catalyst for deep oxidation. The conversions of MEK and toluene were increased as the inlet concentration was decreased and the reaction temperature was increased. The maximum deep conversion of MEK and toluene were 91.81% and 55.69% at $350^{\circ}C$, respectively. The ${\kappa}_3$ constant increases with temperature faster than the ${\kappa}_1$ constant, that is, the surface concentration of ($VOCs{\cdots}O$) is higher than that of (O) at higher temperature according to the Mars-van Krevelen mechanism. Also the activation energy of toluene was larger than MEK for toluene is aromatic compound which have stronger bonding energy.Therefore, the catalytic incineration kinetics of MEK and toluene with Mars-van Krevelen mechanism could be used as the basic data for industrial processes.

• Journal of Life Science
• /
• v.18 no.8
• /
• pp.1023-1030
• /
• 2008

NtMEK2, which is the tobacco MAPK kinase that is upstream of SIPK and WIPK, was identified using the dexamethasone (DEX)-inducible gain-of-function transgenic system. Expression of $NtNEK2^{DD}$, a constitutively active mutant of NtNEK2, leads to HR-like cell death, which indicates that the NtMEK2-SIPK/WIPK cascade controls defense responses in tobacco. However, little is known about the downstream target substrates or defense-related genes that are regulated by the NtMEK2-SIPK/ WIPK cascade. In this study, ACP-based differential display RT-PCR was used to isolate the downstream effectors mediated by the NtMEK2-SIPK/WIPK cascade in $NtNEK2^{DD}$ transgenic plants. The results identified 6 novel differentially expressed genes (DEGs). These included pathogen induced protein 2-4 (pI2-4), monoterpene synthase 2 (MTS2), seven in absentia protein (SINA), cell death marker protein 1 (CDM1), hydroxyproline-rich glycoprotein (HRGP) and unknown genes (DEG45). The induction of these genes was confirmed by RT-PCR of samples obtained from $NtNEK2^{DD}$ plants. Additionally, when compared with other isolated DEGs, the pI2-4, CDM1 and HRGP genes were significantly up-regulated in response to treatment with salicylic acid and tobacco mosaic virus. Taken together, these results suggest that three novel DEGs were regulated by the NtMEK2-SIPK/WIPK cascade involved in disease resistance in tobacco.

• Journal of Korean Society of Occupational and Environmental Hygiene
• /
• v.24 no.2
• /
• pp.238-245
• /
• 2014

Objectives: It was known that workers in synthetic leather company are mainly co-exposed to dimethylformamide(DMF) with methyl ethyl ketone(MEK) or toluene(TOL) instead of a single dimethylformamide. This study was examined to the physico-chemical properties in single DMF and binary mixture DMF with MEK or TOL. Materials: Physico-chemical properties were measured by Korean and American Standard Test Methods. Results: Boiling point, specific gravity and flash point in single DMF were significantly higher than binary mixture DMF with MEK or TOL and such difference was dependent on the mixing ratio of MEK and TOL, and low explosion limit in binary mixture DMF with TOL was only significantly lower than single DMF. However, Reid vapor pressure had significantly higher in binary mixture DMF with MEK or TOL compared with single DMF. Conclusions: Our results demonstrate that the binary mixture DMF with MEK or TOL synergistically increases volatilization of DMF. It was concluded that the interaction between DMF and MEK and/or TOL might play a key role in the volatilization process of DMF under environmental conditions of workplace.

• KSBB Journal
• /
• v.21 no.1 s.96
• /
• pp.34-41
• /
• 2006

The aim of this study is the development of biological removal process of methyl ethyl ketone (MEK) in odor gas, which is generated from the waste food recycling process. To develop the removal process of odor gas, MEK, the selection of proper biofilter support was carried out. When the biofilter equipment was passed by synthetic odor gas composed of 250 ppm of MEK, the maximum removal was achieved to $586.6g-MEK/m^3\;hr$ for polypropylene fibril as support. Under the same experimental conditions, the maximum removal in polyurethane support was obtained to $359.7 g-MEK/m^3\;hr$. Finally, the maximum removal in volcanic stone support was $56.2g-MEK/m^3\;hr$.

• Bulletin of the Korean Chemical Society
• /
• v.33 no.8
• /
• pp.2756-2758
• /
• 2012

• Bulletin of the Korean Chemical Society
• /
• v.32 no.8
• /
• pp.2817-2819
• /
• 2011

• Journal of Korean Society for Atmospheric Environment
• /
• v.22 no.1
• /
• pp.25-33
• /
• 2006

The objective of this research is to improve the adsorption capacity of adsorbent made from MSWI (Municipal Solid Waste Incinerator) fly ash by surface oxidation. Used oxidation agents were $HNO_{3}$, $H_{2}SO_{4}$ and $(NH_{4})_{2}S_{2}O_{8}$. These agents can modify the surface property of an adsorbent such as specific surface area, pore volume, and functional group. The surface structure was studied by BET method with $N_{2}$ adsorption. The acid value and base value were determined by Boehm's method. The adsorption properties were investigated with benzene and MEK (Methylethylketone). According to the results, the specific surface area of the adsorbent was increased from 309.2 $m^{2}$/g to 553.2 $m^{2}$/g by $HNO_{3}$ oxidation. But $H_{2}SO_{4}$ and $(NH_{4})_{2}S_{2}O_{8}$ oxidation was decreased slightly. After Oxidation, surface acid value increased, but base value decreased. FAA-N shows the highest acid value. The content of oxygen increased greatly and oxygen group was created on the adsorbent surface. The surface oxidation improved the adsorbing capacity for MEK. The amount of adsorbing MEK was increased from 189 $m^{2}$/g to 639 $m^{2}$/g by $HNO_{3}$ oxidation.

• Journal of the Korean GEO-environmental Society
• /
• v.11 no.6
• /
• pp.31-37
• /
• 2010

In this study, optimization of MEK and Toluene removal was conducted by HTO(Hybrid Thermal Oxidation) system. HTO system has a multi-bed reaction plate and the plate consisted of wasted heat regeneration part and catalysis part. VOCs removal by HTO system was estimated by changing inlet flow rates with different valve changing times. Under $350^{\circ}C$ of combustion temperature, VOCs was fully converted and the equivalent conversion was 100%. The thermal oxidation efficiency, related to the amount of injected fuel into HTO system and the valve change time, was revealed at the level of 93.0~96.3%. In case of MEK removal by HTO system, the efficiency was ranged from 91.1 to 97.1%. Also, Toluene removal efficiency(93.2~97.4%) was good and stable with respect to the operating conditions. Considering above results, it was proved that HTO system could be a stable and compact system for VOCs, especially MEK and Toluene with high removal efficiency.