• 제목/요약/키워드: Reactor stability

검색결과 342건 처리시간 0.026초

Optimizing and Modeling Brightness Development in Peroxide Bleaching of Thermomechanical Pulp

  • Yoon, Byung-Ho;Wang, Li-Jun;Park, Soo-Kyoung;Kim, Dong-Yoon
    • 한국펄프종이공학회:학술대회논문집
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    • 한국펄프종이공학회 1999년도 추계학술발표논문집
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    • pp.180-186
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    • 1999
  • Alkaline peroxide bleaching of (chemi) mechanical pulp is a very complicated system where various process factors affect the bleaching performance and pulp properties. Traditional on-factor-at a time method is ineffective and costly in finding the optimal bleaching conditions. In this study statistical experimental methods which include three steps. I. e. screening, response surface modeling and optimization, were used to find the conditions for maximal brightness development during one stage alkaline peroxide bleaching of TMP which had an initial brightness of 54.5% Elerpho. The TMP was pretreated with EDTA(0.5% on O. D. pulp. consistency, $30^{\circ}C$ for 60 minutes) and bleached in a 2L Mark V Quantum Reactor at 750rpm, 7.5% of bleaching consistency and with 0.05% magnesium sulfate addition. The ranges of other factors studied were 1~5% hydrogen peroxide on O. D plup, 1~4% sodium hydroxide on O. D pulp and 1~4% sodium silicate on O. D pulp, reaction temperature 50~$90^{\circ}C$ and reaction time 40~180minutes. A models with good predictability was established and the maximal brightness after one stage bleaching was found to be 70% Elerpho at $50^{\circ}C$, 50 minutes 5% hydrogen peroxide on O. D. pulp 3.2~3.4% sodium hydroxide on O. D. pulp 3.2~3.4% sodium hydroxide on O. D pulp and 4% silicate on O. D pulp. However further studies on other pulp properties such as strength and brightness stability shall be carried out in order to find out the optimal bleaching conditions.

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Characterization of Crop Residue-Derived Biochars Produced by Field Scale Biomass Pyrolyzer

  • Jung, Won-K.
    • 한국토양비료학회지
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    • 제44권1호
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    • pp.1-7
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    • 2011
  • Application of biochar to soils is proposed as a significant, long-term, sink for atmospheric carbon dioxide in terrestrial ecosystems. In addition to reducing emissions and increasing the sequestration of carbon, production of biochar and its application to soils will contribute improve soil quality and crop productivity. Objectives were i) to evaluate biochar productivity from crop residues using a low-cost field scale mobile pyrolyzer and ii) to evaluate characteristics of feedstocks and biochars from locally collected crop residues. Pyrolysis experiments were performed in a reactor operated at $400-500^{\circ}C$ for 3-4 hours using biomass samples of post-harvest residues of corn (Zea mays L.), cotton (Gossypium spp.), rice (Oryza sativa L.), sorghum (Sorghum bicolor L.) and wheat (Triticum aestivum L.). Feedstocks differed, but average conversion to biochar was 23%. Carbon content of biomass feedstock and biochar samples were 445 g $kg^{-1}$ and 597 g $kg^{-1}$, respectively. Total carbon content of biochar samples was 34% higher than its feedstock samples. Significant increases were found in P, K, Ca, Mg, and micro-nutrients contents between feedstock and biochar samples. Biochar from corn stems and rice hulls can sequester by 60% and 49% of the initial carbon input into biochar respectively when biochar is incorporated into the soils. Pyrolysis conversion of corn and rice residues sequestered significant amounts of carbon as biochar which has further environmental and production benefits when applied to soils. Field experiment with crop residue biochar will be investigated the stability of biochars to show long-term carbon sequestration and environmental influences to the cropping systems.

