• 제목/요약/키워드: Biological Hydrogen Production

검색결과 151건 처리시간 0.024초

Effects of pH and Carbon Sources on Biohydrogen Production by Co-Culture of Clostridium butyricum and Rhodobacter sphaeroides

  • Lee, Jung-Yeol;Chen, Xue-Jiao;Lee, Eun-Jung;Min, Kyung-Sok
    • Journal of Microbiology and Biotechnology
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    • 제22권3호
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    • pp.400-406
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    • 2012
  • To improve the hydrogen yield from biological fermentation of organic wastewater, a co-culture system of dark- and photo-fermentation bacteria was investigated. In a pure-culture system of the dark-fermentation bacterium Clostridium butyricum, a pH of 6.25 was found to be optimal, resulting in a hydrogen production rate of 18.7 ml-$H_2/l/h$. On the other hand, the photosynthetic bacterium Rhodobacter sphaeroides could produce the most hydrogen at 1.81mol-$H_2/mol$-glucose at pH 7.0. The maximum specific growth rate of R. sphaeroides was determined to be 2.93 $h^{-1}$ when acetic acid was used as the carbon source, a result that was significantly higher than that obtained using either glucose or a mixture of volatile fatty acids (VFAs). Acetic acid best supported R. sphaeroides cell growth but not hydrogen production. In the co-culture system with glucose, hydrogen could be steadily produced without any lag phase. There were distinguishable inflection points in a plot of accumulated hydrogen over time, resulting from the dynamic production or consumption of VFAs by the interaction between the dark- and photo-fermentation bacteria. Lastly, the hydrogen production rate of a repeated fed-batch run was 15.9 ml-$H_2/l/h$, which was achievable in a sustainable manner.

미생물에 의한 수소생산: Dark Anaerobic Fermentation and Photo-biological Process (Microbial hydrogen production: Dark Anaerobic Fermentation and Photo-biological Process)

  • 김미선;백진숙
    • KSBB Journal
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    • 제20권6호
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    • pp.393-400
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    • 2005
  • 수소를 생산하는 미생물은 크게 광합성 세균(photosynthetic bacteria), 혐기성세균(non-photosynthetic anaerobic bacteria), 조류(algae) 등으로 구분되고, 이들의 수소 생성 기작, 사용가능기질 및 수소 발생량은 상당한 차이가 있다. 광합성세균은 Rhodospirillaceae, Chromatiaceae 및 Chlorobiaceae로 구분되며, 이는 각각 홍색비유황세균(purple non-sulfur bacteria), 홍색유황세균(purple sulfur bacteria), 녹색유황세균(green sulfur bacteria)으로 통칭된다. 혐기성 세균은 절대 또는 통성혐기세균중 일부가 수소생산에 관여하며, 조류는 녹조류(green algae)와 남조류(blue-green algae, cyanobacteria)가 알려져 있다. 생물학적 수소생산 기술은 (1) 녹조류(green algae)가 광합성 메카니즘에 의해 수소를 생산하는 직접 물 분해 수소생산(direct bio-photolysis) (2) 광합성 작용에 의해 물을 분해하여 산소를 발생하고, 동시에 공기 중 이산화탄소를 고정하여 고분자 저장물질로 균체 내에 저장한 후 혐기 발효 또는 광합성 발효에 의해 수소를 발생하는 간접 물 분해 수소생산(indirect bio-photolysis or two stage photolysis) (3) 빛이 존재하는 혐기상태 배양 조건에서 홍색 세균에 의한 광합성 발효(photo-fermentation) 또는 (4) 광이 존재하지 않는 조건에서 혐기 미생물에 의해 수소와 유기산을 내는 혐기 발효(dark anaerobic fermentation) (5) 균체 외(in virro) 수소 발생 (6) 일산화탄소 가스 전환 반응(microbial gas shift reaction)에 의한 수소 생산 기술로 구분할 수 있다. 물로부터 생물학적 기술에 의한 수소생산은 공기 중의 이산화탄소를 고정하고, 수소와 산소를 발생하는 원천기술로써 오래 전부터 미국, 유럽에서 태양에너지를 이용하는 광합성 미생물의 분리, 개선 및 반응기에 관한 연구가 축적되어 왔으며, 유기물 즉 바이오매스로부터 혐기 및 광합성 발효를 연속적으로 적용하는 기술은 비교적 최근에 일본을 비롯한 유기성 폐기물이 많은 국가에서 수소에너지 생산과 유기성 폐기물 처리라는 두 가지 목적에 부합하는 연구로써 활발히 진행되고 있다. 유기성 폐기물이나 폐수와 같은 수분함량이 높은 바이오매스는 대부분이 매립처리 되는 실정이지만 높은 수분 함량 때문에 매립 시 발생하는 침출수는 환경오염의 주범으로 가까운 장래에는 매립도 금지될 전망이다. 이와 같은 수소에너지 생산기술과 이용시스템 개발은 화석연료 사용을 최소화 할 수 있으며, 국내에서 다량 발생하는 유기성 폐기물을 이용한 에너지 생산으로 자원 강대국 입지에 설 수 있다. 미생물에 의한 수소생산 기술은 청정에너지 생산과 아울러, 동시에 산소 발생, 공기 중 이산화탄소 고정, 식품공장 폐수 및 음식쓰레기와 같은 유기성 폐기물 처리 등 환경에 이로운 방향으로 진행될 뿐만 아니라, 미생물 자체가 갖는 생물 산업성도 높아서 비타민류, 천연색소, 피부암 치료제등의 고부가가치 의약품 생산도 활성화할 수 있다.

