• Title/Summary/Keyword: 총괄 반응

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Numerical Analysis of Turbulent Combustion of a Kerosene/Oxygen Coaxial Injector with a Recess (리세스가 있는 케로신/산소 동축 분사기의 난류 연소 유동 해석)

  • Choi, Jeong-Yeol;Shin, Jae-Ryul
    • Proceedings of the Korean Society of Propulsion Engineers Conference
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    • 2011.04a
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    • pp.77-78
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    • 2011
  • A multi-step quasi-global mechanism is developed for the kerosene/oxygen combustion analysis including dissociation products. Reaction constants of the global reaction are determined to have agreement with experimental data. The mechanism is used for the numerical analysis of the combustion flow field of the kerosene/oxygen shear coaxial injector. The results from high-resolution numerical analysis confirmed qualitatively that the recess enhance the fuel/air mixing and combustion efficiency by the increased flow instabilities.

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Characteristics of the Bioreactors of Hydrogen-producing Immobilized Cells (II) -Overall Effectiveness Factor in Continuous Reactors- (수소생산 고정화 생물 반응기의 특성(II) -연속 반응기에서의 총괄 효율인자 -)

  • 이명재;선용호;한정우;조영일
    • Microbiology and Biotechnology Letters
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    • v.16 no.6
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    • pp.510-516
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    • 1988
  • The effects of input substrate concentration and dilution rate on mass transfer resistance in the operation of immobilized cell reactors were investigated using Rhodospirillum rubrum KS-301 immobilized by Ca alginate as reactor element and glucose as growth-limiting substrate. The kinetic parameters were obtained to estimate effectiveness factors. In the packed-bed reactor, internal mass transfer resistance was predominating although external resistance could not be neglected. The overall effectiveness factor was decreased with increase of dilution rate. In the continuous stirred-tank reactor, external resistance was nearly neglected and the overall effectiveness factor was not affected by dilution rate. In this experiment the overall effectiveness factors in PBR and CSTR were estimated to be 0.70 and 0.71 at D$_{i}$ = 0.2/h, R = 0.15 cm, and S$_{i}$ : 1.0g/L, respectively.

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Numerical Study on the Effect Recess on the Turbulent Combustion of Kerosene/LOx Coaxial Rocket Injector (케로신-산소 로켓 동축 분사기 난류 연소에서 리세스의 영향에 대한 수치해석)

  • Choi, Jeong-Yeol;Shin, Jae-Ryul
    • Proceedings of the Korean Society of Propulsion Engineers Conference
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    • 2011.11a
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    • pp.92-95
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    • 2011
  • A multi-step quasi-global mechanism is developed for the kerosene/oxygen combustion analysis including dissociation products. Reaction constants of the global reaction are determined to have agreement with experimental data. The mechanism is used for the numerical analysis of the combustion flow field of the kerosene/oxygen shear coaxial injector. The results from high-resolution numerical analysis confirmed qualitatively that the recess enhance the fuel/air mixing and combustion efficiency by the increased flow instabilities.

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Theoretical Estimation of Stoichiometry for Biodegradation of Hazardous Organic Compounds (유해유기물질에 대한 미생물 분해 반응식의 이론적 예측)

  • 우승한;박종문
    • Journal of Soil and Groundwater Environment
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    • v.8 no.2
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    • pp.70-77
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    • 2003
  • Theoretical estimation of overall stoichiometry for the microbial degradation of hazardous organic compounds is described. Half-reaction method based on microbial energetics was used in the theoretical estimation. In addition to the half-reaction method, other theoretical methods such as intermediate formation, oxygenation reaction, and estimation of the standard free energy of formation by group contribution theory were also applied. As a case study, the application of these methods was demonstrated for the estimation of microbial kinetics in the biodegradation of phenanthrene which was chosen as a model hazardous organic compound along with glucose and hexadecane. The cell yield, oxygen requirement, nitrogen requirement, and mineralization ratio could be estimated from the overall stoichiometry. It is believed that these theoretical estimation methods are useful tools for practical design and assessment of bioremediation of soil and groundwater contaminated with hazardous organic compounds.

