• Title/Summary/Keyword: 공기화학반응

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A Study of Nitrous Oxide Decomposition using Calcium Oxide (Calcium Oxide를 이용한 N2O 분해에 관한 CO2의 영향 연구)

  • Paek, Jin-Young;Park, Yeong-Sung;Shun, Dowon;Bae, Dal-Hee
    • Korean Chemical Engineering Research
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    • v.40 no.6
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    • pp.746-751
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    • 2002
  • Fluidized bed combustion is a coal combustion technology that can reduce both SOx and NOx emission; SOx is removed by limestone that is fed into the combustion chamber and the NOx is reduced by low temperature combustion in a fluidized bed combustor and air stepping, but $N_2O$ generation is quite high. $N_2O$ is not only a greenhouse gas but also an agent of ozone destruction in the stratosphere. The calcium oxide(CaO) is known to be a catalyst of $N_2O$ decomposition. This study of $N_2O$ decomposition reaction in fixed bed reactor packed over CaO bed has been conducted. Effects of parameters such as concentration of inlet $N_2O$ gas, reaction temperature, CaO bed height and effect of $CO_2$, NO, $O_2$ gas on the decomposition reaction have been investigated. As a result of the experiment, it has been shown that $N_2O$ decomposition reaction increased with the increasing fixed bed temperature. While conversion of the reaction was decreased with increasing $CO_2$ concentration. Also, under the present of NO, the conversion of $N_2O$ decomposition is decreased. From the result of kinetic study gained the heterogeneous reaction rate on $N_2O$ decomposition. In the case of $N_2O$ decomposition over CaO, heterogeneous reaction rate is. $\frac{d[N_2O]}{dt}=\frac{3.86{\times}10^9{\exp}(-15841/R)K_{N_2O}[N_2O]}{(1+K_{N_2O}[N_2O]+K_{CO_2}[CO_2])}$. In this study, it is found that the calcium oxide is a good catalyst of $N_2O$ decomposition.

Treatment of dyeing wastewater using Moving Bed Bioractor (부유메디아 생물막 공정을 이용한 염색폐수처리)

  • Shin, Dong-Hoon;Lee, Sang-Hun;Ryu, Seung-Han;Park, Jun-Hyung;Jo, Seog-Jin
    • Proceedings of the Korean Society of Dyers and Finishers Conference
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    • 2011.03a
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    • pp.110-110
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    • 2011
  • 염색공업 폐수는 그 성분이 일반적으로 매우 복잡하며, 작업공정의 가동 사항에 따라 수질 변동이 큰것이 특징으로, 각 공정에서 배출되는 염료, 보조화학물질, PVA(Polyvinyl alchol), 전분, wax 등이 포함되어 있으며 pH가 높고, 색도로 인해 하천에 방류될 경우 확산성이 높아 미생물에 의한 자정작용을 방해하여 하천의 수중생태계를 파괴할 우려가 있다. 이러한 염색산업에서 발생하는 폐수는 일반적으로 응집침전, 부상분리법 등의 전처리한 후 활성오니공정으로 처리하는 방법이 널리 이용되고 있으나, 이들 처리공정으로는 폐수 속에 포함되어 있는 다양한화학적 구조의 색소성분 및 유해물질을 완벽하게 제거하는 것이 어려운 실정이다. 유기물 함량이 높은 염색폐수를 처리하기 위해 제안된 기술로는 산소활성슬러지법, 유동상 및 고정상 생물막법, 포괄고정화법 등이 있다. 이러한 기술들중 기존의 처리공정을 증축없이도 처리효율을 높일 수 있는 방법으로 담체를 이용한 부유메디아 생물막공정(Moving-Bed BioReactor, MBBR)이 있다. 이공정은 미생물이 부착, 성장할 수 있는 공극율과 비표면적이 큰 담체를 이용하므로 반응조내의 부유 미생물 뿐만 아니라 담체에 고농도로 부착된 부착 미생물에 의해서도 유기물을 제거하기 때문에 다른 공정들에 비해 처리효율이 뛰어나고 기존의 활성슬러지 공정에 비해 갑작스러운 부하변동 및 유독성 폐수유입에 대해서도 안정적으로 운전이 가능한 장점이 있다. 본연구에서는 부유메디아 생물반응기(Moving-Bed BioReactor, MBBR)을 이용하여 염색폐수내 $COD_{Mn}$, 색도 및 난분해성 물질인 PVA 저감에 대한 Lab-scale test 수행하였다. 실험에 사용된 염색폐수의 수질은 평균 pH 13, $COD_{Mn}$ 900 mg/L, SS 135 mg/L, 색도 1,134 [C.U.], PVA 593 mg/L였으며, 2L의 반응기를 사용하여 회분식 실험을 수행였다. 본 실험에서는 호기성 미생물에 의한 염색폐수의 생분해가 유지되는데 필요한 최적의 용존산소 농도와 이에 필요한 공기 폭기량을 결정하기 위하여 i) DO uptake rate측정과 ii) 담체의 충진율, iii) COD/N ratio, iv) Air 유량, v) 담체내 흡착제의 종류, vi) $Ca^{2+}$ 첨가가 염색폐수의 생분해에 미치는 영향을 살펴보았다. 운전시간을 7일로 하여 COD, 색도, PVA 등을 측정한 결과 담체를 첨가한 경우가 담체를 첨가하지 않은 경우 보다 제거효율이 뛰어났다. 특히 충진율 30%(C/N 3)의 경우에서 COD, 색도, PVA의 제거율이 각각 평균 65%, 70%, 60%로 가장 높은 제거효율을 나타내었다.

