• 제목/요약/키워드: Gas-solid reaction kinetics

검색결과 14건 처리시간 0.028초

하수슬러지 가스화의 kinetics 및 합성가스 생산 연구 (Study on Kinetics and Syngas Production of Sewage Sludge Gasification)

  • 노선아
    • 자원리싸이클링
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    • 제24권6호
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    • pp.3-8
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    • 2015
  • 일정 온도에서 중량 변화를 통하여 가스화 반응 특성을 살펴볼 수 있는 열중량 분석기(thermobalance)를 이용하여 하수슬러지의 수증기 가스화 특성 및 발생 가스의 농도 분석을 실시하였다. 반응 온도 및 수증기의 분압이 증가할수록 가스화 반응이 촉진되어 반응 속도가 증가하는 것으로 나타났다. 반응 kinetics 해석은 기체-고체 화학반응의 세 가지 모델이 이용되었다. 이 중 하수슬러지 촤의 수증기 가스화는 modified volumetric reaction model이 반응 kinetics를 가장 잘 나타내었으며, 이 때 activation energy와 빈도 인자는 각각 155.5 kJ/mol, $14,087s^{-1}atm^{-1}$로 분석되었다. 또한, 수증기의 분압에 따른 반응 차수는 0.68이었다. 합성가스의 발생 특성을 살펴보고자 $900^{\circ}C$에서 생성 합성가스를 분석한 결과 수소의 농도가 가장 높았으며 수증기 분압이 증가할수록 생성기체의 농도 특히 수소 농도가 급격히 증가하였다. 가스화와 동시에 수성가스화 변환반응이 진행되어 생성기체의 수소 생성 농도가 일산화탄소에 비하여 2-4배 높은 값을 나타내었다.

톱밥 촤의 고온 수증기 가스화 특성 (Steam Gasification Kinetics of Sawdust Char at High Temperature)

  • 노선아;윤진한;길상인;민태진;이정규
    • Korean Chemical Engineering Research
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    • 제52권6호
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    • pp.821-825
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    • 2014
  • 바이오매스의 수증기 가스화 특성을 고온 영역에서 살펴보고자 열중량 분석기(thermobalance)에서 톱밥 촤의 수증기 가스화 연구를 수행하였다. 반응 온도를 $850^{\circ}C$에서 $1400^{\circ}C$까지 수증기 분압을 0.3, 0.5, 0.7 atm으로 변화시키며 가스화 실험이 수행되었다. 반응 kinetics 해석은 기체-고체 화학반응의 세 가지 모델이 이용되었고 이 중 modified volumetric model이 중량 변화를 가장 잘 나타내었다. 가스화 온도 $900^{\circ}C$를 기준으로 diffusion control regime과 reaction control regime의 두 단계로 가스화가 구분되었으며 이때 각각의 regime에 대하여 활성화에너지와 빈도인자를 도출하고 수증기 분압의 영향을 살펴보았다. 가스화와 동시에 수성가스화 변환반응이 진행되어 생성기체의 $H_2$ 농도가 CO에 비하여 2배 정도 높은 값을 나타내었다.

NiFe2O4의 수소환원에 의한 나노구조 Fe-Ni 합금의 제조 및 자성특성 (Synthesis and Magnetic Properties of Nanocrystalline Fe-Ni Alloys During Hydrogen Reduction of NiFe2O4)

  • 백민규;도경효;;박종진
    • 대한금속재료학회지
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    • 제49권1호
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    • pp.52-57
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    • 2011
  • Nickel ferrite ($NiFe_2O_4$) powder was prepared through the ceramic route by calcination of a stoichiometric mixture of nickel oxide (NiO) and iron oxide ($Fe_2O_3$). The pressed pellets of $NiFe_2O_4$ were isothermally reduced in pure hydrogen at 800, 900, 1000 and $1100^{\circ}C$. Based on thermogravimetric analysis, the reduction behavior and the kinetic reaction mechanisms of the synthesized ferrite were studied. The initial ferrite powder and various reduction products were characterized by XRD, SEM, reflected light microscope and VSM to reveal the effect of hydrogen reduction on the composition, microstructure, magnetic properties and reaction kinetics of the produced Fe-Ni alloy. Complete reduction of the $NiFe_2O_4$ was achieved with synthesis of homogeneous nanocrystalline Fe-Ni alloys. Arrhenius equation with the approved mathematical formulations for a gas-solid reaction was applied for calculating the activation energy ($E_a$) values and detecting the controlling reaction mechanism.