Production of Hydrogen and Carbon Nanotubes from Catalytic Decomposition of Methane over Ni:Cu/Alumina Modified Supported Catalysts

  • Hussain, Tajammul;Mazhar, Mohammed;Iqbal, Sarwat;Gul, Sheraz;Hussain, Muzammil;Larachi, Faical
    • Bulletin of the Korean Chemical Society
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    • 제28권7호
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    • pp.1119-1126
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    • 2007
  • Hydrogen gas and carbon nanotubes along with nanocarbon were produced from commercial natural gas using fixed bed catalyst reactor system. The maximum amount of carbon (491 g/g of catalyst) formation was achieved on 25% Ni, 3% Cu supported catalyst without formation of CO/CO2. Pure carbon nanotubes with length of 308 nm having balloon and horn type shapes were also formed at 673 K. Three sets of catalysts were prepared by varying the concentration of Ni in the first set, Cu concentration in the second set and doping with K in the third set to investigate the effect on stabilization of the catalyst and production of carbon nanotubes and hydrogen by copper and potassium doping. Particle size analysis revealed that most of the catalyst particles are in the range of 20-35 nm. All the catalysts were characterized using powder XRD, SEM/EDX, TPR, CHN, BET and CO-chemisorption. These studies indicate that surface geometry is modified electronically with the formation of different Ni, Cu and K phases, consequently, increasing the surface reactivity of the catalyst and in turn the Carbon nanotubes/H2 production. The addition of Cu and K enhances the catalyst dispersion with the increase in Ni loadings and maximum dispersion is achieved on 25% Ni: 3% Cu/Al catalyst. Clearly, the effect of particle size coupled with specific surface geometry on the production of hydrogen gas and carbon nanotubes prevails. Addition of K increases the catalyst stability with decrease in carbon formation, due to its interaction with Cu and Ni, masking Ni and Ni:Cu active sites.

삼중수소 저장용기 이종용접부의 수소취화 거동 평가 (II) (Evaluations of Hydrogen Embrittlement Behaviours on Dissimilar Welding Part of SDS Bottles (II))

  • 조경원;최재하;장민혁;이영상;홍태환
    • 한국수소및신에너지학회논문집
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    • 제26권2호
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    • pp.120-126
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    • 2015
  • Recently, the ever-increasing use of fossil fuels for rapid industrial development and population significantly caused an environment pollution and global warming such as climate change. So research and development of sustainable and eco-friendly energy have been performed. Especially the interest in nuclear fusion fuel was significantly increased from the developed countries. The system of fusion energy production was tritium separation, storage and delivery, and purification. Republic of Korea is in charge of Storage and Delivery System (SDS) in the International Thermonuclear Experimental Reactor (ITER). Welding part of the SDS bottles for storing the tritium is known to be susceptible to hydrogen embrittlement. In this study, conducted a study for the relaxation of the stability and hydrogen embrittlement of the weld area. The hydrogen heat treatment was processed through the Pressure-Composition-Temperature (PCT) device according to the time variation. Also mechanical properties such as impact test and hardness test according to using the alkaline cleaning liquid for hydrogen embrittlement relief and the fracture was observed by scanning electron microscopy (SEM) after the mechanical properties evaluation.

키토산올리고당 생산을 위한 다단계 첨가방법 (Stepwise Addition Technology for the High Yield Production of Chitosanoligosaccharide)

  • 이기선;김승모;임현수
    • KSBB Journal
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    • 제14권6호
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    • pp.639-642
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    • 1999
  • 키토산 올리고당을 보다 효율적으로 생산하고자 효소와 기질간의 특성을 조사한 다음, 이를 바탕으로 기질을 단계별로 첨가하여 생산 효율을 높일 수 있었다. 본 실험에 사용된 효소의 안정성을 조사한 결과 pH 5.0에서 6일 후에도 약 90% 이상의 효소활성을 유지하였다. 기질이 초기 농도에 따른 겉보기 수율은 0.5~2% 키토산 용액은 약 90% 이상이었으며, 그이상의 농도일 경우 감소하였다. 그래서, 수율을 증가시키기 위해 초기 반응 속도 및 겉보기 수율이 높은 기실 농도에 기질을 단계 별로 첨가한 결과, 분해 반응에 있어 겉보기 수율은 64.6%에서 83.2%로 증가하였고, 이에 따라 키토산 올리고당의 생산량은 10.52 mg/mL에서 12.26 mg/mL로 증가하였다. TLC분석 결과 Batch type과 기질을 단계별로 첨가하였을 경우의 올리고당 조성은 주로 3-5당이었다. 키토산 올리고당 생산을 위한 최적의 반응 조건은 pH 5.0, 40$^{\circ}C$에서 초기 반응 속도 및 수율이 높은 기질 농도인 2% 키토산 용액에 기질을 3시간마다 첨가할 때였다. 반응 시간에 따른 기질의 양과 효소를 보다 더 최적화하여 키토산 올리고당의 최종 농도와 겉보기 수율을 증가시킬 수 있었다.

