• 제목/요약/키워드: Bioethanol

검색결과 232건 처리시간 0.028초

유채유를 이용한 바이오디젤의 Emergy 분석

  • 장혜현;이석모
    • 한국환경과학회:학술대회논문집
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    • 한국환경과학회 2007년도 춘계 학술발표회 발표논문집
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    • pp.539-541
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    • 2007
  • 유채유를 이용한 바이오디젤의 실질적인 가치는 배럴당 355,000원으로, 현재의 가격은 평가절하되어 있으며 에머지 생산비율(EYR)은 1.27으로서 석유의 8.4에 비하여 효율이 낮아 대체에너지로서의 경쟁력은 없으나 1보다 높아 에너지 소비 절감의 효과는 있다. 환경부하비율(ELR)은 2.46으로 수력발전의 3.3과 Bioethanol의 7.7보다 낮아 환경에 미치는 영향은 작은 것으로 나타났다. 에머지 지속가능성지수(ESI)는 0.52로 재생불가능한 에너지와 외부에서 구입한 재화와 용역에 대한 의존도가 높으므로 지속성이 낮은 것으로 나타났다.

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볏짚으로부터 바이오에탄올 생산을 위한 전처리 및 당화 연구 (Study on Pre-treatment & Saccharification of Rice straw for Bioethanol Production)

  • 이준표;박지연;김덕근;이진석;박순철
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2010년도 추계학술대회 초록집
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    • pp.104.2-104.2
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    • 2010
  • 농산 부산물인 볏짚을 이용하여 수송연료인 휘발유를 대체할 수 있는 바이오에탄올을 생산하기 위한 전단계인 전처리와 당화에 대한 연구를 수행하였다. 볏짚은 농산 부산물 중에서 비교적 발생량이 많으며, 목질계 바이오매스에 비해 소프트하기 때문에 전처리가 용이하다는 장점이 있다. 전처리 방법으로는 여러 가지가 있으나, 본 연구에서는 증기폭쇄에 의한 전처리 방법을 채택하였다. 당화실험은 생물학적 방법인 효소당화를 하였다. 전처리 실험결과 온도가 낮고 처리 시간이 짧을수록 고형물 및 삼성분에 대한 수율이 높은 것으로 나타났다. 삼성분 중의 Glucan 수율은 $180^{\circ}C$ 실험에서 68-71%를 보였으며, $200^{\circ}C$ 실험에서는 59-64%를 보였다. Xylan은 거의 대부분이 소실되어 Xylan을 회수하는 전처리로써는 적합하지 않은 방법으로 나타났다. 반면 Lignin은 거의 제거가 되지 않았다. 당화 실험결과 $180^{\circ}C$에서 전처리한 폭쇄재는 당화 수율이 50%에도 미치지 못하였으나, $200^{\circ}C$에서 전처리한 폭쇄재는 70% 내외를 보여 주었다. 특히 분쇄 세척 멸균한 효소당화 수율은 90%가 넘는 높은 수율을 보였다. 전처리 수율과 당화수율을 종합하여 수율을 분석한 결과 $200^{\circ}C$ 전처리 실험조건에서 효소당화시 미처리 시료와 분쇄 세척 시료보다 멸균까지 실시한 조건에서 Glucan의 종합수율이 55% 내외로 월등히 높은 것으로 나타났다. 증기폭쇄에 의한 볏짚의 전처리는 Glucan의 수율이 낮아 손실이 많은 것으로 나타났으며, 이를 보완할 수 있는 전처리 조건 혹은 다른 전처리 방안이 요구된다.

