톱밥과 여과 탈수 폐오일슬러지의 고형연료 제조 및 열분해 특성

이주용,배성근,서정윤 한국폐기물자원순환학회 2014 한국폐기물자원순환학회지 Vol.31 No.8

The large amount of waste oil sludge was generated from waste oil purification process, oil bunker, or the ocean plant. Although it has high calorific values, it should be treated as a designated waste. During the recycling process of construction and demolition wastes or the trimming process of woods, a lot of sawdust is produced. In this study, the feasibility of BOF (biomass and waste oil sludge fuel) as a renewable energy source was estimated. For manufacturing a BOF, a press type pelletizing was better than an extruder type and also 40 ~ 60% of mixing ratio in waste oil sludge was appropriate to produce a pellet. The pellet was 13 mm in diameter and 20 mm in length. There was no fixed carbon in waste oil sludge, and its carbon content and higher heating value were 63.90% and 9,110 kcal/kg, respectively. With an increse of mixing ratio of sawdust, the carbon content and heating value of the BOF were dropped, but fixed carbon content was increased. The heating value of BOF was in the range of 6,400 ~ 7,970 kcal/kg at the mixing ratio of 40 ~ 60% in waste oil sludge. It means that the BOF can be classified as the 1stgrade solid fuel. In TGA experiment carried out at heating rate of 10oC/min and under nitrogen atmosphere, thermal decomposition of sawdust was occurred in two steps, but waste oil sludge was destructed in one step. The initiated cracking temperature of sawdust and waste oil sludge was 300 and 280oC in respective and after 450oC the thermal decomposition process of sawdust was slowly progressed by 800oC in contrast to waste oil sludge. Thermal decomposition of waste oil sludge was finished around 600oC. It can be considered that this difference is due to the fixed carbon content. Thermal decomposition pattern for the pellet of mixing ratio over 50% in waste oil sludge was similar to that for waste oil sludge and thermal cracking was occurred between 300 and 350oC. As the mixing ratio of waste oil sludge in the pellet increased, the reaction of thermal cracking became fast.

톱밥과 여과 탈수 폐오일슬러지의 고형연료 제조 및 열분해 특성

이주용,배성근,서정윤 한국폐기물자원순환학회 2014 한국폐기물자원순환학회지 Vol.31 No.8

The large amount of waste oil sludge was generated from waste oil purification process, oil bunker, or the ocean plant. Although it has high calorific values, it should be treated as a designated waste. During the recycling process of construction and demolition wastes or the trimming process of woods, a lot of sawdust is produced. In this study, the feasibility of BOF (biomass and waste oil sludge fuel) as a renewable energy source was estimated. For manufacturing a BOF, a press type pelletizing was better than an extruder type and also 40 ~ 60% of mixing ratio in waste oil sludge was appropriate to produce a pellet. The pellet was 13 mm in diameter and 20 mm in length. There was no fixed carbon in waste oil sludge, and its carbon content and higher heating value were 63.90% and 9,110 kcal/kg, respectively. With an increse of mixing ratio of sawdust, the carbon content and heating value of the BOF were dropped, but fixed carbon content was increased. The heating value of BOF was in the range of 6,400 ~ 7,970 kcal/kg at the mixing ratio of 40 ~ 60% in waste oil sludge. It means that the BOF can be classified as the 1stgrade solid fuel. In TGA experiment carried out at heating rate of 10oC/min and under nitrogen atmosphere, thermal decomposition of sawdust was occurred in two steps, but waste oil sludge was destructed in one step. The initiated cracking temperature of sawdust and waste oil sludge was 300 and 280oC in respective and after 450oC the thermal decomposition process of sawdust was slowly progressed by 800oC in contrast to waste oil sludge. Thermal decomposition of waste oil sludge was finished around 600oC. It can be considered that this difference is due to the fixed carbon content. Thermal decomposition pattern for the pellet of mixing ratio over 50% in waste oil sludge was similar to that for waste oil sludge and thermal cracking was occurred between 300 and 350oC. As the mixing ratio of waste oil sludge in the pellet increased, the reaction of thermal cracking became fast.

