• 청정기술
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• 제24권1호
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• pp.70-76
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• 2018

오거 반응기를 이용하여 해조류 바이오매스인 다시마로부터 열분해 오일 제조 실험을 수행하였으며, 열분해 오일의 물리화학적 특성을 살펴보았다. 주요 공정 변수인 열분해 온도 및 오거 컨베이어 속도의 최적 조건은 각각 $412^{\circ}C$, 20 rpm이었으며, 이 때 열분해 오일의 최대 수율은 32 wt%이었다. 낮은 탄소 함량 및 높은 산소 함량으로 인해, 다시마 유래 열분해 오일의 발열량($23.6MJ\;kg^{-1}$)은 기존 화석연료의 약 60% 이었다. 열분해 오일의 GC/MS 분석 결과, 1,4-Anhydro-d-galactitol, dianhydromannitol, 1-hydroxy 2-propanone, isosorbide 등이 주요 화합물로 확인되었다. 촤는 탄소 함량이 낮고 산소함량이 높아 발열량($13.0MJ\;kg^{-1}$)이 낮으며 다량의 무기 성분 및 황을 포함하고 있는 것으로 확인되었다.

• 청정기술
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• 제26권1호
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• pp.79-87
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• 2020

The bio-oil produced from the fast pyrolysis of lignocellulosic biomass contains a high amount of oxygenates, causing variation in the properties of bio-oil, such as instability, high acidity, and low heating value, reducing the quality of the bio-oil. Consequently, an upgrading process should be recommended ensuring that these bio-oils are widely used as fuel sources. Catalytic fast pyrolysis has attracted a great deal of attention as a promising method for producing upgraded bio-oil from biomass feedstock. In this study, the fast pyrolysis of tulip tree was performed in a bubbling fluidized-bed reactor under different reaction temperatures, with and without catalysts, to investigate the effects of pyrolysis temperature and catalysts on product yield and bio-oil quality. The system used silica sand, ferric oxides (Fe₂O₃ and Fe₃O₄), and H-ZSM-5 as the fluidized-bed material and nitrogen as the fluidizing medium. The liquid yield reached the highest value of 49.96 wt% at 450 ℃, using Fe₂O₃ catalyst, compared to 48.45 wt% for H-ZSM-5, 47.57 wt% for Fe₃O₄ and 49.03 wt% with sand. Catalysts rejected oxygen mostly as water and produced a lower amount of CO and CO₂, but a higher amount of H₂ and hydrocarbon gases. The catalytic fast pyrolysis showed a high ratio of H₂/CO than sand as a bed material.

• 유기물자원화
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• 제12권2호
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• pp.52-60
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• 2004

본 연구는 슬러지처분을 위해서 유기성페기물 감량화, 에너지 회수기술 공정시도, 자연순환형 슬러지 처분을 위한 최종 시스템개발의 기초연구이다. 본 연구는 full-규모의 건조시스템과 반자동식 로타리 킬른식 열분해로를 이용하여 실험하였다. 운전매개변수는 온도를 건조는 $160{\sim}175^{\circ}C$와 열분해온도는$450{\sim}800^{\circ}C$로 변화시켜 실험을 실행하였고, 고형물의 열분해 공정의 체류시간은 9min으로 실험을 t실행하였다. 본 연구에서 중요한 실험매개변수는 운전시간, 슬러지 수분함량, 고형물량에 따라 온도를 변화시켜 열분해특성을 연구하였다. 운전시간 9분의 일정한 상태에서 $670^{\circ}C$조건은 탄소쇄 $C_1{\sim}C_3$의 물질의 생성은 증가하였지만, $C_4{\sim}C_6$를 함유한 오일성분은 감소하는 것으로 나타났다.