Effect of Initial Glucose Concentrations on Carbon and Energy Balances in Hydrogen-Producing Clostridium tyrobutyricum JM1

  • Jo, Ji-Hye;Lee, Dae-Sung;Kim, Jun-Hoon;Park, Jong-Moon
    • Journal of Microbiology and Biotechnology
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    • 제19권3호
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    • pp.291-298
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    • 2009
  • The carbon metabolism of newly isolated Clostridium tyrobutyricum JM1 was investigated at varying initial glucose concentrations (27.8-333.6mM). Because an understanding of metabolic regulations was required to provide guidance for further effective metabolic design or optimization, in this case, maximizing hydrogen production, carbon and energy balances by C. tyrobutyricum JM1 were determined and applied in anaerobic glucose metabolism. The overall carbon distribution suggested that initial glucose concentrations had strong influence on the stoichiometric coefficients of products and the molar production of ATP on the formation of biomass. C. tyrobutyricum JM1 had a high capacity for hydrogen production at the initial glucose concentration of 222.4 mM with high concentrations of acetate and butyrate.

해양바이오수소개발 사업의 상업생산을 위한 예비경제성평가 (Economic Feasibility Study for Commercial Production of Bio-hydrogen)

  • 박세헌;유영돈;강성균
    • Ocean and Polar Research
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    • 제38권3호
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    • pp.225-234
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    • 2016
  • This project sought to conduct an economic feasibility study regarding the commercial production of bio-hydrogen by the marine hyperthermophilic archaeon, Thermococcus onnurineus NA1 using carbon monoxide-containing industrial off-gas. We carried out the economic evaluation of the bio-hydrogen production process using the raw material of steel mill by-product gas. The process parameter was as follows: $H_2$ production rate was 5.6 L/L/h; the conversion of carbon monoxide was 60.7%. This project established an evaluation criterion for about 10,000 tonne/year. Inflation factors were considered as 3%. The operating costs were recalculated based on prices in 2014. The total investment required for development was covered 30% by capital and 70% by a loan. The operation cost for the 0.5-year test and integration, and the cost for the first three months in the 50% production period were considered as the working capital in the cost estimation. The costs required for the rental of office space, facilities, and other related costs from the construction through to full-scale production periods were considered as continuing expenses. Materials, energy, waste disposal and other charges were considered as the operating cost of the development system. Depreciation, tax, maintenance and repair, insurance, labor, interest rate charges, general and administrative costs, lubrication and miscellaneous expenses were also calculated. The hydrogen price was set at US$ 4.15/kg for the economic evaluation. As a result, the process was considered to be economical with the payback period of 6.3 years, NPV of 18 billion Won and IRR of 26.7%.

패류로부터 분리된 젖산균에 의한 젖산의 생산 (Production of Lactic Acid by Lactic Acid Bacteria Isolated from Shellfish)

  • 강창호;정호건;구자룡;소재성
    • KSBB Journal
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    • 제30권4호
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    • pp.161-165
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    • 2015
  • Lactic acid and its derivatives are widely used in the food, pharmaceutical, and cosmetic industries. It is also a major raw material for the production of poly-lactic acid (PLA), a biodegradable and environmentally friendly polymer and a possible alternative to synthetic plastics derived from petroleum. For PLA production by new strains of lactic acid bacteria (LAB), we screened LAB isolates from shellfish. A total of 51 LAB were isolated from 7 types of shellfishes. Lactic acid production of individual isolates was examined using high-performance liquid chromatography using a Chiralpak MA column and an ultraviolet detector. Lactobacillus plantarum T-3 was selected as the most stress-resistant strain, with minimal inhibition concentrations of 1.2 M NaCl, 15% ethanol, and 0.0020% hydrogen peroxide. In a 1 L fermentation experiment, $\small{D}$-lactic acid production of 19.91 g/L fermentation broth was achieved after 9 h cultivation, whereas the maximum production of total lactic acid was 41.37 g/L at 24 h.

