• 제목/요약/키워드: Catalytic wet oxidation

검색결과 39건 처리시간 0.049초

촉매습식산화에 의한 Ethylene Glycol의 분해 (Decomposition of Ethylene Glycol by Catalytic Wet Air Oxidation)

  • 안상준;최장승;이동근
    • 한국염색가공학회지
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    • 제13권4호
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    • pp.264-271
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    • 2001
  • Catalytic wet oxidation of ethylene glycol as refractory compound was studied in a batch slurry reactor using lwt% $Pt/A1_2O_3$, lwt% $Pt/TiO_2,\;Mn/CeO_2$(1:1) and 5wt% $Mn/Al_2O_3$. Experiments were conducted to investigate theeffects of temperature, initial ethylene glycol concentration, catalyst dosage and PH on the ethylene glycol decomposition. When compared with the uncatalyzed reaction, the use of catalysts could increase the rate of ethylene glycol decomposition. The lwt% $Pt/A1_2O_3$ catalyst was preferable to the other catalysts for the destructive oxidation of ethylene glycol. The reaction rate was first order with respect to initial concentration of ethylene glycol. In acidic condition the removal efficiency of ethylene glycol was good, but there was a significant leaching of platinum. Small amount of acetic acid, oxalic acid, masonic acid and formic acid as intermediates were detected during catalytic wet air oxidation of ethylene glycol.

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고농도 페놀 폐수의 습식산화와 호기성 생물학적 통합처리 (Integrated Wet Oxidation and Aerobic Biological Treatment of the Wastewater Containing High Concentration of Phenol)

  • 최호준;이승호;유용호;윤왕래;서일순
    • KSBB Journal
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    • 제22권4호
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    • pp.244-248
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    • 2007
  • 고농도 페놀폐수 전처리 습식산화공정의 반응온도, 초기 pH 및 균일촉매 ($CuSO_4$) 등이 후처리 호기성 생물학적 공정에 미치는 영향을 조사하였다. 습식산화에서의 높은 반응온도와 산성 초기조건이 후처리 생물학적 산화공정에서 높은 산화속도와 최종 COD 제거율을 유발하였다. 습식산화에서 균일촉매를 사용하면 전처리 습식산화반응은 낮은 반응온도에서도 높은 COD 제거속도를 보였으나, 후처리 생물학적 산화공정에서는 낮은 최종 COD 제거율을 나타내었다.

SBA-15 Supported Fe, Ni, Fe-Ni Bimetallic Catalysts for Wet Oxidation of Bisphenol-A

  • Mayani, Suranjana V.;Mayani, Vishal J.;Kim, Sang Wook
    • Bulletin of the Korean Chemical Society
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    • 제35권12호
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    • pp.3535-3541
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    • 2014
  • Bisphenol A is considered as pollutant, because it is toxic and hazardous to living organisms even at very low concentrations. Biological oxidation used for removing this organic from waste water is not suitable and consequently application of catalytic wet oxidation has been considered as one of the best options for treating bisphenol A. We have developed Fe/SBA-15, Ni/SBA-15 and Fe-Ni/SBA-15 as heterogeneous catalysts using the advanced impregnation method for oxidation of bisphenol A in water. The catalysts were characterized with physico-chemical characterization methods such as, powder X-ray diffraction (PXRD), FT-IR measurements, N2 adsorption-desorption isotherm, thermo-gravimetric analysis (TGA), scanning electron microscopy (SEM), transmission electron microscopy (TEM) and inductively coupled plasma optical emission spectroscopy (ICP-OES) analysis. This work illustrates activity of the catalysts for heterogeneous catalytic degradation reaction revealed with excellent conversion and recyclability. The degradation products identified were not persistent pollutants. GC-MS analysis identified the products: 2,4-hexadienedioic acid, 2,4-pentadienic acid and isopropanol or acetic acid. The leachability study indicated that the catalysts release very little metals to water. Therefore, the possibility of water contamination through metal leaching was almost negligible.

