• 유기물자원화
• /
• 제15권3호
• /
• pp.97-105
• /
• 2007

본 연구는 유기성 고형폐기물 처리에 적합한 벤치스케일 침출상 반응조를 이용하여 효율적인 산발효 및 수소발효의 거동특성을 살펴보았다. 산발효조는 혐기성 소화슬러지를 식종한 후 희석율 2.0, 3.0, $4.0d^{-1}$로 운전이 되었으며, 수소발효조는 열처리된 소화슬러지를 식종한 후 희석율 2.0, 4.0, $6.0d^{-1}$로 운전이 되었다. 산발효조는 희석율 $3.0d^{-1}$에서 운전되었을 때 최대의 COD 전환율 56.2%가 얻어졌으며 이때 전환된 COD는 모두 유기산으로 전환되었다. 반면에 수소발효조는 산발효조보다 높은 COD 전환율(49.3%)을 보여주지 못했지만, 높은 에너지 수율을 가지고 있을 뿐 아니라 친환경 청정에너지인 수소가스(전체 COD 중 5.1%)를 부산물로 얻을 수 있었다. 그러므로 처리목적에 따라 산발효나 수소발효를 유기성 고형폐기물에 적용할 수 있으며, 이는 혐기성처리 기술의 경제성을 향상시킬 수 있다.

• 한국환경과학회지
• /
• 제21권10호
• /
• pp.1255-1263
• /
• 2012

Batch cultivations were performed to evaluate the influences of the initial pH condition on mesophilic and thermophilic acidogenic fermentation with food waste recycling wastewater. In both conditions of mesophilic and thermophilic fermentation, TVFAs production rates were maximized at the initial pH 7 condition as 0.15 and 0.23 g TVFAs/L hr, respectively. And pH was also maintained stably between 6 and 7 during 72hr acidogenic cultivation at both conditions. However, predominant VFA components were different according to reaction temperature conditions. In mesophilic condition, propionic acid which has low conversion efficiency to methane was accumulated up to 1,348 mg/L while acetic and butyric acid were predominant in thermophilic condition. Therefore, thermophilic acidogenic fermentation was superior for the effective VFAs production than mesophilic condition. From the DGGE analysis, the band patterns were different according to the initial pH conditions but the correlations of the each band were increased in similar pH conditions. These results mean that microbial communities were certainly affected by the initial pH condition. Consequently, the adjustment of the initial pH to neutral region and thermophilic operation are needed to enhance acidogenic fermentation of food waste recycling wastewater.

• Journal of Microbiology and Biotechnology
• /
• 제2권4호
• /
• pp.248-254
• /
• 1992

The initial growth of Clostridium acetobutylicum was not inhibited by 1 atm of H$_2$ while H$_2$ reduced glucose consumption in a solventogenic culture of a phosphate limited 2-stage chemostat. Under 1 atm of H$_2$, a solventogenic culture consumed hydrogen, but an acidogenic culture produced hydrogen. H$_2$ consumption by the solventogenic culture was enhanced by the addition of 5 mM neutral red, an artificial electron carrier with a redox potential of -325 mV. Hydrogenase activity, measured in both directions of production and consumption, showed that activity coupled with methyl viologen is higher in an acidogenic culture than in a solventogenic culture, and that the two cultures have similar activities for methylene blue reduction. The solventogenic culture showed a higher activity coupled with neutral red than the acidogenic culture. From these results, it is hypothesized that hydrogen producing hydrogenase activity is high during the acidogenic phase, and decreases as solventogenesis starts, and that the solventogenic culture produces a second hydrogenase which uses an electron carrier other than ferredoxin. This hypothesis was supported by the fact that enzyme activities involved in electron flow can be coupled to neutral red, indepedent of ferredoxin, and that neutral red addition to the fermentation system increased butanol yield, with a decrease in production of less reduced fermentation products, and $H^2$.

