진공증착법으로 제작한 V2O5 박막의 두께 및 결정성에 따른 전기변색 특성을 체계적으로 조사하였다. 증착된 박막은 노란색을 띄고 있었으며 140˚C 보다 높은 기판온도에서 증착된 V2O5 박막은 결정질로 낮은 기판온도에서 증착된 박막들은 비정질로 밝혀졌다. 리튬 이온 주입에 따른 V2O5 박막의 광 변조 특성 결과 V2O5 박막의 두께와 결정성에 관계없이 300~500nm 파장영역에서는 산화발색이 500~1100nm 파장영역에서는 환원 발색이 나타났다. 비정질과 결정질 Lix V2O5 박막의 optical band gap 에너지는 리튬 이온 주입양이 증가함에 따라 (x=0.0~0.6) 각각 0.75 [eV], 0.17 [eV]씩 높은 에너지쪽으로 이동하였다. 비정질 Lix V2O5 박막의 coloration efficiency는 근적외선 영역에서는 리튬 이온 주입과 박막두께에 따라 거의 변화가 없었으나 blue와 near-UV 영역에서는 absorption edge가 500nm 파장근처에서 높은 에너지 부근으로 이동됨으로 인하여, 박막두께가 증가하고 리튬 이온주입양이 감소할수록 coloration efficiency가 상당히 증가하는 것으로 나타났다. 그러나 결정질 Lix V2O5 박막의 경우 coloration efficiency는 전파장영역에서 리튬 이온 주입양과 박막두께에 거의 영향을 받지 않는 것으로 밝혀졌다.

V2O5-TiO2 catalysts were prepared by various methods. V2O5-TiO2 were prepared by sol-gel method with different drying conditions (aerogel and xerogel), and V2O5 supported on TiO2 obtained by sol-gel method with precipitation-deposition method and impregnation method. The performance of the V2O5-TiO2 catalysts was investigated for the selective oxidation of hydrogen sulfide in the stream containing both ammonia and excess water. All the catalysts showed good dispersion of vanadium and they had high H2S conversion with no or little production of sulfur dioxide. The V2O5-TiO2 aerogel catalyst prepared by sol-gel method with drying under super critical condition had the highest surface area which led to better catalytic activity compared to those by other synthesis methods.

질소산화물 등의 배출규제 강화로 인한 사용처의 확대로 SCR(선택적 촉매 환원) 촉매 수요가 증가하고 있으며, 이에 따라 폐촉매 발생량도 증가할 것으로 예상된다. 폐촉매는 지정폐기물로 분류되어 처리시에 비용이 발생하여, 물리적으로 재생하여 재사용 하거나 유가금속을 회수하는 방법으로 재활용하고 있다. 그러나 재생의 횟수가 제한적이고, 유가금속 회수는 비용이 고가이며 촉매의 85~90%를 차지하는 TiO2가 폐기된다는 문제점이 있다. 따라서, 본 연구에서는 SCR 촉매를 경제적이며 지속적으로 사용하기 위해 피독된 SCR 촉매 내 피독물질만 화학적으로 수세 및 정제하고 유가금속/TiO2의 함량을 높이는 최적의 세정 용매를 도출하는 촉매 재활성을 위한 기초연구를 수행하였다. 비교대상 촉매인 Poisoned 촉매를 5가지 세정용매로 화학적 처리결과, acetic acid 용매가 V2O5 1.19 wt%의 높은 함량과 57.6%의 높은 피독물질 제거효율을 나타내며 다른 산 처리 용매에 비해 촉매 재생성이 높은 것으로 분석되었다. 세정 용매의 농도와 세정 시간에 따른 V2O5 함량과 피독물질 제거효율에 미치는 영향을 알아보기 위해 각각 변수를 두어 실험을 진행하였다. 본 연구를 통해 0.1 N acetic acid로 처리한 촉매가 가장 높은 NOX전환율을 나타냈으며, 유가금속/TiO2 함량 또한 높게 나타나 본 연구 목표에 가장 적합한 세정용매로 판단되었다.

In this article we present the precise positions of XP and the finite verb moving to the functional categories in the Old English (OE) main clauses in association with the label algorithm advocated in Chomsky 2013. With V2 and V3 phenomena in Old English the previous studies did not show any consistent accounts on the moved positions of XP and the finite verb mingled with the status of OE pronouns in the main clauses. In the previous studies some proposed IP-V2 and others did CP-V2 in conjunction with the different status (clitic, weak pronoun or Agr clitic) of the OE Pronouns. In contrast we show a consistent account that XP moves to CP Spec and the finite verb moves to C in the OE V2 contexts including wh-clauses whereas XP moves to IP in the V3 clauses due to the label algorithm where the ϕ-feature of C and T makes two lexical items share prominent features in order to complete the labeling of CP and TP respectively.