톱밥과 여과 폐중유슬러지의 고형연료 연소 특성

이주용,서정윤 한국폐기물자원순환학회 2015 한국폐기물자원순환학회지 Vol.32 No.1

Waste heavy oil sludge is considered oil waste that can be utilized as a renewable energy source. Although it has high calorific values, it should be treated as a designated waste. During the recycling process of construction and demolition wastes or the trimming process of woods, a lot of sawdust is produced. In this study, the feasibility of BOF (biomass and waste heavy oil sludge fuel) as a source of renewable energy was estimated. To investigate its combustion characteristics, a lab scale batch type combustion reactor was used, and temperature fluctuation and the flue gas composition were measured for various experimental conditions. The results could be summarized as follows: The solid fuel pellets manufactured from waste heavy oil sludge and sawdust had C 50.21 ~ 54.77%, H 10.25 ~ 12.66%, O 25.84 ~ 34.83%, N 1.01 ~ 1.04%, S 1.03 ~ 1.07%. Their lower heating values ranged from 4,780 kg/kcal to 5,530 kg/kcal. The density of the solid fuel pellets was increased from 0.63 g/cm3 to 0.85 g/cm3 with increasing the mixing ratio of waste heavy oil sludge. The maximum CO2 concentration in the flue gas was increased with increasing waste heavy oil sludge content in BOF. SO2 concentration in the flue gas was showed a tendency such as the highest CO2 concentration in the flue gas. With increasing waste heavy oil sludge content in BOF, the combustion time became rather shorter although the increase of the CO2 concentration in the flue gas was delayed. Because the carbon conversion rate showed small difference with increasing the mixing ratio of waste heavy oil sludge in BOF, BOF with the mixing ratio of waste heavy oil sludge of 30% was effective for combustion. With increasing the mixing ratio of waste heavy oil sludge in BOF, activation energy and the amount of total CO emissions were increased, while activation energy was decreased with increasing the air/fuel ratio. Therefore, the optimal air/fuel ratio for the combustion of BOF was 1.5.

파일럿 규모 버너에서 커피찌꺼기 바이오원유 및 폐스티로폼 열분해오일 혼합연료의 연소특성

최상규 ( Sang-kyu Choi ),최연석 ( Yeon-seok Choi ),정연우 ( Yeon-woo Jeong ),한소영 ( So-young Han ),응웬반꾸잉 ( Quynh Van Nguyen ) 한국폐기물자원순환학회 2020 한국폐기물자원순환학회지 Vol.37 No.8

The combustion characteristics of mixed fuels, consisting of bio-crude oil from coffee grounds and pyrolysis oil from polystyrene foam waste, were studied in a pilot-scale burner, along with blends of pyrolysis oil from polystyrene foam waste and kerosene. The used burner system was previously developed for bio-crude oil combustion; thus, it was equipped with an air-blast atomizing nozzle and adopted downward injection. The mixture of bio-crude oil from coffee grounds and kerosene exhibited a distinct phase separation and could not be placed into the burner directly. The bio-crude oil was heated before being supplied to the fuel nozzle due to its high viscosity, while the blends of pyrolysis oil from polystyrene foam waste did not require preheating because they were less viscous. Under atmospheric conditions, the pyrolysis oil from polystyrene foam waste was blended at least 50% to prevent incomplete combustion. The blends of bio-crude oil from coffee grounds and pyrolysis oil from polystyrene foam waste emitted relatively more NO due to the fuel-bound nitrogen in bio-crude oil. When kerosene was mixed with the pyrolysis oil from polystyrene foam waste, the flame temperature generally increased while the CO emission initially increased drastically and then decreased. The NO emission decreased with the kerosene mixing ratio, which might be attributed to the combined effect of fuel-bound nitrogen and other NO formation mechanisms.