Kinetics of CO2 Absorption in Aqueous DETA and DEEA Solutions by Wetted-Wall Column (젖은 벽탑을 이용한 디에틸렌트리아민과 디에틸에탄올아민 수용액의 CO2 흡수속도 측정)

  • You, Jong Kyun;Lee, Jun;Hong, Yeon Ki
    • Korean Chemical Engineering Research
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    • v.60 no.4
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    • pp.582-587
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    • 2022
  • Biphasic solvents are attracting attention as energy-reducing solvents for capturing CO2 from flue gas in combustion process. In this study, considering diethylenetriamine (DETA) and diethylethanolamine (DEEA) mixed solvents, one of the biphasic solvents by blending of two types of amines, the CO2 absorption rates of DETA and DEEA was measured by wetted wall column. The effects of DETA and DEEA concentrations and operating temperature on the overall mass transfer coefficient were investigated. As a result, the overall mass transfer coefficient was proportional to the DETA concentration. However, in the case of the DEEA concentration, the effect was small and when the concentration was exceeded, the overall mass transfer coefficient decreased. The DETA aqueous solution showed little change in the overall mass transfer coefficient with the operating temperature, whereas the DEEA aqueous solution increased the overall mass transfer coefficient with the operating temperature. As a result of obtaining the observed reaction rate constant under the pseudo-first-order reaction assumption, it was found that the observed reaction rate constant in DETA aqueous solution was proportional to the DETA concentration, but DEEA did not fit the pseudo-first-order reaction assumption.

Development of Bioreactors for Hydrogen-Producing Immobilized Photosynthetic Bacteria(II) : Evaluation of Immobilized Bioreactor for Hydrogen Productivity and Mass Transfer Resistance (광합성 박테리아를 이용한 고성능 수소 생산 고정화 생물반응기의 개발(II) :고정층 반응기와 연속 교반탱크 반응기에서의 수소 생산성 및 물질전달 저항 비교)

  • 선용호;한정우
    • KSBB Journal
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    • v.8 no.3
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    • pp.256-265
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    • 1993
  • In this study, it was observed that hydrogen productivity varied with changes of input g1ucose concentration and dilution rate in FBR( Fixed Bed Reactor), and CSTR(Continuous Stirred Tank Reactor). We evaluated and compared reaction rate Parameters and internal external and overall mass transfer resistances of immobilized carrier in both reactors. Apparent $K_m$ decreased with increasing dilution rate in FBR but showed a constant value above $0.4h^{-1}$ of dilution rate in CSTR. The experimental results in FBR showed nearly analogous to those in CSTR, however, the performance of FBR resulted in lower hydrogen productivity and an external effectiveness factor but a higher internal effectiveness factor than in CSTR. The overall effectiveness factor obtained with various input 91ucose concentrations showed similar values in both reactors.

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Study of Ignition Characteristics of CH4/Hot Air Diffusion Flame Using a Flame-Controlling Continuation Method (화염제어 연속계산법을 이용한 CH4-고온공기 확산화염의 점화특성 연구)

  • Song, Keum-Mi;Oh, Chang-Bo
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.35 no.6
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    • pp.625-632
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    • 2011
  • The ignition characteristics of a $CH_4$/hot air counterflow diffusion flame were investigated numerically using a flame-controlling continuation method. For the chemical reactions, the GRI-v1.2 reaction mechanism was used in the simulation. The maximum flame temperature was presented in the space of the inverse global strain rate, and showed S-curve-type behavior. The flame temperatures and velocities of the upper and middle branches were compared for different global strain rates. In addition, the global strain rate was compared with the local strain rates defined at the flame surface and the boundaries of the fuel and oxidizer sides of the fuel/air mixing layer. These local strain rates correlated well with the global strain rate.

흑연의 연소

  • 한국원자력산업회의
    • Nuclear industry
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    • v.7 no.9 s.55
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    • pp.57-65
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    • 1987
  • 소련의 체르노빌원자력발전소에서 사고가 발생한지도 거의 1년반이 되고 있다. 이 사고에서는 중성자감속재로 사용되고 있던 흑연블록의 연소가 피해를 크게 했다고 한다. 본고에서는 흑연의 연소, 즉 가스화반응을 총괄하였다.

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Mixing and Oxygen Transfer Characteristics of Three Phase Fluidized Bed for Water Quality Management of Aquaculture (양어장 수질관리를 위한 삼상유동층 반응기의 혼합 및 산소전달특성)

  • LEE Byung-hun;KIM Jeong-sook;KANG Im-suk
    • Journal of Aquaculture
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    • v.7 no.4
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    • pp.239-249
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    • 1994
  • This study was conducted to elucidate mixing characteristics of the media to dertermine hydraulic model parameters of the three phase fluidized bed for the water quality management of aquaculture. The volume and H/D ratio of the reactor were 1.76 Liter and 10.9, respectively. The experimental results showed that variance $(\sigma^2)$ and dispersion number $(D/{\mu}L)$ were above 0.47 and $0.35\~\infty$, respectively. Therefore, the condition of the reactor was almost ideal complete mixing. The dependence of the overall oxygen-transfer coefficient $(K_{La})$ on each experimental variables through a multple linear regression was given by the following equation ; $$K_{La}\;=\;44.9(D_i/D_c)^{-0.4611}\;A_f^{0.8622}\;C_m^{-0.0746}\;d_p^{-0.4302}$$

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