An Effective Process for Removing Organic Compounds from Oily Sludge

  • Jing, Guolin;Luan, Mingming;Chen, Tingting;Han, Chunjie
    • 대한화학회지
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    • 제55권5호
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    • pp.842-845
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    • 2011
  • Wet air oxidation (WAO) of oily sludge was carried out using $Fe^{3+}$ as catalyst, placed in a 0.5 L batch autoclave in the temperature range of $250-330^{\circ}C$. Experiments were conducted to investigate the effects of temperature, the initial COD, reaction time, concentration of catalyst and $O_2$ excess (OE) on the oxidation of the oily sludge. The results showed that in the WAO 88.4% COD was achieved after 9 min reaction at temperature of $330^{\circ}C$, OE of 0.8 and the initial COD of 20000 mg/L. Temperature was found to have a significant impact on the oxidation of oily sludge. Adding a catalyst significantly improved the COD removal. Homogenous catalyst, $Fe^{3+}$, showed effective removal for pollutants. COD removal was 99.7% in the catalytic wet air oxidation (CWAO) over $Fe^{3+}$ catalyst. The results proved that the CWAO was an effective pretreatment method for the oily sludge.

퀴놀린 폐수의 습식산화와 호기성 생물학적 통합처리 (Integrated Wet Oxidation and Aerobic Biological Treatment of the Quinoline Wastewater)

  • 권순석;문해미;이용학;유용호;윤왕래;서일순
    • KSBB Journal
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    • 제23권3호
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    • pp.245-250
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    • 2008
  • 퀴놀린은 생물학적으로 거의 산화 분해되지 않았으나, 250$^{\circ}C$ 습식산화에서 니코틴산과 초산 등으로 산화 분해되었다. 퀴놀린 습식산화는 균일촉매 $CuSO_4$ 또는 쉽게 습식산화 분해되는 페놀에 의해 반응조건이 완화되었다. 퀴놀린 습식산화 반응의 주 생성물 중 하나인 니코틴산은 호기성 Bacillus 종균에 의해 산화 분해되었다. 촉매를 사용하지 않은 고온에서의 퀴놀린 습식산화 생성물의 생물학적 산화는 저온에서 진행된 균일 촉매 ($CuSO_4$) 습식산화와 퀴놀린-페놀 혼합용액 습식산화 반응 생성물의 생물학적 산화에 비하여 늦게 진행되었다. 반면에, 호기성 균주의 습식산화 생성물에의 적응은 생물학적 처리에서의 니코틴산 산화 분해 반응의 지체기를 크게 단축시켰다.

Carbon bead-supported copper-dispersed carbon nanofibers: An efficient catalyst for wet air oxidation of industrial wastewater in a recycle flow reactor

  • Yadav, Ashish;Verma, Nishith
    • Journal of Industrial and Engineering Chemistry
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    • 제67권
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    • pp.448-460
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    • 2018
  • Copper nanoparticle-doped and graphitic carbon nanofibers-covered porous carbon beads were used as an efficient catalyst for treating synthetic phenolic water by catalytic wet air oxidation (CWAO) in a packed bed reactor over 10-30 bar and $180-230^{\circ}C$, with air and water flowing co-currently. A mathematical model based on reaction kinetics assuming degradation in both heterogeneous and homogeneous phases was developed to predict reduction in chemical oxygen demand (COD) under a continuous operation with recycle. The catalyst and process also showed complete COD reduction (>99%) without leaching of Cu against a high COD (~120,000 mg/L) containing industrial wastewater.