고체 산 촉매를 이용한 고산가 음폐유의 에스테르화 반응 동역학 연구 및 반응 최적화

이화성(Hwa Sung Lee),이준표(Joon Pyo Lee),이진석(Jin Suk Lee),김덕근(Deog Keun Kim) 한국유화학회 2017 한국응용과학기술학회지 Vol.34 No.3

지구 온난화, 석유고갈, 환경오염에 대한 해결 방안으로 수송부분에서 국제적으로 바이오연료에 관한 연구가 활발하게 이루어지고 있다. 그 중 바이오디젤은 석유계 디젤과 비교해 이산화탄소 및 대기오염 물질 배출이 적고 세탄가가 높은 장점을 가지고 있다. 현재 국내 바이오디젤 수요는 지속적으로 증가하고 있으나 원료부족으로 인해 수입의존도가 커지고 있는 상황이다. 이러한 문제를 해결하기 위해 본 연구는 현재 사용되지 않는 음폐유(약 33 % 유리지방산 함유)를 Amberlyst-15 촉매가 이용한 에스테르화 반응을 통해 바이오디젤 원료로서 활용가능성을 확인 하였다. 다양한 반응 조건의 영향을 조사하기 위한 실험을 수행한 결과 반응온도 383 K에서 97.62 %의 전환율을 얻었으며, 반응속도는 353 K에서 373 K로 증가 할 때 최대 1.99 배까지 상승하였다. 또한 동역학적 결과를 이용하여 29.75 kJ/mol의 활성화 에너지를 확인하여 선행연구에서 연구된 타 고체촉매에 비해 에스테르화반응에 Amberlyst-15 더 적합함을 확인하였다. 그리고 메탄올 몰 비가 증가함에 따라 최대 91.43 %의 반응 전환율을 확인하였고, 촉매량 영향의 경우 0 wt%에서 20 wt%까지 증가시킨 결과반응 전환율이 43.78 %에서 94.62 %까지, 초기 반응 속도는 1.1∼1.4 배로 상승하는 것을 확인하였다. 교반속도의 경우 100∼900 rpm의 조건에 따라 실험을 수행하였으나 반응 전환율에는 큰 영향을 주지 않음을 확인하였고 반응 시간에 따른 영향의 경우 240 분 까지 산가 감소를 보이다가 300 분이 지나면서부터 산가가 상승하는 결과를 가져왔다. 그리고 위 실험들을 통해 도출된 최적 조건을 적용하여 음폐유 에스테르화 반응에 적용하였고 그 결과 반응시간 60 분에서 음폐유와 모사 폐유지간의 13 %의 반응 전환율 차이를 보였으나 최종 240 분 반응 전환율은 모사 폐유지 98.12 %, 음폐유는 97.62 %로 거의 유사한 결과를 얻었다. Transport biofuels have been recognized as a promising means to resolve the following issues like global warming, oil depletion and environmental pollutions. Among various biofuels, biodiesel has several advantages such as less emission of air pollutants and higher cetane values compared to diesel oil. Demand for biodiesel in Korea is increasing that leads to higher dependence on the imported feedstocks. Therefore, it is important to utilize the waste materials collected domestically for biodiesel production. Food waste oil collected in waste treatment facility has not been used for biodiesel production due to high free fatty contents in the oil. In this work, biodiesel conversion of food waste oil by Amberlyst 15 was studied. Synthetic and actual food waste oils have been used in the study. First, the effects of the major operating parameters including reaction temperature, methanol to oil molar ratio and catalyst loading on the conversion rates and yields were determined with synthetic waste oil. Kinetic modelling work was also done to determine the activation energy of the reaction. From the work, optimization reaction conditions were determined to be 383K, 1: 26.1 for methanol molar ratio to oil, 10 wt.% for catalyst loading and 360 min for reaction time. Activation energy of the reaction is determined to be 29.75 kJ/mol, lower than those reported in the previous works. So the solid catalyst, Amberlyst 15, was more efficient for esterification than the solid catalysts employed in the other works. Agitation rates have the negligible effects on the conversion rates and yields. With the identified optimization conditions, conversion of the actual food waste oil was also carried out. The esterification yield of actual food waste oil in 60 min was 13% lower than that of synthetic waste oil but the final yields in 240 min were similar each other, 98.12% for synthetic oil and 97.62% for actual waste oil.