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Ni/γ-Al2O3 촉매상에서 이산화탄소에 의한 프로판의 개질 (Reforming of Propane by Carbon Dioxide using Ni/γ-A12O3 Catalysts)

  • 김경훈;김종화;장성진;박대원
    • 공업화학
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    • 제8권3호
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    • pp.382-388
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    • 1997
  • 본 연구는 펄스 반응기 및 고정층 연속반응기를 사용하여 ${\gamma}$-알루미나에 담지된 니켈촉매상에서 이산화탄소에 의한 프로판의 개질반응 특성을 고찰한 것이다 Ni/${\gamma}$-$A1_2O_3$촉매가 NiO/${\gamma}$-$A1_2O_3$촉매보다 $CO_2$의 해리능력과 프로판의 개질 능력이 우수한 것으로 나타났다. 프로판과 $CO_2$의 혼합물에 산소를 추가한 결과 프로판의 전환율이 증가하였고 표면의 탄소침적도 감소함을 알 수 있었다. Ni/${\gamma}$-$A1_2O_3$$Ga_2O_3$의 기계적 혼합 촉매는 Ni/${\gamma}$-$A1_2O_3$자체보다 촉매의 활성이 오래 유지되었고 두 상의 협동에 의한 상승효과(synergistic effect)가 관찰되었다.

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Synthesis of Magnetic Sonophotocatalyst and its Enhanced Biodegradability of Organophosphate Pesticide

  • Lirong, Meng;Jianjun, Shi;Ming, Zhao;Jie, He
    • Bulletin of the Korean Chemical Society
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    • 제35권12호
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    • pp.3521-3526
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    • 2014
  • A magnetic sonophotocatalyst $Fe_3O_4@SiO_2@TiO_2$ is synthesized for the enhanced biodegradability of organophosphate pesticide. The as-prepared catalysts were characterized using different techniques, such as X-ray diffraction (XRD) and transmission electron microscopy (TEM). The radial sonophotocatalytic activity of $Fe_3O_4@SiO_2@TiO_2$ nanocomposite was investigated, in which commercial dichlorvos (DDVP) was chosen as an object. The degradation efficiency was evaluated in terms of chemical oxygen demand (COD) and enhancement of biodegradability. The effect of different factors, such as reaction time, pH, the added amount of catalyst on $COD_{Cr}$ removal efficiency were investigated. The average $COD_{Cr}$ removal efficiency reached 63.13% after 240 min in 12 L sonophotocatalytic reactor (catalyst $0.2gL^{-1}$, pH 7.3). The synergistic effect occurs in the combined sonolysis and photocatalysis which is proved by the significant improvement in $COD_{Cr}$ removal efficiency compared with that of solo photocatalysis. Under this experimental condition, the $BOD_5/COD_{Cr}$ ratio rose from 0.131 to 0.411, showing a remarkable improvement in biodegradability. These results showed that sonophotocatalysis may be applied as pre-treatment of pesticide wastewater, and then for biological treatment. The synthesized magnetic nanocomposite had good photocatalytic performance and stability, as when it was used for the fifth time, the $COD_{Cr}$ removal efficiency was still about 62.38%.

