There is a need for the purification of indoor air owing to a high rate of pollution in today’s world. For this, cabin air filters (CAFs) are widely used, which requires the addition of certain adsorbents to increase the volatile organic compound (VOC) removal efficiency. However, this addition causes high-pressure resistance, which may hamper commercial applications by requiring more energy and negatively affecting fresh air delivery rate. Hence, in this study, a high-performance combined CAF (CCAF) with excellent dust and chemical filtration performance and low differential pressure was prepared using granular activated carbon (GAC)/activated carbon fiber (ACF) mixed medium. The GAC/ACF mixed medium had higher air permeability than the ACF medium of the same weight, and it exhibited similar ultrafine dust filtration performance to the ACF medium without an increase in differential pressure. In addition, the GAC/ACF mixed medium showed excellent gas removal performance without increasing differential pressure by combining the VOC removal characteristics of the GAC and ACF filter media. The improved VOC removal performance of the GAC/ACF mixed medium was due to the hybrid effect of the hierarchical pore structures of the GAC and the nearly uniform pore structures of the ACF, which resulted in a slow and increased gas adsorption by the GAC and rapid gas adsorption of the ACF.

The performance characteristics and usefulness of the duct-type gas removal system to which the catalytic combustion method was applied were investigated by experiment. Benzene, toluene, ethylbenzene, and xylene were selected for performance tests on gas detection and removal of the catalytic combustion system. Accelerated experiments were performed to evaluate the gas sensing performance, the adsorption performance of activated carbon, and the basic performance and durability of the catalytic combustion system. The amount of gas adsorption in the adsorption stage was changed according to the type of activated carbon, adsorption temperature and time. The adsorption amount increased with increasing temperature and particle size. BTEX gas removal rate was about 96%, and the performance of the module was maintained for more than 4,000 hours.

Fly ash consists of various metal oxides which can remove SO2 gas by the catalyst effect. When fly ash is added in the preparation process of pitch-based activated carbon, the pitch particles aggregate and fly ash is embedded in the activated carbon. To increase SO2 gas removal performance, activated carbon was prepared by surface-treated fly ash and petroleum-based pitch. Carboxyl groups were introduced into the fly ash by malic acid treatment. The introduced carboxyl groups acted as an activation agent to create micropore around the fly ash, and created micropores were exposed to the fly ash outside of the activated carbon. The exposed fly ash increased removal amount of SO2 gas by a catalytic effect of the metal oxides. The SO2 gas removal performance improved by 34% because of the catalyst effect of the exposed fly ash and improvement in the micropore structure in the activated carbon.

The Odor-causing compounds from grilled meat restaurants are mainly ammonia, aldehydes, and volatile organic compounds (VOCs). Acetaldehyde is known to have the greatest odor contribution. This study examines the application of silica gel for acetaldehyde in gas stream. Heat-pretreated silica gel showed relatively good adsorption performance and at 150oC, its breakthrough capacity reached up to 51 mg/g. By using Thomas' dynamic model, which well estimated the adsorption performance in this study, the effects of inlet concentration and retention time on adsorption capacity were evaluated. The adsorbent saturated with acetaldehyde was regenerated by reducing the pressure, which was controlled by the vacuum pump. The design factors were found to be 10 sec−1 of space velocity, -184 kPa·hr of desorption condition, and 10 to 1 of the ratio of cross sectional area to the height for the fixed-bed. The cyclic operation of adsorption and desorption step in the fixed bed packed with silica gel appeared to have 7.0-8.8 mg/g of acetaldehyde removal capacity and 99% of regeneration.

A membrane contactor technique is proposed to selectively remove the SO2 gas from the ship exhaust gas. Membrane contactor system operates with two independent streams of liquid and gaseous phase, with a large contact area between the streams, resulting in high mass transfer coefficient values. In this study, hydrophobic polypropylene substrate was used to greatly minimize the wetting of the membranes. The performance of three absorbents -distilled water, NaOH, and Na2SO3 aqueous solution- was investigated in terms of SO2 removal efficiency within a specific range of different parameters (gas flow rate, absorbent molarities, liquid flow rate, L/G ratio). Finally, optimum operating parameters for a high SO2 removal efficiency were suggested; and the overall mass transfer coefficient and HTU values were examined.

To remove SO2 from flue gas, a thin film nanocomposite (TFN) hollow fiber membrane was decorated with Nafion/TiO2 nanoparticles. Morphological and structural analyses of the TFN membranes were performed using FTIR, SEM, EDX, TEM, and AFM. The gas permeation experiments were performed with pure gases and a mixed gas within a pressure range of 1-3 bar and feed gas flow rate of 0.03-0.15 L/min. The obtained experimental results suggest that the addition of Nf/TiO2 nanoparticles improved the membrane performance by introducing sulfonate and hydroxyl functional groups to the membrane, and thus increased SO2 permeability and selectivity. The SO2 permeability was found to be 411-1671 GPU, while the ideal selectivities achieved for SO2/N2 and SO2/CO2 were 2928 and 72, respectively. Overall, an SO2 removal efficiency of 93% was achieved by using the Nf/TiO2 incorporated TFN membrane.