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Tubular Type Direct Methanol Fuel Cell for in situ NMR Diagnosis (In Situ NMR 진단용 원통형 직접 메탄올 연료전지)

  • Joh, Han-Ik;Um, Myung-Sup;Han, Kee-Sung;Han, Oc-Hee;Ha, Heung-Yong;Kim, Soo-Kil
    • Journal of the Korean Electrochemical Society
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    • v.12 no.4
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    • pp.329-334
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    • 2009
  • This study is to develop a fuel cell system applicable to an in situ NMR (Nuclear magnetic resonance) diagnosis. The in situ NMR can be used in real time monitoring of various reactions occurring in the fuel cell, such as oxidation of fuel, reduction of oxygen, transport phenomena, and component degradation. The fuel cell for this purpose is, however, to be operated in a specifically designed tubular shape toroid cavity detector (TCD), which constrains the fuel cell to have a tubular shape. This may cause difficulties in effective mass transport of reactants/products and uniform distribution of assembly pressure. Therefore, a new flow field designed in a particular way is necessary to enhance the mass transport in the tubular fuel cell. In this study, a tubular-shaped close-type flow field made of non-magnetic material is developed. With this flow field, oxygen is effectively delivered to the cathode surface and the produced water is readily removed from the membrane-electrode assembly to prevent flooding. The resulting DMFC (direct methanol fuel cell) outperforms the open-type flow field and exhibits $36\;mW/cm^2$ even at room temperature.

A Study on the Treatment of Swine Wastewater Using Titanium Dioxide Prepared by Hydrothermal Method (수열합성법으로 제조된 이산화티탄에 의한 축산폐수 처리에 관한 연구)

  • Yang, Jin-Seop;jung, Won Young;Baek, Seung Hee;Lee, Gun Dae;Park, Seong Soo;Hong, Seong-Soo
    • Applied Chemistry for Engineering
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    • v.18 no.2
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    • pp.148-154
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    • 2007
  • This study was performed to evaluate the application of $TiO_2$ on the photocatalytic treatment of swine wastewater. $TiO_2$ sol was prepared by hydrothermal method with the agent ratio($(C_2H_5)_2NH_2\;mol/Ti(OC_3H_7)_4\;mol)=1$ and R ratio ($H_2O\;mol/Ti(OC_3H_7)_4\;mol)=42$. The effect of parameter on the removal efficiency of swine wastewater in a batch type immobilized photocatalyst system such as initial pH, intensity of UV, dosage of $TiO_2$, air flow rate, and concentration of $H_2O_2$ was examined. Wastewater was effectively eliminated in the presence of both UV light illumination and $TiO_2$. Photocatalytic activity was higher in acidic condition compared to neutral and alkaline conditions. In addition, photocatalytic activity increased with increasing UV light intensity, dosage of $TiO_2$, the flow rate of air and the amount of $H_2O_2$ added as an oxidant, but the excess amount of $H_2O_2$ dosage decreased the removal efficiency.

Decolorization of Azo Dyeing Wastewater Using Underwater Dielectric Barrier Discharge Plasma (수중 유전체장벽방전 플라즈마를 이용한 아조 염색폐수 색도제거)