• 한국축산시설환경학회지
• /
• 제4권2호
• /
• pp.175-182
• /
• 1998

For the recycling of swine takes 2 different steps in fermenting procedure, acidogenic reactor and methanogenic reactor, the activity of involved microbes can be maintained at the maximum level. This study showed applying 2 separate steps in anaerobic fermentation has improved fermenting efficiency over the conventional 1 step fermentation. Accordingly, the results are coincident with the hypothesis in which 2 steps acidogenic and methanogenic reactor fermentation is more efficient than conventional (1 step) fermentation that makes poisonous materials be obviate and abate. And the results also get the effective performance in the production of methane gas.

• 상하수도학회지
• /
• 제18권1호
• /
• pp.15-21
• /
• 2004

The purpose of this research was to investigate loading rate of influent for acidogenic fermentation. Laboratory batch experiments were conducted, at $35^{\circ}C$, HRT 18hr, pH 6 and used 3.5L reactor. Loading rate of influent was varied 2.0 to 4.0g VSS/L, TOA concentration is decreased according to increasing loading rate Over 2.5g VSS/L. When loading rate is 2.0g VSS/L, hydrolysis percentage show the maximum value of 87%. Most of SCFA is consist of HAc, HPr, I-HBu and MBu. HAc concentration is 5,233mg/L in the 2.0g VSS/L condition. So, for this study, we think that limiting loading rate is 2.5g VSS/L. SCFA species was investigated to HAc, HPr, I-HBu and n-HBu during our studying. HAc/SCFA ratio is about 89.3%, SCFA production rate is highest to $1,104mg\;COD/L/d{\cdot}gPCOD$ for 2.0g VSS/L loading rate.

• 한국축산시설환경학회지
• /
• 제4권2호
• /
• pp.167-174
• /
• 1998

It is known that the anaerobic fermentation of organic matter (OM) is divided into 2 phases, acidogenic phase in which OM is digested into volatile fatty acid (VFA), and methanogenic phase where the produced VFA is converted to CH4 and CO2. In a natural fermenting procedure, these 2 phases occur at the same time. However the total production of end products (methane) may be limited if these 2 phases occur at the same time. This is believed to be due to the difference in growth rate, substrate-utilizing efficiency and favorable environment for each microbes (acidogens and methanogens), involved in each phase. It is therefore suggested for the maximum recycling of organic waste (such as animal waste) through providing 2 different steps in fermenting procedure, acidogenic phase and methanogenic phase, in each case the activity of involved microbes can be maintained at the maximum level. The results obtained from these experiments are summarized as follows : The loading rates of swine waste were made through 2.5, 5 and 10 gVS / l / d to identify its acidogenic fermenting character in this study. The VFA yield was maximized at 10 gVS / l / d of loading rate. On the basis of this study was executed to identify the optimum HRT of 1, 2 and 4 days at 10 gVS / l / d of loading rate in acidogenic phase. The maximum VFA yield was obtained at 1 days of HRT.

• 한국축산시설환경학회지
• /
• 제6권2호
• /
• pp.73-81
• /
• 2000

A two-phase anaerobic digestion system for the treatment of swine waste was constructed in a commercial hog farm. The digester system was composed of 4 major units; slurry storage pit, acidogenic digester, methanogenic digester and sedimentation pit. A biogas boiler unit was also attached to maintain the digester temperature of 37$^{\circ}C$. Substrate lading was made with 2hr-interval by pumping about 2.1$m^3$ of slurry type swine waste from the slurry pit into the acidogenic digester, which corresponds to hydraulic retention time of 4 days for the acidogenic digester and of 11 days for the methanogenic digester. Digester temperature were well maintained as the set temperature of 37$^{\circ}C$ in the methanogenic digester, while the temperature in the acidogenic digester showed around 34$^{\circ}C$. pH also showed a steady-state results of 7.3 in the acidogenic digester and of 7.6 in the methanogenic digester during the operation period. Average biogas production rate was 0.66$m^3$/$m^3$ digester volume. Reduction rate of total solid and volatile solid were 42.8% and 5.8%, respectively. Total nitrogen and ammonia nitrogen were not reduced during the anaerobic fermentation, however, most of VFAs seemed to be converted to the biogas,. These fermentation performance data may suggest that he newly developed a two-phase anaerobic digester for the swine waste treatment worked so successfully.