The water removal characteristics in a PEMFC trapezoidal gas channel are investigated with the volume of fluid (VOF) method. For the case of wall contact angle of 60 degree, liquid water attaches on the top wall and moves toward the exit. In contrast, liquid water moves along the channel side corner or GDL surface irregularly for the higher wall contact angles. The hydrophillic wall contact angle of 60 degrees provides more favorable diffusion of reactants to cathode reaction sites as the GDL surface water coverage ratio approaches zero even if the water flow rate increases.

Gas hydrate (GH)-based desalination process have a potential as a novel unit desalination process. GHs are nonstoichiometric crystalline inclusion compounds formed at low temperature and a high pressure condition by water and a number of guest gas molecules. After formation, pure GHs are separated from the remaining concentrated seawater and they are dissociated into guest gas and pure water in a low temperature and a high pressure condition. The condition of GH formation is different depending on the type of guest gas. This is the reason why the guest gas is a key to success of GH desalination process. The salt rejection of GH based desalination process appeared 60.5-93%, post treatment process is needed to finally meet the product water quality. This study adopted reverse osmosis (RO) as a post treatment. However, the test about gas rejection by RO process have to be performed because the guest gas will be dissolved in a GH product (RO feed). In this research, removal potential of dissolved gas by RO process is performed using lab-scale RO system and GC/MS analysis. The relation between RO membrane characteristics and gas removal rate were analyzed based on the GC/MS measurement.

분리막 및 다양한 CO2 포집공정들의 연구에 있어, 경제성 평가는 각 공정들을 비교 분석하며 개발된 기술의 경제적 타당성을 검토하는데 중요한 역할을 한다. 본 연구에서는 분리막 기반의 CO2 포집공정에 대한 경제성 분석을 수행하여 그 결과를 살펴보았다. 분리막 공정의 전산모사와 최적화를 위하여 분리막 모델링 및 Aspen HYSYS®를 활용하였으며, 최적화 결과를 바탕으로 CAPEX 및 OPEX를 제시하여 분리막 공정의 경제성 평가를 진행하였다.

The volume of fluid method is applied to study the effects of the gas channel wall contact angle on the removal characteristics of a water slug in a right angle PEMFC gas channel. While maintaining the same GDL surface contact angle, two different contact angle distributions on the control area in the corner region are compared via the water coverage ratio and water volume fraction. The water coverage ratios of the hydrophobic channel corner case mainly show smaller values than that of the hydrophilic case except around 27 ms. The water volume fraction of the hydrophobic corner case is supposed to drop down quickly around 27 ms due to the dynamic movement of the liquid water compared to the hydrophilic case. In overall, the hydrophobic corner case shows better water slug removal characteristics.

The volume of fluid (VOF) method is applied to study the effects of the gas channel cross-section shape on the removal characteristics of a water slug in a trapezoidal PEMFC gas channel. Two different open angles 50 and 60 degrees are selected to investigate the effect of cross-section shape on the behavior of a liquid water slug. In comparison to the 50 degrees case, the water slug is removed slightly faster for the 60 degrees case.

To study the effects of the gas channel wall contact angle on the behavior of a liquid water slug, numerical simulations are performed with the volume of fluid (VOF) method. Two different contact angle combinations on the side and top channel walls are selected. In comparison to the reference case, the water slug is removed faster when the hydrophobic contact angle is applied selectively in the corner section.

The study was conducted to determine greenhouse gas (GHG) inventories in grasslands. After ‘Low Carbon Green Growth’ was declared a national vision on 2008, Medium-term greenhouse gas reduction was anticipated for 30% reduction compared to Business As Usual (BAU) by 2020. To achieve the reduction targets and prepare to enforce emissions trading (2015), national GHG inventories were measured based on the 1996 Intergovernmental Panel on Climate Change Guidelines (IPCC GL). The national Inventory Report (NIR) of Korea is published every year. Grassland sector measurement was officially added in 2014. GHG removal of grassland soil was measured from 1990 to 2012. Grassland area data of Korea was used for farmland area data in the「Cadastral Statistical Annual Report (1976~2012)」. Annual grassland area corresponding to the soil classification was used「Soil classification and commentary in Korea (2011)」. Grassland area was divided into ‘Grassland remaining Grassland’ and ‘Land converted to Grassland’. The accumulated variation coefficient was assumed to be the same without time series changes in grassland remaining grassland. Therefore, GHG removal of soil carbon was calculated as zero (0) in grassland remaining grassland. Since the grassland area increases constantly, the grassland soil sinks constantly . However, the land converted to grassland area continued to decrease and GHG removal of soil carbon was reduced. In 2012 (127.35Gg CO2), this removal decreased by 76% compared to 1990 (535.71 Gg CO2). GHG sinks are only grasslands and woodlands. The GHG removaled in grasslands was very small, accounting for 0.2% of the total. However, the study provides value by identifying grasslands as GHG sinks along with forests.

