• Applied Chemistry for Engineering
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• v.34 no.6
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• pp.584-589
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• 2023

The physicochemical properties of VOx/TiO₂ catalysts with different TiO₂ supports were analyzed, and SCR reactions were performed. VOx/TiO₂ catalysts were prepared by impregnation using anatase TiO₂, which was manufactured by Sigma Aldrich and prepared from TiOCl₂ and titanium isopropoxide (TTIP) as a precursor. They are denoted as VS, VC, and VP. The specific surface area of the VS was 1/10 or less of that of the VC and VP, and the dispersibility of vanadium oxide was relatively low. As a result of XPS analysis, the ratio of adsorbed oxygen was higher in VS and VP with Ti³⁺ than in VC. In VC and VP, vanadium mainly existed in V⁴⁺ and V³⁺ states in relation to the dispersibility of vanadium oxide. The amount of adsorbed oxygen contributed more to NH₃-SCR activity than vanadium oxide dispersibility below 250 ℃, while vanadium oxide dispersibility contributed more to activity beyond 300 ℃. The fast SCR activity in all three samples was the highest at NO₂/NOx = 0.5, followed by VS < VC < VP samples. It was determined that the dispersibility of vanadium oxide had a significant effect on fast NH₃-SCR activity.

• Proceedings of the Korea Air Pollution Research Association Conference
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• 2003.05b
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• pp.99-99
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• 2003

육상에서 발생하는 공해 물질뿐만 아니라 해상에서 발생하는 공해 물질에 대한 관심이 높아진 가운데 선박에서 발생하는 탄화수소, 질소산화물, 일산화탄소, 이산화황 및 입자상 물질의 규제에 관한 방안이 가시화되고 있는 현실이다. 선박엔진에서 발생하는 질소산화물 제거 연구를 위해서 당사에서는 엔진 연료 분사 시스템에 관한 연구와 더불어 후처리 설비인 SCR 연구를 병행하고 있다. 본 연구는 당사 개발 촉매인 PILC(Pillared Interlayer Clay)를 이용한 SCR 적용에 관한 연구 결과중 촉매 특성에 관한 부분이다. (중략)

• Journal of the Korean Institute of Telematics and Electronics
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• v.11 no.2
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• pp.40-45
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• 1974

It is indicated that in SCR the anode current can be controlled by ajusting the gate voltage when the magnitude of anode current lies in the range of 10-2 to 10-3 Amperes. This fact is applied to make a simple sinusoidal oscillator circuit which has the negative resistance characteristics in its gate circuit by inserting a proper resistor into its cathode circuit.

• Proceedings of the Korea Air Pollution Research Association Conference
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• 2001.11a
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• pp.425-426
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• 2001

선택적촉매환원(Selective Catalytic Reduciton: SCR)공정은 배기가스 중 질소산화물을 암모니아와 촉매상에서 반응시켜 무해한 질소와 물로 전환하는 기술이다(Bosch, 1988). SCR 공정에서 우수한 촉매가 확보되었을 경우, 설비의 성능은 촉매층로 유입되는 유동의 조건에 따라 좌우되므로 최적의 유동조건을 갖도록 반응기의 구조와 가이드 베인등 유로변경장치를 설계하는 것은 매우 중요하다(Cho, 1994). (중략)

• Proceedings of the Korea Air Pollution Research Association Conference
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• 2002.04a
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• pp.293-294
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• 2002

화석연료의 연소로부터 발생되는 질소산화물은 산성비, 광화학스모그 및 오존층 파괴에 관여하는 환경오염물질로서 대기오염의 주범이 되고 있다. 연소 후 배기가스 중의 질소산화물 제어를 위한 선택적 촉매환인공정(Selective Catalytic Reduction: SCR)은 안정적이며 고효율 설계가 가능하여 범용적으로 사용되고 있는 기술이다. SCR 공정은 최초 미국에서 개발되었으나 일본과 독일에서 발전시켜왔으며 국내에서도 공정의 핵심기술인 촉매에 대한 다양한 연구를 수행하여 일부에서는 상용화 수준에 이르고 있다. (중략)

• Proceedings of the KIEE Conference
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• 2006.07c
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• pp.1372-1373
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• 2006

An electrostatic discharge (ESD) protection device, so called, N-type SCR with P-type MOSFET pass structure (NSCR_PPS), was analyzed for high voltage I/O applications. A conventional NSCR_PPS device shows typical SCR-like characteristics with extremely low snapback holding voltage, which may cause latchup problem during normal operation. However, a modified NSCR_PPS device with proper junction/channel engineering demonstrates highly latchup immune current- voltage characteristics.

• Journal of the Korean Society of Fisheries and Ocean Technology
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• v.14 no.2
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• pp.79-87
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• 1978

