• Proceedings of the Korean Society for Agricultural Machinery Conference
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• 2017.04a
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• pp.117-117
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• 2017

2012년 국내 총 폐기물(지정폐기물 제외) 발생량은 382,009 톤/일 으로 이 중 12.8%를 차지하는 생활폐기물 중 음식물 채소류폐기물 발생량은 13,209 톤/일 으로 이중 음식물 폐기물은 탈수 후 사료 제조 또는 매립 처리되고 있다. 본 연구에서는 고수분 음식물 쓰레기를 재활용한 고형연료 제조에 필요한 건조장치를 개발하고 실험을 통해 그 성능을 확인하고자 하였다. 본 연구를 위해 건조용량 500 kg/hr인 실험실용 열분해장치를 제작하였다. 회사 구내식당 및 창원시에서 수거된 음식물 쓰레기를 실험 원료로 사용하였다. 건조공기 투입 온도에 따른 음식물 쓰레기의 건조 특성을 파악하였다. 음식물 쓰레기 건조실험 결과, 총 건조소요시간은 약 20시간 정도로 나타났으며, 건조속도는 약 2.90 %/hr로 나타났다. 건조시간은 연구 목표치인 1회당 15시간보다 5시간 소요된 것으로 나타났으나 투입 및 배출에 소요되는 예열 및 냉각 시간을 제외하면 약 16시간으로 연구목표치에 근접한 것으로 판단된다. 투입건조공기 온도에 따른 건조시간은 큰 차이를 보이지 않았으며, 특히 $155^{\circ}C$에서 21시간으로 나타나 향후 폐열 활용 시 $200^{\circ}C$ 이상의 고온의 공기를 사용하지 않아도 건조작업이 가능함을 확인하였다. 건조시간 단축을 위해서는 투입공기의 온도보다는 투입공기와 음식물 쓰레기의 접촉 면적이 큰 영향을 끼치는 것으로 판단된다.

• Journal of The Korean Association For Science Education
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• v.24 no.2
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• pp.328-342
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• 2004

This study aims to develop STS modules which consider the local concerns of Korean society and their authentic evaluation instruments. Their titles are as follows: 'Health-Aiding Foods, are they necessary?', 'Competition between Alien and Native Species', 'Living Lesson of Lake Shihwa', and 'Problems of food wastes; Would you like to throw them away, if they are money?' All of them deal with issues unique to Korean local situations. Each module consisted of two versions; a student worksheet and a teachers' guide. Students' activities were categorized into six processes such as group activities, investigation, discussion and presentation, experiments, field trip, and multiple intelligence activities. Various assessment tools and abilities for the decision-making in their STS classes were also included. In order to validate these modules, 24 teachers who have been teaching science, biology and environmental science in the secondary schools reviewed these modules and provided feedbacks about their validity and usefulness. We expect that the various rubrics included in each module will provide teachers creative and flexible assessment methods for students' understandings and their decision-making abilities toward the issues.

• Applied Chemistry for Engineering
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• v.28 no.4
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• pp.485-489
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• 2017

Polyethylene terephthalate (PET) has been widely applied in polymers and packaging industries to produce synthetic fibers, films, drink bottles or food containers. Therefore, it has become one of the major plastic wastes. In this article, glycolysis known as one of the main methods in PET chemical recycling was investigated using a glycol to break down the polymer into a monomer. Glycolysis of PET and ethylene glycol was performed in a micro-tubing reactor under various conditions. The effect of glycolysis conditions on the product distribution was investigated at experimental conditions of the EG/PET ratio of 1~4, the reaction time of 15~90 min and the reaction temperature of $250{\sim}325^{\circ}C$ with Mn and Cu catalysts. The highest yield of bis (2-hydroxyethyl) terephthalate monomer (BHET) was obtained as 89.46 wt% under the condition of the reaction temperature of $300^{\circ}C$ and the time of 30 min using 10 wt% $Cu/{\gamma}-Al_2O_3$ catalyst, with the PET and ethylene glycol ratio of 1 : 2.

