• Clean Technology
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• v.22 no.3
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• pp.141-153
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• 2016

Numerous stationary NO_x emission sources have employed a suitable deNO_x technology that is typically selective catalytic reduction (SCR) of NO_x by NH₃ over V₂O₅/TiO₂-based catalysts with on-demand monolithic structures. These structured catalysts undergo a time-on-deterioration of deNO_xing activity on site. Thus, we need more efficient, more deactivation-tolerant, more economic deNO_x systems and for which, their performance management is essential. This review has covered details of strategies to successfully manage the performance of SCR catalysts and timely replace them to new or rejuvenated ones. Key considerations to maintain the catalyst activity will be reviewed. Details of the sequential addition of new catalysts and the replacement of life-end catalysts and their regeneration will be discussed with general guidances to determine the time for such a replacement. Finally, a better way to get more economic approaches to deNO_x system management will be proposed here.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.13 no.11
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• pp.5610-5614
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• 2012

Performance of catalyst was studied with various operating conditions for selective catalytic reduction of $NO_x$ with $NH_3$. It is confirmed that catalysts containing Mn and Cu have a good efficiency in the usage of oxygen by the $H_2$-TPR analysis. In the case of catalyst #1, $NO_x$ conversion was decrease with the increase of reaction temperature. But in the case of catalyst #2, $NO_x$ conversion was increased and then remained constant with the increase of reaction temperature. This phenomenon is due to the difference of the $NH_3$ oxidation of both catalysts.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2001.11a
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• pp.46-47
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• 2001

황을 포함하는 촉매는 황을 포함하지 않은 촉매보다 저온영역에서 상대적으로 우수한 활성을 갖는 것으로 관찰하였다. $V_2$$O_{5}$가 담지된 촉매는 황에 인해 표면에 polymeric vanadate가 형성되었기 때문인 것으로 확인되어 polymeric vanadate가 탈질제거 활성에 유리한 활성점으로 확인되었다. 또한 활성저하 실험에서 반응온도의 영향이 큰 것으로 확인되었는데 $300^{\circ}C$이상의 반응온도에서는 생성된 염이 제거되는 온도영역이므로 염의 생성으로 인한 활성 저하는 확인 할 수 없다. 그러므로 $300^{\circ}C$이상의 반응온도에서는 활성저하가 관찰되지 않아 본 연구에서 제조된 촉매는 $300^{\circ}C$이상의 온도에서 조업되는 것이 바람직하다.

• Journal of Korean Society of Environmental Engineers
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• v.32 no.10
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• pp.928-935
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• 2010

A bag filter system was partially burnt down during a trial run of waste wood incineration boiler. This brought about unburned hydrocarbon which caused a rapid deactivation of low temperature SCR catalyst set up in two stage after the bag filter. The deactivated catalyst was investigated in order to trace the origin by several characterization methods such as XRD, EDX, BET, TGA, SEM. The deactivated catalyst was regenerated by different methods such as acid washing, water washing in ultrasonication, and calcination treatment under air condition. It is found the calcination treatment under air condition at $450^{\circ}C$ for 2 hours to be the best regeneration method. The catalytic activity was measured in the form of 2 cm ${\times}$ 2 cm ${\times}$ 10 cm (catalyst weight 10 g) honeycomb type. A deNOx efficiency of the regenerated catalyst showed 100% at $180^{\circ}C$ which is the same level of fresh one.

• Clean Technology
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• v.27 no.3
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• pp.207-216
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• 2021

Major anthropogenic emissions of elemental mercury (Hg⁰) occur from coal-fired power plants, and the emissions can be controlled successfully using NH₃-SCR (selective catalytic reduction) systems with catalysts. Although the catalysts can easily convert the gaseous mercury into Hg²⁺ species, the reactions are greatly dependent on the flue gas constituents and SCR conditions. Numerous deNO_xing catalysts have been proposed for considerable reduction in power plant mercury emissions; however, there are few studies to date of elemental mercury oxidation using SCR processes with MW- and full-scale coal-fired boilers. In these flue gas streams, the chemistry of the mercury oxidation is very complicated. Coal types, deNO_xing catalytic systems, and operating conditions are critical in determining the extent of the oxidation. Of these parameters, halogen element levels in coals may become a key vehicle for obtaining better Hg⁰ oxidation efficiency. Such halogens are Cl, Br, and F and the former one is predominant in coals. The chlorine exists in the form of salts and is transformed to gaseous HCl with a trace amount of Cl₂ during the course of coal combustion. The HCl acts as a very powerful promoter for high catalytic Hg⁰ oxidation; however, this can be strongly dependent on the type of coal because of a wide variation in the chlorine contents of coal.

