• 제목/요약/키워드: NHCs

검색결과 6건 처리시간 0.019초

9성분계 모델 콜타르 흡수유 중에 함유된 질소고리화합물의 메탄올 추출 (Methanol Extraction of Nitrogen Heterocyclic Compound Contained in Model Coal Tar Fraction of Nine Components System)

  • 김수진;강호철
    • 공업화학
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    • 제25권2호
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    • pp.142-146
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    • 2014
  • 9성분계 모델 콜타르 유분 중에 함유된 질소고리화합물(NHC)의 분리를 분배평형에 의해 검토했다. 원료로서는 NHC group (NHCs; quinoline (Q), iso-quinoline (iQ), indole (In), quinaldine(Qu)), 2환 방향족 화합물 group (BACs; 1-methylnaphthalene (1MN), 2-methylnaphthalene (2MN), dimethylnaphthalene (DMN)), biphenyl (Bp)과 phenyl ether (Pe)로 제조한 모델 콜타르 유분을, 용매로서는 메탄올 수용액을 각각 사용했다. 액-액 접촉 장치로서는 회분 교반기를 각각 사용했다. 평형조작 온도가 상승함에 따라 NHCs의 분배계수는 증가했으나, 역으로 BACs를 기준한 NHCs의 선택도는 감소했다. 초기 물/용매의 체적비가 감소함에 따라 BACs를 기준한 NHCs의 선택도는 급격히 감소했으나, NHCs의 분배계수는 증가했다. 일정 조건하에서, 각 group별 분배계수와 BACs를 선택도의 순서는 NHCs > Bp > BACs > Pe와 NHCs > Bp > Pe를 각각 나타냈다. 또한 전체 성분에 대한 분배계수의 순서는 In > iQ = Q > Qu > Bp > 1MN = 2MN > Pe > DMN을 나타냈다. 메탄올 추출에 의해 얻어진 NHCs의 최대 수율과 BACs를 기준한 NHCs의 최대 선택도는 각각 94%, 23이었다. 본 연구를 통해 얻어진 실험적 결과를 이용하여 콜타르 중에 함유된 NHCs의 회수공정을 검토했다.

수계중 이환형 질소고리화합물(NHCs)의 초음파적 분해 (Sonolytical Decomposition of NHCs in Aqueous Solution)

  • 유영억;야스아키 마에다
    • 한국환경과학회지
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    • 제16권4호
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    • pp.393-397
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    • 2007
  • The sonolytic decomposition of NHCs(Nitrogen Heterocyclic Compounds), such as atrazine[6-chloro-N-ethyl-N'-(1-methylethyl)-1,3,5-triazine-2,4-diamine], simazine(6-chloro-N,N'-diethyl-1,3,5-triazine-2,4-diamine), trietazine(6-chloro-N,N,N'-triethyl-1,3, 5-triazine-2,4-diamine), in water was investigated at a ultrasound frequency of 200kHz with an acoustic intensity of 200W under argon and air atmospheres. The concentration of NHCs decreased with irradiation, indicating pseudo-first-order kinetics. The rates were in the range $1.06{\sim}2.07({\times}10^{-2}min^{-1})$ under air and $1.30{\sim}2.59({\times}10^{-2}min^{-1})$ under argon at a concentration of $200{\mu}M$ of NHCs. The rate of hydroxyl radicals(${\bullet}{OH}$) formation from water is $19.8{\mu}M\;min^{-1}$ under argon and $14.7{\mu}M\;min^{-1}$ under air in the same sonolysis conditions. The sonolysis of NHCs is effectively inhibited, but not completely, by the addition of t-BuOH(2-methyl-2-propanol), which is known to be an efficient ${\bullet}{OH}$ radical scavenger in aqueous sonolysis. This suggests that the main decomposition of NHCs proceeds via reaction with ${\bullet}{OH}$ radical; a thermal reaction also occurs, although its contribution is small. The addition of appropriate amounts of Fenton's reagent $[Fe^{2+}]$ accelerates the decomposition. This is probably due to the regeneration of ${\bullet}{OH}$ radicals from hydrogen peroxide, which would be formed from recombination of ${\bullet}{OH}$ radicals and which may contribute a little to the decomposition.