Viscosity Characteristics of Waste Cooking Oil with Ultrasonic Energy Irradiation

김태한,한정근 한국농업기계학회 2012 바이오시스템공학 Vol.37 No.6

Purpose: While rapeseed oil, soy bean oil, palm oil and waste cooking oil are being used for biodiesel, the viscosity of them should be lowered for fuel. The most widely used method of decreasing the viscosity of vegetable oil is to convert the vegetable oil into fatty acid methyl ester but is too expensive. This experiment uses ultrasonic energy, instead of converting the vegetable oil into fatty acid methyl ester, to lower the viscosity of the waste cooking oil. Methods: For irradiation treatment, the sample in a beaker was irradiated with ultrasonic energy and the viscosity and temperature were measured with a viscometer. For heating treatment, the sample in a beaker was heated and the viscosity and temperature were measured with a viscometer. Kinematic viscosity was calculated by dividing absolute viscosity with density. Results: The kinematic viscosity of waste cooking oil and cooking oil are up to ten times as high as that of light oil at room temperature. However, the difference of two types of oil decreased by four times as the temperature increased over 83oC. When the viscosity by the treatment of ultrasonic energy irradiation was compared to one by the heating treatment to the waste cooking oil, the viscosity by the treatment of ultrasonic energy irradiation was lower by maximum of 22% and minimum of 12%, than one by the heating treatment. Conclusions: Ultrasonic energy irradiation lowered the viscosity more than the heating treatment did, and ultrasonic energy irradiation has an enormous effect on fuel reforming.

톱밥과 여과 탈수 폐오일슬러지의 고형연료 연소특성

이주용,배성근,서정윤 한국폐기물자원순환학회 2014 한국폐기물자원순환학회지 Vol.31 No.8

Waste oil sludge was generated from waste oil purification process, oil bunker, or the ocean plant. Although it has high calorific values, it should be treated as a designated waste. During the recycling process of construction and demolition wastes or the trimming process of woods, a lot of sawdust is produced. In this study, the feasibility of BOF (biomass and waste oil sludge Fuel) as a source of renewable energy was estimated. To estimate combustion characteristics, a lab scale batch type combustion reactor was used and temperature fluctuation and the flue gas composition were measured for various experimental conditions. The results could be summarized as follows: the maximum CO2 concentration in the flue gas was increased with increasing waste oil sludge content in BOF. SO2 concentration in the flue gas was showed a tendency such as the highest CO2 concentration in the flue gas. With increasing waste oil sludge content in BOF, the combustion time was rather shorter although the increase of the CO2 concentration in the flue gas was delayed. Because the carbon conversion rate showed small difference with increasing the mixing ratio of waste oil sludge in BOF, BOF with the mixing ratio of waste oil sludge of 40% was effective for combustion. With decreasing the air/fuel ratio and the mixing ratio of waste oil sludge in BOF, activation energy and frequency factor were increased. The optimal air/fuel ratio for the combustion of BOF was 1.5.

