• Title/Summary/Keyword: NO Oxidation

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바나듐계 촉매상에서 암모니아를 이용한 질소산화물의 환원반응속도에 수분이 미치는 영향에 관한 연구 (Effect of Water on the Kinetics of Nitric Oxides Reduction by Ammonia over V-based Catalyst)

  • 김영득;정수진;김우승
    • 한국자동차공학회논문집
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    • 제20권6호
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    • pp.73-82
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    • 2012
  • The main and side reactions of the three selective catalytic reduction (SCR) reactions with ammonia over a vanadium-based catalyst have been investigated using synthetic gas mixtures in the temperature range of $170{\sim}590^{\circ}C$. The three SCR reactions are standard SCR with pure NO, fast SCR with an equimolar mixture of NO and $NO_2$, and $NO_2$ SCR with pure $NO_2$. Vanadium based catalyst has no significant activity in NO oxidation to $NO_2$, while it has high activity for $NO_2$ decomposition at high temperatures. The selective catalytic oxidation of ammonia and the formation of nitrous oxide compete with the SCR reactions at the high temperatures. Water strongly inhibits the selective catalytic oxidation of ammonia and the formation of nitrous oxide, thus increasing the selectivity of the SCR reactions. However, the presence of water inhibits the SCR activity, most pronounced at low temperatures. In this study, the experimental results are analyzed by means of a dynamic one-dimensional isothermal heterogeneous plug-flow reactor (PFR) model according to the Eley-Rideal mechanism.

귀금속 함량에 따른 디젤산화촉매의 이산화질소 배출 특성 (Emission Characteristics of NO2 in Diesel Oxidation Catalyst according to the Content of Precious Metal)

  • 김훈명;박용성;이광구
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2012년도 제45회 KOSCO SYMPOSIUM 초록집
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    • pp.37-38
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    • 2012
  • Two catalyst systems with different content of precious metal coated on DOC are carefully tested in a diesel engine to investigate the emission characteristics of $NO_2$. Three types of experiment methods ($NO_2$ conversion test, ETC mode test, and BPT test) are applied to compare the performance of the two catalyst systems. All the experimental results consistently indicate that it is possible to satisfy $NO_x$ regulation by properly lowering the content of precious metal without the loss of PM removal performance.

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EFFECT OF ETHENE $(C_2 H_4)$ ON THE PLASMA $DeNO_X$ PROCESS FROM DIESEL ENGINE EXHAUST

  • Park, Kwang-Seo;Kim, Dong-Inn;Lee, Hyeong-Sang;Chun, Bae-Hyeock;Yoon, Woong-Sup;Chun, Kwang-Min
    • International Journal of Automotive Technology
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    • 제2권2호
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    • pp.77-83
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    • 2001
  • Effect of ethene on the $DeNO_X$ conversion process in a simulated diesel engine operating conditions was investigated experimentally and theoretically. With the addition of even a small amount of ethene the NO to $NO_2$ conversion enhances greatly. The energy required to convert one NO molecule is 27 eV with 250 ppm ethene added, while 137 eV without ethene at 473 K. The effect of energy density, temperature, and the initial concentrations of ethene and oxygen are also discussed and the results show that the increase of the mentioned parameters lead to the promotion of NO oxidation. A kinetic model used in this study shows good agreement with the experimental result. Byproducts like formaldehyde ($CH_2$ 0) and methyl nitrite ($CH_3$ ONO) predicted by model calculation are broken up into CO and $H_2O$ eventually when high energy is delivered to the gas mixture. Sensitivity analysis shows that the main reactions of NO oxidation when ethene is added we: $HO_2+ NO \arrow NO_2 + OH, RO_2 + NO \arrow NO_2 + RO$, where R is a hydrocarbon radical. Also the direct oxidizing reaction of NO with O cannot be neglected.

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조류의 오존산화에 관한 연구 (A Study on Ozone Oxidation of Algae)

  • 김은호;성낙창;최용락
    • 생명과학회지
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    • 제9권5호
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    • pp.590-595
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    • 1999
  • The objectives of this research were to estimate variation characteristics of TOC, UV-254 and NH4+-N, etc, if odorous generated algaes flowed into water treatment plant and they contacted with ozone known as typical advanced treatment. It was estimated that pH decreased from initial 7.4 to 2.1 after ozone contact 100min. pH declined to early 10min. suddenly and then pH drop did almost occur. TOC and UV-254 continued to decrease with passed time of ozone contact. NO3--N concentration was much higher than NH4+-N and NO2--N for whole test period. Because ozone oxidized organic matters as various kinds of ion material and ion intensity of sample was extended, conductivity showed high as passed time of ozone contact. Owing to ozone oxidation of algae, color did almost disappear after ozone contact 20min.

