• 기계와재료
• /
• v.24 no.2
• /
• pp.38-46
• /
• 2012

인구의 증가와 급속한 산업화 그리고 편안함을 추구하고자 하는 문명의 이기로 인한 에너지 사용량 증가는 환경오염을 가속화시키는 문제를 유발하고 있어 전 세계적으로 심각한 사회문제로 대두되고 있다. 이에 반해 삶의 질의 향상에 따라 보다 쾌적한 환경에 대한 욕구와 인식의 변화로 환경보호에 대한 관심이 증가하는 추세이며, 이에 따라 각 국의 환경규제는 날로 강화되고 있다. 이러한 환경문제를 해결하기 위한 국제협력이 활발해지면서 무역과 연계된 국제 환경규제가 가속화되고 있으며, 환경선진국은 이러한 환경규제를 무역장벽으로 이용하고 있어 국가의 대외경쟁력에도 직 간접적으로 영향을 미치고 있다. 환경오염물질 중 질소산화물(NOx), 황산화물(SOx), 일산화탄소(CO), 이산화탄소($CO_2$) 및 휘발성유기화합물(VOCs), 다이옥신 그리고 입자상물질(PM)과 같은 대기오염물질은 대기 중으로 쉽게 확산되는 특성에 의해 인접한 지역까지 영향을 미치기 때문에 국제적인 규제대상의 초점이 되고 있으며, 경제협력개발기구(OECD, Organization for Economic Cooperation and Development), 유엔산하 국제해사기구(IMO, International Maritime Organization) 및 국제연소기구협회(CIMAC, International Council on Combustion engines)등 여러 국제기구를 중심으로 각종 규제수단을 개발하여 적용하고 있다. 특히, 국제해사기구(IMO)에서는 선박에서 발생되는 오염물질 등에 대한 규제강화를 위하여 새로운 국제해양오염방지협약(MARPOL)을 채택, 발효하여 그 규제 범위를 넓혀감에 따라 선박에 대한 각종 환경규제가 대폭 강화되고 있어 친환경 선박 및 관련 기술 개발이 활발히 진행 중에 있다. 이 글에서는 선박에서 배출되는 대기오염물질 중 그 자체로도 인체에 유해하며, 산성비, 광화학스모그 등 다양한 환경문제를 유발시키는 대표적인 물질인 질소산화물(NOx)과 질소산화물 배출규제에 대한 대응기술인 선택적촉매환원법(SCR, Selective Catalytic Reduction)과 SCR 탈질시스템에 사용되는 SCR 촉매에 대해 소개하고자 한다.

• Clean Technology
• /
• v.27 no.1
• /
• pp.61-68
• /
• 2021

Selective catalytic reduction (SCR) is widely used as a method of removing nitrogen oxide in large-capacity thermal power generation systems. Uniform mixing of the injected ammonia and the inlet flue gas is very important to the performance of the denitrification reduction process in the catalyst bed. In the present study, a computational analysis technique was applied to the ammonia injection system design process of a denitrification facility. The applied model is the denitrification facility of an 800 MW class coal-fired power plant currently in operation. The flow field to be solved ranges from the inlet of the ammonia injection system to the end of the catalyst bed. The flow was analyzed in the two-dimensional domain assuming incompressible. The steady-state turbulent flow was solved with the commercial software named ANSYS-Fluent. The nozzle arrangement gap and injection flow rate in the ammonia injection system were chosen as the design parameters. A total of four (4) cases were simulated and compared. The root mean square of the NH3/NO molar ratio at the inlet of the catalyst layer was chosen as the optimization parameter and the design of the experiment was used as the base of the optimization algorithm. The case where the nozzle pitch and flow rate were adjusted at the same time was the best in terms of flow uniformity.

• Applied Chemistry for Engineering
• /
• v.32 no.3
• /
• pp.237-242
• /
• 2021

Simultaneous removal technologies of multi-pollutants such as particulate matters (PMs), NOx, SOx, VOCs and ammonia have received consistent attention due to the enhancement of pollutant abatement efficiency in addition to the stringent environmental regulation and emission standard. Pretreatment of insoluble NO by an ozone oxidation can be considered to be more effective route for saving space occupation as well as operation cost in comparison with that of traditional selective catalytic reduction (SCR) process. Moreover the primary advantage of ozone oxidation process is that the simultaneous removal with acidic gas including SOx is also available. Herein, we highlight recent studies of multi-pollutant abatement via ozone oxidation process and the promising research topics for better application in industrial sectors.

• Journal of Korean Society of Environmental Engineers
• /
• v.33 no.5
• /
• pp.368-377
• /
• 2011

A package type of SCR (selective catalytic reduction) system that was proposed for removing the $NO_x$ found in flue gas from the small scale of air pollution sources was evaluated. The efficiency of the SCR system is determined by the proper utilization of catalytic media installed inside of the system, and the proper distribution of flow velocity and $NH_3$ concentration in the flue gas is a crucial factor for using the catalytic media. In this study, the distributions of $NH_3$ concentration were estimated under the various arrays and shapes of AIG at the given gas flow condition. The value of RMS (%) in $NH_3$ concentration is 95.3% at co-current flow (at $0^{\circ}$) injection but it is 90.1% at the condition of counter-current flow (at $120^{\circ}$) condition, which implies the counter-current injection is more favorable. By rearranging the $NH_3$ injection flow rates based on the distribution of velocity and $NH_3$ distribution in basic calculation, the value of RMS (%) in $NH_3$ concentration was reduced to 62.8%. The enhanced effect of $NH_3$ mixing by the combined effect of arrays and shapes are complied in the study.

