• 한국토양비료학회지
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• 제18권4호
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• pp.325-335
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• 1985

농산폐유기물(農産廢有機物)을 원료(原料)로한 메탄가스시설(施設)을 Philippine소재(所在) 국제미작연구소(國際米作硏究所)에 설치(設置)하여 가스발생량(發生量 ) 시험(試驗)을 한 결과(結果)는 다음과 같다. 1. 원료(原料) 자원별(資源別) 메탄가스발생량조사(發生量調査) 가. 볏짚, 왕겨, 옥수수줄기 및 야자수열매껍질은 분요혼합(糞尿混合)으로 가스발생량(發生量)이 증대되었음. 나. 야자수열매껍질을 1주일(週日) 호기발효(好氣醱酵)시킨후(後) 메탄발효원(醱酵源)으로 활용(活用)한 결과(結果)는 무처리(無處理)에 비(比)하여 가스발생량(發生量)이 증대되었음. 다. 볏짚을 메탄발효원료(醱酵原料)로 활용(活用)한 결과(結果) 전처리(前處理)한 볏짚에 비(比)해 가스발생량(發生量)이 증대되었으며 발생기간(發生期間)도 연장(延長)되었음. 라. 질소함량(窒素含量)이 높은 Azolla는 분뇨대신(糞尿代身) 메탄발효원(醱酵源)으로 활용(活用)이 가능(可能)하였음. 마. 메탄발효액(醱酵液)의 pH 6이하(以下)에서는 가스발생(發生)이 어려웠음. 2. 취사용(炊事用) 매탄가스시설(施設) 가스발생기간(發生期間) 연장시험(延長試驗) 가. 볏짚괴(塊)(Compact straw)분뇨혼합처리(糞尿混合處理)는 볏짚 (Loose straw)분뇨혼합처리(糞尿混合處理)에 비(比)하여 원료(原料) 투입(投入) 및 제거작업(除去作業)이 용이(容易)하였으나 가스발생량(發生量)이 다소(多少)낮았음. 나. 볏짚분뇨(糞尿)를 혼합(混合)하여 메탄발효(醱酵)시킨 결과(結果), 6인가족(人家族) 취사이용(炊事利用)이 가능(可能)한 가스는 70일(日) 발생(發生)되었음. 다. 발효조(醱酵槽)를 지하(地下)에 매설(埋設)하고 그늘시설(施設)을 한 결과(結果) 발효액온(醱酵液溫)이 일정(一定)하게 유지(維持)되어 가스발생량(發生量)이 증대되고 발전기간(發全期間)도 연장(延長)되었음. 3 경제성분석(經濟性分析) 가. 3,600Kcal로 환산한 메탄가스 생산비용(生産費用)은 0.14불(弗)/$m^3$로 같은 열량(熱量)인 LPG 0.54불(弗)/kg, 석유(石油) 0.32불(弗)/kg보다 낮았음. 나. 메탄발효(醱酵)로 유기질비료생산(有機質肥料生産), 공해방지(公害防止) 및 가스사용(使用)이 편리(便利)한 점(點)을 감안한다면 메탄가스는 타연료(他燃料)에 비(比)해 가장 유효한 대체(代替)에너지임.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2010년도 추계학술대회 초록집
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• pp.101-101
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• 2010

Anaerobic digestion(AD) is the most promising method for treating and recycling of different organic wastes, such as organic fraction of municipal solid waste, household wastes, animal manure, agro-industrial wastes, industrial organic wastes and sewage sludge. During AD, i.e. organic materials are decomposed by anaerobic forming bacteria and fina1ly converted to excellent fertilizer and biogas which is a mixture of carbon dioxide and methane. AD has been one of the leading technologies that can make a large contribution to produce renewable energy and to reduce $CO_2$ and other green-house gas(GHG) emission, it is becoming a key method for both waste treatment and recovery of a renewable fuel and other valuable co-products. Currently some 80% of the world's overall energy supply of about 400 EJ per year in derived from fossil fuels. Nevertheless roughly 10~15% of this demand is covered by biomass resources, making biomass by far the most important renewable energy source used to date. The representative biofuels produced from the biomass are bioethanol, biodiesel and biogas, and currently biogas plays a smaller than other biofuels but steadily growing role. Traditionally anaerobic digestion applied for different biowaste e.g. sewage sludge, manure, other organic wastes treatment and stabilization, biogas has become a well established energy resource. However, the biowaste are fairly limited in respect to the production and utilization as renewable source, but the plant biomass, the so called "energy crops" are used for more biogas production in EU countries and the investigation on the biomethane potential of different crops and plant materials have been carried out. In Korea, with steadily increasing oil prices and improved environmental regulations, since 2005 anaerobic digestion was again stimulated, especially on the biogasification of different biowastes and agro-industrial biomass including "energy crops". This study have been carried out to investigate anaerobic biodegradability by the biochemical methane potential(BMP) test of animal manures, different forage crops i.e. "energy crops", plant and industrial organic wastes in the condition of thermophilic temperature, The biodegradability of animal manure were 63.2% and 58.2% with $315m^3CH_4/tonVS$ of cattle slurry and $370m^3CH_4/tonVS$ of pig slurry in ultimate methane yields. Those of winter forage crops were the range 75% to 87% with ultimate methane yield of $378m^3CH_4/tonVS$ to $450m^3CH_4/tonVS$ and those of summer forage crops were the range 81% to 85% with ultimate methane yield of $392m^3CH_4/tonVS$ to $415m^3CH_4/tonVS$. The forge crops as "energy crops" could be used as good renewable energy source to increase methane production and to improve biodegradability in co-digestion with animal manure or only energy crop digestion.

