• 한국환경농학회지
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• 제21권4호
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• pp.255-260
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• 2002

가축분뇨를 혐기소화하여 메탄가스를 생산하고 난 다음 혐기성 소화액비를 비료자원으로 활용하기 위하여 농가포장에서 액비의 시용기준을 구명하였다. 벼 생육상황은 분얼기및 출수기에 액비 70%+화학비료 30% 및 액비 100%구의 경수만 타 처리구보다 약간 많았다. 시기별 식물체 중 전질소 함량은 표준시비구가 생육초기에 기비 및 분얼비의 영향으로 타 처리구보다 높았다. 벼 수량은 액비 70%+화학비료 30% 및 액비 100%구가 표준시비구보다 약간 증수되었으나, 액비 50%+화학비료 50%구는 표준시비구보다 약간 낮았다. 수확기 질소흡수량, 시비질소 효율 및 시비질소 이용율은 수량이 많았던 액비 70%+화학비료 30% 및 액비 100%구에서 높았다. 시기별 토양 중 $NH_4-N$함량 및 $NO_3-N$함량 변화는 표준시비구 및 액비 50%+화학비료 50%구가 생육초기에만 타 처리구보다 약간 높았다. 시기별 관개수 중 $NH_4-N$함량 변화는 분얼비의 영향으로 급격히 증가하였다가 급격히 감소하였는데 증가한 시기에는 표준시비구 > 액비 50%+화학비료 50%구가 타처리구보다 높았으나, $NO_3-N$함량은 처리 간 차이가 없었다. 시기별 침투수 중 $NH_4-N$함량 및 $NO_3-N$함량 변화는 무비구가 생육초기에 타 처리구보다 약간 높았는데, 이것은 벼 생육불량에 의한 양분흡수가 적어지면서 상대적으로 지중으로 침투가 많았기 때문인 것으로 생각다. 따라서 혐기성 소화액비의 적정 시용기준은 표준시비량의 질소성분 70%을 액비로서 전량기비로 시용하고, 나머지 30% 질소성분을 화학비료로 분얼비 10% 수비 20% 시용하는 것이 효과적이었다.

• 한국물환경학회지
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• 제22권4호
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• pp.599-604
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• 2006

Nitrogen removal with the combined SHARON (Single reactor system for high ammonium removal over nitrite)ANAMMOX (Anaerobic ammonium oxidation) process using the effluent of ADEPT (Anaerobic digestion elutriated phased treatment) slurry reactor with very low C/N ratio for piggery waste treatment was investigated. For the preceding SHARON reactor, ammonium nitrogen loading and removal rate were $0.97kg\;NH_4-N/m^3_{reactor}/day$ and $0.68kg\;NH_4-N/m^3_{reactor}/day$ respectively. In steady state, bicarbonate alkalinity consumption for ammonium nitrogen converted to $NO_2-N$ or $NO_3-N$ was 8.4 gram per gram ammonium nitrogen. The successive ANAMMOX reactor was fed with the effluent from SHARON reactor. The loading and removal rate of the soluble nitrogen defined as the sum total of $NH_4-N$, $NO_2-N$ and $NO_3-N$ in ANAMMOX reactor were $1.36kg\;soluble\;N/m^3_{reactor}/day$ and $0.7kg\;soluble\;N/m^3_{reactor}/day$, respectively. The average $NO_2-N/NH_4-N$ removal ratio by ANAMMOX was 2.41. Fluorescence in situ hybridization (FISH) analysis verified that Candidatus Kuenenia stuttgartiensis were dominate, which means that they played an important role of nitrogen removal in ANAMMOX reactor.