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Pretreatment and enzymatic saccharification process of rapeseed straw for production of bioethanol

  • Lee, Heon-Hak;Jeon, Min-Ki;Yoon, Min-Ho
    • 농업과학연구
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    • 제43권4호
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    • pp.641-649
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    • 2016
  • This study was conducted to evaluate the yield of bio-ethanol produced by separate hydrolysis and fermentation (SHF) with the pretreated rapeseed straw (RS) using crude enzyme of Cellulomonas flavigena and Saccharomyces cereviase. Crude enzyme of C. flavigena showed enzymatic activity of 14.02 U/mL for CMC 133.40 U/mL, for xylan 15.21 U/mL, for locust gum and 15.73 U/mL for rapeseed straw at pH 5.0 and $40^{\circ}C$, respectively. The hemicellulose contents of RS was estimated to compromise 36.62% of glucan, 43.20% of XMG (xylan + mannan + galactan), and 2.73% of arabinan by HPLC analysis. The recovering ratio of rapeseed straw were investigated to remain only glucan 75.2% after 1% $H_2SO_4$ pretreatment, glucan 45.44% and XMG 32.13% after NaOH, glucan 44.75% and XMG 5.47% after $NH_4OH$, and glucan 41.29% and XMG 41.04% after hot water. Glucan in the pretreatments of RS was saccharified to glucose of 45.42 - 64.81% by crude enzyme of C. flavigena while XMG was made into to xylose + mannose + galactose of 58.46 - 78.59%. Moreover, about 52.88 - 58.06 % of bio-ethanol were obtained from four kinds of saccharified solutions by SHF using S. cerevisiae. Furthermore, NaOH pretreatment was determined to show the highest mass balance, in which 21.22 g of bio-ethanol was produced from 100 g of RS. Conclusively, the utilization of NaOH pretreatment and crude enzyme of Cellulomonas flavigena was estimated to be the best efficient saccharification process for the production of bio-ethanol with rapeseed straw by SHF.

Performance and Spatial Succession of a Full-Scale Anaerobic Plant Treating High-Concentration Cassava Bioethanol Wastewater

  • Gao, Ruifang;Yuan, Xufeng;Li, Jiajia;Wang, Xiaofen;Cheng, Xu;Zhu, Wanbin;Cui, Zongjun
    • Journal of Microbiology and Biotechnology
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    • 제22권8호
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    • pp.1148-1154
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    • 2012
  • A novel two-phase anaerobic treatment technology was developed to treat high-concentration organic cassava bioethanol wastewater. The start-up process and contribution of organics (COD, total nitrogen, and $NH_4^+$-N) removal in spatial succession of the whole process and spatial microbial diversity changing when sampling were analyzed. The results of the start-up phase showed that the organic loading rate could reach up to $10kg\;COD/m^3d$, with the COD removal rate remaining over 90% after 25 days. The sample results indicated that the contribution of COD removal in the pre-anaerobic and anaerobic phases was 40% and 60%, respectively, with the highest efficiency of 98.5%; TN and $NH_4^+$-N had decreased to 0.05 g/l and 0.90 g/l, respectively, and the mineralization rate of total nitrogen was 94.8%, 76.56% of which was attributed to the anaerobic part. The microbial diversity changed remarkably among different sample points depending on the physiological characteristics of identified strains. Moraxellaceae, Planococcaceae, and Prevotellaceae were dominant in the pre-anaerobic phase and Bacteroidetes, Campylobacterales, Acinetobacter, Lactobacillus, Clostridium, and Bacillus for the anaerobic phase. Methanosarcinaceae and Methanosaeta were the two main phylotypes in the anaerobic reactor.

Optimization of The Organosolv Pretreatment of Yellow Poplar for Bioethanol Production by Response Surface Methodology

  • Kim, Ho-Yong;Hong, Chang-Young;Kim, Seon-Hong;Yeo, Hwanmyeong;Choi, In-Gyu
    • Journal of the Korean Wood Science and Technology
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    • 제43권5호
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    • pp.600-612
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    • 2015
  • We investigated the optimization of the organosolv pretreatment of yellow poplar for bioethanol production. Response surface methodology was used to determine the optimal conditions of three independent variables (reaction temperature, reaction time, and sulfuric acid (SA) concentration). Reaction temperature is the most significant variable in the degradation of xylan and lignin in the presence of an acid catalyst, and ethanol production increased with a decrease in the lignin content. The highest ethanol concentration ($42.80g/{\ell}$) and theoretical ethanol yield (98.76%) were obtained at $152^{\circ}C$ (2.5 bar) with 1.6% SA for 16 min. However, because of excessive degradation of the raw material, the overall ethanol yield was less than under other pretreatment conditions which has approximately 50% of WIS recovery rate after pretreatment. The optimal conditions for the maximum overall ethanol yield ($146^{\circ}C$ with 1.22% SA for 15.9 min) were determined with a predicted yield of 17.11%, and the experimental values were very close (17.15%). Therefore, the quadratic model is reliable.