• 한국토양비료학회지
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• 제44권1호
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• pp.104-111
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• 2011

In order to assess the performance of co-digester using pig slurry and food waste at the farm scale biogas production facility, the anaerobic facility that adopts the one-stage CSTR of 5 $m^3\;day^{-1}$ input scale was designed and installed under the conditions of the OLR of 2.33 kg $m^3\;day^{-1}$ and HRT of 30 days in an pig farmhouse. Several operation parameters were monitored for assessment of the process performance. The anaerobic facility was operated in three stages to compare the performance of the anaerobic co-digester. In the Stage I, that was fed with a mix of pig slurry to food waste ratio of 7:3 in the input volume, where input TS content was 4.7 (${\pm}0.8$) %, and OLR was 0.837-1.668 kg-VS $m^3\;day^{-1}$. An average biogas yield observed was 252 $Nm^3\;day^{-1}$ with methane content 67.9%. This facility was capable of producing an electricity of 626 kWh $day^{-1}$ and a heat recovery of 689 Mcal day-1. In Stage II, that was fed with a mixture of pig slurry and food waste at the ratio of 6:4 in the input volume, where input TS content was 6.9 (${\pm}1.9$) %, and OLR was 1.220-3.524 kg-VS $m^3\;day^{-1}$. The TS content of digestate was increased to 3.0 (${\pm}0.3$) %. In Stage III, that was fed with only pig slurry, input TS content was 3.6 (${\pm}2.0$) %, and OLR was 0.182-2.187 kg-VS $m^3\;day^{-1}$. In stage III, TS and volatile solid contents in the input pig slurry were highly variable, and input VFAs and alkalinity values that affect the performance of anaerobic digester were also more variable and sensitive to the variation of input organic loading during the digester operation. The biogas produced in the stage III, ranged from 11.3 to 170.0 $m^3\;day^{-1}$, which was lower than 222.5-330.2 $m^3\;day^{-1}$ produced in the stage II.

• 한국토양비료학회지
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• 제44권5호
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• pp.895-902
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• 2011

혐기성소화에서 원료로 가축분뇨와 음식물 쓰레기의 혼합비에 따른 유기물 제거율은 60:40에서 총고형물 (TS) 및 휘발성고형물 (VS)이 각각 약 80%로 가장 높은 제거효율을 보였다. 통합소화에 의한 누적가스발생량을 비교하였을 때에도 가축분뇨 60%와 음식물 쓰레기 40%를 투입한 처리 (60:40)에서 가장 많은 가스 발생량을 나타내었다. 그러나 통합소화액의 염분함량을 고려할 때 가축분뇨 0.1%, 음식물 쓰레기 0.6%의 염분을 함유한 원료를 대상으로 혼합비율을 달리하여 투입하였을 때 음식물 쓰레기 100% 투입의 경우에 소화액의 염분함량은 0.45%, 음식물 쓰레기 60%와 가축분뇨 40% 투입에서 0.32, 음식물쓰레기 40%와 가축분뇨 60% 투입에서 0.27%, 음식물 쓰레기 20%와 가축분뇨 80% 투입에서 0.21로 나타났다. 따라서 본 연구결과를 토대로 하여 가축분뇨와 음식물 쓰레기를 통합소화하고 소화액을 액비로 농경지에 안정적으로 사용하기 위해서는 음식물 쓰레기의 투입 한계비율은 30%이하가 적정 하다고 판단할 수 있었다. 하지만 통합 소화액을 액비로서 농경지에 지속적으로 사용 가능하게 하기 위해서는 원료별, 발생원별로 너무 다양한 음식물 쓰레기의 염분함량에 대한 조사와 더불어 통합소화를 위한 적정 혼합비율 설정 및 토양 및 작물 재배를 통한 검증이 이루어져야 할 것으로 생각된다.

• 공업화학
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• 제23권1호
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• pp.28-34
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• 2012

본 연구에서는 UASB 반응조를 이용하여 음폐수 탈리액을 원료로 하여 중온소화($35{\pm}0.5^{\circ}C$)와 고온소화($55{\pm}0.5^{\circ}C$)법을 통한 운전을 실시하였다. 20일 동안은 중온소화로 운전을 하면서 5일 간격으로 유출수 재순환 비를 단계적으로 변화시켰다. 고온소화 역시 중온소화와 마찬가지 조건으로 운전을 실시하였다. 실험결과 중온소화 시 유기물제거율은 90% 이상, 메탄수율은 약 66~70%로 나타났다. 고온소화 시 유기물제거율은 80% 이상, 메탄수율은 약 62~68%로 나타났다. 또한, 유출수 반송을 3Q 이상으로 반송하여 운전할 경우 경제적이며 안정적인 운전을 할 수 있었다.

