• Journal of Korean Society of Environmental Engineers
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• v.37 no.11
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• pp.636-641
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• 2015

Waste energy conversion to SRF (Solid Refuse Fuel) has the effects not alternative fossil fuel usage but also the reduction of greenhouse gas. But the direct burning of the SRF including a plastic waste generates air pollution problem like soot, dioxin, etc. so that an application of pyrolysis and gasification treatment should be needed. The purpose of this study is to supply a basic thermal data of the pyrolysis gasification characteristics in the plastic-rich SRF which are needed for developing the novel pyrolyser or gasifier. To do so, a bench-scale test rig was newly engineered, and then experiments were achieved for the production characteristics of gas, tar, and char. While SRF sample, gasification air ratio, holding time changed as 2 g, 0.691, 32 min respectively, the $H_2$ 1.36%, $CH_4$ 2.18%, CO 1.88%, $Cl_2$ 15.9 ppm, HCl 6.4 ppm were composed. Also light tar benzene $4.03g/m^3$, naphthalene $0.39g/m^3$, anthracene $0.11g/m^3$, pyrene $0.06g/m^3$, gravimetric tar $18g/m^3$, and char 0.29 g was formed.

• The Magazine of the Society of Air-Conditioning and Refrigerating Engineers of Korea
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• v.34 no.5
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• pp.47-54
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• 2005

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 2003.11a
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• pp.21-24
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• 2003

• Proceedings of the KIEE Conference
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• 2002.07c
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• pp.1820-1822
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• 2002

본 논문에서는 반도체 제조공정에서 발생하는 $CF_4$의 분해와 제거를 위하여 3상 교류 플라즈마 토치를 제작하고, 플라즈마를 발생시켜 $CF_4$제거 가능성과 이에 따른 문제점에 대해 알아보았다. 매우 강하고 안정한 C-F 결합을 깨고 $CF_4$가스를 분해하기 위해서는 1100[$^{\circ}C$]정도의 고온이 필요한데, 본 실험의 플라즈마 플레임의 경우 $CF_4$가스를 열분해 광분해 시키기에는 충분한 온도와 에너지를 가지고 있다고 사료된다. 하지만 고온의 플라즈마와 토치 내부의 복잡한 유동과 고온의 플라즈마에 의한 전극의 융삭문제는 플라즈마를 연속적으로 발생시켜 $CF_4$가스의 제거효율을 높이기 위해서는 필히 개선해야 할 문제점인 것으로 사료된다.

• Proceedings of the Korean Vacuum Society Conference
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• 2013.08a
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• pp.169.1-169.1
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• 2013

산업 및 기술의 발전에 의해 많은 신소재들이 개발되고 있다. 그 중에서 SiC는 고온재료, LED, 반도체 등의 우주선 표면재료, 핵융합로 구조재료, 고온 씰, 히터 등 여러 산업분야에서 관심을 가지면서 다양한 가스를 이용한 합성법이 개발되어 있다. 최근에는 분말의 형태 및 크기를 용도에 맞게 개발해서 사용하고 있는 상황이다. 그런데 각 합성법에 따른 합성원리에 대해서는 여러 가지 주장이 있다. 그 중에서 몇 가지 합성법에 대해서 고찰하고 합성의 원리를 추론한다. 그리고 그 중의 한 가지인 CH3SiCl3 가스를 이용한 SiC 나노분말 합성과 SiC의 결정성장 과정에서 나타나는 whisker의 형성을 확인했다. 정교한 SiC 분말합성은 일반적으로 sol-gel, 플라즈마(DC, AC 및 ICP 등) 등을 이용한 방법이 개발되어 있다. 이와 같이 정교한 SiC 나노분말 등은 실리콘 유기 화합물 중합체(trichloromethylsilane, polycarbosilane 등)의 열분해를 통해 합성 할 수 있으며, 열분해 는 약 1,000{\sim}1,500^{\circ}C의 온도 영역에서 일어난다. 이 과정에서 고분자의 열분해 및 재결합 이 동반되고 부산물로서 HCl, CH4 등의 유해가스를 같이 생성한다. 합성된 SiC 나노분말은 전형적인 ${\beta}-SiC$로 XRD의 관찰결과 (111), (220), (311)의 방향성을 갖는 것을 확인했으며 평균입자의 크기는 약 30 nm 정도다.

