• 한국화재소방학회논문지
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• 제33권5호
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• pp.7-12
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• 2019

목재 연료의 연소 시 생성되는 탄화가 열분해 과정에 미치는 영향을 고찰해 보기 위해서 ISO 5660-1 콘칼로리미터 실험을 수행하였고 Fire dynamics simulator (FDS) 전산해석 결과와 비교 분석하였다. 목재 연료로는 건축자재, 가구재 등에 대표적으로 사용되는 Douglas-fir를 사용하였다. Douglas-fir 연소 시 측정된 열방출률은 FDS 전산해석을 통해 예측한 결과와 비교적 잘 일치하였지만 탄화 층의 표면반응을 고려하지 않는 FDS 전산해석 모델은 훈소과정에서 지속적으로 방출되는 열을 예측하지 못하였다. 그럼에도 불구하고 FDS 전산해석을 통해 탄화 층은 가연물에 열장벽을 형성하여 내부로의 열전달을 방해하고 열적 두께를 두껍게 하여 열분해율을 감소시키는 것을 확인하였다.

• 에너지공학
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• 제14권1호
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• pp.1-10
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• 2005

석탄의 열분해 압력이 촤의 연소 반응성에 미치는 영향을 가압열중량 분석기를 사용하여 고찰하였다. 사용되어진 탄은 알라스카, 아다로, 데니소브스키탄으로서 압력을 상압, 8기압, 15기압으로 변화시키면서 휘발분 방출량을 측정하고 열분해 압렵별로 생성된 촤의 반응성을 상압하 500℃에서 평가하였으며 생성된 촤의 결정구조, 표면적 및 기공특성, 화학적 특성을 분석하였다. 열분해 압력이 증가함에 따라 휘발분 방출량은 감소하였고 고압에서 생성된 촤의 반응성이 작았음을 알 수 있었다. 이는 반응표면적과 기공특성의 차이로 생각되어지며 열분해 압력에 따른 촤의 화학적 특성과 결정구조는 큰 차이를 보이지 않았다. 상압, 5기압 15기압하에서 3개 촤의 연소 반응속도를 측정하였으며 알라스카 촤의 경우, 15기압에서 연소반응성 지수 획득실험을 수행하여 56.8KJ/mole의 활성화에너지, 222.34(1/min)의 빈도계수 값을 얻었다.

• 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.

• 한국연소학회:학술대회논문집
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• 한국연소학회 2007년도 제34회 KOSCO SYMPOSIUM 논문집
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• pp.54-59
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• 2007

In a view of capturing $CO_2$ as a greenhouse gas, an experimental study was conducted on the combustion characteristics of pulverized coal in $O_2$/$CO_2$ environment using TGA/DSC and DTF facilities. The effects of gas composition and concentration on the processes of devolatilization and char burning experienced by coal particles in combustion furnace and on the concentration of products such as $CO_2$, CO and $NO_x$ were observed using TGA/DSC and DTF respectively. As results, it were found that the rate of devolitilation is nearly independent on the $O_2$ concentration if it is over 20% but the char burning rate is a sensitive function of $O_2$ percent, and the two rates can be controlled by $O_2$ concentration in order to be similar with those of air combustion case. It was also found that high concentration $CO_2$ can be captured by oxy-coal combustion and high concentration of CO and low value of $NO_x$ are exhausted in that case. Additionally, NO reducing reaction by CO with char as catalyst was observed and a meaningful results were obtained.

• 한국연소학회지
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• 제16권1호
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• pp.8-14
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• 2011

Biomass gasification is a promising technology in terms of clean energy and flexible options for end use such as heat, steam, electricity, gaseous or liquid fuels. In a gasification process, reduction of tar is very important because it can cause any mechanical problems and small tar implies high energy efficiency. However, generation and conversion mechanisms of tar have not been fully understood due to its complex nature. In this study, characteristics of tar generated from different gasification stages were investigated. Korean pine woodchip was used as feedstock and tar was sampled in a separate way during devolatilization and char gasification stage, investigated. As a result. more various kinds of hydro carbon compounds were identified in the devolatilization stage than char gasification stage because primary tar compounds are released mostly from pyrolysis of cellulose and hemicellulose. When the reaction temperature increased up to $900^{\circ}C$, tar composition becomes simplified into about 10 aromatic compounds mostly with 1-4 rings without substitution up to phenanthrene. The sampled tar in the char gasification stage mostly contains 5-7 simple aromatic compounds.