연료전지차량용 연료개질기에 대한 최적연료비교연구 (A Comparative Study of Various Fuel for Newly Optimized Onboard Fuel Processor System under the Simple Heat Exchanger Network)

  • 정익환;박찬샘;박성호;나종걸;한종훈
    • Korean Chemical Engineering Research
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    • 제52권6호
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    • pp.720-726
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    • 2014
  • PEMFC(Proton Exchange Membrane Fuel Cell) 차량은 미래 청정수송기관으로 각광받고 있지만 수소스테이션의 인프라부족으로 현재는 수소를 공급해주는 연료개질기를 함께 장착하여 구동하여야 한다. 탄화수소연료로부터 수소를 생산하는 연료개질기를 대상으로 다양한 연구가 진행되어왔는데 기존연구에서는 열적중립 조건의 ATR(Auto-Thermal Reformer) 반응기에 대해 집중적으로 분석하거나 공정최적화부문에서 최대수소생산을 목표로 주로 열효율을 목적함수로 설정하여 평가해 왔다. 본 연구에서는 100 kW PEMFC용 연료개질기를 대상으로 간단한 소형시스템을 얻기 위해 외부 유틸리티가 필요없는 단열열교환망으로 구성된 조건에서 기존 열효율이 아닌 수소효율을 새로이 정의하여 가솔린, LPG, 디젤 각 연료에 대해 최적운전조건을 도출하였다. 가솔린의 경우 기존 비교문헌보다 9.43% 연료절감효과를 얻음으로써 제안한 목적함수의 타당성을 입증하였고, 추가적으로 수소효율 및 열교환량, 열교환면적에 대한 민감도 분석을 실시하였다. 마지막으로 제안한 시스템을 한국시장에 적용할 경우 LPG 연료를 사용하는 연료개질기가 가장 경제적임을 알 수 있었다.

각종 혐기성 미생물 발효에 의한 유기산 및 수소생산 (Hydrogen and Organic Acids Production by Fermentation Using Various Anaerobic Bacteria)

  • 김미선;윤영수;심상준;박태현;이정국
    • 한국수소및신에너지학회논문집
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    • 제13권4호
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    • pp.321-329
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    • 2002
  • Clostridium butyricum, Lactobacillus amylophillus, Lactobacillus amylovorus, Lactobacillus acidophillus, AI-9 produced hydrogen and /or organic acids using glucose, lactose and starch at the anaerobic culture conditions. Cl. butyricum NCIB 9576 evolved 1,700 ml H2/L-culture broth and accumulated butyric acid, acetic acid, propionic acid and ethanol in its culture broth when lactose was used as a carbon source during 24 hrs of fermentation. L. amylovorus ATCC 33620 accumulated lactic and acetic acids and some reducing sugars when starch was used as a carbon source without hydrogen production. Instead of starch as a carbon source, L. amylovorus ATCC 33620 produced lactic acid from algal biomass during fermentation and the acid-heat or freeze-thaw pretreatment of algal biomass accelerate the lactic acid fermentation.

산업배열 및 부산물을 활용한 1톤급 바이오수소 생산 시뮬레이터 동적 열설계 (Dynamic thermal Design of a 1-ton Class Bio-Hydrogen Production System Simulator Using Industrial Waste Heat and by-Products)

  • 김혜준;김석연;안준
    • 설비공학논문집
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    • 제29권5호
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    • pp.259-268
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    • 2017
  • This paper proposes a hydrogen-based social economy derived from fuel cells capable of replacing fossil fuels and resolving global warming, It thus provides an entry for developing economically feasible social configurations to make use of bio-hydrogen production systems. Bio-hydrogen production works from the principle that microorganisms decompose water in the process of converting CO to $CO_2$, thereby producing hydrogen. This study parts from an analysis of an existing 157-ton class NA1 bio-hydrogen reactor that identifies the state of feedstock and reactor conditions. Based on this analysis, we designed a 1-ton class bio-hydrogen reactor process simulator. We carried out thermal analyses of biological heat reactions, sensible heat, and heat radiation in order to calculate the thermal load of each system element. The reactor temperature changes were determined by modeling the feed mixing tank capacity, heat exchange, and heat storage tank. An analysis was carried out to confirm the condition of the feed mixing tank, heat exchanger, heat storage tank capacity as well as the operating conditions of the system so as to maintain the target reactor temperature.