• Proceedings of the KSME Conference
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• 2007.05b
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• pp.3435-3439
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• 2007

The aim of this study is to find out the condition that generates maximum $H_2$ through the calculation of equilibrium model with conditions of pyrolysis gases of Refuse Plastic Fuel(RPF). This study deals with the computational simulation of a RPF gasification using an equilibrium model based on minimization of the Gibbs free energy. An equilibrium analysis was carried out to determine species composition of Syngas in RPF gasification and reactions to variation of temperature, $O_2$/Fuel ratio and Steam/Fuel ratio. Calculated results showed that $O_2$/Fuel ratio, Steam/Fuel ratio and temperature affected on mole fraction of $H_2$, CO.

• Journal of the Korean Society of Combustion
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• v.12 no.4
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• pp.57-61
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• 2007

The aim of this study is to find out the condition that generates maximum $H_2$ through the calculation of equilibrium model with conditions of pyrolysis gases of Refuse Plastic Fuel(RPF). This study deals with the computational simulation of a RPF gasification using an equilibrium model based on minimization of the Gibbs free energy. An equilibrium analysis was carried out to determine species composition of Syngas in RPF gasification and reactions to variation of temperature, $O_2/Fuel$ ratio and Steam/Fuel ratio. Calculated results shows that hydrocarbons in pyrolyzed gas are converted to synthesis gas which is formed on hydrogen and carbon monoxide.

• Korean Chemical Engineering Research
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• v.49 no.4
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• pp.417-422
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• 2011

The low temperature pyrolysis of ABS resin has been carried out in a batch reactor under the atmospheric pressure. The effect of the reaction temperature on the yield of pyrolytic oils has been determined in the present study. The oil products formed during pyrolysis were classified into gas, gasoline, kerosene, gas oil and heavy oil according to the petroleum product quality standard of Ministry of Knowledge Economy. The conversion reaches 80% after 60 min at $500^{\circ}C$ in the pyrolysis of ABS resin. The amount of the final product was ranked as gas heavy oil > gasoline > gas oil > kerosen based on the yield. The yields of heavy oil and gas oil increase with an increase in the reaction time and temperature.

• Korean Chemical Engineering Research
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• v.62 no.1
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• pp.36-43
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• 2024

Fishing net waste (FNW) constitutes over half of all marine plastic waste and is a major contributor to the degradation of marine ecosystems. While current treatment options for FNW include incineration, landfilling, and mechanical recycling, these methods often result in low-value products and pollutant emissions. Importantly, FNWs, comprised of plastic polymers, can be converted into valuable resources like syngas and pyrolysis oil through pyrolysis. Thus, this study presents a process for generating high-purity hydrogen (H₂) by catalytically pyrolyzing FNW in a CO₂ environment. The proposed process comprises of three stages: First, the pretreated FNW undergoes Ni/SiO₂ catalytic pyrolysis under CO₂ conditions to produce syngas and pyrolysis oil. Second, the produced pyrolysis oil is incinerated and repurposed as an energy source for the pyrolysis reaction. Lastly, the syngas is transformed into high-purity H₂ via the Water-Gas-Shift (WGS) reaction and Pressure Swing Adsorption (PSA). This study compares the results of the proposed process with those of traditional pyrolysis conducted under N₂ conditions. Simulation results show that pyrolyzing 500 kg/h of FNW produced 2.933 kmol/h of high-purity H₂ under N₂ conditions and 3.605 kmol/h of high-purity H₂ under CO₂ conditions. Furthermore, pyrolysis under CO₂ conditions improved CO production, increasing H₂ output. Additionally, the CO₂ emissions were reduced by 89.8% compared to N₂ conditions due to the capture and utilization of CO₂ released during the process. Therefore, the proposed process under CO₂ conditions can efficiently recycle FNW and generate eco-friendly hydrogen product.

• Proceedings of the Korean Institute of Resources Recycling Conference
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• 2005.10a
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• pp.75-82
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• 2005

Pyrolysis of biomass is one of the promising methods to obtain energy and valuable chemical stocks. Fast pyrolysis of Q. acutissima and L. letolepis has been carried out in a bubbling fluidized bed reactor to determine the optimum operating conditions of the pyrolyzer. Effects of reaction temperature, Uo/Umf, L/D ratio, and feed rate have been determined and the optimum conditions are as follows: $T\;=\;400^{\circ}C,\;U_o/U_{mf}\;=\;3.0,\;L/D\;=\;2.0$. Maximum yield of bio-oil was about 55% and the main compositions were carbohydrates, guaiacols, furans, phenols, and syringols. Product gas was consists of CO, $CO_2$, light hydrocarbons and the measured gas yield using the compositions agreed with the calculated value.