기-고체 반응 모델을 이용한 Kideco탄의 이산화탄소 촉매 석탄가스화 반응 특성 (Reactivity Study on the Kideco Coal Catalytic Coal Gasification under CO2 Atmosphere Using Gas-Solid Kinetic Models)

  • 이도균;김상겸;황순철;이시훈;이영우
    • 청정기술
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    • 제21권1호
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    • pp.53-61
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    • 2015
  • 본 연구는 인도네시아 아역청탄인 키데코(Kideco)탄의 촤(char)-이산화탄소 촉매가스화 kinetic분석을 열중량분석기(thermogravimetric analysis, TGA)를 이용하여 수행하였다. 촉매는 탄산칼륨 및 탄산나트륨을 선정하였으며, 석탄과 촉매의 물리적 혼합을 통하여 촤를 제조하였다. 촤-이산화탄소 촉매가스화반응은 탄산나트륨 7 wt%, 850 ℃에서 이산화탄소 농도가 60 vol%일 때 가장 빠른 탄소전환율을 보여주었다. 750~900 ℃ 등온조건에서 촤-이산화탄소 촉매가스화 반응결과, 온도가 증가할수록 탄소전환율 속도가 빨라졌으며, 기-고체 반응모델 shrinking core model (SCM), random pore model (RPM), volumetric reaction model (VRM) 및 modified volumetric reaction model (MVRM)을 실험결과에 적용하였을 때, MVRM이 키데코탄의 가스화반응 거동을 잘 예측하였다. 또한 Arrhenius plot을 통한 활성화에너지는 탄산나트륨을 첨가한 촤가 탄산 칼륨을 첨가한 촤보다 더 우수한 촉매 활성을 보여주었다.

초고압 절연 스페이서의 자동가압 겔화 성형 공정을 위한 경화 보압의 최적화 (Optimization of Curing Pressure for Automatic Pressure Gelation Molding Process of Ultra High Voltage Insulating Spacers )

  • 이찬용;조한구;이재형
    • 한국전기전자재료학회논문지
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    • 제37권1호
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    • pp.56-62
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    • 2024
  • By introducing curing kinetics and chemo-rheology for the epoxy resin formulation for ultra-high voltage gas insulated switchgear (GIS) Insulating Spacers, a study was conducted to simulate the curing behavior, flow and warpage analysis for optimization of the molding process in automatic pressure gelation. The curing rate equation and chemo-rheology equation were set as fixed values for various factors and other physical property values, and the APG molding process conditions were entered into the Moldflow software to perform optimization numerical simulations of the three-phase insulating spacer. Changes in curing shrinkage according to pack pressure were observed under the optimized process conditions. As a result, it was confirmed that the residence time in the solid state was shortened due to the lowest curing reaction when the curing holding pressure was 3 bar, and the occurrence of deformation due to internal residual stress was minimized.

Evolution, Fields of Research, and Future of Chemical-Looping Combustion (CLC) process: A Review

  • Shahrestani, Masoumeh Moheb;Rahimi, Amir
    • Environmental Engineering Research
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    • 제19권4호
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    • pp.299-308
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    • 2014
  • This study presents a review on Chemical looping combustion (CLC) development, design aspects and modeling. The CLC is in fact an unmixed combustion based on the transfer of oxygen to the fuel by a solid oxygen carrier material avoiding the direct contact between air and fuel. The CLC process is considered as a very promising combustion technology for power plants and chemical industries due to its inherent capability of $CO_2$ capturing, which avoids extra separation costs of the of $CO_2$ from the rest of flue gases. This review covers the issues related to oxygen carrier materials. The modeling works are reviewed and different aspects of modeling are considered, as well. The main drawbacks and future research and prospects are remarked.

Methane carbon dioxide reforming for hydrogen production in a compact reformer - a modeling study

  • Ni, Meng
    • Advances in Energy Research
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    • 제1권1호
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    • pp.53-78
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    • 2013
  • Methane carbon dioxide reforming (MCDR) is a promising way of utilizing greenhouse gas for hydrogen-rich fuel production. Compared with other types of reactors, Compact Reformers (CRs) are efficient for fuel processing. In a CR, a thin solid plate is placed between two porous catalyst layers to enable efficient heat transfer between the two catalyst layers. In this study, the physical and chemical processes of MCDR in a CR are studied numerically with a 2D numerical model. The model considers the multi-component gas transport and heat transfer in the fuel channel and the porous catalyst layer, and the MCDR reaction kinetics in the catalyst layer. The finite volume method (FVM) is used for discretizing the governing equations. The SIMPLEC algorithm is used to couple the pressure and the velocity. Parametrical simulations are conducted to analyze in detail the effects of various operating/structural parameters on the fuel processing behavior.