• 상하수도학회지
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• 제34권4호
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• pp.259-266
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• 2020

In this study, a pilot-scale (3 ㎥/day) membrane distillation (MD) process was operated to treat digestate produced from anaerobic digestion of livestock wastewater. In order to evaluate the performance and energy cost of MD process, it was compared with the pilot scale (10 ㎥/day) reverse osmosis (RO) process, expected competitive process, under same feed condition. As results, MD process shows stable permeate flux (average 10.1 L/㎡/hr) until 150 hours, whereas permeate flux of RO process was decreased from 5.3 to 1.5 L/㎡/hr within 24 hours. In the case of removal of COD, TN, and TP, MD process shows a high removal rate (98.7, 93.7, and 99% respectively) stably until 150 hours. However, in the case of RO process, removal rate was decreased from 91.6 to 69.5% in COD and from 93.7 to 76.0% in TP during 100 hours of operation. Removal rate of TN in RO process was fluctuated in the range of 34.5-62.9% (average 44.6%) during the operation. As a result of energy cost analysis, MD process using waste heat for heating the feed shows 18% lower cost compare with RO process. Thus, overall efficiency of the MD process is higher then that of the RO process in terms of permeate flux, removal rate of salts, and operating cost (in the case of using waste heat) in treating the anaerobic digestate of livestock wastewater.

• 한국축산시설환경학회지
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• 제5권3호
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• pp.189-196
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• 1999

Anaerobic digestion is a naturally occuring microbial process involving the decomposition of organic materials such as livestock manure. This study explores the effect of the operating conditions, HRT (Hydraulic Retention Time) and feeding frequency on treatment efficiency for digestion of pig slurry, which has been one of most difficult organic waste for proper treatment in livestock production industry in Korea at the present time. The pilot-scale CSTR of 5 m3 in volume was designed. manufactured, and operated at the temperature of 35$\pm$1$^{\circ}C$. The digester was designed to hydraulically stir for complete mixing and to supply heat from the water bath to maintain mesophilic temperature. The HRT of the digester for Test 1 and Test 2, and Test 3 was set for 17 days and 13 days respectively and pig slurry was fed once a day with 300$\ell$ each for Test 1 and Test 3, while twice with 150$\ell$each for Test 2. Test 2 showed better performance by increase of 4% in VS removal efficiency and 5% in biogas production rate. This is mainly attributed to smaller temperature drop by feeding frequently with half amount, which eventually led to lesser impact on anaerobic mocrobes in the digester. Test 2 maintained optimum pH 7.8 which uplifted the activaton of sulfur-reduction bacteria, alkalinity of around 4,000mg/$\ell$, VA of over 3,000mg/$\ell$ for whole period of experiment. Further research may require to provide the practical operation strategy of anaerobic treatment system for treatment of pig slurry.

• 유기물자원화
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• 제29권4호
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• pp.77-86
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• 2021

본 연구에서는 유기성폐자원에너지 인센티브제도의 기초자료로 활용하고자 음식물폐기물, 음폐수 및 다양한 유기성폐기물이 처리되는 혐기소화조의 운영방식의 물질수지와 에너지수지 산정 결과를 통하여 에너지효율을 평가하고자 한다. 바이오가스화 시설 11개소의 물질수지 분석 결과 유기성폐기물을 제외한 반입물 중 공정수 21.1%, 시상수 25.7 % 다량 투입되는 것을 확인하였다. 그에 따라 연계처리수의 전체 유출물의 87.6 %를 차지하였다. 또한 총 유입물량의 15.7 %가 바이오가스로 전환되며, 총고형물(TS)가 평균 22 %임을 감안할 때 평균 75 %의 물질 전환율을 확인하였다. 에너지수지 분석 결과, 유입물의 잠재에너지 대비 바이오가스 열량을 분석하여 에너지 전환율은 평균 78.5%을 확인하였다. 바이오가스를 생산하기 위한 외부에너지원을 포함한 바이오가스 생산효율은 평균 69.4 %이며, 미이용된 유출에너지를 적용한 바이오가스 플랜트 효율은 평균 58.9 %로 나타났다.

