• Applied Biological Chemistry
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• 제37권5호
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• pp.326-333
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• 1994

볏짚의 사료가치를 증진시키기 위하여 과산화수소에 의한 전처리와 섬유소 및 리그닌분해력이 강한 Pleurotus florida 균주로 발효사료를 제조하고 화학성분, 결정도 및 in vitro 소화율을 조사하여 사료적 가치를 검토하였다. P. florida에 의한 볏짚발효시 hemicellulose, cellulose 및 lignin은 각각 22.5%, 11.4%, 28.1% 감소하였고, $H_2O_2$나 $H_2O_2(pH\;11.5)$ 전처리 후 발효시에는 4% 이하의 저농도에서 감소가 심하였으며 발효기간이 경과할수록 cellulose, lignin 등이 감소하였고 아미노산함량은 무처리 볏짚에 비하여 배양 30일 후에 약 28.9% 증가하였으며 4% $H_2O_2$ 전처리 후 발효시는 35.1% 증가하였다. 볏짚 섬유소의 결정도는 $H_2O_2$ 처리 및 P. florida에 의한 발효처리로 감소하였고 $H_2O_2(pH\;11.5)$ 처리시 증가하였으며 $H_2O_2(pH\;11.5)$ 처리 후 수세시의 잔류볏짚의 결정도는 더욱 증가하였고 P. florida에 의한 볏짚배양 30일 후 in vitro 소화율은 17.1% 증가하였으며, $H_2O_2$ 전처리 후 발효시킨 볏짚은 6% 이하의 저농도에서 소화율 상승효과가 있었다.

• 한국환경보건학회지
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• 제27권1호
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• pp.119-123
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• 2001

철 농도변화에 따른 대사산물 생성에 대한 반응은 중온조건에서 회분식 실험으로 수해하였다. 철의 농도가 40mg/$\ell$까지는 철 농도의 증가에 따라 수소생성율도 증가하였다. acetate 생성율은 철의 농도가 증가함에 따라 감소하였다. Butyrate, ethanol 및 butanol은 각각 철 농도가 200,200 및 400mg/$\ell$에서 최대 생성율을 나타내었다. 철의 농도가 200mg/$\ell$이상의 농도엘 때에 propionate, i-butyrate 및 valerate 생성율이 철의 농도가 200mg/$\ell$ 이하의 경우 보다 낮았다. 미생물농도의 경우 철 농도가 300mg/$\ell$까지는 농도가 증가함에 따라 미생물농도도 증가하였다.

• 한국수소및신에너지학회논문집
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• 제17권4호
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• pp.379-388
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• 2006

Two mesophilic trickling bed bioreactors filled with two different types of media, hydrophilic- and hydrophobic-cubes, were designed and conducted for hydrogen production under the anaerobic fermentation of sucrose. Each bioreactor consisted of the column packed with polymeric cubes and inoculated with heat-treated sludge obtained from anaerobic digestion tank. A defined medium containing sucrose was fed by the different hydraulic retention time(HRT), and recycle rate. Hydrogen concentrations in gas-phase were constant, averaging 40% of biogas throughout the operation. Hydrogen production rate was increased till $10.5\;L{\cdot}h^{-1}{\cdot}L^{-1}$ of bioreactor when influent sucrose concentrations and recycle rates were varied. At the same time, the hydrogen production rate with hydrophobic media application was higher than its hydrophilic media application. No methane was detected when the reactor was under a normal operation. The major fermentation by-products in the liquid effluent of the both trickling biofilters were acetate, butyrate and lactate. In order to run in the long term operation of both reactor filled with hydrophilic and hydrophobic media, biofilm accumulation on hydrophilic media and biogas produced should be controlled through some process such as periodical backwashing or gas-purging. Four sample were collected from each reactor on the opposite hydrogen production rate, and their bacterial communities were compared by terminal restriction fragment length polymorphism (T-RFLP) analysis of PCR products generated using bacterial 16s rRNA gene primers (8f and 926r). It was expressed a marked difference in bacterial communities of both reactors. The trickling bed bioreactor with hydrophobic media demonstrates the feasibility of the process to produce hydrogen gas. A likely application of this reactor technology can be hydrogen gas recovery from pre-treatment of high carbohydrate-containing wastewaters.