일메나이트 중 철의 선택적 염화와 선광된 TiO2의 추가 염화반응에 대한 글로벌 피팅함수 (Global Fitting Functions for Kinetics of Fe-Selective Chlorination in Ilmenite and Successive Chlorination of Beneficiated TiO2)

  • 정동규;원용선;김용하;정은진;송덕용
    • 한국재료학회지
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    • 제29권7호
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    • pp.412-424
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    • 2019
  • Global fitting functions for Fe-selective chlorination in ilmenite($FeTiO_2$) and successive chlorination of beneficiated $TiO_2$ are proposed and validated based on a comparison with experimental data collected from the literature. The Fe-selective chlorination reaction is expressed by the unreacted shrinking core model, which covers the diffusion-controlling step of chlorinated Fe gas that escapes through porous materials of beneficiated $TiO_2$ formed by Fe-selective chlorination, and the chemical reaction-controlling step of the surface reaction of unreacted solid ilmenite. The fitting function is applied for both chemical controlling steps of the unreacted shrinking core model. The validation shows that our fitting function is quite effective to fit with experimental data by minimum and maximum values of determination coefficients of $R^2$ as low as 0.9698 and 0.9988, respectively, for operating parameters such as temperature, $Cl_2$ pressure, carbon ratio and particle size that change comprehensively. The global fitting functions proposed in this study are expressed simply as exponential functions of chlorination rate(X) vs. time(t), and each of them are validated by a single equation for various reaction conditions. There is therefore a certain practical merit for the optimal process design and performance analysis for field engineers of chlorination reactions of ilmenite and $TiO_2$.

Multiphase-Particle in Cell 해석 기법을 이용한 원뿔형 분사층 반응기 내 바이오매스의 급속열분해 반응 전산해석 (CPFD Simulation for Fast Pyrolysis Reaction of Biomass in a Conical Spouted Bed Reactor using Multiphase-particle in Cell Approach)

  • 박훈채;최항석
    • 한국폐기물자원순환학회지
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    • 제34권7호
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    • pp.685-696
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    • 2017
  • This study focuses on computational particle fluid dynamics (CPFD) modeling for the fast pyrolysis of biomass in a conical spouted bed reactor. The CPFD simulation was conducted to understand the hydrodynamics, heat transfer, and biomass fast pyrolysis reaction of the conical spouted bed reactor and the multiphase-particle in cell (MP-PIC) model was used to investigate the fast pyrolysis of biomass in a conical spouted bed reactor. A two-stage semi-global kinetics model was applied to model the fast pyrolysis reaction of biomass and the commercial code (Barracuda) was used in simulations. The temperature of solid particles in a conical spouted bed reactor showed a uniform temperature distribution along the reactor height. The yield of fast pyrolysis products from the simulation was compared with the experimental data; the yield of fast pyrolysis products was 74.1wt.% tar, 17.4wt.% gas, and 8.5wt.% char. The comparison of experimental measurements and model predictions shows the model's accuracy. The CPFD simulation results had great potential to aid the future design and optimization of the fast pyrolysis process for biomass.

인도네시아 갈탄의 촤-CO2 촉매가스화 반응특성연구 (Kinetic Study on Char-CO2 Catalytic Gasification of an Indonesian lignite)

  • 이도균;김상겸;황순철;이시훈;이영우
    • Korean Chemical Engineering Research
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    • 제52권4호
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    • pp.544-552
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    • 2014
  • 본 연구는 인도네시아 갈탄인 로토(Roto) 탄의 촤(char)-$CO_2$ 촉매가스화 kinetic 분석을 열중량분석기(thermogravimetric analysis, TGA)를 이용하여 수행하였다. 촉매는 $Na_2CO_3$, $K_2CO_3$, $CaCO_3$ 및 천연광물 촉매로 dolomite을 선정하였으며, 석탄과 촉매의 물리적 혼합을 통하여 촤를 제조하였다. 촤-$CO_2$ 촉매가스화반응은 $850^{\circ}C$에서 $CO_2$ 농도가 60 vol%, 촉매 함량은 $Na_2CO_3$를 7 wt% 혼합할 때 가장 빠른 탄소전환율을 보여주었다. $750{\sim}900^{\circ}C$ 등온조건에서 촤-$CO_2$ 촉매 가스화 반응결과, 온도가 증가할수록 탄소전환율 속도가 빨라졌으며, 기-고체 반응모델 shrinking core model(SCM), volumetric reaction model(VRM), modified volumetric reaction model(MVRM)을 실험결과에 적용하였을 때, MVRM 이 로토 탄의 가스화반응 거동을 잘 예측하였다. 특히 Arrhenius plot을 통한 활성화에너지는 $Na_2CO_3$$K_2CO_3$를 혼합한 촤의 활성화에너지가 각각 67.03~77.09 kJ/mol, 53.14~67.99 kJ/mol으로 우수한 촉매 활성을 보여주었다.