• Microbiology and Biotechnology Letters
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• v.9 no.2
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• pp.65-69
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• 1981

As a process to utilize agricultural residues, simultaneous hydrolysis-fermentation (SSF) was compared with fermentation of enzymic hydrolyzate using koji cultures of Trichoderma sp. KI 7-2 and a thermotolerant yeast Saccharomyces cerevisiae NCYC 716. Cellobiose was not detected in SSF broth whilst 15 mg/$m\ell$ of the disaccharide was found in enzymic hydrolysate of rice straw using the same enzyme source. It was found that converting glucose to ethanol in SSF process reactivated the cellobiase activity, which is inhibited by the accumulation of glucose in enzymic hydrolysis process. Cutting milled rice straw was fermented as effectively as ball milled one in SSF process. From tile results discussions are made on the product inhibition mechanism of cllulolytic enzyme system.

• 한국신재생에너지학회:학술대회논문집
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• 2011.05a
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• pp.173.1-173.1
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• 2011

The high fuel flexibility of gas turbine power system has boosted their use in a wide variety of applications. Recently, the demand for biogas generated from the digestion of organic wastes and sewage waste water as a fuel for gas turbines has increased. We investigated the performance of high pressure biogas compression system and operating conditions for supplying biogas. The total flow per minute of biogas from food waste water digestion tank is $54Nm^3$. The main type of biogas compression system is the reciprocating system and screw type system. The target of biogas mechanical data is the as belows; inlet pressure 0.045bar, supplying biogas temperature is $30{\sim}60^{\circ}C$, and final pressure is above the 25 bar. Also, inlet conditions of biogas consist of CH4 48.5%~83%, $H_2S$ Max. 500ppm, $NH_3$ Max. 1,500ppm and Siloxane 2.7~4.6ppm. The boosting Blower system raises a pressure from 0.045bar to 1bar before main compressor. The main system lay out of reciprocating consisits of compressor driver, filter, cooling system, blowdown vessel, control system and ESD(Emergency Shut Down) system. And an enclosure package needs to be installed for reducing noise up to 75dB. The system driver is the electronic motor of explosion proof type. Forthe compressor system reliable operation, the cleaning system something like particulate filter needs to be set up in the inlet of compressor and Coalescing Filter in the outlet of compressor. Particulate Filter has to be removed above $10{\mu}m$ size of the particles in biogas. The coalescing filter(Micofine Borosilicate Glass Fibers Filter treated phenol acid) also removes moisture and oil of above $0.3{\mu}m$ to be involved in high pressure biogas up to 90%~98%.

• Proceedings of the Korean Society of Dyers and Finishers Conference
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• 2012.03a
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• pp.67-67
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• 2012

식생활 및 사회 환경 변화에 따라 식품 폐기물이 많이 발생하고 있다. 이 폐기물을 처리하는 데 막대한 비용이 소요되고 환경오염도 심각한 상황이다. 이에 식품 폐기물의 자원화를 통해 자원의 부가가치를 높이고, 처리비용 절감과 함께 환경오염 방지, 새로운 유기소재의 확보 등의 효과를 볼 것으로 사료된다. 본 연구는 바나나 껍질로부터 추출한 물질의 다양한 기능성을 조사하고, 인디고의 환원제로서 유효성을 확인하여 천연염색 분야에 식품 폐기물의 활용 방안을 모색하는데 목적이 있다. 이를 위하여 바나나 껍질은 건조 후 증류수로 $100^{\circ}C$에서 1시간 동안 추출, 농축하여 분말로 만들어 사용하였다. 바나나 껍질 추출물의 기능성을 알아보기 위해 총당분석(Phenol- sulfuric method), 항산화(DPPH radicals 소거활성), 황색포도상구균에 대한 항균성 실험(Paper disc diffusion)을 하였다. 또한 인디고 염색시 화학환원제 대신 이 분말을 사용하였고, 그 환원력 측정은 환원 포텐셜과 염색 실험을 통해 평가하였다. 본 연구에서 제조한 바나나 껍질 추출물은 항산화능이 우수하였고, 높은 당 함량을 나타냈다. 황색 포도상구균에 대한 항균성을 지녀 향후 기능성 물질로서 응용가능성이 클 것으로 전망된다. 바나나껍질 추출물은 합성인디고 환원에 효과적이었다. 인디고 환원은 바나나껍질 추출물을 첨가하면서 바로 시작되고, 24시간 경과 후 최대 염착량과 최고 전압값을 나타냈다. 바나나 껍질 추출물의 농도가 높아질수록 인디고 환원력은 높아지고 염착량도 증가하는 것으로 나타났다. 따라서 바나나 껍질 추출물은 인디고 환원에서 화학물질인 하이드로설파이트를 대체하여 사용할 수 있는 효과적인 천연유기환원제로 사용할 수 있을 것으로 기대된다.