• 대한환경공학회지
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• 제27권9호
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• pp.958-964
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• 2005

혐기성균에 의해 각종 탄수화물로부터 생성되는 수소가스의 량을 측정하였으며, 이 때 생성되는 유기산의 생성 특성을 파악하고자 하였다. 또한 이를 기초로 카드뮴과 구리와 같은 중금속이 배양액에 존재할 경우 혐기성균에 의한 수소생산량과 발효산물의 변화양상을 파악하고자 하였다. sucrose가 탄소원으로 사용되었을 때 3.43 mol H2/mol hexose의 최적 수소 생산량을 보였으며, 발효산물인 유기산은 acetic acid와 butyric acid가 주로 생성되었다. 카드뮴과 구리가 배양액에 존재함에 따라 수소생산량이 낮아지는 경향을 보인 반면, 유기산 중에서 acetic acid의 생성이 높아지는 경향을 나타내었으며 수소생산에 미치는 영향은 구리가 더 큰 것으로 나타났다.

• 한국수소및신에너지학회논문집
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• 제25권1호
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• pp.11-18
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• 2014

This study was conducted to investigate the effect of thermal pre-treatment on bio-hydrogen from food waste. Two continuous reactors operated and VFAs(volatile fatty acids) production and microbial communities were analyzed. The average hydrogen yield was 0.50 and 0.33mol $H_2/mol$ $hexose_{added}$ in thermally treated food added reactor(R1) and control(R2), respectively. Butyrate concentration was similarly 7,500mg/L in both reactors, but two times higher lactate concentration was observed in R2(3,800mg/L). The results of FISH(fluorescence in situ hybridization) showed that the relative microorganism to hydrogen producing bacteria was 78 and 27% in R1 and R2, respectively.

• KSBB Journal
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• 제17권2호
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• pp.142-147
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• 2002

기포탑 회분식 xanthan 발효에서 xanthan 생성속도와 분자량에 영향을 미치는 산소전달제한을 피하기 위하여 과산화수소수를 산소공금 보조수단으로 사용하였다. 과산화수소수 주 입은 xanthin 생성을 가역적으로 저해하였다. 반면이 직경 8 mm 유리구슬 유동화 입자는 기-액 산소전달속도를 증가시켜서 기-액-고 삼상유동충 생물반응기에서의 xanthan 발효는 기포탑 발효에 비하여 높은 단위균체량 당 xanthan 생성속도 및 점도수윤 그리고 반응기 공간-시간 수윤(space-time yield)을 보였다.

• 한국수소및신에너지학회논문집
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• 제22권3호
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• pp.326-332
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• 2011

The authors examined the effects of operating parameters on the $H_2$ production by dark fermentation of the wastewater generated from food waste recycling facilities, in short "food waste wastewater (FWW)". Central composite design based response surface methodology was applied to analyze the effect of initial pH (5.5-8.5) and substrate concentration (2-20 g Carbo. COD/L) on $H_2$ production. The experiment was conducted under mesophilic ($35^{\circ}C$) condition and a heat-treated ($90^{\circ}C$ for 20min)anaerobic digester sludge was used as a seeding source. Although there was a little difference in carbohydrate removal, $H_2$ yield was largely affected by the experimental conditions, from 0.38 to 1.77 mol $H_2$/mol $hexose_{added}$. By applying regression analysis, $H_2$ yield was well fitted based on the coded value to a second order polynomial equation (p = 0.0243): Y = $1.78-0.17X_1+0.30X_2+0.37X_1X_2-0.29X_1{^2}-0.35X_2{^2}$, where $X_1$, $X_2$, and Y are pH, substrate concentration (g Carbo. COD/L), and hydrogen yield (mol $H_2$/mol $hexose_{added}$), respectively. The 2-D response surface clearly showed a high inter-dependency between initial pH and substrate concentration, and the role of these two factors was to control the pH during fermentation. According to the statistical optimization, the optimum condition of initial pH and substrate concentration were 7.0 and 13.4 g Carbo. COD/L, respectively, under which predicted $H_2$ yield was 1.84 mol $H_2$/mol $hexose_{added}$. Microbial analysis using 16S rRNA PCR-DGGE showed that $Clostridium$ sp. such as $Clostridium$ $perfringens$, $Clostridium$ $sticklandii$, and $Clostridium$ $bifermentans$ were main $H_2$-producers.