• 유기물자원화
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• 제4권1호
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• pp.13-21
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• 1996

고농도 황산염과 중금속을 함유한 피혁폐수를 처리하기 위하여, 반응조의 처리도, 황환원균과 메탄균 사이의 기질경쟁 및 크롬농도에 대한 메탄균의 활성을 평가하였다. COD는 $35^{\circ}C$의 반응조 온도에서 유기부하량 2.0 gCOD/l.day와 18시간의 수리학적 체류시간에서 70% 이상의 제거율을 얻을 수 있었다. 황환원균과 메탄균 사이의 기질경쟁에서 황환원균에 의해 이용된 COD는 운전초기 15%에서 실험종료시 43%까지 증가되었다. 이는 유기물 분해로부터 발생되는 대부분의 전자가 황환원균에 의해 이용되어 황산염 환원에 의한 황화물이 생성되므로 메탄균의 활성은 강력히 억제되었다. 전 실험기간 동안 크롬농도는 90% 이상 제거되었으며, 크롬농도의 높은 제거율에도 불구하고 반응조의 처리능력은 거의 감소되지 않았다. 이는 반응조내에서 제거된 3가 크롬이 미생물의 활성에 영향을 미치지 않은 점으로 볼 때 3가 크롬이 6가 크롬에 비해 미생물에 대한 독성영향이 심하지 않다고 볼 수 있다.

• 상하수도학회지
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• 제28권1호
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• pp.25-32
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• 2014

In order to investigate the effective pretreatment methods in WAS(=waste activated sludge) solubilization, the values of SCOD yield per unit SS (SCOD/gSS.hr) were compared. After the hydrodynamic cavitation with pH of 12.5, SCOD increased to 7800 mg/L, SS decreased to 45 % and the solubilization rate was 29 %. Combination of alkality (pH 12.5) and the cavitation seems to be the optimal condition for sludge solubilization. After the cavitational pretreatment, efficiencies of anaerobic digestion of the unfiltered sludge(the control), raw sludge and pretreated sludge were evaluated with BMP(=biochemical methane potential) tests. For evaluation of the biodegradability characteristics of pretreated sewage sludge, the methane production has been measured for 6 months. The methane production of pretreated sludge increased 1.4 times than that of untreated sludge. The result indicates that the cavitationally pretreated sludge was a better biodegradability substrate in anaerobic condition compared to raw sludge. It is obvious that cavitational pretreatment could enhance not only solubilization but also biodegradability of WAS. In conclusion, cavitational pretreatment of WAS to convert the particulate into soluble portion was shown to be effective in enhancing the digestibility of the WAS.

• 한국토양비료학회지
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• 제44권5호
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• pp.903-915
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• 2011

최근 농산 바이오매스를 이용한 혐기적 메탄생산은 가장 실질적인 바이오 에너지 생산 방법으로 주목받고 있다. 그러나 국내의 경우 폐기물 처리 측면에서 가축분뇨, 음식물쓰레기, 하수슬러지에 대한 혐기소화 연구가 주를 이루고 있으며, 농업생산과정에서 발생하는 각종 농산 바이오매스에 대한 혐기소화 연구는 매우 미흡한 실정이다. 특히 국내에서 농산 바이오매스의 혐기적 매탄 생산 퍼텐셜은 측정 방법이 표준화되어 있지 않아 다양한 연구자들의 연구결과를 비교 활용하는데 어려움이 있어 왔다. 외국의 경우 독일은 VDI 4630, 미국은 ASTM E2170-01을 혐기적메탄 생산 퍼텐셜 및 유기물 분해율 분석의 표준분석 방법으로 활용하고 있다. 따라서 독일과 미국의 메탄생산 퍼텐셜 분석법을 비교 검토하여 메탄 생산 퍼텐셜을 정의하고, 분석방법, 영향인자, 기술적인 계산 방법등을 고찰하였다. 한편 국내외 농산 바이오매스의 메탄 생산 퍼텐셜 측정 현황을 살펴보고자, 국내의 경우에는 1980년대에 실시되었던 볏짚 등의 18종의 농산 바이오매스와 식품산업부산물 등의 연구 자료를 조사하였으며, 국외는 43개 농산바이오매스에 대하여 곡류, 채소류, 특용작물, 과수, 기타작물로 분류하고, 사료작물인 사탕수수, 사탕무, 옥수수 등은 에너지 작물로 분류하여 216건의 메탄 생산 퍼텐셜에 대한 연구자료를 조사하였다.