• KSBB Journal
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• v.24 no.1
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• pp.70-74
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• 2009

For continuous culture of cellulolytic enzymes production to saccharify food wastes, refill concentration of Mandel's medium for continuous culture was 0.5%, and refill intervals were determined to 12 hours by analysis of COD and total nitrogen concentration after 4-days batch culture in flask level. As a result, amylase and FPase productivities were 3.5 and 1.0 U/L.hr, respectively. In 10 L bioreactor, the batch culture mode was compared with fed-batch, fill-and-draw for continuous production of cellulolytic enzyme. Enzyme productivities were most high at batch culture and followed by fed-batch culture. Amylase and FPase activities were 42.3 and 5.6 U/L.hr at batch culture, and 23.0, 2.8 U/L.hr at fed-batch culture, respectively. As a result, in continuous cultivation of cellulolytic enzymes by T. inhamatum KSJ1, the mode of fed-batch was most effective in 10 L bioreactor.

• The Korean Journal of Mycology
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• v.20 no.4
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• pp.354-359
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• 1992

The effect of the addition of various vegetable oils on the mycelial growth was studied. Most vegetable oils were proved to be stimulative for the mycelial growth, and the best mycelial growth (12 mg/ml) was obtained with the addition of cotton seed oil. Several agricultural wastes i.e., rice straw, peanut hull, sawdust, rice hull, cocoa hull, coffee waste and beer waste were empolyed as substrates for sporophore production of p. sajor-caju. The biological efficiency(BE) for sporophore productions of rice straw and peanut hull were 36.4% and 32.6%, respectively. The highest yield of sporophore was obtained from the mixture of rice straw (50%) and beer waste (50%)(BE 109.6%) followed by peanut hull (50%) and beer waste (50%)(BE; 74.5%).

• Environmental Engineering Research
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• v.24 no.4
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• pp.662-669
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• 2019

Anaerobic digestion is a popular sewage sludge (Ss) treatment method as it provides significant pollution control and energy recovery. However, the low C/N ratio and poor biodegradability of Ss necessitate pretreatment methods that improve solubilization under anaerobic conditions in addition to anaerobic co-digestion with other substrates to improve the process efficiency. In this study, three pretreatment methods, namely microwave irradiation, ultrasonication, and heat treatment, were investigated, and the corresponding improvement in methane production was assessed. Additionally, the simplex centroid design method was utilized to determine the optimum mixture ratio of food waste (Fw), livestock manure (Lm), and Ss for maximum methane yield. Microwave irradiation at 700 W for 6 min yielded the highest biodegradability (62.0%), solubilization efficiency (59.7%), and methane production (329 mL/g VS). The optimum mixture ratio following pretreatment was 61.3% pretreated Ss, 28.6% Fw, and 10.1% Lm. The optimum mixture ratio without pretreatment was 33.6% un-pretreated Ss, 46.0% Fw, and 20.4% Lm. These results indicate that the choice of pretreatment method plays an important role in efficient anaerobic digestion and can be applied in operational plants to enhance methane production. Co-digestion of Ss with Fw and Lm was also beneficial.

• Journal of Hydrogen and New Energy
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• v.27 no.5
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• pp.554-561
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• 2016

Depending on the Bio-gas sources, main component gases of $CH_4$ and $CO_2$ are shown to be variously present in amounts. For the anaerobic digester, The concentration of $CH_4$ and $CO_2$ in the gases are 60~70 and 30~35 vol%. For the landfill gas, $CH_4$ and $CO_2$ are 40~60 and 40~60 vol%. For the food wastes, $CH_4$ and $CO_2$ are 60~80 and 20~40 vol%, respectively. In this study, maximum conversion rates of $CO_2$ were obtained from the variety of concentrations of $CH_4$ and $CO_2$ by the catalysts of reforming reactions. Moreover, in order to get maximum producing amount of synthetic gas, experimental studies were performed to optimize the reaction variables. On the basis of $CH_4$, 243 ml, R [$CH_4/(O2+CO_2)$] value were varied from 0.8 to 1.35, in the study of $CH_4$ and $CO_2$ reforming reactions. It was shown that the optimal results were obtained for 1.35 of R value. And also, at $850^{\circ}C$ and 1 atm, the production rate of synthetic gas was 90% and the conversion rates of $CH_4$ and $CO_2$ were higher than 99% and 90%, respectively.