• Journal of the Korean Applied Science and Technology
• /
• v.36 no.2
• /
• pp.668-675
• /
• 2019

Fine dust in air pollutants is recognized as one of the most serious social environmental problems. Most of the NOx is generated in a combustion process such as that of a coal-fired power plant, and therefore efficient elimination of the NOx from the coal-fired power plants is needed. This study investigates the removal efficiency of using $TiO_2$, a photocatalyst, to remove NOx by Selective Catalytic Reduction (SCR). To evaluate the NOx removal efficiency, $TiO_2$ catalyst and phosphate binder were mixed on the surface of the $Al_2O_3$ substrate with the exothermic agent, and the substrate was heat-treated. The NOx removal efficiency of the catalysts was evaluated according to the temperature, and XRD, SEM, TG-DTA and BET analyzes were performed to investigate the physicochemical properties of the catalysts. NOx removal efficiency was 58.7%~65.9% at 20min, 63.7~66.0% at 30min with temperature change according to time($250^{\circ}C{\sim}500^{\circ}C$). The $TiO_2$ used in the SCR for NOx removal is judged to have the most efficient removal efficiency at $300^{\circ}C$.

• 한국전산유체공학회:학술대회논문집
• /
• 2010.05a
• /
• pp.368-375
• /
• 2010

To alleviate NOx emission, a variety of approaches has been applied. In marine diesels, the application of SCR systems has been considered an effective exhaust aftertreatment method for NOx emission control. Most current SCR systems use a various catalyst for the reaction of ammonia with NOx to form nitrogen and water. In theory, it is possible to achieve 100% NOx if the NH3-to-NOx ratio is 1:1. However, the reaction has a limited non-uniformity of the exhaust gas flow and ammonia concentration distribution. Therefore it is necessary to investigate the optimum flow conditions. In order to achieve uniform flow at monolith front face, we are equipped with a various mixed device. In this paper, it is presented that the mixed devices play an important role improvement of flow patterns and particle distributions of NH3 by numerical simulation.

• Journal of computational fluids engineering
• /
• v.15 no.4
• /
• pp.9-16
• /
• 2010

To alleviate NOx emission, a variety of approaches has been applied. In marine diesels, the application of SCR systems has been considered an effective exhaust aftertreatment method for NOx emission control. Most current SCR systems use a various catalyst for the reaction of ammonia with NOx to form nitrogen and water. In theory, it is possible to achieve 100% NOx if the $NH_3$-to-NOx ratio is 1:1. However, the reaction has a limited non-uniformity of the exhaust gas flow and ammonia concentration distribution. Therefore, it is necessary to investigate the optimum flow conditions. In order to achieve uniform flow at monolith front face, we are equipped with a various mixed devices. In this paper, it is presented that the mixed devices play an important role improvement of flow patterns and particle distributions of $NH_3$ by numerical simulation.

• Journal of Advanced Marine Engineering and Technology
• /
• v.36 no.6
• /
• pp.814-822
• /
• 2012

To improve the flow and mixing characteristics of marine SCR system, two different mixer including up-down and swirl type mixer were considered. The purpose of this study is to analyse turbulence intensity and uniformity index in detail and to improve the performance of SCR with respect to the mixer structure. The results showed that, the concentration uniformity index is improved by about 5% with the utilization of both mixers in the front of catalyst part. Although the RMS value and relative turbulence intensity increased after the up-down type mixer, it could observed that the value of two parameters decreased with the flow proceeding forward to the downstream. For the case of swirl type mixer, the decrease of RMS value and relative turbulence intensity were relatively smaller than that of up-down type mixer, and uniform distribution of relative turbulence intensity was observed. As a results, it could be concluded that the mixing effects and the distance of the two kinds of mixer were different.

• Transactions of the Korean Society of Automotive Engineers
• /
• v.22 no.5
• /
• pp.73-83
• /
• 2014

CFD(computational fluid dynamics) model is developed to simulate direct injection of ammonia gas phase from ammonia transporting materials into the SCR catalyst in the exhaust pipe of the engine with solid SCR. Configurations of one-hole and four-hole nozzle, circumferential type, porous tube type, and the effect of mixer configurations which commonly used in liquid injection of AdBlue are considered for complex geometries. Mal-distribution index related to concentration of ammonia gas, flow uniformity index related to velocity distribution, and pressure drop related to flow resistance are compared for different configurations of complex geometries at the front section of SCR catalyst. These results are used to design the injection system of ammonia gas phase for solid SCR of target vehicle.

• Journal of Power System Engineering
• /
• v.13 no.4
• /
• pp.5-10
• /
• 2009

Urea-SCR system, the selective catalytic reduction using urea as reducing agent, is a powerful technique to reduce nitrogen oxides(NOx) emitted from diesel engines. However, a tank of urea(32.5 wt%)-water solution can be frozen in low ambient temperature levels of below $-11^{\circ}C$. The purpose of this study is to understand freezing and melting phenomena of the urea-water solution, and its can be applied to get the urea-water solution from frozen it within 5 minutes after cold start. Factors considered were the type of heater and the urea tank shape. From the results, it was found that melting volume of cartridge heater B during 5 minutes of heating period was 83ml when supplying electric power of 150W. Horizontal heater B, which was put in the narrow bottom space of the tank T1, had fast melting characteristics.