• 보존과학회지
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• 제33권5호
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• pp.345-354
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• 2017

전남 진도군 소재 사찰의 보수 공사 중 벽화가 발견되어 제작기법 파악을 위해 교착제로 사용된 물질을 확인하고자 하였다. 이에 해당 벽화 시편에 대해 열분해/GC/MS와 IR 분석을 실시하였으며, 열분해/GC/MS분석은 직접 열분해와 온라인 메틸화법을 도입하였다. IR 분석에서 아교, 옻, 황칠 등 전통 교착제와 초산아크릴계 수지의 스펙트럼을 벽화시편과 비교했을 때 유사하지 않았으며, 건성유인 아마인유와 비교했을 때도 유사도가 낮았다. 벽화시편의 열분해/GC/MS 분석 결과를 옻, 황칠, 아교, 초산아크릴수지와 비교했을 때 이들 물질이 아닌 것으로 나타났다. 한편, 벽화시편에서 팔미트산, 옥타데칸산, nonanedioic acid, 옥타데센산 등 건성유에 특징적인 물질이 검출되었고, 경화 건성유와 유사한 열분해/GC/MS 크로마토그램이 관찰되었다. 따라서, 벽화는 건성유를 교착제로 사용하여 제작된 것으로 판단되었다.

• 한국수소및신에너지학회논문집
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• 제30권6호
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• pp.567-577
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• 2019

Due to the depletion of fossil fuels and environmental pollution, demand for alternative energy is gradually increasing. Among the various methods, a method to convert biomass into alternative fuel has been proposed. The bio-fuel obtained from biomass through pyrolysis process is called pyrolysis oil (PO) or bio-oil. Because PO is difficult to use directly in conventional engines due to its poor fuel properties, various methods have been proposed to upgrade pyrolysis-oil. The simplest approach is to mix it with conventional fossil fuels. However, due to their different polarity of PO and fossil fuel, direct mixing is impossible. To resolve this problem, emulsification of two fuels with a proper surfactant was proposed, but it costs additional time and cost. Alternatively, the use of alcohol fuels as an organic solvent significantly improve the fuel properties such as fuel stability, calorific value and viscosity. In this study, blends of diesel, n-butanol, and coffee ground pyrolysis oil (CGPO) which is one of the promising PO, was applied to diesel generator. Combustion and emissions characteristics of blended fuels were investigated under the entire load range. Experimental results show that ignition delay is similar to that of diesel at high load. Although, hydrocarbon and carbon monoxide emissions are comparable to diesel, significant reduction of nitrogen oxides and particulate matter emissions were observed.

• 공업화학
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• 제32권2호
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• pp.205-213
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• 2021

The present study aimed to determine the effect of co-pyrolysis of sawdust biomass and scrap tyre waste employing different blending ratios of sawdust to waste tyre such as 100:0, 75:25, 50:50, 25:75, and 0:100. The thermochemical characterization of feedstocks was carried out by employing the proximate, ultimate analysis, and thermogravimetric (TGA) analyses, calorific values, and scanning electron microscope coupled with energy dispersive x-ray analysis (SEM-EDX) to select the blending ratio having better bioenergy potential amongst the studied ratios. The blending ratio of 25:75 (sawdust to waste tyre) was selected for the co-pyrolysis study in a fixed-bed pyrolysis reactor system based on its solid biofuels properties such as heating value (30.18 MJ/kg), and carbon (71.81 wt%) and volatile matter (63.82 wt%) contents. The pyrolysis temperatures were varied as 500, 600 and 700 ℃ while the other parameters such as heating rate and nitrogen flowrate were maintained at 30 ℃/min and 0.5 L/min respectively. The bio-oil yields as 31.9, 47.1 and 61.2 wt%, bio-char yields as 34.5, 34.2 and 31.4 wt% and gaseous product yields as 33.6, 18.60 and 7.3 wt% at the pyrolysis temperatures of 500, 600 and 700 ℃ respectively were obtained. The blends of sawdust and waste tyres showed the improved energy characteristics which could provide the solution for the beneficial management of sawdust and scrape tyre wastes via co-pyrolysis processing.

• 한국기후변화학회지
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• 제8권3호
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• pp.231-237
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• 2017

In this study, the $N_2O$ emission factor of the facility was developed by measuring the kiln type pyrolysis melting facility. This used PAS (Photoacoustic Spectroscopy) method and measured the $N_2O$ emission concentration. From March 2016 to April 2016, it was measured over a total of two times and $N_2O$ concentrations were measured continuously for 24 hours using a 24 hour continuous measuring instrument (LSE-4405). The measured $N_2O$ emission concentration of the pyrolysis melting facility was 0.263 ppm on average and the emission concentration distribution in the range of 0.013~0.733 ppm was obtained. Therefore, the $N_2O$ emission factor of the kiln-type pyrolysis melting facility was estimated to be $0.829gN_2O/ton$-Waste. As a result of comparing the $N_2O$ emission factor of the thermal kiln type pyrolysis melting facility and the previous study, previous studies were about 18 times higher. It is estimated that this is due to the difference of furnace temperature, oxygen concentration and denitrification facilities. It is considered that the study of the emission factor of pyrolysis melting facility is an important factor in improving the credibility of greenhouse gas inventory in waste incineration sector.