• 한국표면공학회지
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• 제15권3호
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• pp.146-151
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• 1982

The electrochemical reaction behavior of nickel electrode of the nickel-cadium battery system in potassium hydroxide solution has been studied by cyclic voltammetry, controlled potential electrolysis and X-ray diffraction method. It has been found that the reaction mechanism of positive nickel electrode for charging was assumed to be proten transfer step with a rate controlling diffusion process and char-ging state of positive electrode was amorphous $\beta$-NiOOH.

• 한국수소및신에너지학회논문집
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• 제24권5호
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• pp.413-420
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• 2013

Effect of inherent volatile matters in fuels on electrochemical reactions of anode was investigated for a single direct carbon fuel cell (DCFC). Raw coals used as power source in the DCFC release light gases into the atmosphere under the operating temperature of DCFC ($700^{\circ}C$) by thermal decomposition and only char remained. These exhausted gases change the gas composition around anode and affect the electrochemical oxidation reaction of system. To investigate the effect of produced gases, comparative study was conducted between Indonesian sub-bituminous coal and its char obtained through thermal treatment, carbonizing. Maximum power density of raw coal ($52mW/cm^2$) was appeared higher than that of char ($37mW/cm^2$) because the gases produced from the raw coal during thermal decomposition gave additional positive results to electrochemical reaction of the system. The produced gases from coals were analyzed using TGA and FT-IR. The influence of volatile matters on anodic electrolyteelectrode interface was observed by the equivalent circuit induced from fitting of impedance spectroscopy data.

• 한국연소학회지
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• 제15권2호
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• pp.41-49
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• 2010

Various coals from many countries around the world have been used for pulverized coal boiler in power plants in Korea. In this study, the gasification reactivities of various coal chars with $CO_2$ were investigated. Carbon conversion was measured using a real time gas analyzer with NDIR CO/$CO_2$ sensor. In a lab scale furnace, each coal sample was devolatilized at $950^{\circ}C$ in nitrogen atmosphere and became coal char and then further heated up to reach to a desired temperature. Each char was then gasified with $CO_2$ under isothermal conditions. The reactivities of coal chars were investigated at different temperatures. The shrinking core model (SCM) and volume reaction model(VRM) were used to interpret the experiment data. It was found that the SCM and VRM could describe well the experimental results within the carbon conversion of 0-0.98. The gasification rates for various coals were very different. The gasification rate for any coal increased as the volatile matter content increased.

• 청정기술
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• 제15권1호
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• pp.31-37
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• 2009

본 연구는 하수슬러지 탄화물과 활성화제의 화학적 활성화반응을 이용한 활성탄 제조공정을 다루고 있다. 일반적으로 활성화제로는 알칼리 약품을 이용하는데 본 연구에서는 탄소와 활성화반응이 잘 이루어지는 KOH와 NaOH를 사용하였다. 실험결과, KOH로 제조된 활성탄이 NaOH로 제조된 활성탄보다 요오드 흡착력과 비표면적(BET) 등의 물성이 우수하였다. 하수슬러지 탄화물과 활성화제의 최적 침적비율은 KOH 75 wt%, NaOH 50 wt%임을 알 수 있었다. 5 M 염산용액으로 세척하여 중화시킨 후 증류수로 세정하는 활성탄 세정방법을 사용하였다. 본 연구의 최적 실험조건에서 하수슬러지 탄화물을 이용하여 제조된 활성탄의 경우 BET표면적 값이 약 $600m^2/g$에 이르렀다.

• Elastomers and Composites
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• 제51권3호
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• pp.195-205
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• 2016

A series of aromatic poly(hydroxyamide)s (PHAs) containing varying oligo(oxyethylene) substituents and 1,3-phenylene imide ring unit in the main chain were synthesized by the direct polycondensation reaction. The inherent viscosities of the PHAs exhibited in the range of 0.89~1.12 dL/g in DMAc or DMAc/LiCl solution. The PH-2~5 copolymers were easily soluble in strong aprotic solvents: DMAc, NMP, DMSO etc. and the PH-5 copolymer was soluble in less polar solvents such as m-creasol and pyridine with LiCl salt on heating. However, all PBOs were quite insoluble in other solvents, but only partially soluble in sulfuric acid. All copolymers (PH-2~5) could afford the flexible and tough films by solution casting. We identified that the PHAs were converted to the PBOs by the thermal cyclization reaction in the range of $200{\sim}380^{\circ}C$. The 10% weight loss temperatures and char yields of the PBOs were recorded in the range of $382{\sim}647^{\circ}C$ and 38.7~73.1% values at $900^{\circ}C$. The tensile strength and initial modulus of the PH-5 in the copolmers showed the highest values of 2.46 GPa and 49.55 MPa, respectively. The LOI values of the PHAs were in the range 26.6~29.0%, and increased with increasing 1,3-phenylene imide ring unit.