In this study, the porous ceramic filter was developed to be able to remove both dust and hazardous gas contained in fuel gas at high temperature. The porous ceramic filters were fabricated and used as a catalyst support. And the effects have been investigated such as the mean particle size, organic content and addition of foaming agent on the porosity, compressive strength and pressure drop of ceramic filters. With the increase of mean powder size and the organic content for the cordierite filter, the porosity was increased, but the compressive strength and pressure drop were decreased. From the results of the research, the optimum condition for the fabrication of ceramic filters could be acquired and they had the porosity of 58%, the compressive strength of 13.4 MPa and the pressure drop of 250 Pa. It was expected that this ceramic filter was able to be applied to the glass melting furnace, combustor, and dust/toxic gas removal filter.

The deodorization performances of ammonia, acetic acid and acetaldehyde were tested for each of all forty five air cleaners sold in the online shops and department stores. The removal performances of toluene and formaldehyde were also investigated and the results were compared to the deodorization performances for the air cleaners. Filter-type and complex type air cleaners which used activated carbon filters showed superior in odor removal performances to those of ionizer type and wet type air cleaners. Toluene and formaldehyde were readily removed for the most of filter-type and complex type air cleaners. Ionizer air cleaners had little removal ability for the toluene and formaldehyde.

In recent models of semiconductor manufacturing clean rooms, air washers are used to remove airborne gaseous contaminants such as NH3, SOx and organic gases introduced from outdoor air into clean room. Meanwhile, there is a large quantity of exhaust air produced from clean room. It is desirable to recover heat from exhaust air and use it to reheat outdoor air. In the present study, an experiment was conducted to investigate heat recovery, particle collection, and gas removal in a heat recovery type air washer system for semiconductor manufacturing clean rooms.

In the present research, we prepared the activated carbon (AC) sorbents to remove gas-phase mercury. The mercury adsorption of virgin AC, chemically treated AC and fly ash was performed. Sulfur impregnated and sulfuric acid impregnated ACs were used as the chemically treated ACs. A simulated flue gas was made of SOx, NOx and mercury vapor in nitrogen balance. A reduced mercury adsorption capacity was obtained with the simulated gas as compared with that containing only mercury vapor in nitrogen. With the simulated gas, the sulfuric acid treated AC showed the highest performance, but it might have the problem of corrosion due to the emission of sulfuric acid. It was also found that the high sulfur impregnated AC also released a portion of sulfur at 140℃. Thus, it was concluded that the low sulfur impregnated AC was suitable for the treatment of flue gas in terms of stability and efficiency.

Biogas has been used to remove water content and hydrogen sulfide (H2S). Removing water requires a low temperature process; thus, our study investigated removing H2S under high pressure and low temperature. Several experiments were conducted to investigate removal of H2S from a biogas stream by optimizing chemical absorption and the chemical reaction with a Fe/EDTA solution. The roles of Fe/EDTA were studied to enhance removal efficiency of H2S due to oxidization by Fe+3/EDTA. The objective of this study was to explore the feasibility of enhancing toxic gas treatment in a biogas facility. A biogas purification strategy affords many advantages. For example, the process can be performed under mild environmental conditions and at low temperature, and it removes H2S selectively. As the Fe-EDTA concentration increased, the H2S conversion rate increased because the Fe-EDTA complex was highly stable. The optimal pH to stabilize the chemical complex during oxidation of H2S was 9.0.

In this study the production of methane gas and the removal efficiency of nutrients in the anaerobic co-digestion facilitieswith food waste/food waste leachate (FWL), animal manure and food waste leachate (A-MIX), and sewage sludge andfood waste leachate (S-MIX) were investigated. The average amount of the theoretical methane production was 578.4CH4·L/kg·VSin from the anaerobic digestion facilities with FWL, 606.0CH4·L/kg·VSin from those with A-MIX and 570.0CH4·L/kg·VSin from those with S-MIX, respectively. The amount of the practical methane production was 350.7CH4·L/kg·VSin from the anaerobic digestion facilities with FWL, 379.5CH4·L/kg·VSin from those with A-MIX and 348.8CH4·L/kg·VSin from those with S-MIX, respectively. The nutrient compositions of FWL were 3.2g/100g for carbohydrates, 1.8g/100g for proteins and 1.9g/100g for lipids. The nutrient compositions of A-MIX were 0.4g/100g for carbohydrates,2.55g/100g for proteins 0.4g/100g and 0.7g/100g for lipids, respectively. The nutrient compositions of S-MIX were0.4g/100g for carbohydrates, 2.4g/100g for proteins 1.6g/100g and 0.4g/100g for lipids, respectively. The removalratio of carbohydrate was very high over 75% in all facilities and that of lipid was very low below 25%.