• 한국폐기물자원순환학회지
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• 제34권5호
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• pp.518-527
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• 2017

The development of renewable energy is currently strongly required to address environmental problems such as global warming. In particular, biomass is highlighted due to its advantages. When using biomass as an energy source, the conversion process is essential. Fast pyrolysis, which is a thermochemical conversion method, is a known method of producing bio-oil. Therefore, various studies were conducted with fast pyrolysis. Most studies were conducted under a lab-scale process. Hence, scaling up is required for commercialization. However, it is difficult to find studies that address the process analysis, even though this is essential for developing a scaled-up plant. Hence, the present study carries out the process analysis of biomass pyrolysis. The fast pyrolysis system includes a biomass feeder, fast pyrolyzer, cyclone, condenser, and electrostatic precipitator (ESP). A two-stage, semi-global reaction mechanism was applied to simulate the fast pyrolysis reaction and a circulating fluidized bed reactor was selected as the fast pyrolyzer. All the equipment in the process was modeled based on heat and mass balance equations. In this study, process analysis was conducted with various reaction temperatures and residence times. The two-stage, semi-global reaction mechanism for circulating fluidized-bed reactor can be applied to simulate a scaled-up plant.

• 공업화학
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• 제22권6호
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• pp.636-641
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• 2011

1990년대 중반부터 지속적으로 산불건수가 증가하고 있으며, 그 규모 또한 대형화 되고 있다. 하지만 이러한 산불의 대형화 추세에도 낙엽, 초본류, 침엽수 및 활엽수에 따른 국 내외에는 수종별 열분해 및 연소 특성에 관한 연구가 미미한 실정이다. 본 논문에서는 국내 산림의 대표적인 침엽수인 적송의 생목과 간벌목을 대상으로 TGA를 이용 열분해 및 연소 특성에 대한 연구를 수행하였다. 적송 생목의 경우 $200^{\circ}C$ 부근에서 발화되고 열분해는 $230^{\circ}C$에서부터 시작되었다. 적송 간벌목의 경우는 발화온도와 열분해 온도가 각각 180와 $205^{\circ}C$부근에서 시작되었다. TGA 분석으로 얻은 실험데이터로부터 열분해반응에서 활성화에너지는 전화율 증가에 따라 증가하였다. 그러나 연소반응에서의 활성화에너지는 감소하는 경향을 나타냈다.

• 한국건설순환자원학회논문집
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• 제11권4호
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• pp.391-399
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• 2023

최근 증가하는 폐플라스틱의 재활용 방법으로 저온 열분해 기술이 연구되고 있다. 폐플라스틱 저온 열분해 기술은 에너지 자원으로 활용할 수 있는 열분해유를 생산하지만, 고체의 잔류물이 발생한다. 폐플라스틱 열분해 잔류물은 활용 범위가 낮아 대부분 매립 처리하고 있다. 본 연구에서는 혼합 폐플라스틱 열분해 잔류물를 활성탄으로 재활용하기 위한 연구를 수행하였다. 혼합 폐플라스틱 열분해 잔류물의 화학적 활성화를 통해 활성탄을 제조하고, 그 특성에 대해 조사하였다. 공업분석을 통해 잔류물의 고정탄소량이 33.69 %인 것으로 확인하였다. 활성탄 제조에는 화학적 활성화를 활용하였으며. 활성화제로 KOH를 사용하였다. KOH와 잔류물의 혼합비율의 영향을 조사하기 위해 0.5, 1.0, 2.0의 비율로 시료를 혼합하였다. 혼합한 시료는 활성화 온도는 800 ℃에서 1시간 동안 화학적 활성화를 진행하였다. BET를 통한 활성탄 특성 분석 결과 KOH의 혼합비율이 증가할수록 비표면적이 증가하는 것을 확인하였다.