• 제목/요약/키워드: biomass production

검색결과 1,543건 처리시간 0.023초

Fungal Fermentation of Lignocellulosic Biomass for Itaconic and Fumaric Acid Production

  • Jimenez-Quero, A.;Pollet, E.;Zhao, M.;Marchioni, E.;Averous, L.;Phalip, V.
    • Journal of Microbiology and Biotechnology
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    • 제27권1호
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    • pp.1-8
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    • 2017
  • The production of high-value chemicals from natural resources as an alternative for petroleum-based products is currently expanding in parallel with biorefinery. The use of lignocellulosic biomass as raw material is promising to achieve economic and environmental sustainability. Filamentous fungi, particularly Aspergillus species, are already used industrially to produce organic acid as well as many enzymes. The production of lignocellulose-degrading enzymes opens the possibility for direct fungal fermentation towards organic acids such as itaconic acid (IA) and fumaric acid (FA). These acids have wide-range applications and potentially addressable markets as platform chemicals. However, current technologies for the production of these compounds are mostly based on submerged fermentation. This work showed the capacity of two Aspergillus species (A. terreus and A. oryzae) to yield both acids by solid-state fermentation and simultaneous saccharification and fermentation. FA was optimally produced at by A. oryzae in simultaneous saccharification and fermentation (0.54 mg/g wheat bran). The yield of 0.11 mg IA/g biomass by A. oryzae is the highest reported in the literature for simultaneous solid-state fermentation without sugar supplements.

Effect of Culture Conditions on Growth and Production of Docosahexaenoic Acid (DHA) using Thraustochytrium aureum ATCC 34304

  • Hur Byung-Ki;Cho Dae-Won;Kim Ho-Jung;Park Chun-Ik;Suh Hyung-Joon
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제7권1호
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    • pp.10-15
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    • 2002
  • Environmental and medium factors were investigated as basic data for optimizing DHA production when using Thraustochytrium aureum. To study the effect of environmental conditions, the rotation speed and culture temperature were changed. Plus the trend of the growth characteristics, lipid content in the biomass, and DHA content in lipids were evaluated according to various initial glucose concentrations. The biomass, lipid, and DHA analyses showed that the physiological characteristics of T. aureum were closely related with the environmental and medium conditions, as in the case of other marine microorganisms. For example, a low rotation speed of 50 rpm lowered the cell growth rate as well as the DHA content in the lipids. A low temperature had a negative effect on the cell growth, yet a positive effect on the lipid content in the biomass. Different initial glucose concentrations had no effect on the lipid content in the biomass or DHA content in the lipids, yet did affect the cell growth. Accordingly, these results show that environmental and medium factors must be synthetically considered in order to optimize DHA production when using T. aureum.

Fertilization Effects on Fine Root Biomass, Production, and Turnover Rate in a Pinus rigida Plantation

  • Hwang, Jaehong;Son, Yowhan
    • The Korean Journal of Ecology
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    • 제26권2호
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    • pp.59-64
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    • 2003
  • We examined the effects of fertilization [control (C), 200 kg N ha^{-1} + 25 kg P ha^{-1}$ (LNP), and 400 kg N $ha^{-1} + 50 kg P ha^{-1}$ (HNP)] on fine root (< 2 mm diameter) dynamics using monthly soil coring method in a 39-year-old Pinus rigida plantation of central Korea. The average fine root biomass (live + dead) (kg $ha^{-1}$ $\pm$ SE) during the first growing season for C, LNP, and HNP was 1301 $\pm$ 54, 1084 $\pm$ 47, and 1328 $\pm$ 22, respectively. The fine root production (kg $ha^{-1}$ $\pm$ SE) was 2394 $\pm$ 128 for C, 2048 $\pm$ 101 for LNP, and 2768 $\pm$ 150 for HNP, respectively. Over the same period, fertilization treatments had impact on N and P concentrations of live fine root. Nitrogen and P inputs (kg $ha^{-1}$ $yr^{-1}$) into the soil through fine root turnover for C, LNP, and HNP were 16.6 and 0.9, 17.2 and 0.9, and 24.1 and 1.6, respectively. There were no significant differences in fine root biomass and production during the first growing season after fertilization. However, fertilization increased fine root N and P concentrations, and in consequence resulted in increased N and P inputs into soil through fine root turnover.

