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전영남,Dae Won Ji,Kunio Yoshikawa 대한기계학회 2013 JOURNAL OF MECHANICAL SCIENCE AND TECHNOLOGY Vol.27 No.1
A study on pyrolysis, steam gasification, and carbonization-activation was conducted to produce energy and resource from waste sewage sludge. Carbonization-activation is a sequential process of pyrolysis and steam gasification. The experiment was conducted with a batch-type fixed bed reactor. A comparative analysis on the formation characteristics of products, such as gas, tar, and char, was conducted to evaluate the three cases. For sludge char, carbonization-activation showed the largest amount of porosity in the char, and its specific surface area was 80.28 m2/g with an average pore diameter of 6.229 nm. The best adsorption ability of benzene, a light tar, was 175 mg/g. For the producer gas, steam gasification obtained the largest amount of 20.1 L. Similarly, carbonization-activation showed a large value of 16.6 L. Hydrogen and carbon monoxide concentrations were higher in the producer gas due to steam reforming compared with carbonization-activation. Energy yields were 209 kJ and 226 kJ for steam gasification and carbonization-activation, respectively. The amount of tar formation did not show a significant difference, but the largest one was found in steam gasification. The gravimetric tar amount for steam gasification was 23.5 g/Nm3. However, the selected light tar displayed the lowest concentration for the carbonization- activation. Such concentrations were 2.79 g/Nm3, 0.75 g/Nm3, 0.14 g/Nm3, and 0.14 g/Nm3 for benzene, naphthalene, anthracene, and pyrene, respectively. Therefore, carbonization-activation was found to be the most effective process for producing high quality sludge char and producer gas for utilizing waste sludge into renewable energy and resources.
안드로이드 스마트폰에서 앱 설치 정보를 이용한 리패키징 앱 탐지 기법
전영남,안우현 한국사이버테러정보전학회 2012 융합보안 논문지 Vol.12 No.4
최근 안드로이드 스마트폰에서 리패키징을 이용한 악성코드가 급증하고 있다. 리패키징은 이미 배포되고 있는 앱의 내부를 수정한 후 다시 패키징하는 기법이지만, 악성코드 제작자가 기존 앱에 악성코드를 삽입하여 배포할 때 흔히 사 용되고 있다. 하지만, 앱을 제공하는 안드로이드 마켓이 다양하고, 각 마켓에서 제공하는 앱이 매우 많기 때문에 모든 앱을 수집해서 분석하는 것은 불가능하다. 이를 해결하기 위해 본 논문은 RePAD 기법을 제안한다. 이 기법은 사용자의 스마트폰에 탑재된 클라이언트 앱과 원격 서버로 구성되는 시스템이다. 클라이언트는 적은 부하로 사용자가 설치한 앱 의 출처와 정보를 추출하여 원격 서버로 전송하고, 서버는 전송된 정보를 바탕으로 앱의 리패키징 여부를 탐지한다. 따 라서 리패키징 앱 판별을 위해 앱의 정보를 수집하는 시간과 비용을 줄일 수 있다. 실험을 위해 클라이언트 앱과 원격 서버를 갤럭시탭과 윈도우즈 기반의 PC에 각각 구현하였다. 여러 마켓에서 수집된 앱 중 7 쌍의 앱이 리패키징된 것으 로 판정하였고, 갤럭시탭에서 평균 1.9%의 CPU 부하와 최대 3.5M의 메모리 사용량을 보였다.
전영남,임문섭,조대영 한국폐기물자원순환학회 2015 한국폐기물자원순환학회지 Vol.32 No.3
Refuse plastic fuel (RPF) as materials for the recycling processes (Materiel Recycling) present difficulties with the mixing, the demolishing, the molding and the drying steps. While using RDF as a fuel by pyrolysis, accompanying tar and soot causes many problems like clogging, the corrosion and the erosion of the chloride channel. Using the intermittent pyrolysis equipment during the decomposition of the RPF gases H2, CH4, CO and among the by-products of Cl2 and HCl, Tar is produced in a large quantity. With understanding the by-products decomposition system of the Cl2, H2, Tar and the gases H2, CH4, CO we can understand the nature of the generation of the products. The experimental conditions were chosen according to the temperature of the decomposition (300 ~ 900o℃), While varying RPF 2 g, pyrolysis temperature 700℃ during a holding time of 32 min : the H2 gas 1.71%, CH4 2.54%, CO 4.63%, Cl2 12.86 ppm, HCl 30.2 ppm were composed. Also light tar benzene 18.45 g/㎥, naphthalene 0.86 g/㎥, anthracene 0.09 g/㎥, pyrene 0.04 g/ ㎥, gravimetric tar 31.8 g/㎥, and char 0.45 g was formed.
덤프 소각기에서 CCI_4/C_3H_8 분해 특성에 관한 연구
전영남,채종성,송형운,김미환 조선대학교 환경연구소 2001 環境硏究 Vol.17 No.1
A major source of the hazardous waste generated is from chemical industries producing plastics, herbicides, pesticides and chlorinated solvents. All of these process produce a class of hazardous waste termed the chlorinated hydrocarbons(CHCs), either directly or from undesirable side reactions. Generally, hazardous waste is physical characteristics of difficult destruction at high temperature. We investigated the destruction characteristics of hazardous waste through incineration. A nonequilibrium combustion model was used to describe the effect of the chemical kinetics due to the flame inhibition characteristics of CCl_4 which was used as the surrogate of hazardous waste. In this study, the numerical simulation data for 3-dimensional dump combustor shows a quantitative good agreement with experimental data. Also dump incinerator shows high destruction efficience of CCl_4. And parametric screening studies was carried out through numerical simulation with changed CCl_4/C_3H_8 ratio, waste injection velocity and waste equilibrium ratio.
스토커형 저공해 소각로 설계를 위한 비반응 유동해석에 관한 연구
전영남,오현명,김미환 조선대학교 환경연구소 2000 環境硏究 Vol.16 No.1
The numerical simulation of non-reactive turbulent model and cold flow experiment were carried out to propose the incinerator type for the domestic refuses and to investigate the design factor and operating conditions. The "standard stoker incinerator" proposed in this study was modified from central flow type with carrying out by material and numerical simulations repeatedly. The stoker has the characteristics of good mixing between refuse and hot combustion gas in primary combustion chamber and between unburned gas inflowing and secondary air jet in secondary chamber. Also there was no recirculation zone in secondary chamber so that mixing time was increased with higher residence time. Therefore this incinerator could be possible for domestic refuse to burn up with the low emission and high efficiency combustion. Parametric screening studies were achieved in standard stoker incinerator. The parameters are stoker type, secondary air inflow type, secondary air injection angles, secondary injection air flow rate and primary air inflow rate. The results are as follows: 1. In the same conditions with standard stoker incinerator, flow pattern was not almost changed by changing inclined stoker type. 2. The injection potion and angle of secondary air had an effect on flow field in secondary combustion chamber. 3. Flow pattern was not almost changed with the variation of the flow rate of primary and secondary air injection. The results of parametric studies said that the main factors for the design are the incinerator configuration of secondary combustion chamber and/or the position and angle of secondary air injection.