• 한국물환경학회지
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• 제35권4호
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• pp.299-307
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• 2019

The purpose of this study was to investigate the effect of low temperature thermal pre-treatment on biodegradation of waste activated sludge for anaerobic digestion as a countermeasure for increasing sludge generation. The experimental condition was accomplished in 2 %, 4 %, and 6 % TS concentration, and $70^{\circ}C$, $80^{\circ}C$, $90^{\circ}C$ of temperature for a maximum of 120 minutes retention time. Then, it was followed by analysis of physical/chemical properties, BMP test and composition of biogas. The biogas characteristic was evaluated by applying the modified Gomperz model. As a result, solubility of dissolved substrate, such as $SCOD_{Cr}$, soluble carbohydrate, and soluble protein, and biogas production increased as temperature increased. Solubilization efficiency at $90^{\circ}C$ was 18.4 %, 17.03 % and 16.88% in 2 %, 4 %, and 6 % TS concentration respectively. Also, solubilization rates of carbohydrate and protein similarly increased. BMP test results also showed that methane production in excess sludge increased to 0.194, 0.187 and $0.182m^3/kg$ VS. respectively, and lag phase decreased to 0.145, 0.220, 0.351 day due to acceleration of the hydrolysis step. Consequently, low-temperature thermal pre-treatment could increase biodegradability of sludge, positively affecting biogas production and sludge reduction.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2011년도 춘계학술대회 초록집
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• pp.172-172
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• 2011

Anaerobic digestion(AD) has successfully been used for many applications that have conclusively demonstrated its ability to recycle biogenic wastes. AD has been successfully applied in industrial waste water treatment, stabilsation of sewage sludge, landfill management and recycling of biowaste and agricultural wastes as manure, energy crops. During AD, i.e. organic materials are decomposed by anaerobic forming bacteria and fina1ly converted to excellent fertilizer and biogas which is primarily composed of methane(CH4) and carbon dioxide(CO2) with smaller amounts of hydrogen sulfide(H2S) and ammonia(NH3), trace gases such as hydrogen(H2), nitrogen(N2), carbon monoxide(CO), oxygen(O2) and contain dust particles and siloxanes. The production and utilisation of biogas has several environmental advantages such as i)a renewable energy source, ii)reduction the release of methane to the atomsphere, iii)use as a substitute for fossil fuels. In utilisation of biogas, most of biogas produced from small scale plant e.g. farm-scale AD plant are used to provide as energy source for cooking and lighting, in most of the industrialised countries for energy recovery, environmental and safety reasons are used in combined heat and power(CHP) engines or as a supplement to natural. In particular, biogas to use as vehicle fuel or for grid injection there different biogas treatment steps are necessary, it is important to have a high energy content in biogas with biogas purification and upgrading. The energy content of biogas is in direct proportion to the methane content and by removing trace gases and carbon dioxide in the purification and upgrading process the energy content of biogas in increased. The process of purification and upgrading biogas generates new possibilities for its use since it can then replace natural gas, which is used extensively in many countries, However, those technologies add to the costs of biogas production. It is important to have an optimized purification and upgrading process in terms of low energy consumption and high efficiency giving high methane content in the upgraded gas. A number of technologies for purification and upgrading of biogas have been developed to use as a vehicle fuel or grid injection during the passed twenty years, and several technologies exist today and they are continually being improved. The biomethane which is produced from the purification and the upgrading process of biogas has gained increased attention due to rising oil and natural gas prices and increasing targets for renewable fuel quotes in many countries. New plants are continually being built and the number of biomethane plants was around 100 in 2009.