고창지역 소나무림의 바이오매스 및 순생산량에 관한 연구 (Biomass and Net Primary Production of Pinus densiflora Stands in Gochang regions)

  • 서연옥;이영진
    • 농업생명과학연구
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    • 제44권5호
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    • pp.45-53
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    • 2010
  • 본 연구의 목적은 전라북도 고창군 일대의 소나무림을 대상으로 바이오매스 추정식을 개발하고 이를 바탕으로 바이오매스 및 순생산량, 줄기밀도와 바이오매스 확장계수를 분석하고자 하였다. 유령임분과 성숙임분의 경우 평균 임령이 각각 10년과 48년으로 나타났으며 임목 전체 건중량은 8.59 kg, 166.66 kg으로 나타났고 임분밀도를 고려한 단위면적당 지상부 건중량은 17.55 Mg/ha, 122.05 Mg/ha으로 나타났다. 지하부를 포함한 임목전체 건중량은 21.48 Mg/ha, 154.16 Mg/ha으로 나타났다. 부위별 바이오매스 구성비는 유령임분에서 성숙임분으로 갈수록 줄기목질부, 줄기 수피, 뿌리는 증가하는 경향을 보이는 반면, 잎, 가지 구성비는 감소하는 경향으로 나타났다. 지상부 순생산량은 유령임분에서 6.30 Mg/ha으로 나타났고 임목 전체에서는 6.95 Mg/ha으로 나타났으며, 성숙 임분에서 11.61 Mg/ha, 임목전체에서 13.19 Mg/ha으로 나타났다. 줄기밀도($g/cm^3$)는 유령임분과 성숙임분에서 각각 0.338, 0.448로 나타났으며, 임령이 증가함에 따라 증가하는 일반적인 경향으로 나타났다. 바이오매스 확장계수는 유령임분과 성숙임분에서 각각 2.304~2.508, 1.318~1.644의 범위로 나타났다.

농업부산물 부존량 조사 및 발전 가능량의 추정 (Estimation of Power Generation Capacity from Agricultural Biomass)

  • 홍성구
    • 한국농공학회:학술대회논문집
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    • 한국농공학회 2003년도 학술발표논문집
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    • pp.595-598
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    • 2003
  • Elemental data was collected for agricultural biomass such as pruned branches with respect to unit area production and heating values. The results indicated that higher heating values for the biomass was comparable to those of woody biomass. Approximate estimations of power generation from biomass showed that over 100kW power plants could be installed in some districts.

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바이오리파이너리를 이용한 바이오연료 및 바이오화합물의 생산 (Production of Biofuels and Biochemicals by Biorefinery)

  • 이채영;한선기
    • 한국수소및신에너지학회논문집
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    • 제27권6호
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    • pp.702-711
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    • 2016
  • The authors reviewed information about biorefining of biomass by using academic information databases. Feedstocks were classified into triglycerides biomass, sugar biomass, starchy biomass, lignocellulosic biomass, and organic waste biomass. Biorefinery is an integrated system converting biomass into biofuels and biochemicals by various physical, chemical, biological, and thermochemical technologies. This paper presented a comprehensive summaries of opportunities, recent trends and challenges of biorefinery. A brief overview of promising building blocks, their sources from biomass, and their derivatives were also provided. In conclusion, this paper demonstrated the feasibility of biorefinery producing biofuels and biochemicals from biomass.

갈락토스-글루코스 혼합당 수소 발효 (Hydrogen Fermentation of the Galactose-Glucose Mixture)

  • 천효창;김상현
    • 한국수소및신에너지학회논문집
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    • 제23권4호
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    • pp.397-403
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    • 2012
  • Galactose, an isomer of glucose with an opposite hydroxyl group at the 4-carbon, is a major fermentable sugar in various promising feedstock for hydrogen production including red algal biomass. In this study, hydrogen production characteristics of galactose-glucose mixture were investigated using batch fermentation experiments with heat-treated digester sludge as inoclua. Galactose showed a hydogen yield compatible with glucose. However, more complicated metabolic steps for galactose utilization caused a slower hydrogen production rate. The existence of glucose aggravated the hydrogen production rate, which would result from the regulation of galactose-utilizing enzymes by glucose. Hydrogen produciton rate at galactose to glucose ratio of 8:2 or 6:4 was 67% of the production rate for galactose and 33% for glucose, which could need approximately 1.5 and 3 times longer hydraulic retention time than galacgtose only condition and glucose only condition, respectively, in continuous fermentation. Hydrogen production rate, Hydrogen yield, and organic acid production at galactose to glucose ratio of 8:2 or 6:4 were 0.14 mL H2/mL/hr, 0.78 mol $H_2$/mol sugar, and 11.89 g COD/L, respectively. Galactose-rich biomass could be usable for hydogen fermenation, however, the fermentation time should be allowed enough.

