• 제목/요약/키워드: Chemical Reactor

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감압 상태 순환유동층 반응기에서 플라즈마 그래프팅에 의한 미세입자 표면 개질 (Surface Modification of Fine Particle by Plasma Grafting in a Circulating Fluidized Bed Reactor under Reduced Pressure)

  • 박성희
    • Korean Chemical Engineering Research
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    • 제53권5호
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    • pp.614-619
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    • 2015
  • 미세입자의 플라즈마 표면 개질을 감압상태하의 순환유동층 반응기에서 수행하였다. 플라즈마에 의해 처리된 폴리스타이렌 입자는 폴리에틸렌글리콜로 표면에 그래프팅하였다. 표면 개질 전 입자와 플라즈마 처리된 입자 그리고 그래프팅된 입자의 특성은 각각 DPPH 방법, FTIR, SEM 그리고 접촉각 측정으로 분석하였다. 플라즈마 처리된 폴리스타이렌 입자의 표면에 과산화물이 잘 형성되었다. 또한, 폴리에틸렌글리콜의 그래프팅 중합에 의해 플라즈마 처리된 입자 표면에 그래프팅이 잘 분산되었다. 따라서 감압상태의 순환 유동층 반응기에서 플라즈마 처리에 의한 PEG-g-PS 입자를 성공적으로 형성할 수 있었다.

수직 싸이클론의 ${Ca(OH)}_{2}$ 배소에서 $FeS_{2}$의 열적반응에 관한 연구 (A kinetic study of pyrite in the lime roasting of a vertical cyclone)

  • 조종상
    • 한국결정성장학회지
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    • 제9권1호
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    • pp.119-125
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    • 1999
  • 본 연구는 싸이클론 반응로에서 $FeS_{2}$의 반응 특성에 관한 조사를 연구하였다. 수학적인 모형도로 이 반응로에서 $FeS_{2}$의 oxidation과 suifation 등을 전개하엿다. 모형은 $FeS_{2}$에서 chemical control shrinking core로서 그리고 ${Ca(OH)}_{2}$에서 fluid film control shrinking core로서 가정하였으며 수식으로서 발전시켰다. 본 실험은 이 반응 파라메터들의 영향에 연구로서 진행하였으며 즉 반응로의 온도변화, $FeS_{2}$의 입자크기, 공기 주입비율, 시료 주입비율, 그리고 $FeS_{2}$${Ca(OH)}_{2}$ 비율 등이다. Oxidation과 Sulfation에 의한 반응물들은 화학적 및 물리적으로 특성을 기술하였다.

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화학증착 탄화규소에 의한 흑연의 표면개질 연구 -수평형 화학증착반응관에서 탄화규소 성장특성- (A Study on the Surface Modification of Graphite by CVD SiC -Growth Characteristics of SiC in a Horizontal CVD Reactor-)

  • 김동주;최두진;김영욱;박상환
    • 한국세라믹학회지
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    • 제32권4호
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    • pp.419-428
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    • 1995
  • Polycrystalline silicon carbide (SiC) thick films were depostied by low pressure chemical vapor deposition (LPCVD) using CH3SiCl3 (MTS) and H2 gaseous mixture onto isotropic graphite substrate. Effects of deposition variables on the SiC film were investigated. Deposition rate had been found to be surface-reaction controlled below reactor temperature of 120$0^{\circ}C$ and mass-transport controlled over 125$0^{\circ}C$. Apparent activation energy value decreased below 120$0^{\circ}C$ and deposition rate decreased above 125$0^{\circ}C$ by depletion effect of the reactant gas in the direction of flow in a horizontal hot wall reactor. Microstructure of the as-deposited SiC films was strongly influenced by deposition temperature and position. Microstructural change occurred greater in the mass transport controlled region than surface reaction controlled region. The as-deposited SiC layers in this experiment showed stoichiometric composition and there were no polytype except for $\beta$-SiC. The preferred orientation plane of the polycrystalline SiC layers was (220) plane at a high reactant gas concentration in the mass transfer controlled region. As depletion effect of reactant concentration was increased, SiC films preferentially grow as (111) plane.

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FAULT DETECTION, MONITORING AND DIAGNOSIS OF SEQUENCING BATCH REACTOR FOR INTEGRATED WASTEWATER TREATMENT MANAGEMENT SYSTEM

  • Yoo, Chang-Kyoo;Vanrolleghem, Peter A.;Lee, In-Beum
    • Environmental Engineering Research
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    • 제11권2호
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    • pp.63-76
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    • 2006
  • Multivariate analysis and batch monitoring on a pilot-scale sequencing batch reactor (SBR) are described for integrated wastewater treatment management system, where a batchwise multiway independent component analysis method (MICA) are used to extract meaningful hidden information from non-Gaussian wastewater treatment data. Three-way batch data of SBR are unfolded batch-wisely, and then a non-Gaussian multivariate monitoring method is used to capture the non-Gaussian characteristics of normal batches in biological wastewater treatment plant. It is successfully applied to an 80L SBR for biological wastewater treatment, which is characterized by a variety of error sources with non-Gaussian characteristics. The batchwise multivariate monitoring results of a pilot-scale SBR for integrated wastewater treatment management system showed more powerful monitoring performance on a WWTP application than the conventional method since it can extract non-Gaussian source signals which are independent and cross-correlation of variables.