Treatment of Oily Wastewater with WPO and CWO

  • Han, Mei;Chen, Yihui;He, Fang;Yu, Li
    • 대한화학회지
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    • 제58권1호
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    • pp.68-71
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    • 2014
  • Petroleum refining unavoidably generates large volumes of oily wastewater. The environmentally acceptable disposal of oily wastewater is a current challenge to the petroleum industry. Nowadays, more attentions have been focused on the treatment techniques of oily wastewater. Oily wastewater contained highly concentrated and toxic organic compounds. Wet peroxide oxidation (WPO) and catalytic wet oxidation (CWO) were applied to eliminate pollutants to examine the feasibility of the WPO/CWO of oily wastewater. The results indicated that more than 80% chemical oxygen demand (COD) removal from oily wastewater was achieved with CWO. Homogenous catalyst, $NaHCO_3$ and $Na_2CO_3$ and NaOH showed effective removal for pollutants in oily wastewater. Greater than 90% COD removal was achieved with WPO. It was concluded that WPO was a far more effective process for oily wastewater.

촉매 습식산화에 의한 반응성 염료 분해(2) (Decomposition of Reactive Dyes by Catalytic Wet Air Oxidation Process(2))

  • 최장승;우성훈;박승조
    • 대한환경공학회지
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    • 제22권11호
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    • pp.2077-2083
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    • 2000
  • 산업 현장에서 많이 사용되고 있는 반응성 염료인 remazol $black_5$를 연구 대상물로 선택하여 촉매습식 산화공법으로 처리하였다. 이때 반응성 염료성분의 분해효율, 촉매 첨가량 및 반응온도와 상호 관련하여 검토한 결과를 정리하였다. 이산화티탄 담체에 백금을 5.0wt% 담지한 촉매 1.5g/L, 6기압, $200^{\circ}C$ 이상에서 remazol $black_5$는 약 95% 이상 분해되었다. 반응온도 $250^{\circ}C$에서 240분 촉매산화를 하였을 때 uv 흡광 잔존율은 4%이고 반응온도가 $250^{\circ}C$, 120분 경과 후 색도 제거율은 약 95% 이상이었다.

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아조염료 Reactive Black 5 폐수의 촉매습식산화 (Catalytic Wet Oxidation of Azo Dye Reactive Black 5)

  • 서일순;유신석;고미소;정사무엘;정철구;홍정아;윤왕래
    • Korean Chemical Engineering Research
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    • 제48권2호
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    • pp.259-267
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    • 2010
  • 불균일 촉매 CuO를 이용한 반응성 아조계 염료 Reactive Black 5(RB5) 폐수의 촉매습식산화에서 반응온도($190{\sim}230^{\circ}C$) 및 촉매농도(0.00~0.20 g/l)가 폐수의 색도 및 총 유기탄소 TOC 제거에 미치는 영향을 조사하였다. 폐수의 색도는 분광광도계를 사용하여 측정하였고, 습식산화속도는 TOC를 이용하여 산출하였다. 열분해 조건($230^{\circ}C$, 120 min)에서 폐수의 색도는 약 90%까지 제거되었지만 TOC는 제거되지 않았다. RB5 폐수 촉매 습식산화에서의 폐수의 색도 및 TOC 제거속도는 반응온도 및 촉매농도를 증가시킴에 따라 증가하였다. 촉매의 영향은 0.01 g CuO/l에서 이미 상당히 크게 나타났으며 0.05 g CuO/l 이상에서의 촉매농도 증가에 따른 효과는 작았다. 폐수 색도의 초기변화는 색도에 대한 1차 반응속도론으로 나타낼 수 있었으며, TOC 변화는 폐수 TOC를 쉽게 산화되는 TOC와 난분해성 TOC 로 구분한 global 모델로 묘사할 수 있었다. 반응온도의 폐수 색도 및 TOC 제거속도에 미치는 영향은 Arrhenius 상관관계식으로 묘사할 수 있었다. RB5 폐수의 열분해, 습식산화 및 0.20 g CuO/l의 촉매농도를 사용한 촉매습식산화 조건에서의 색도 제거반응의 활성화에너지는 각각 108.4, 78.3 및 74.1 kJ/mol의 값을 나타내었다. RB5 폐수 촉매습식산화에서의 TOC 제거반응에서 산화 최종산물로의 전환에 대한 난분해성 중간산물로의 전환 비는 페놀 습식산화에 비하여 상대적으로 높았다.