  • Jo, Jin Oh;Lee, Sang Baek;Mok, Young Sun
    • Applied Chemistry for Engineering
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    • v.24 no.5
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    • pp.544-550
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    • 2013
  • This work investigated the environmental application of an underwater dielectric barrier discharge plasma reactor consisting of a porous hydrophobic ceramic tube to the decolorization of an azo dyeing wastewater. The reactive species generated by the plasma are mostly short-lived, which also need to be transferred to the wastewater right after the formation. Moreover, the gas-liquid interfacial area should be as large as possible to increase the decolorization rate. The arrangement of the present wastewater treatment system capable of immediately dispersing the plasmatic gas as tiny bubbles makes it possible to effectively decolorize the dyeing wastewater alongside consuming less amount of electrical energy. The effect of discharge power, gas flow rate, dissolved anion and initial dye concentration on the decolorization was examined with dry air for the creation of plasma and amaranth as an azo dye. At a gas flow rate of $1.5Lmin^{-1}$, the good contact between the plasmatic gas and the wastewater was achieved, resulting in rapid decolorization. For an initial dye concentration of $40.2{\mu}molL^{-1}$ (volume : 0.8 L; discharge power : 3.37 W), it took about 25 min to attain a decolorization efficiency of above 99%. Besides, the decolorization rate increased with decreasing the initial dye concentration or increasing the discharge power. The presence of chlorine anion appeared to slightly enhance the decolorization rate, whereas the effect of dissolved nitrate anion was negligible.

Acidic Properties of Tungsten Oxide Supported on Zirconia and Catalytic Activities for Acid Catalysis (Zirconia에 담지된 산화텅스텐 촉매의 산 성질과 산 촉매활성)

  • Sohn, Jong Rack;Park, Man Young
    • Applied Chemistry for Engineering
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    • v.10 no.2
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    • pp.247-251
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    • 1999
  • Tungsten oxide supported on zirconia was prepared by drying powdered $Zr(OH)_4$ with ammonium metatungstate aqueous solution, followed by calcining in air at high temperature. Upon the addition of only small amount of tungsten oxide (1 wt % $WO_3$) to $ZrO_2$, both the acidity and acid strength of catalyst increased remarkably, showing the presence of $Br{\ddot{o}}nsted$ and Lewis acid sites on the surface of $WO_3$/$ZrO_2$. The high acid strength and large amount of acid sites on $WO_3$/$ZrO_2$ were due to the presence of the W=O bond nature of complex formed by the interaction between $WO_3$ and $ZrO_2$. The catalyst containing 20 wt % $WO_3$, calcined at 973 K, showed the highest catalytic activity for the 2-propanol dehydration, while the catalyst containing 15 wt % $WO_3$, calcined at 1023 K, exhibited the highest catalytic activity for the cumene dealkylation. For the 2-propanol dehydration the catalytic activities of $WO_3$/$ZrO_2$ catalysts were roughly correlated with their acidities.

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Study on Destruction of Chlorinated Organic Compounds in a Two Stage Molten Carbonate Oxidation System (2단 용융탄산염산화시스템에서 염소유기화합물 분해에 관한 연구)

  • Eun, Hee-Chul;Yang, Hee-Chul;Cho, Yung-Zun;Lee, Han-Soo
    • Korean Chemical Engineering Research
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    • v.46 no.6
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    • pp.1148-1152
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    • 2008
  • Molten carbonate oxidation (MCO) is one of the promising alternative technologies for the treatment of the chlorinated organic compounds because it is capable of trapping chlorine during a destruction of them. In this study, destructions of chlorinated organic compounds ($C_6H_5Cl$, $C_2HCl_3$ and $CCl_4$) and an insulated oil containing PCBs were performed by using the two stage molten carbonate oxidation system. MCO reactor temperature largely affected the destruction of the chlorinated organic compounds. Destruction of the chlorinated organics very efficient in the primary MCO reactor however a significant amount of CO was emitted from the MCO system. This CO emission was gradually decreased by an increase in the primary reactor temperature and oxidizing air feed rate. The HCl emission from the MCO system was below 7 ppm regardless of tested conditions. The chlorine collection efficiencies were in the range of 99.95-99.99%. The destruction of PCBs in the insulated oil was efficient at a temperature above $900^{\circ}C$ and overall destruction efficiency of them was determined as over 99.9999%.

Ammonia Conversion in the Presence of Precious Metal Catalysts (귀금속촉매하에서 암모니아의 전환반응)

  • Jang, Hyun Tae;Park, YoonKook;Ko, Yong Sig
    • Korean Chemical Engineering Research
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    • v.46 no.4
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    • pp.806-812
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    • 2008
  • The ammonia decomposition reaction has been of increasing interest as a means of treating ammonia in flue gas in the presence of precious metal catalyst. Various catalysts, $Pt-Rh/Al_2O_3$, $Pt-Rh/TiO_2$, $Pt-Rh/ZrO_2$, $Pt-Pd/Al_2O_3$, $Pd-Rh/Al_2O_3$, $Pd-Rh/TiO_2$, $Pd-Rh/ZrO_2$, $Pt-Pd-Rh/Al_2O_3$, $Pd/Ga-Al_2O_3$, $Rh/Ga-Al_2O_3$, and Ru/Ga-$Al_2O_3$, were synthesized by using excess wet impregnation method. Using a homemade 1/4" reactor at $10,000{\sim}50,000hr^{-1}$ of space velocity in the presence of precious metal catalyst ammonia decomposition reactions were carried out to investigate the catalyst activity. The inlet ammonia concentration was maintained at 2,000 ppm, with an air balance. Both $T_{50}$ and $T_{90}$, defined as the temperatures where 50% and 90% of ammonia, respectively, are converted, decreased significantly when alumina-supported catalysts were applied. In terms of catalytic performance on the ammonia conversion in the presence of hydrogen sulfide, $Pt-Rh/Al_2O_3$ catalyst showed no effect on the poisoning caused by hydrogen sulfide. These results indicate that platinum-rhodium bimetallic catalyst is a useful catalyst for ammonia decomposition.