에탄 열분해 반응이 동반된 관형 반응기에서의 열전달 및 화학반응 특성 연구 (THE CHARACTERISTICS OF HEAT TRANSFER AND CHEMICAL REACTION FOR THERMAL CRACKING OF ETHANE IN TUBULAR REACTOR)

  • 신찬영;안준
    • 한국전산유체공학회지
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    • 제21권1호
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    • pp.43-49
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    • 2016
  • Thermal cracking is commonly modeled as plug flow reaction, neglecting the lateral gradients present. In this paper, 2-dimensional computational fluid dynamics including turbulence model and molecular reaction scheme are carried out. This simulation is solved by means of coupled implicit scheme for stable convergence of solution. The reactor is modeled as an isothermal tube, whose length is 1.2 m and radius is 0.01 m, respectively. At first, The radial profile of velocity and temperature at each point are predicted in its condition. Then the bulk temperature and conversion curve along the axial direction are compared with other published data to identify the reason why discussed variations of properties are important to product yield. Finally, defining a new non-dimensional number, Effect of interaction with turbulence, heat transfer and chemical reaction are discussed for design of thermal cracking furnace.

소성Dolomite 수화물계의 축열시스템에 관한 연구 - 소성Dolomite 수화반응층의 전열해석 - (A Study on Heat Storage System Using Calcined Dolomite - Numerical Analysis of Heat Transfer in Calcined Dolomite Hydration Pocked Bed -)

  • 박영해;김종식
    • 한국태양에너지학회 논문집
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    • 제22권1호
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    • pp.9-21
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    • 2002
  • To develope chemical heat pump using available energy sources, solar heat and other kinds of waste thermal energy, we have studied the heat transfer rate in cylindrical bed reactor packed with calcined Dolomite. Two dimensional (radial and circumferential) Partial differential equations, concerning heat and mass transfer in packed bed of calcined Dolomite, are solved numerically to describe the characteristics of the reaction of calcined Dolomite and heat transfer. The results obtained by numerical analysis about two dimensional profiles of temperature and conversion of reactant in the packed bed reactor and the amount of exothermic heat released from the reactor are follows. It was found that all of calcined Dolomite packed bed kept the reaction temperature of about 750K throughout the entire part of the bed, immediately after the steam was introduced exothermic reaction of hydration was proceeded from the packed bed inpu to output and from wall side to center. The rate of thermochemical reaction depends on the temperature and concentration and it is also governed by the boundary conditions and heat transfer rate in the particle packed bed.

생물막 여과 반응기를 이용한 양어장 순환수의 동시 질산화 및 탈질산화 반응 (Simultaneous Nitrification and Dennrincation of Recirculating Aquaculture Water by Biofilter Reactor)

  • 이민규;서근학;오영회
    • 한국환경과학회지
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    • 제6권4호
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    • pp.409-415
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    • 1997
  • In order to Investigate the possibility as a simple technique of wastewater treatment for recirculating aquaculture system, the experiment by a biofilter unfit was carried out. The high and stable removal efficiency of nitrogen could be obtained by selecting the optimum recycle ratio and DO concentration. It was found that the proper combination of nitrifacation and denitrfication step in the reactor would be required for increasing the removal efficiency. The extent of nitrogen removal gradually decreased UO the rise of re- cycle ratio since the depression of denitrificatlon by the lack of hydrogen donor. The depression of nitrogen removal was overcome by increasing the CIN ratio In the wastewater. The extent of phosphorus removal was increased slightly with the increase of DO concentration and recycle ratio, but high removal efficiency was not observed. However, the extent of COD removal was not affected by recycle ratio and DO concentration and showed the stable removal of above 90%.

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Photocatalytic Oxidation of Indoor Air Volatile Organic Compounds (VOCs) in pub Level

  • Jo, Wan-Kuen;Kim, Dong-Hyun;Ki, Jae-Chang;Huh, Jeung-Soo
    • Journal of Korean Society for Atmospheric Environment
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    • 제19권E4호
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    • pp.157-168
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    • 2003
  • This study evaluated the technical feasibility of the application of titanium oxide (TiO$_2$) photocatalysis for the removal of VOCs in low ppb concentrations commonly associated with non -occupational indoor air quality issues. A series of experiments were conducted to evaluate four parameters (relative humidity (RH), hydraulic diameter (HD), photocatalytic oxidation (PCO) reactor material (RM), and inlet port size (IPS) of PCO reactor) for the PCO destruction efficiencies of the selected target VOCs. None of the target VOCs presented significant dependency on the RH, which is inconsistent with a few previous studies. However, it is noted that the three parameters (HD, RM and IPS) should be considered for better VOCs removal efficiencies for the application of TiO$_2$ photocatalytic technology for cleansing non -occupational indoor air. The PCO destruction of VOCs at concentrations associated with non-occupational indoor air quality issues can be up to nearly 100%. The amount of CO generated during PCO would be negligible in comparison to the indoor CO levels. These results can make the PCO reactor an important tool in the effort to improve non-occupational indoor air quality.

Dicyclohexyl-24-crown-8과 Tetraphenylborate에 의한 원자로 냉각수로부터 세슘 핵종의 이온쌍 용매추출 (Ion-Pair Extraction of Cs Radionuclides by Dicyclohexyl-24-crown-8 and Tetraphenylborate for Their Determination in Reactor Coolant)

  • 이인종;김시중;이철
    • 대한화학회지
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    • 제27권4호
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    • pp.262-267
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    • 1983
  • 가압형 경수로의 일차 냉각수로부터 세슘 핵종을 선택적으로 분리하여 그 방사능을 결정하기 위한 Scheme이 연구되었다. 세슘의 분리는 dicyclohexyl-24-crown-8과 sodium tetraphenylborate에 의한 이온쌍 용매추출에 의해서 이루어졌으며 추출에 미치는 수소, 세슘, 나트륨 및 borate 이온의 영향이 연구되었다. 요오드와 크세논 핵종의 방해 현상은 각각 티오황산나트륨에 의한 요오드의 환원과 1N 염산수용액에 의한 역추출에 의해서 제거될 수 있었다

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