• 대한환경공학회지
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• 제33권5호
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• pp.368-377
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• 2011

소규모의 대기오염 배출원으로부터 질소산화물을 저감하는 방법으로 제안된 패키지형 SCR (selective catalytic reduction) 시스템 내에서 암모니아 농도제어에 관한 연구가 시행되었다. SCR 시스템의 효율은 촉매층의 효율적인 활용에 좌우되며 촉매층의 효율적인 사용은 시스템에 유입되는 배기가스의 유동균일도와 암모니아 농도의 균일도에 의해 좌우된다. 본 연구에서는 주어진 최적의 유동조건에서 SCR 시스템 내에 배치된 AIG 형상과 분사 유량 조정에 따른 암모니아 농도분포를 평가하였다. 기본 유동조건에서 분사구의 각도에 따른 전산해석 결과, 배가스 유동에 대해 동류방향($0^{\circ}$)으로 암모니아를 분사한 경우의 농도분포의 RMS(%) 수치는 약 95.3%, 대향방향인 $120^{\circ}$의 각도를 가지는 경우 90.1%로 파악되어 대향방향으로의 분사가 더 효율적인 것으로 파악되었다. 유동박리영역에서 벗어나도록 분사구의 위치를 변경하고 기초계산에서의 속도분포와 농도분포를 기준으로 환원제 유량을 조정한 결과 RMS(%) 수치를 최대 62.8%까지 하강시키는 효과를 가져왔다. AIG 형상 및 배치구조에 혼합증진의 효과를 정리하였다.

• 한국자동차공학회논문집
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• 제22권3호
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• pp.1-11
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• 2014

The aim of this study is to investigate the effect of SCR reactor on the exhaust emissions characteristics in order to develop a urea-SCR aftertreatment system for reducing $NO_x$ emissions. The experiments are conducted by using a flue tube LPG steam boiler with the urea-SCR aftertreatment system. The urea-SCR aftertreatment system utilizes the ammonia converted from 17% aqueous urea solution injected in front of SCR catalyst as a reducing agent for reducing $NO_x$ emissions. The equivalence ratio, urea injection amount, ammonia slip and $NO_x$ conversion efficiency relative to boiler load are applied to discuss the experimental results. In this experiment, the average equivalence ratio is calculated by changing only the fuel consumption rate while the intake air amount is constantly fixed at $25,957.11cm^3/sec$. The average equivalence ratios are 1.38, 1.11, 0.81 and 0.57 when boiler loads are 100, 80, 60 and 40%. The $NO_x$ conversion efficiency is raised with increasing urea injection amount, and $NH_3$ slip is also boosted at the same time. Consequently, the $NO_x$ conversion efficiency relative to boiler load should be examined in combination with urea injection amount and $NH_3$ slip. The results are calculated by 89, 85, 77 and 79% for the boiler loads of 100, 80, 60 and 40%. The appropriate amount of urea injection for the respective boiler load can be not discussed by only $NO_x$ emissions, and should be determined by considering the $NO_x$ conversion efficiency, $NH_3$ slip and reactive activation temperature simultaneously. In this study, the urea amounts of 230, 235, 233 and 231 mg/min are injected at the boiler loads of 100, 80, 60 and 40%, and the final $NH_3$ slips are measured by 8.48, 5.58, 11.97 and 11.34 ppm at the same conditions. THC emission is affected by the SCR reactor under other experimental conditions except 100% engine load, and CO emission at only 40% engine load. The rest of exhaust emissions are not affected by the SCR reactor under all experimental conditions.

• 공업화학
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• 제24권6호
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• pp.599-604
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• 2013

본 연구는 공침법으로 Ti가 첨가된 Mn-Cu 혼합산화물을 이용하여 $200^{\circ}C$ 이하의 저온 영역에서의 $NH_3$-SCR 반응특성에 관한 것이다. 제조된 촉매들은 BET, XRD, XPS, TPD를 이용하여 각각의 물리/화학적 특성을 분석하였다. Mn-Cu 혼합산화물은 매우 큰 비표면적과 저온에서의 높은 SCR 효율을 나타내었으며, Ti가 첨가된 경우 상대적으로 높은 SCR 효율과 $N_2$ 선택도를 나타내었다. 이러한 결과는 Ti가 첨가됨에 따라 화학 흡착된 산소종($Me-O_{ads}$)이 증가하여 NO가 $NO_2$로의 산화가 촉진되고, $Mn^{3+}$와 같은 $NH_3$의 흡착점의 수가 증가되었기 때문이다.