Mammalian Reproduction and Pheromones (포유동물의 생식과 페로몬)

  • Lee, Sung-Ho
    • Development and Reproduction
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    • v.10 no.3
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    • pp.159-168
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    • 2006
  • Rodents and many other mammals have two chemosensory systems that mediate responses to pheromones, the main and accessory olfactory system, MOS and AOS, respectively. The chemosensory neurons associated with the MOS are located in the main olfactory epithelium, while those associated with the AOS are located in the vomeronasal organ(VNO). Pheromonal odorants access the lumen of the VNO via canals in the roof of the mouth, and are largely thought to be nonvolatile. The main pheromone receptor proteins consist of two superfamilies, V1Rs and V2Rs, that are structurally distinct and unrelated to the olfactory receptors expressed in the main olfactory epithelium. These two type of receptors are seven transmembrane domain G-protein coupled proteins(V1R with $G_{{\alpha}i2}$, V2R with $G_{0\;{\alpha}}$). V2Rs are co-expressed with nonclassical MHC Ib genes(M10 and other 8 M1 family proteins). Other important molecular component of VNO neuron is a TrpC2, a cation channel protein of transient receptor potential(TRP) family and thought to have a crucial role in signal transduction. There are four types of pheromones in mammalian chemical communication - primers, signalers, modulators and releasers. Responses to these chemosignals can vary substantially within and between individuals. This variability can stem from the modulating effects of steroid hormones and/or non-steroid factors such as neurotransmitters on olfactory processing. Such modulation frequently augments or facilitates the effects that prevailing social and environmental conditions have on the reproductive axis. The best example is the pregnancy block effect(Bruce effect), caused by testosterone-dependent major urinary proteins(MUPs) in male mouse urine. Intriguingly, mouse GnRH neurons receive pheromone signals from both odor and pheromone relays in the brain and may also receive common odor signals. Though it is quite controversial, recent studies reveal a complex interplay between reproduction and other functions in which GnRH neurons appear to integrate information from multiple sources and modulate a variety of brain functions.

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Enhanced Bioslurping System for Remediation of Petroleum Contaminated Soils (Enhanced Bioslurping system을 이용한 유류오염 토양의 복원)

  • Kim Dae-Eun;Seo Seung-Won;Kim Min-Kyoung;Kong Sung-Ho
    • Journal of Soil and Groundwater Environment
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    • v.10 no.2
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    • pp.35-43
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    • 2005
  • Bioslurping combines the three remedial approaches of bioventing, vacuum-enhanced free-product recovery, and soil vapor extraction. Bioslurping is less effective in tight (low-permeability) soils. The greatest limitation to air permeability is excessive soil moisture. Optimum soil moisture is very soil-specific. Too much moisture can reduce air permeability of the soil and decrease its oxygen transfer capability. Too little moisture will inhibit microbial activity. So Modified Fenton reaction as chemical treatment which can overcome the weakness of Bioslurping was experimented for simultaneous treatment. Although the diesel removal efficiency of SVE process increased in proportion to applied vacuum pressure, SVE process was difficulty to remediation quickly semi- or non-volatile compounds absorbed soil strongly. And SVE process had variation of efficiency with distance from the extraction well and depth a air flow form of hemisphere centering around the well. Below 0.1 % hydrogen peroxide shows the potential of using hydrogen peroxide as oxygen source but the co-oxidation of chemical and biological treatment was impossible because of the low efficiency of Modified Fenton reaction at 0.1 % (wt) hydrogen peroxide. NTA was more efficiency than EDTA as chelating agent and diesel removal efficiency of Modified Fenton reaction increased in proportion to hydrogen peroxide concentration. Hexadecane as typical aliphatic compound was removed less than Toluene as aromatic compound because of its structural stability in Modified Fenton reaction. What minimum 10% hydrogen peroxide concentration has good remediation efficiency of diesel contaminated groundwater may show the potential use of Modified Fenton reaction after bioslurping treatment.