• 한국수소및신에너지학회논문집
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• 제26권3호
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• pp.199-205
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• 2015

Organic wastes such as food waste (FW), livestock wastewater (LW), and sewage sludge (SWS) can produce hydrogen ($H_2$) by anaerobic acid fermentation. Expecially, FW which has high carbohydrate content produces $H_2$ and short chain fatty acids by indigenous $H_2$ producing microorganisms without adding inoculum, however $H_2$ production rate (HPR) and yield have to be improved to use a commercially available technology. In this study, LW was mixed to FW in different ratios (on chemical oxygen demand (COD) basis) as an auxiliary substrate. The mixture of FW and LW was pretreated at pH 2 using 6 N HCl for 12 h and then fermented at $37^{\circ}C$ for 28 h. HPR of FW, 254 mL $H_2/L/h$, was increased with the addition of LW, however, mixing ratio of LW to FW was reversely related to HPR, exhibiting HPR of 737, 733, 599, and 389 mL $H_2/L/h$ at the ratio of FW:LW=10:1, 10:2, 10:3, and 10:4 on COD basis, respectively. Maximum HPR and $H_2$ production yield of 737 $H_2/L/h$ and 1.74 mol $H_2/mol$ hexoseadded were obtained respectively at the ratio of FW:LW=10:1. Butyrate was the main organic acid produced and propionate was not detected throughout the experiment.

• KSBB Journal
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• 제18권2호
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• pp.145-148
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• 2003

P. aeruginosa F722는 탄화수소를 분해하는 과정에 biosurfactant (BS)를 생산한다. 탄화수소 분해에 사용되는 C-배지에서 BS 생산량은 0.78 g/ $\ell$이었으나, 질소원과 탄소원을 각각 0.05% (w/v) NH$_4$Cl + 0.1% (w/v) yeast extract과 3.0% (w/v) glucose로 조정한 경우는 BS 생산량이 1.66 g/ $\ell$로 증가하였다. 최적의 BS 생산조건으로 배양하는 동안 air 1.0 LPM를 공급해 주었을 때는 공기를 공급하지 않을 때의 1.66 g/ $\ell$보다 약 20% 증가한 1.94 g/ $\ell$이었다 뿐만 아니라, glucose 분해속도는 대수증식기와 정지기에서 air를 공급하지 않은 경우 0.25, 0.18 h$^{-1}$ 였으나, 공기를 1.0 LPM으로 공급한 경우 0.33, 0.29 h$^{-l}$ 로 조사되었다.

• 상하수도학회지
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• 제24권6호
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• pp.703-712
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• 2010

This study performed to extract operation factors of major organic wastes, which were food wastes and waste activated sludge generated in industries in order to use them as a substrate for bio-H2 production. According to the results of experimental analysis for hydrogen production capacity by various organic concentrations, the hydrogen production yield was the highest at 80 g/L, and the efficiency was improved by the pretreatment of waste activated sludge (acid treatment, alkali treatment). Hydrogen production efficiency was improved by mixing food wastes and waste activated sludge if waste activated sludge was below than 30%, however, it was decreased when it was more than 50%. The impacts of heavy metals on the hydrogen production shows that the inhibition level depends on the concentration of Cr, Zn, and Cu, Fe was able to enhance the hydrogen production.