신 재생에너지로서 바이오매스에 대한 현황 고찰 (Overview of the Biomass as a Renewable Energy)

  • 이진휘;김재곤;임의순;정충섭;임화준
    • 한국응용과학기술학회지
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    • 제29권4호
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    • pp.638-652
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    • 2012
  • 본 연구는 바이오매스에 기인한 에너지와 관련하여, 첨부된 문헌에 의하여 작성되었으며, 바이오에탄올, 바이오디젤 및 바이오가스에 대하여 본 논문을 작성하게 된 배경, 제조공정, 각국의 생산량, 시장현황, 규격 및 정책을 다루었다. 이 논문은 바이오 에너지와 관련하여 전반적인 지식과 장차 바람직한 방향을 모색하는 데에 도움을 줄 것이다. 바이오에너지는 신재생에너지로서 유용한 에너지이며, 다각도로 활용 방안을 모색하여야 한다. 결론에 현재의 상황을 고려하여 몇가지 방향을 제시하였다.

초식동물 배설물로부터 분리한 Bacillus sp. H9-1의 섬유소 분해효소생산 최적화 (Optimization of Cellulolytic Enzyme Production for newly isolated Bacillus sp. H9-1 from Herbivore Feces)

  • 윤영미;안기홍;김중곤;차영록;박유리;안종웅;문윤호;안승현;구본철;박광근
    • KSBB Journal
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    • 제28권1호
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    • pp.42-47
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    • 2013
  • This study was performed to find cellulolytic strain of enzymatic saccharification for bioethanol production. Cellulolytic strains were isolated from 59 different feces of herbivores from Seoul Grand Park located in Gwacheon Gyeonggi-Do. The celluloytic strain was selected by congo red staining and DNS method. Among the isolated strains, H9-1 strain isolated from the feces of rabbit has the highest CMCase activity. H9-1 strain was identified as Bacillus sp. based on 16S rDNA gene sequencing. The optimal conditions for CMCase activity by Bacillus sp. H9-1 were at $40^{\circ}C$ and at initial pH 8.

Construction of a Thermotolerant Saccharomyces cerevisiae Strain for Bioethanol Production with Reduced Fermentation Time and Saccharifying Enzyme Dose

  • Lim, Ji Sung;Jang, You Ri;Lim, Young Hoon;Kim, Keun
    • Journal of Microbiology and Biotechnology
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    • 제22권10호
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    • pp.1401-1405
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    • 2012
  • A thermotolerant Saccharomyces cerevisiae mutant strain, TT6, was constructed after multi-parental hybridization of five mutant strains obtained by UV or NTG treatment of the original strain, S. cerevisiae KV1. When incubated at $40^{\circ}C$ in YPD broth, TT6 began to grow exponentially in 10 h, but KV1 did not show any noticeable growth even after 22 h. The thermotolerant growth of TT6 was confirmed by serial dilution assay at $42^{\circ}C$; TT6 grew at a cell concentration ($10^{-5}$) 10,000 times lower than that of KV1 ($10^{-1}$). Whereas ethanol production from YP containing 23% (w/v) glucose by KV1 decreased with increasing temperature from $30^{\circ}C$ to $36^{\circ}C$, ethanol production by TT6 did not decrease at temperatures up to $37^{\circ}C$. When TT6 was tested for ethanol production at $36^{\circ}C$ by simultaneous saccharification and fermentation (SSF) from 23% corn, 24 h of fermentation time or 50% of the glucoamylase dose was saved when compared with KV1 at $30^{\circ}C$. The ethanol yield from corn by SSF with TT6 at $36^{\circ}C$ was 91.7% of the theoretical yield, whereas that of KV1 at $30^{\circ}C$ was 90.6%.