This is an experimental study on friction welding and heat treatment of engine exhaust valve materials whose welding combination is SCr4 as stem to 21-4N as head and SUH3 to 21-4N. In this study, not only the experiments of friction welding under the selected optimum welding condition and the examination of the mechanical properties were carried out, but also the heat treatment of friction welded specimens under the two selected conditions was taken to obtain the better welding character, eliminating the latent stress and the hardness peak which appeared at the welded zones of heat resisting steel(21-4N, SUH3) and low alloyed steel ($SCr_4$) friction weldments. The results obtained by the experiments and consideration in this study are as follows: I) It was experimentally proved quite reasonable that 'speed=3,OOO rpm, heating pressure Pl=8 kg/ mm2, upsetting pressure p, = 20 kg/mm', heating time $t_1$ = 3 see, upsetting time TEX>$t_2$ = 2.5 sec' was selected as the optimum welding condition for friction-welding the engine exhaust valve materials $SCr_4$ to 21-4 Nand SUH 3 to 21-4 N. 2) The results of the previous study and this one on friction welding of such dissimilar materials as SUH 3-SUH 31, SCr 4-SUH 31, SCr 4-SUH 3, SUH 3-CRK 22, SCr4-21-4 Nand SUH3-21-4 N agreed with each other substantially in the friction welding characteristics at welded interface zones. 3) It was also certified quite satisfactory that '600\ulcornerCX30 min. Xroom air cooling' as an optimum heat treatment condition of the friction welded materials SCr 4-21-4 Nand SUH 3-21-4 N was experimentally determined to eliminate the latent stress and the hardness peak at welded zones. 4) About 20% of the tensile strength before heat treatment of friction welded specimens was decreased after heat treatment 600\ulcornerCX30 min. Xair cooling, but the location of fracture was moved from heat affected zone to parent $SCr_4$ & SUH3. 5) Microscopic examination of the weld joints friction-welded and heat-treated under the above mentioned conditions revealed that the weld zone is very narrow and has a fine grained intermixed structure without any welding defects. 6) The above mentioned conditions can be also utilized as friction welding parameters of the other dissimiar materials for engine valve production.

• Korean Chemical Engineering Research
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• v.51 no.2
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• pp.163-170
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• 2013

Selective catalytic reduction of $NO_x$ by $NH_3$ ($NH_3$-SCR) over $V_2O_5/TiO_2$-based catalysts is recently reported to be an anthropogenic emitter of $N_2O$ that is a global warming gas with a global warming potential of 310. Therefore, this review will get a touch on significance of some parameters regarding $N_2O$ formation in the $deNO_xing$ reaction for fossil fuels-fired power plants applications. The $N_2O$ production in $NH_3$-SCR reaction with such catalysts occurs via side reactions between $NO_x$ and $NH_3$ in addition to $NH_3$ oxidation, and the extent of these undesired reactions depends strongly on the loadings of $V_2O_5$ as a primary active component and the promoter as a secondary one ($WO_3$ and $MoO_3$) in the SCR catalysts, the feed and operating variables such as reaction temperature, $NO_2/NO_x$ ratio, oxygen concentration, gas hourly space velocity, water content and thermal excursion, and the physical and chemical histories of the catalysts on site. Although all these parameters are associated with the $N_2O$ formation in $deNO_xing$ reaction, details of some of them have been discussed and a better way of suppressing the $N_2O$ production in commercial SCR plants has been proposed.

• Journal of the Korean Applied Science and Technology
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• v.37 no.4
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• pp.723-732
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• 2020

The spent RHDS (Residue HydroDeSulfurization) catalyst is deactivated mainly by deposition of various contaminants such as coke, sulfur and vanadium on the surface of catalyst. To eliminate those contaminants, the following remanufacturing process was conducted. The first, heavy oil on the surface of the spent RHDS catalyst was removed by kerosene and dehydrated. The second, the high temperature incineration was carried out to eliminate coke and sulfur components deposited on the surface of spent RHDS catalyst. The third, the excessive quantity of Vanadium deposited on the surface of catalyst was removed by leaching process as follows: ultrasonic agitation was carried out at 50℃, for 10 seconds with 0.5% and 1% oxalic acid solution. The purpose of this process is to find out regenerated RHDS catalyst can be used as SCR catalyst for NOx reduction by controlling the vanadium residual content of the regenerated RHDS catalyst through leaching process. The composition of regenerated RHDS catalyst was analyzed by XRF and the NOx reduction efficiency was also measured by continuous catalytic fixed bed reactor. As the result, regenerated catalyst, with 0.5% oxalic acid, ultrasonic agitation in 10 seconds, showed the most stable NOx reduction efficiency. Also, in comparison with commercial SCR catalyst, the NOx reduction performance of regenerated catalyst was similar to that of commercial SCR catalyst at the temperature 375℃ and higher whereas was lower than commercial SCR catalyst at the temperature range between 200~250℃. Therefore, it was confirmed that the regenerated catalyst as powder form wash coated on the surface of metal corrugated substrate can be used for commercial SCR catalyst.

• Journal of the Korean Society of Food Science and Nutrition
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• v.34 no.6
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• pp.904-909
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• 2005

To produce functional food ingredient from the soybean curd residue (SCR), alkaline fermentation was performed with SCR from cold processed (D-SCR) or hot processed (P-SCR) tofu. The solid- state fermentation was performed by Bacillus firmus NA-1 at $42^{\circ}C$. The fermentation of heat-treated D- SCR resulted in higher production of peptides and fibrinolytic enzyme compared with D-SCR without heating. The P-SCR showed higher production of peptides, fibrinolytic enzyme, indicating alkaline pH after fermentation for 18 hr. When the moisture content of P-SCR was reduced to $60\%$, the production of peptides and fibrinolytic enzyme were enhanced. The P-SCR fortified with $10\%$ MFS (micronized full-fat soy flour) showed higher fibrinolytic enzyme activity and consistency index by fermentation of Bacillus firmus NA-1 Furthermore, the P- SCR fortified with $20\%$ MFS indicated relatively higher peptide content, fibrinolytic enzyme activity and enhanced flavor. By increasing the addition of MFS, the peptide content of fermented P-SCR was increased significantly, but fibrinolytic enzyme was slightly decreased.