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산화/환원 소성분위기에서 석회석 및 시멘트 원료물질의 소성거동 특성 (Calcination Properties of Cement Raw Meal and Limestone with Oxidation/Reduction Condition)

  • 문기연;최문관;조진상;조계홍
    • 자원리싸이클링
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    • 제29권5호
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    • pp.64-72
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    • 2020
  • 시멘트 산업의 질소산화물 배출량 감축을 위해 소성로에 다단연소공정을 적용할 경우, 질소산화물을 질소로 환원시키고 미연소 물질을 완전히 연소시켜 연소효율을 증대할 수 있는 산화/환원 구간이 필수적이다. 이에 본 연구에서는 시멘트 소성로 calciner에 산화/환원 구간 설정 시 최종 생산품인 시멘트 클링커의 품질안정성을 확보할 수 있는 최적 산화/환원 소성분위기를 거시적으로 관찰하고자 하였으며, 소성조건에 따른 원료물질의 질량변화, 탈탄산률, 소성완료율 등을 조사하였다. 실험결과, 대체로 환원분위기보다 산화분위기에서 원료물질의 열분해가 촉진되는 경향을 나타내며, 원료물질 자체 성분특성에 따라 비교적 CaO 함량이 높은 석회석의 열분해가 시멘트 조합원료보다 늦게 진행되는 것을 알 수 있었는데 이는 소성로 내 CO2 분압에 의한 현상으로 생각된다. 산화/환원 소성분위기에 따른 원료물질의 열분해 특성은 일반적인 석회석 열분해 온도보다 낮은 온도범위에서 비교적 큰 차이를 보였는데, 소성온도 750℃ 구간에 산화분위기 형성에 따라 원료물질의 열효율 향상을 기대할 수 있을 것으로 생각된다. 다만, 본 연구의 경우 실험실 규모의 연구로서 현장공정과는 차이가 있기 때문에, pilot plant 규모의 실검증결과가 필요한 것으로 판단된다.

상수처리에서 염소 및 오존산화를 이용한 색도제거 (Chromaticity removal by chlorine and ozone oxidation in water treatment)

  • 이정훈;김진근
    • 상하수도학회지
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    • 제31권4호
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    • pp.273-279
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    • 2017
  • Optimal processes to remove chromaticity at E water treatment plant(WTP) mainly caused by algae of E lake in Jeju island were investigated based on lab-tests of chlorine and ozone oxidation. 42.9% of chromaticity of filtered water was removed by chlorine oxidation under pH 7.0~8.0, dose of 1.0 mg/L with contact time of 30~60 min. On the other hand, chromaticity removal was 71.4% when post-ozone dose of 0.9~1.9 mg/L and pH 9.0, while it was increased to 86.7% under post-ozone dose of 3.1~7.3 mg/L and pH 9.0. However, there was no significant chromaticity removal efficiency increase when ozone doses were higher than 5.0 mg/L regardless of feeding point(i.e., pre-ozonation and post-ozonation) and pHs(i.e., 7.0 and 9.0.) under the experimental conditions. Based on the results, chlorine oxidation using existing chlorination facilities at the WTP is recommended for lower chromaticity while ozone oxidation is recommended for higher chromaticity by installing new ozone feeding facilities.

비귀금속계 금속을 이용한 일산화질소 산화 촉매 연구 (A Study of Nitric Oxide Oxidation Catalyst Using Non-noble Metals)

  • 신중훈;홍성창
    • 공업화학
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    • 제32권4호
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    • pp.385-392
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    • 2021
  • 본 연구에서는 Co/CeO2 촉매 제조 시 코발트의 첨가 함량 및 세리아의 소성온도에 따른 물리·화학적 특성 및 일산화질소 산화 성능을 비교하였다. Co/CeO2 촉매의 구조적 특성은 XRD, BET 분석을 통하여 확인하였으며, 코발트 표면밀도에 따른 표면 결정 상태를 제안하였다. 또한, Raman, XPS 분석을 통하여 촉매의 산화가 및 산소 결합 상태를 확인하였으며, 일산화질소 산화 성능과의 관계를 제안하였다. H2-TPR 분석을 통하여 촉매의 특성 변화에 따른 산소전달특성을 확인하였으며, 일산화질소 산화를 위한 촉매의 활성점(Co3+)을 제안하였다.

Effect of Steady-State Oxidation on Tensile Failure of Zircaloy Cladding

  • Kim, Taeho;Choi, Kyoung Joon;Yoo, Seung Chang;Lee, Yunju;Kim, Ji Hyun
    • 방사성폐기물학회지
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    • 제20권2호
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    • pp.161-170
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    • 2022
  • The effect of oxidation time on the characteristics and mechanical properties of spent nuclear fuel cladding was investigated using Raman spectroscopy, tube rupture test, and tensile test. As oxidation time increased, the Raman peak associated with the tetragonal zirconium oxide phase diminished and merged with the Raman peak associated with the monoclinic zirconium oxide phase near 333 cm-1. Additionally, the other tetragonal zirconium oxide phase peak at 380 cm-1 decreased after 100 d of oxidation, whereas the zirconium monoclinic oxide peak became the dominant peak. The oxidation time had no effect on the tube rupture pressure of the oxidized zirconium alloy tube. However, the yield and tensile stresses of the oxidized nuclear fuel cladding tube decreased after 100 d of oxidation. The results of the scanning electron microscopy and transmission electron microscopy were represented with the in-situ Raman analysis result for the oxide characteristics generated on the cladding of spent nuclear fuel.