• 대한기계학회논문집A
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• 제24권11호
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• pp.2762-2770
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• 2000

The refuse incineration plant has an important role in saving the combustion energy for local heating system. But harmful combustion gas(NOx etc.) leads to some serious environmental problem. To reduce the gas, a SCR(Selective Catalytic Reduction)system is installed and it is controlled by adjusting the flow of ammonia gas(NH3) . In this paper, we apply a repetitive control method to reduce NOx by adjusting the flow of ammonia gas for SCR system in a refuse incineration plant which is located in Haeundae, Pusan, Firstly, we analyze the inlet NOx period by FFt method, and verify its periodic variations. Secondly, we design a repetitive control system by using state space model method. Lastly, the effectiveness of repetitive control system is shown by comparing to a conventional PID control in simulation and experimental results.

• 공업화학
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• 제18권4호
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• pp.350-355
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• 2007

천연망간광석을 이용한 질소산화물의 선택적촉매환원 반응에서 배가스 내에 포함된 수분의 영향을 연구하였다. 실험은 천연망간광석 촉매상에서 NO와 $NH_3$의 반응을 독립 또는 동시에 반응시켰다. 천연망간광석 촉매의 격자산소를 통하여 저온에서 $NH_3$가 산화될 수 있으며, $NH_3$의 산화로 인하여 생긴 NO 및 $NO_2$의 농도는 수분이 없을 때보다 수분이 존재할 때에 $300^{\circ}C$ 이상 고온에서 더 높게 나타났다. 수분은 천연망간광석 촉매상에서 NO 및 $NH_3$와 경쟁흡착하며, 이것은 고온 및 저온에서의 선택적촉매환원 반응을 저해하는 요인으로 작용할 수 있다. 촉매제조시 dipping한 수분도 $NH_3$와 경쟁흡착을 하여 $250^{\circ}C$ 이하에서 NOx 전환율이 감소하였다. NMO는 소성온도별로 활성특성이 달라지고 수분의 유무에 관계없이 $400^{\circ}C$의 최적소성온도를 갖는다.

• 한국자동차공학회논문집
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• 제17권1호
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• pp.154-161
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• 2009

This study is a part of project of urea-SCR system development for an in-use medium duty diesel engine. This study shows the effect of ammonia oxidation catalyst and SCR volume on $NO_X$ reduction performance. When AOC(Ammonia Oxidation Catalyst) is not used, the urea injection should be controlled accurately to prevent $NH_3$ slip. However, it is found that the accurate $NH_3$ slip control is not easy without AOC in real engine operating conditions, because $NH_3$ and $NO_X$ reaction characteristics change with many factors such as exhaust gas temperature and $NH_3$ absorbance on SCR. SCR volume is also one of important design parameters. This study shows that $NO_X$ reduction efficiency increases with increase of SCR volume especially at high space velocity and low exhaust gas temperature conditions. Additionally, this paper shows the emissions of EURO-2 medium duty diesel engine can be improved to the level of EURO-5 with a DPF and urea-SCR system.

• 한국환경과학회지
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• 제12권1호
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• pp.47-54
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• 2003