모델 콜타르 유분 중에 함유된 질소고리화합물의 추출에 관한 메탄올과 포름아마이드의 비교 (Comparison of Methanol with Formamide on Extraction of Nitrogen Heterocyclic Compounds Contained in Model Coal Tar Fraction)

  • 김수진
    • 공업화학
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    • 제26권2호
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    • pp.234-238
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    • 2015
  • 모델 콜타르 유분 중에 함유된 질소고리화합물(NHC)의 분리를 메탄올과 포름아마이드 추출에 의해 비교했다. 원료로서는 4종류의 NHC (NHCs : 퀴놀린, 이소퀴놀린, 인돌, 퀴날딘), 3종류의 2환 방향족 화합물(BACs : 1-메틸나프탈렌, 2-메틸나프탈렌, 디메틸나프탈렌), 비페닐과 페닐에테르로 제조한 모델 콜타르 유분을 사용했다. 용매로서는 메탄올과 포름아마이드 수용액을 사용했다. 원료와 용매의 접촉 장치로서는 회분 교반기를 사용했다. 사용한 용매와 무관하게, 초기 용매 함수율의 감소와 평형조작 온도의 상승은 NHCs의 분배계수를 급격히 증가시켰으나, 역으로 BACs를 기준한 NHCs의 선택도를 감소시켰다. 초기 용매/원료의 체적비가 감소함에 따라 NHCs의 분배계수는 감소했으나, BACs를 기준한 NHCs의 선택도는 거의 일정했다. 동일한 실험조건에서, NHCs의 분배계수는 메탄올 추출이 포름아마이드 추출에 비해 약 3~5배 높았으나, BACs를 기준한 NHCs의 선택도는 역으로 포름아마이드 추출이 메탄올 추출에 비해 3~7배 높았다. 또한, NHCs의 용해력과 선택도의 밸런스에 NHCs의 추출처리속도를 부가하여 두 용매 추출법을 비교했다.

Decomposition of Nitogen Heterocyclic Compounds(NHCs) in Aqueous Solution by Sonication

  • Yoo, Young-Eok;Maeda, Yasuaki
    • 한국환경과학회:학술대회논문집
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    • 한국환경과학회 2003년도 International Symposium on Clean Environment
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    • pp.171-176
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    • 2003
  • The sonolytic decomposition of NHCs, such as atrazine[6-chloro-N-ethyl-N' -(1-methylethyl)-1,3,5-triazine-2,4-diamine], simazine( 6-chloro-N,N' -diethyl-l ,3,5-triazine-2,4-diamine), trietazine(6-chloro-N,N,N'-triethyl-l,3,5-triazine-2,4-diamine), in water was investigated at a ultrasound frequency of 200kHz with an acoustic intensity of 200W under argon and air atmospheres. The concentration of NHCs decreased with irradiation, indicating pseudo-first-order kinetics. The rates were in the range 1.06∼2.07 (x10/sup -3/ min/sup -1/) under air and 1.30∼2.59(x10/sup -3/ min/sup -1/)under argon at a concentration of 200μM of NHCs. The rate of hydroxyl radicals(·OH) formation from water is 19.8μM min/sup -1/ under argon and 14.7 μM min/sup -1/ under air in the same sonolysis conditions. The sonolysis of NHCs is effectively inhibited, but not completely, by the addition of t-BuOH(2-methyl-2-propanol), which is known to be an efficient ·OH radical scavenger in aqueous sonolysis. This suggests that the main decomposition of NHCs proceeds via reaction with ·OH radical; a thermal reaction also occurs, although its contribution is small. The addition of appropriate amounts of Fenton's reagent [Fe/sup 2+/] accelerates the decomposition. This is probably due to the regeneration of ·OH radicals from hydrogen peroxide, which would be formed from recombination of ·OH radicals and which may contribute a little to the decomposition.

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Simultaneous degradation of nitrogenous heterocyclic compounds by catalytic wet-peroxidation process using box-behnken design

  • Gosu, Vijayalakshmi;Arora, Shivali;Subbaramaiah, Verraboina
    • Environmental Engineering Research
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    • 제25권4호
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    • pp.488-497
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    • 2020
  • The present study investigates the feasibility of nitrogenous heterocyclic compounds (NHCs) (Pyridine-Quinoline) degradation by catalytic wet peroxidation (CWPO) in the presence of nanoscale zerovalent iron supported on granular activated carbon (nFe0/GAC) using statistical optimization technique. Response surface methodology (RSM) in combination with Box-Behnken design (BBD) was used to optimize the process parameters of CWPO process such as initial pH, catalyst dose, hydrogen peroxide dose, initial concentration of pyridine (Py) and quinolone (Qn) were chosen as the main variables, and total organic carbon (TOC) removal and total Fe leaching were selected as the investigated response. The optimization of process parameters by desirability function showed the ~85% of TOC removal with process condition of initial solution pH 3.5, catalyst dose of 0.55 g/L, hydrogen peroxide concentration of 0.34 mmol, initial concentration of Py 200 mg/L and initial concentration of Qn 200 mg/L. Further, for TOC removal the analysis of variance results of the RSM revealed that all parameter i.e. initial pH, catalyst dose, hydrogen peroxide dose, initial concentration of Py and initial concentration of Qn were highly significant according to the p values (p < 0.05). The quadratic model was found to be the best fit for experimental data. The present study revealed that BBD was reliable and effective for the determination of the optimum conditions for CWPO of NHCs (Py-Qn).