• Journal of the Korean Crystal Growth and Crystal Technology
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• v.26 no.6
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• pp.238-242
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• 2016

The effect of the alkali, alkali earth metal elements on selective catalytic reduction(SCR) catalyst deactivation behavior were investigated in terms of microstructure, surface area, pore volume and De-NOx test. Poisoned SCR catalyst were manufactured by injection of $K_2CO_3$, $Na_2CO_3$, $Ca(CH_3COO)_2{\cdot}H_2O$, $C_4H_6MgO_4{\cdot}4H_2O$, $H_3PO_4$ solutions in the new SCR catalyst at $350^{\circ}C$ for 6 hours. New and poisoned catalysts surface were similar. But specific surface area, pore volume decrease from Na, Mg, K, Ca, P compared to new SCR catalyst. Especially, Na poisoned catalyst surface area and pore size extremely decreased by $10.20m^2/g$, $0.061cm^2/g$. De-NOx test results of new and poisoned catalysts at $150{\sim}450^{\circ}C$ indicated that alkali metal (K, Na) poisoned SCR catalysts have the lowest De-NOx efficiency, alkali earth metal poisoned SCR catalysts (Ca, Mg) De-NOx efficiency are higher than alkali metal poisoned SCR catalysts. P poisoned SCR catalyst De-NOx efficiency is similar new SCR catalyst. It were considered that physical deactivation of SCR catalyst was affected by SCR catalyst surface area and pore volume change.

• Proceedings of the KAIS Fall Conference
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• 2011.12a
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• pp.289-291
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• 2011

저온용 Mn-Cu계 촉매의 적정 적용온도를 파악하기 위해 다양한 조건에서 소성하였으며 소성한 촉매를 사용하여 반응온도, 유속 등에 따른 탈질효율 변화를 조사하였다. 실험결과 촉매의 전처리과정에서 바나듐-티타니아계 촉매보다 낮은 일정온도 이상으로 적용시 촉매의 산화가, pore 등에서 변화가 일어나며 궁극적으로 활성저하로 귀결됨을 알 수 있었다.

• Ceramist
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• v.10 no.1
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• pp.53-64
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• 2007

• Proceedings of the KAIS Fall Conference
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• 2010.11a
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• pp.294-297
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• 2010

본 연구논문에서는 주요 대기 오염물질인 $NO_x$를 처리하기 위해 다양한 종류의 촉매를 사용하여 탈질 특성을 조사하였다. 여러 종류의 담체에 다양한 종류의 활성물질을 답지한 촉매를 사용하였으며, 고정층 반응기를 이용하여 반응온도, 공간속도, 수분함량 등과 같은 공정조건에 따른 탈질효율도 측정하였다. 전체적으로 담지된 활성물질이 증가할수록 탈질효율도 증가함을 알 수 있었다.

• Proceedings of the KAIS Fall Conference
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• 2011.05a
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• pp.320-322
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• 2011

저온에서의 탈질능력이 우수한 망간계 촉매를 바탕으로 수소-TPR 장치를 사용하여 저온에서의 활성을 파악하였다. 상기 결과를 바탕으로 주요 공정조건인 반응온도, 유속, 수분함량, 주입물 농도, 주입가스 중 수분함량 등에 대한 탈질능의 변화를 조사하였다. 실험결과 망간계 촉매의 경우 반응온도가 증가할수록 탈질능력은 감소하였으며 수분함량에 대해서도 탈질효율이 크게 영향을 받음을 알 수 있었다.