This paper have examined the optimum combination of SNCR and SCR by varying SNCR injection temperature and NSR ratio along with SCR space velocity. NOx reduction experiments using a SNCR/SCR combined process have been conducted in simple NO/NH$_3$/O$_2$ gas mixtures. Total gas flow rate was kept constant 4 liter/min throughout the SNCR and SCR reactors, where initial NOx concentration was 500 ppm in the presence of 5% O$_2$. Commercial catalyst, sulfated V$_2$O$\_$5/-WO$_3$/TiO$_2$, was used for SCR NOx reduction. The residence time and space velocity were around 1.67 sec, 2,400 h$\^$-1/ and 6,000 h$\^$-1/ in the SNCR and SCR reactors, respectively. SNCR NOx reduction effectively occurred in a temperature window of 900-950$^{\circ}C$. About 88% NOx reduction was achieved with an optimum temperature of 950$^{\circ}C$ and NSR=1.5. SCR NOx reduction using commercial V$_2$O$\_$5/-WO$_3$-SO$_4$/TiO$_2$ catalyst occurred in a temperature window of 200-450$^{\circ}C$ 80-98% NOxreduction was possible with SV=2400 h$\^$-1/ and a molar ratio of 1.0-2.0. A SNCR/SCR(SV=6000 h$\^$-1/) combined process has shown same NOx reduction compared with a stand-alone SCR(SV=2400 h$\^$-1/) unit process of 98% NOx reduction. The NH$_3$-based chemical could routinely achieve SNCR/SCR combined process total NOx reductions of 98% with less than 5 ppm NH$_3$ slip at NSR ranging from about 1.5 to 2.0, SNCR temperature of 900$^{\circ}C$-950$^{\circ}C$, and SCR space velocity of 6000 h$\^$-1/. Particularly, more than 98% NOx reduction was possible using the combined process under the conditions of T$\_$SNCR/=950$^{\circ}C$, T$\_$SCR/=350$^{\circ}C$, 5% O$_2$, SV=6000 h$\^$-1/ and NH$_3$/NOx=1.5. A catalyst volume was about three times reduced by SNCR/SCR combined process compared with SCR process under the same controlled conditions.

• 동력기계공학회지
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• 제19권6호
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• pp.26-32
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• 2015

The purpose of this study is to investigate the de-NOx performance characteristics according to the $TiO_2$ crystal structures ratio of $V_2O_5$ SCR catalysts. The anatase(100%) SCR catalyst showed the highest desorption peak of 80ppm at about $250^{\circ}C$, and $NH_3$ was not desorbed at $500^{\circ}C$. It can be confirmed that there was many $NH_3$ desorbed at a high temperature among other various crystal structures, which is because the catalyst was more acidized to increase the intensity of acid sites as the content of subacid sulfate ions($NH_2SO_4$) in the rutile phase increases. The anatase/rutile(7%/93%) SCR had the smallest width of de-NOx performance drop according to thermal aging, and had strong durability against thermal aging.

• 공업화학
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• 제17권4호
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• pp.409-413
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• 2006

$150{\sim}200^{\circ}C$의 저온조건에 적용하기 위한 탈질공정으로서 저온 플라즈마 및 암모니아 SCR 공정을 복합시킨 탈질공정에 대한 실험적인 연구가 수행되었다. 실험결과 저온조건에서 일반적인 SCR 반응에 비해 매우 빠른 반응속도를 갖는 fast SCR 반응의 가능성을 확인할 수 있었으며, 효과적인 fast SCR 반응을 위해서는 SCR 반응기에 투입되는 $NO_{2}/NO_{x}$의 비가 0.3~0.5 범위에 있음을 알 수 있었다. 본 연구에서는 저온운전에 따른 암모늄염의 발생문제, 배기가스에 포함되어 있는 탄화수소가 공정에 미치는 영향, 유사한 공정과의 운전전력 비교 등 해당기술을 활용하기 위해 기본적으로 필요한 자료를 제공하고 있다.

• 한국자동차공학회논문집
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• 제18권5호
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• pp.85-90
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• 2010

As the environmental regulation of vehicle emission is strengthened, investigations for $NO_x$ and PM reduction strategies are popularly conducted. Two current available technologies for continuous $NO_x$ reduction onboard diesel vehicles are Selective Catalytic Reduction (SCR) using aqueous urea and lean $NO_x$ trap (LNT) catalysts. The experiments were conducted to investigate the $NO_x$ reduction performance of SCR system which can control the ratio of $NO/NO_2$, temperature and SV(space velocity), and the model gas was used which is similar to a diesel exhaust gas. The maximum reduction efficiency is indicated when the $NO:NO_2$ ratio is 1:1 and the SV is 30,000 $h^{-1}$ in $300^{\circ}C$. Generally, ammonia slip from SCR reactors are rooted to incomplete conversion of $NH_3$ over the SCR. In this research, slip was occurred in 6cases (except low SV and $NO:NO_2$ ratio is 1:1) after SCR. Among 6 case of slip occurrence, the maximum conversion efficiency is observed when SV is 60,000 $h^{-1}$ in $400^{\circ}C$.