• 유기물자원화
• /
• 제8권3호
• /
• pp.112-117
• /
• 2000

음식물쓰레기는 높은 함수율과 VS(volatile solids) 함량으로 인해 수거, 운반 및 매립에 있어서 부패, 악취, 침출수 등의 주요 원인이 되고 있다. 음식물쓰레기의 산발효는 기질의 생분해도와 식종균의 분해능력과 같은 발효제한요소에 의해서 영향을 받는데, 음식물쓰레기의 생분해도는 잘 분해되지 않으며 전체 양의 약 50%를 차지하는 셀룰로우스 성분(야채류)과 깊은 연관이 있다. 이에 대한 효과적이면서도 경제적인 방법은 셀룰로우스의 분해능력이 뛰어난 미생물을 식종하는 것으로, 본 연구에서는 루멘미생물을 이용하여 산발효의 낮은 효율을 향상시키려 하였으며 그 값을 중온 산발효균과 비교하였다. Leaching bed 반응조에 루멘미생물을 식종했을 때의 산발효 효율은 희석율 $3.0d^{-1}$에서 71.2%의 최대값을 얻었으며, 한편 중온 산발효균을 식종하였을 때는 희석율 $4.5d^{-1}$에서 59.8%의 최대값을 얻었다. 이는 루멘미생물의 음식물쓰레기 분해능력이 보다 뛰어남을 보여주는 것이다.

• Journal of Microbiology and Biotechnology
• /
• 제22권5호
• /
• pp.668-673
• /
• 2012

Biohydrogen production from organic wastewater by anaerobically activated sludge fermentation has already been extensively investigated, and it is known that hydrogen can be produced by glucose fermentation through three metabolic pathways, including the oxidative decarboxylation of pyruvic acid to acetyl-CoA, oxidation of NADH to $NAD^+$, and acetogenesis by hydrogen-producing acetogens. However, the exact or dominant pathways of hydrogen production in the anaerobically activated sludge fermentation process have not yet been identified. Thus, a continuous stirred-tank reactor (CSTR) was introduced and a specifically acclimated acidogenic fermentative microflora obtained under certain operation conditions. The hydrogen production activity and potential hydrogen-producing pathways in the acidogenic fermentative microflora were then investigated using batch cultures in Erlenmeyer flasks with a working volume of 500 ml. Based on an initial glucose concentration of 10 g/l, pH 6.0, and a biomass of 1.01 g/l of a mixed liquid volatile suspended solid (MLVSS), 247.7 ml of hydrogen was obtained after a 68 h cultivation period at $35{\pm}1^{\circ}C$. Further tests indicated that 69% of the hydrogen was produced from the oxidative decarboxylation of pyruvic acid, whereas the remaining 31% was from the oxidation of NADH to $NAD^+$. There were no hydrogen-producing acetogens or they were unable to work effectively in the anaerobically activated sludge with a hydraulic retention time (HRT) of less than 8 h.

• 유기물자원화
• /
• 제8권3호
• /
• pp.118-123
• /
• 2000

음식물쓰레기는 함수율과 휘발성 유기물질의 함량이 높기 때문에 수거, 운반 및 매립에 있어 많은 문제점이 야기되고 있다. 음식물쓰레기의 산발효는 pH, 체류시간 등과 같은 환경조건에 의해서 영향을 받는데, 음식물쓰레기의 각 구성성분은 각기 다른 환경조건에서 분해가 진행된다. 전분, 셀룰로우스 및 단백질은 각각 최적의 pH 및 체류시간을 가지고 있어, 전분의 경우는 낮은 pH에서 셀룰로우스는 체류시간이 증가할수록 그리고 단백질은 체류시간의 증가 및 중성 pH에 접근할수록 그 분해가 증가한다. 이러한 사실은 산발효의 환경조건을 조절함으로써 음식물쓰레기의 분해가 향상될 수 있음을 말하여 준다. 산발효 단계에 따라 희석율의 값을 3.0에서 $1.0d^{-1}$로 조절한 경우, 산발효 효율은 71.2%에서 81.1%로 크게 증가하였다. 이때 주된 산발효 산물은 뷰틸산에서 초산으로 점차 변화하였는데, 이것은 산발효의 효율향상이 야채류와 육류의 분해 증가에 기인함을 보여주는 것이다.