단기 수리학적 충격부하시 침전지 내장형 상분리 산화구공정의 처리 안정성 평가 (Stability Evaluation of Phased Isolation Intra-Clarifier Ditch Process on Short-Term Hydraulic Shock Loading)

  • 홍기호;장덕
    • 상하수도학회지
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    • 제19권6호
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    • pp.791-799
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    • 2005
  • The phased isolation intra-clarifier ditch system used in this study is a simplified novel process enhancing simultaneous removal of biological nitrogen and phosphorus in municipal wastewater in terms of elimination of additional pre-anaerobic reactor, external clarifier, recycle of sludge, and nitrified effluent recirculation by employing intrachannel clarifier. Laboratory-scale phased isolation ditch system was used to assess the treatability on municipal wastewater. When the system was operated at the HRTs of 6~12hours, SRTs of 9~31days, and cycle times of 2~8hours, the system showed removals of BOD, TN, and TP as high as 88~97%, 70~84%, and 65~90%, respectively. The rainfall in Korea is generally concentrated in summer because of site-specific characteristics. Especially, the wet season has set in on June to August. In combined sewers, seasonal variations are primarily a function of the amount of stormwater that enters the system. In order to investigate the effect of hydraulic shock loading on system performance, the laboratory-scale system was operated at an HRT of 6hours (two times of influent flowrate) during two cycles (8hours). The system performance slightly decreased by increasing of influent flowrate and decreasing of system HRT. Nitrification efficiency and TN removal were slightly decreased by increasing of influent flowrate (decreasing of system HRT), whereas, the denitrification was not affected by hydraulic shock loading. However, the higher system performance could be achieved again after four cycles. Thus, the phased isolation technology for enhanced biological nutrient removal in medium- and small-scale wastewater treatment plants suffering fluctuation of influent quality and flowrate.

YSZ 첨가 페라이트 매체상에서 메탄으로부터 합성 가스 및 수소의 단계적 생산 (Stepwise Production of Syngas and Hydrogen from Methane on Ferrite Based Media Added with YSZ)

  • 제한솔;차광서;김홍순;이영석;박주식;김영호
    • 한국수소및신에너지학회논문집
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    • 제21권1호
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    • pp.50-57
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    • 2010
  • Stepwise production of syn-gas and hydrogen from methane on ferrite based media added with yttria-stabilized zirconia (YSZ) was carried out using a fixed bed infrared reactor. In this study, all M-ferrite (M=Co, Cu, Mn and Ni) media were prepared by co-precipitation method, and there the YSZ was added as a binder to improve thermal stability, reactivity, and resistance against carbon deposition. Most of the ferrite media containing YSZ showed the good redox property for temperature programmed reduction/oxidation (TPR/O) tests. Notably, the Cu-substituted ferrite medium with YSZ showed the great resistance against carbon deposition as well as the good reactivity for the stepwise production of syngas and hydrogen. Furthermore, it also showed the good durability without significant deactivation during five repeated cyclic tests.

The Operation of Polymer Electrolyte Membrane Fuel Cell using Hydrogen Produced from the Combined Methanol Reforming Process

  • Park, Sang Sun;Jeon, Yukwon;Park, Jong-Man;Kim, Hyeseon;Choi, Sung Won;Kim, Hasuck;Shul, Yong-Gun
    • Journal of Electrochemical Science and Technology
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    • 제7권2호
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    • pp.146-152
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    • 2016
  • A combined system with PEMFC and reformer is introduced and optimized for the real use of this kind of system in the future. The hydrogen source to operate the PEMFC system is methanol, which needs two parts of methanol reforming reaction and preferential oxidation (PROX) for the hydrogen fuel process in the combined operation PEMFC system. With the optimized methanol steam reforming condition, we tested PROX reactions in various operation temperature from 170 to 270 ℃ to investigate CO concentration data in the reformed gases. Using these different CO concentration, PEMFC performances are achieved at the combined system. Pt/C and Ru promoted Pt/C were catalysts were used for the anode to compare the stability in CO contained gases. The alloy catalyst of PtRu/C shows higher performance and better resistance to CO than the Pt/C at even high CO amount of 200 ppm, indicating a promotion not only to the activity but also to the CO tolerance. Furthermore, in a system point of view, there is a fluctuation in the PEMFC operation due to the unstable fuel supply. Therefore, we also modified the methanol reforming by a scaled up reactor and pressurization to produce steady operation of PEMFC. The optimized system with the methanol reformer and PEMFC shows a stable performance for a long time, which is providing a valuable data for the PEMFC commercialization.