This study examined the catalytic destruction of 1,2-dichlorobenzene on V2O5/TiO2 nanoparticles. The V2O5/TiO2 nanoparticles were synthesized by the thermal decomposition of vanadium oxytripropoxide and titanium. The effects of the synthesis conditions, such as the synthesis temperature and precursor heating temperature, were investigated. The specific surface areas of V2O5/TiO2 nanoparticles increased with increasing synthesis temperature and decreasing precursor heating temperature. In addition, the removal efficiency of 1,2-dichlorobenzene was promoted by a decrease in heating temperature. However, the removal efficiency of 1, 2-dichlorobenzene was decreased by an anatase to rutile phase transformation at temperatures 1,300℃.

V2O5/TiO2 catalyst impregnated ceramic candle filters are in principle, capable of performing shallow-bed dust filtration plus a catalytic reaction, promoted by a catalytic deposited in their inner structure. Pilot-scale V2O5/TiO2 catalyst impregnated ceramic candle filters were prepared, characterized and tested for their activity towards the SCR reaction. The effect on NO conversion of operating temperature, gas hourly space velocity, amount of deposited catalyst, pressure drops and long-term experiment (life of catalytic filter) was determined. The following effects of V2O5/TiO2 catalyst impregnated ceramic candle filters in SCR reaction are observed: (1) It increases the activity and widens the temperature window for SCR. (2) When the content of V2O5 catalyst increases further from 3 to 9wt.%, activity of NO increases. (3) NO conversion at first increases with temperature and then decreases at high temperatures (above 400℃ over), possibly due to the occurrence of the ammonia oxidation reaction.

A (5 wt.%)Mn-(1 wt.%)V2O5/TiO2 catalyst were prepared by co-precipitation method and used for low-temperature selective catalytic reduction (SCR) of NOx with ammonia in the presence of oxygen. The properties of the catalysts were studied by X-ray diffraction (XRD), temperature programmed reduction (TPR) and scanning electron microscope-energy dispersive X-ray spectroscopy (SEM-EDS). The experimental results showed that (5 wt.%)Mn-(1 wt.%)V2O5/TiO2 catalyst yielded 81% NO conversion at temperature as low as 150℃ and a space velocity of 2,400 h-1. Crystalline phase of Mn2O3 was present at ≥15% Mn on V2O5/TiO2. XRD confirmed the presence of manganese oxide (Mn2O3) at 2θ=32.978°(222). The XRD patterns presented of (5 wt.%)Mn-(1 wt.%)V2O5/TiO2 did not show intense or sharp peaks for manganese oxides and vanadia oxides. The TPR profiles of (5 wt.%)Mn-(1 wt.%)V2O5/TiO2 catalyst showed main reduction peak of a maximum at 595℃.

V2O5/TiO2 catalysts promoted with Mn were prepared and tested for selective catalytic reduction of NOx in NH3. The effects of promoter content, degree of catalyst loading were investigated for NOx activity while changing temperatures, mole ratio, space velocity and O2 concentration. Among the various V2O5 catalysts having different metal loadings, V2O5(1 wt.%) catalyst showed the highest activity(98%) under wide temperature range of 200-250℃. When the V2O5 catalyst was further modified with 5 wt.% Mn as a promoter, the highest activity(90-47%) was obtained over the low temperature windows of 100-200℃. From Mn-V2O5/TiO2, it was found that by addition of 5 wt.% Mn on V2O5/TiO2 catalyst, reduction activity of catalyst was improved, which resulted in the increase of catalytic activity and NOx reduction. According to the results, NOx removal decreased for 10%, but the reaction temperature down to 100℃.

The rise of multiple negation which bears negative concord can be explained in terms of the word order change from (S)XV having preverbal predicate negation to (S)VX having postverbal predicate negation in the history of English language. In a multiple negative sentence with V2 where a second negative adverb appears in the second stage of the Jespersen`s negative cycle, the first negator performs the grammatical function of focalization in the Spec of CP and the second one confirms the negative meaning in 1P. The linguistic circumstances in which ne.....na￣/no￣>na￣ht/no￣ht was preferred to ne seem to be closely related to the grammatical function of focalization which was realized in the syntactic structure of V2. The head C in V2 word order has a focus feature as the uninterpretable EPP-feature of OCC, and this feature induces the operation Agree that is accompanied by the internal Merge of a focus element. It is widely recognized that the negator ne in CP has come to be weak and cliticized, but it is still treated as an independent constituent in the multiple negative sentences with V2.