• 플랜트 저널
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• 제18권3호
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• pp.52-61
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• 2022

본 연구는 실제 운영중인 영동에코발전본부 1호기 125 MW 우드펠릿 발전소를 대상으로 탈질설비 운전조건이 NOx 발생량에 미치는 영향을 시험하였다. SNCR 요소 유량 증가에 따라 NOx 농도는 점차 감소하였으나 SCR 후단 암모니아 슬립은 상승하였다. 시험대상 보일러는 고온의 내부온도로 인해 SNCR 운영에 불리한 구조이며 노즐의 최적위치 검토가 필요할 것이다. SCR 희석공기 온도변화는 NOx 발생량에 영향을 미치지 않았다. SCR 암모니아 유량 증가는 SCR 후단 NOx 농도를 감소시켰고 NOx 제거효율도 증가시켰다. 다만 암모니아 슬립 자체 기준치를 초과하지 않는 암모니아 유량 111 kg/h가 최대 운전기준으로 추정된다. SCR 믹서 압력 상승은 NOx 농도를 감소시키고 제거효율도 최대로 측정되어 NOx 생성을 가장 효과적으로 억제하는 변수로 파악되었다.

• 대한기계학회논문집B
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• 제38권1호
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• pp.41-48
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• 2014

Urea-SCR 시스템은 주로 열해리와 증발시간의 부족으로 인해 발생하는 암모니아 슬립 현상과 관련된 몇 가지 문제점들을 가지고 있으며, 이러한 문제점들은 분사된 요소수용액의 불균일한 분포를 초래한다. 따라서 본 연구에서는, 배기가스와 요소수용액 사이의 증발 및 혼합특성을 강화시키기 위해 인젝터 장착 각도 그리고 믹서의 장착 및 설치 각도와 같은 다양한 매개변수들을 바꾸며 전산해석 연구를 수행하였다. 그 결과, 이와 같은 매개변수들이 배기가스와 요소수용액의 증발 및 혼합특성에 상당한 영향을 미친다는 것을 알 수 있었으며, 이 매개변수들의 최적화가 요구된다. 또한, 본 논문은 Urea-SCR 분사 시스템의 DeNOx 성능을 증가시키고 암모니아 슬립을 감소시키기 위한 최적 설계 시 유용한 기준을 제안할 것이다.

• 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.

• 대한기계학회논문집B
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• 제41권6호
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• pp.397-407
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• 2017

본 논문에서는 연비손실 없이 높은 $NO_X$ 저감성능을 보이는 승용 디젤 엔진의 SCR 시스템을 위한 요소수의 분사전략을 제시하였다. 배출되는 $NO_X$량 대비 요소수가 화학량론적 1:1인 피드포워드 분사 전략과 함께 모델기반의 촉매 내 $NH_3$ 흡장률 추정 기법을 통하여 피드백 분사 제어전략을 함께 사용함으로써 과도상태에서 $NO_X$ 저감성능과 $NH_3$ 슬립 성능을 모두 만족시키고자 하였다. 제안된 분사전략을 적용하여 디젤산화촉매기와, 미립자필터가 장착된 2.2L 디젤 엔진을 갖춘 실제 차량에서의 실험을 통하여 제어기의 높은 $NO_X$ 저감률과 낮은 $NH_3$ 슬립 성능을 검증하였다.

• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2002년도 춘계합동학술대회 논문집
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• pp.206-209
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• 2002

본 논문에서는 폴리실리콘의 재결정화 공정에서 발생하기 쉬운 폴리실리콘의 엉김현상, 슬립, 부분적인 실리콘 기판의 녹음현상 등을 방지하기 위한 방법을 제시한다. 그리고 재결정화 된 박막의 질을 향상시키기 위한 폴리실리콘과 보호 산화막(capping oxide)의 두께 변화에 따른 실험 결과를 살펴본다. 폴리실리콘의 엉김현상은 매몰 산화막(buried oxide)과 액체 상태의 실리콘 사이의 wetting angle과 관계되는데, 이를-방지하기 위해서는 재결정화할 폴리실리콘과 산화막의 계면에 질소를 주입시켜주면 되는데, 이는 재결정화할 시료를 암모니아 가스 분위기에서 열처리를 통하여 해결할 수 있다. 그러고 실러콘 기판의 국부적 녹음 현상 및 슬립은 실리콘 기판의 윗면을 mechanical damage에 의해서 약 $20{\mu}m$ 정도의 거칠기를 가지도록 하면 이러한 현상을 방지할 수 있다. 그러고 폴리실리콘이 재결정활 될 때 부피의 변화가 발생하며, 이로 인하여 재결정화된 박막의 두께는 위치에 따라 변화한다. 재결정화된 박막 두께의 균일도를 유지하기 위해서는 재결정화할 폴리실리콘 두께의 3배 이상이 되는 보호 산화막을 사용하였을 때 원하는 균일도를 얻을 수 있었다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2008년도 추계학술대회B
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• pp.3096-3101
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• 2008

Selective Catalytic Reduction (SCR) technology is well-known to be effective for the reduction of NOx emission. So car manufacturers has adopted Ures-SCR system to be satisfied with emission regulation. This paper discusses the effective of $NH_3/NOx$ ratio and SCR catalyst temperature in the $NH_3$-SCR reactor on DeNOx performance. So it is shown the characteristic of NOx conversion and ammonia slip using the $NH_3$ instead of Urea-Solution. From the result of this study, it is found to optimize $NH_3/NOx$ ratio to have the best case of high NOx conversion and low ammonia slip at variable SCR catalyst temperatures. Lastly, it is also found the characteristics of NOx conversion and ammonia slip with compared with Urea.