• 한국토양비료학회지
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• 제49권3호
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• pp.227-234
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• 2016

The influence of mixing on biogas production and organic material removal performance of solid state anaerobic digestion of dairy manure and sawdust bedding mixtures was evaluated using 22 L volume lab-scale digesters. After 45 days of anaerobic digestion at $37^{\circ}C$, cumulative methane yield of unmixed test unit ($73.1N{\cdot}mL/g-VS$) was almost 1.3 times of that of mixed one ($56.3N{\cdot}mL/g-VS$). The biodegradable volatile solids removal rate of unmixed test unit was 67%, which was almost 28% greater than mixed one. Our results reveal that unmixed condition is better than mixed one in terms of biogas production and organic material reduction.

• Journal of Biosystems Engineering
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• 제35권1호
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• pp.53-63
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• 2010

The performance of two serial completely stirred tank reactors (CSTRs) for treatment of swine manure (SM) with Chinese cabbage silage (CCS) was studied. The two CSTRs of 41 liters each were connected in series and first reactor was fed swine manure with Chinese cabbage silage in 3:1 proportion by VS basis. The FOS/TAC, methane content (%) and pH were utilized as the parameters for the digester stability control. The FOS/TAC value was found to be effective indicator for instant digester condition. The stability of reactors can be obtained with the FOS/TAC value up to 1.0 with accumulation of FOS value below 10,000 mg/L. Material exchange method was effective in transferring the excess volatile fatty acids (VFA) from the first reactor to the second one and maintaining stability in both the reactors. The biogas yield and the methane yield was 0.55-0.61 and 0.41-0.42 L/g VS fed, respectively, at organic loading rate (OLR) of 2.2-2.6 g VS/L with total HRT of 32 days.

• 대한산업공학회지
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• 제22권1호
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• pp.155-164
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• 1996

Biomass to methane via anaerobic digestion conversion is a good supply method of substitutable energy resources. The economic viability of this technology is contingent upon managing the production facilities in a cost effective manner. The problem is to determine the batch production sequence as well as the batch residence times in the digester so as to maximize total gas production over a given planning horizon. The problem is difficult to solve since the batch sequencing decisions and the batch residence time decisions cannot be isolated. This paper developes a heuristic algorithm which is based on a dynamic programming procedure for the multiple feedstock sequencing and scheduling biogas production systems and demonstrates to yield good results.

• 한국환경과학회지
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• 제31권12호
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• pp.1127-1134
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• 2022

Herein , the effect of changes in the organic loading rate in anaerobic digestion was evaluated. The experiment was carried out by a laboratory -scale semi-continuous stirred tank reactor, and feedstock was food-waste leached. The organic loading rate was increased by 0.5 kgVS/m3 in each phase from 1.0 kgVS/m3 to 4.0 kgVS/m3. At the end of the operation, to check the failure of the reactor, the organic loading rate was increased by 1.0 kgVS/m3 in each phase and reached 6.0 kgVS/m3. This shows that the biogas yield decreased as organic loading rate increased. Biogas production seemed to be unstable at 3.5-6.0 kgVS/m3. Moreover, biogas production dramatically fell to approximately 0 mL at 6.0 kgVS/m3, which was decided as the operation failure on the 16th day of the las tphase. The result of the reactor analysis shows that the cumulation of volatile fatty acid increased as the organic loading rate increased. This seems to occur due to the decreasein pH in the reactor and led to extinction of anaerobic bacteria, which were the biogas products. Although the buffer compound (alkalinity) could prevent the decline in pH, the concentration of alkalinity was found to be lacking at a high organic loading rate

• 대한환경공학회지
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• 제34권12호
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• pp.840-846
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• 2012

현재 이산화탄소에 의한 지구기후변화는 세계적으로 논의되고 있다. 화석연료를 대신할 수 있는 청정 연료를 찾고 있다. 에너지 생산을 위한 지속가능한 바이오가스 사용은 이산화탄소 배출에 기여하지 않아 온난화가스를 줄이는데 높은 잠재력을 가지고 있다. 모사 바이오가스(메탄 : 이산화탄소 = 60% : 40%)를 이용한 높은 수소 합성가스 생산을 위한 촉매 수증기 개질연구를 하였다. 표면연소의 3D 적외선 매트릭스 버너에 바이오가스를 적용하였다. 개질기에는 Ru 촉매를 이용하였다. 변수별 연구로 수증기/탄소 비, 바이오가스 성분비, 공간속도, 개질기 온도를 진행하였다. 수증기/탄소 비, 바이오가스 성분비, 공간속도, 개질기 온도가 각각 3.25, 60% : 40%, $14.7L/g{\cdot}hr$, $550^{\circ}C$일 때, 수소 농도, 메탄 전환율이 최대값을 나타내었다. 위 조건에서 수소 수율, 수소/일산화탄소 비, 일산화탄소 선택도, 에너지 효율은 0.65, 2.14, 0.59, 51.29%를 나타내었다.