재생연료유 원료물질의 성상분석을 통한 재활용 가능성 평가

박준석,김정대 한국폐기물자원순환학회 2012 한국폐기물자원순환학회지 Vol.29 No.8

This research was performed to evaluate the physicochemical characteristics of waste oil, waste solvent, and waste paint as waste derived fuel (WDF) feeding materials and WDF. Low heating values (LHVs) were in the ranges of 8,313.8 ~ 10,989.5 kcal/kg for waste oil, 4,109.1 ~ 9,890.6 kcal/kg for waste solvent, 5,733.7 ~ 8,051.0 kcal/kg for waste paint, and 5,184.2 ~ 10,679.0 kcal/kg for WDF. Sulfur contents showed 0.010 ~ 1.900% for waste oil, 0.000 ~ 0.073% for waste solvent, 0.004 ~ 0.581% for waste paint, and 0.001 ~ 0.700%, respectively. Chloride contents showed the ranges of 2 ~ 4,870 mg/kg for waste oil, 0 ~ 12,900 mg/kg for waste solvent, 0 ~ 10,700 mg/kg for waste paint, and 'not detected' ~ 4,070 mg/kg for WDF. Cd, As, and Hg were detected minimally in a few sample only. Other heavy metals showed below standard permission value for WDF. Feeding materials for WDF showed greatly different characteristics within even same sorts of wastes. And, as results of LHV, S, Cl, and heavy metal contents, WDF samples investigated in this research satisfied the standard permission value for WDF.

Viscosity Characteristics of Waste Cooking Oil with Ultrasonic Energy Irradiation

Kim, Tae Han,Han, Jung Keun Korean Society for Agricultural Machinery 2012 바이오시스템공학 Vol.37 No.6

Purpose: While rapeseed oil, soy bean oil, palm oil and waste cooking oil are being used for biodiesel, the viscosity of them should be lowered for fuel. The most widely used method of decreasing the viscosity of vegetable oil is to convert the vegetable oil into fatty acid methyl ester but is too expensive. This experiment uses ultrasonic energy, instead of converting the vegetable oil into fatty acid methyl ester, to lower the viscosity of the waste cooking oil. Methods: For irradiation treatment, the sample in a beaker was irradiated with ultrasonic energy and the viscosity and temperature were measured with a viscometer. For heating treatment, the sample in a beaker was heated and the viscosity and temperature were measured with a viscometer. Kinematic viscosity was calculated by dividing absolute viscosity with density. Results: The kinematic viscosity of waste cooking oil and cooking oil are up to ten times as high as that of light oil at room temperature. However, the difference of two types of oil decreased by four times as the temperature increased over $83^{\circ}C$. When the viscosity by the treatment of ultrasonic energy irradiation was compared to one by the heating treatment to the waste cooking oil, the viscosity by the treatment of ultrasonic energy irradiation was lower by maximum of 22% and minimum of 12%, than one by the heating treatment. Conclusions: Ultrasonic energy irradiation lowered the viscosity more than the heating treatment did, and ultrasonic energy irradiation has an enormous effect on fuel reforming.

톱밥과 여과 탈수 폐오일슬러지의 고형연료 연소특성

이주용,배성근,서정윤 한국폐기물자원순환학회 2014 한국폐기물자원순환학회지 Vol.31 No.8

Waste oil sludge was generated from waste oil purification process, oil bunker, or the ocean plant. Although it has high calorific values, it should be treated as a designated waste. During the recycling process of construction and demolition wastes or the trimming process of woods, a lot of sawdust is produced. In this study, the feasibility of BOF (biomass and waste oil sludge Fuel) as a source of renewable energy was estimated. To estimate combustion characteristics, a lab scale batch type combustion reactor was used and temperature fluctuation and the flue gas composition were measured for various experimental conditions. The results could be summarized as follows: the maximum CO2 concentration in the flue gas was increased with increasing waste oil sludge content in BOF. SO2 concentration in the flue gas was showed a tendency such as the highest CO2 concentration in the flue gas. With increasing waste oil sludge content in BOF, the combustion time was rather shorter although the increase of the CO2 concentration in the flue gas was delayed. Because the carbon conversion rate showed small difference with increasing the mixing ratio of waste oil sludge in BOF, BOF with the mixing ratio of waste oil sludge of 40% was effective for combustion. With decreasing the air/fuel ratio and the mixing ratio of waste oil sludge in BOF, activation energy and frequency factor were increased. The optimal air/fuel ratio for the combustion of BOF was 1.5.