Biomass Production Potential of Chlorella vulgaris Under Different CO2 Concentrations and Light Intensities

  • Lee, Chang-Min;Kim, Mi-Jeong;Sanjay, Kumar;Kwag, Jung-Hoon;Ra, Chang-Six
    • Journal of Animal Science and Technology
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    • 제53권3호
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    • pp.261-268
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    • 2011
  • The increasing demand of the crops (soybean and corn) for biofuel production has increased the focus of the animal nutritionists to look for alternative feeds, which are economic and environmental friendly. To identify microalgae as suitable candidate as an alternative feed, growth response of Chlorella vulgaris was studied under varying concentrations of carbon dioxide (0.07, 1.4, 3.0 and 5.0%) and photon densities (39.19, 72.97, 105.41, 116.22, 135.14, $175.68\;{\mu}mol/m^2/s$) by employing a photo-bioreactor. Swine wastewater was also investigated as nutritional source to economize the biomass production. Results showed that the higher biomass production was found to be at 3.0% $CO_2$ compared to other $CO_2$ concentrations. However, no difference in biomass production was found at $105.41\;{\mu}mol/m^2/s$ and above photon densities with 12 h of photoperiodicity. It was observed that C. vulgaris could easily grow in 200 times diluted swine wastewater and growth was found to be similar with that of artificial medium. Provided the conducive conditions for optimal growth, it has also the potentiality of depleting ammonia nitrogen ($NH_4$-N) and orthophosphate ($PO_4^{3-}$-P) completely from the wastewater after 3~4 days of cultivation. Thus, growing C. vulgaris would not only solve the problem of animal feed, but also help in biological $CO_2$ mitigation and wastewater treatment.

Ammonium Production During the Nitrogen-Fixing Process by Wild Paenibacillus Strains and Cell-Free Extract Adsorbed on Nano $TiO_2$ Particles

  • Shokri, Dariush;Emtiazi, Giti
    • Journal of Microbiology and Biotechnology
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    • 제20권8호
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    • pp.1251-1258
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    • 2010
  • During the nitrogen-fixing process, ammonia ($NH_3$) is incorporated into glutamate to yield glutamine and is generally not secreted. However, in this study, $NH_3$-excreting strains of nitrogen-fixing Paenibacillus were isolated from soil. The ammonium production by the Paenibacillus strains was assayed in different experiments (dry biomass, wet biomass, cell-free extract, and cell-free extract adsorbed on nano $TiO_2$ particles) inside an innovative bioreactor containing capsules of $N_2$ and $H_2$. In addition, the effects of different $N_2$ and $H_2$ treatments on the formation of $NH_3$ were assayed. The results showed that the dry biomass of the strains produced the most $NH_3$. The dry biomass of the Paenibacillus strain E produced the most $NH_3$ at 1.50, 0.34, and 0.27 ${\mu}M$ $NH_3$/mg biomass/h in the presence of $N_2$ + $H_2$, $N_2$, and $H_2$, respectively, indicating that a combined effluent of $N_2$ and $H_2$ was vital for $NH_3$ production. Notwithstanding, a cell-free extract (CFE) adsorbed on nano $TiO_2$ particles produced the most $NH_3$ and preserved the enzyme activities for a longer period of time, where the $NH_3$ production was 2.45 ${\mu}M$/mg CFE/h over 17 h. Therefore, the present study provides a new, simple, and inexpensive method of $NH_3$ production.

Production and Characterization of Multi-Polysaccharide Degrading Enzymes from Aspergillus aculeatus BCC199 for Saccharification of Agricultural Residues

  • Suwannarangsee, Surisa;Arnthong, Jantima;Eurwilaichitr, Lily;Champreda, Verawat
    • Journal of Microbiology and Biotechnology
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    • 제24권10호
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    • pp.1427-1437
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    • 2014
  • Enzymatic hydrolysis of lignocellulosic biomass into fermentable sugars is a key step in the conversion of agricultural by-products to biofuels and value-added chemicals. Utilization of a robust microorganism for on-site production of biomass-degrading enzymes has gained increasing interest as an economical approach for supplying enzymes to biorefinery processes. In this study, production of multi-polysaccharide-degrading enzymes from Aspergillus aculeatus BCC199 by solid-state fermentation was improved through the statistical design approach. Among the operational parameters, yeast extract and soybean meal as well as the nonionic surfactant Tween 20 and initial pH were found as key parameters for maximizing production of cellulolytic and hemicellulolytic enzymes. Under the optimized condition, the production of FPase, endoglucanase, ${\beta}$-glucosidase, xylanase, and ${\beta}$-xylosidase was achieved at 23, 663, 88, 1,633, and 90 units/g of dry substrate, respectively. The multi-enzyme extract was highly efficient in the saccharification of alkaline-pretreated rice straw, corn cob, and corn stover. In comparison with commercial cellulase preparations, the BCC199 enzyme mixture was able to produce remarkable yields of glucose and xylose, as it contained higher relative activities of ${\beta}$-glucosidase and core hemicellulases (xylanase and ${\beta}$-xylosidase). These results suggested that the crude enzyme extract from A. aculeatus BCC199 possesses balanced cellulolytic and xylanolytic activities required for the efficient saccharification of lignocellulosic biomass feedstocks, and supplementation of external ${\beta}$-glucosidase or xylanase was dispensable. The work thus demonstrates the high potential of A. aculeatus BCC199 as a promising producer of lignocellulose-degrading enzymes for the biomass conversion industry.