• 한국자동차공학회논문집
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• 제24권3호
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• pp.302-309
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• 2016

Urea-SCR system is currently regarded as promising NOx reduction technology for diesel engines. SCR system has to achieve maximal NOx conversion in combination with minimal $NH_3$ slip. In this study, model based open loop control for urea injection was developed and assessed in the European Transient Cycle (ETC) for heavy duty diesel engine. On the basis of the transient modeling, the kinetic parameters of the $NH_3$ adsorption and desorption are calibrated with the experimental results performed over the zeolite based catalyst. $NH_3$ storage or surface coverage of SCR catalyst can not be measured directly and has to be calculated, which is taken into account as a control parameter in this model. In order to reduce $NH_3$ slip while maintaining NOx reduction, $NH_3$ storage control algorithm was applied to correct the basic urea quantity. If the actual $NH_3$ surface coverage is higher than the maximal $NH_3$ surface coverage, the urea injection quantity is significantly reduced in the ETC cycle. By applying this logic, the resulting $NH_3$ slip peak can be avoided effectively. With optimizing the kinetic parameters based on standard SCR reaction, it suggests that a simplified, less accurate model can be effective to evaluate the capability of model based control in the ETC cycle.

• 한국자동차공학회논문집
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• 제19권2호
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• pp.50-56
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• 2011

To meet the NOx limit without a penalty of fuel consumption, Urea-SCR system is currently regarded as promising NOx reduction technology for diesel engines. SCR system has to achieve maximal NOx conversion in combination with minimal $NH_3$ slip. In this study, map based open loop control for urea injection was developed and assessed in the European Transient Cycle (ETC) for heavy duty diesel engine. The basic urea quantity set-value which was calculated using the look up tables of engine out NOx, exhaust flow rate and optimum NSR resulted in NOx reduction of 80% and the average $NH_3$ slip of 24 ppm and maximum of 79 ppm. In order to reduce $NH_3$ slip, $NH_3$ storage control algorithm was applied to correct the basic urea quantity and reduced $NH_3$ slip levels to the average 15 ppm and maximum 49 ppm while keeping NOx reduction of 76%. With high and increasing SCR temperature, the $NH_3$ storage capacity decreases, which leads to $NH_3$ slip. The resulting $NH_3$ slip peak can be avoided by stopping or significantly reducing the urea injection during the SCR temperature gradient is over $30^{\circ}C/min$.

• 한국자동차공학회논문집
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• 제20권1호
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• pp.95-105
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• 2012

The selective catalytic reduction (SCR) system is a highly-effective aftertreatment device for NOx reduction of diesel engines. Generally, the ammonia ($NH_3$) was generated from reaction mechanism of SCR in the SCR system using the liquid urea as the reluctant. Therefore, the precise urea dosing control is a very important key for NOx and $NH_3$ slip reduction in the SCR system. This paper investigated NOx and $NH_3$ emission characteristics of urea-SCR dosing system based on model-based control algorithm in order to reduce NOx. In the map-based control algorithm, target amount of urea solution was determined by mass flow rate of exhaust gas obtained from engine rpm, torque and $O_2$ for feed-back control NOx concentration should be measured by NOx sensor. Moreover, this algorithm can not estimate $NH_3$ absorbed on the catalyst. Hence, the urea injection can be too rich or too lean. In this study, the model-based control algorithm was developed and evaluated on the numerical model describing physical and chemical phenomena in SCR system. One channel thermo-fluid model coupled with finely tuned chemical reaction model was applied to this control algorithm. The vehicle test was carried out by using map-based and model-based control algorithms in the NEDC mode in order to evaluate the performance of the model based control algorithm.

• 한국자동차공학회논문집
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• 제18권2호
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• pp.122-128
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• 2010

To meet the NOx limit without a penalty of fuel consumption, urea-SCR system is currently regarded as promising NOx reduction technology for diesel engines. SCR system has to achieve maximal NOx conversion in combination with minimal $NH_3$ slip. In this study, the performance characteristics of urea-SCR system with open loop control were assessed in the European Transient Cycle(ETC) for heavy duty diesel engine. The SCR inlet temperaure varied in the range of 200 to $340^{\circ}C$ in the ETC cycle. Open loop control calculated the urea flow rate based on the NOx and NSR map which gave for each combination of SCR inlet temperature and space velocity the normalized $NH_3$ to NOx stoichiometric ratio which resulted in a steady-state $NH_3$ slip of 20ppm. During the ETC cycle, the open loop control with the optimized NSR offset achieved NOx reduction of 80% while keeping the average $NH_3$ slip below 10ppm and maximum 20ppm. It was also found that NOx sensor was cross-sensitive to $NH_3$ and a control strategy for cross-sensitivity compensation was required in order to use a NOx sensor as feedback device.