• Title/Summary/Keyword: Biomass to Liquid

검색결과 219건 처리시간 0.035초

BTL(Biomass to Liquid) 기술 현황 (Development Status of BTL (Biomass to Liquid) Technology)

  • 채호정;정광은;김철웅;정순용
    • 에너지공학
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    • 제16권2호
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    • pp.83-92
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    • 2007
  • 석유자원 고갈에 따른 대체에너지 개발의 필요성과 더불어 온실가스인 $CO_{2}$ 저감 등 높은 환경개선 효과로 인하여 새로운 청정연료로 바이오매스로부터 제조되는 BTL(Biomass to Liquid)-디젤에 대한 관심이 유럽을 중심으로 크게 증가하고 있다. 본 논문에서는 BTL-디젤 기술 개발 현황 및 BTL 공정의 세부 공정기술들을 조사하였다. BTL 공정은 바이오매스 전처리 및 가스화, 합성가스 정제, F-T(Fischer-Tropsch) 합성 및 upgrading 공정 등으로 나눌 수 있으며, BTL 만의 차별적 기술로 합성가스 제조를 위한 가스화 공정과 함성가스 조성 조절을 포함하는 BTL 공정에 최적화된 F-T 합성 촉매 개발이 매우 중요하다. 대표적인 BTL 기술로 독일의 Choren 사는 Carbo-V 가스화 기술을 개발하여 세계 최초로 BTL 공정 상업화를 이루었으며, 네덜란드의 ECN은 tar와 BTX를 제거하기 위한 독자적인 OLGA 기술을 개발하여 가스화 시스템과 연계한 공정을 개발하였다. 또한 미국과 일본 등 많은 나라에서 경쟁적으로 기술개발을 재촉하고 있는 상황이다. 국내의 경우 이에 대한 연구는 전무하나 국내 에너지 안보를 위한 에너지 Mix 정책과 지구온난화 등 환경문제에 대응하기 위하여 BTL 기술 개발은 매우 중요한 의미를 가질 수 있으므로 독창적 기술의 선점이 매우 중요할 것으로 판단된다.

SCB액비가 속성수의 생장 및 biomass 생산에 미치는 영향 (Growth and Biomass Production of Fast Growing Tree Species Treated with Slurry Composting and Biofiltration Liquid Fertilizer)

  • 김현철;여진기;구영본;신한나;최진용;이헌호
    • 한국토양비료학회지
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    • 제44권2호
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    • pp.206-214
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    • 2011
  • SCB액비, 저장액비, 화학비료, 지하수 및 무처리에 따른 포플러 및 버드나무 클론, 백합나무의 생존율은 전체 평균 94.4%로 나타나 양호하였으며, 잎과 줄기의 비율은 각각 63.5%, 36.5%로 매년수확구의 식재당년 지상부 biomass는 잎의 비율이 높았다. 처리구별 줄기발생 수는 SCB액비, 저장액비, 화학비료, 지하수 및 무처리구가 평균 4.2, 4.6, 4.5, 4.7, 4.9개로 크게 차이가 나타나지 않았으며 버드나무 클론들의 줄기 수가 포플러 클론 및 백합나무 보다 많았다. 줄기직경과 지상부 biomass에 대하여 개체당 유도된 회귀모델을 통해 추정된 biomass 생산량은 화학비료>저장액비>지하수>SCB액비>무처리구 순으로 나타났다. 수종 및 클론별 지상부 biomass 생산량은 모든 처리구에서 현사시 클론들이 우수하게 나타났으며, SCB액비 처리에 따른 잎과 줄기의 질소함량을 분석한 결과 무처리구 보다 질소함 량이 높게 나타나 SCB액비에 함유된 질소를 체내에 흡수하는 것으로 판단된다. 따라서, SCB액비를 biomass 매년수확구에 처리한 결과 화학비료, 저장액비, 지하수 처리구보다 생산량이 적게 나타났지만 무처리구 보다는 생산량이 증가하여 향후 처리방법이나 적정 처리량 등을 구명하여 적용한다면 화학비료와 비슷한 효과를 얻을 수 있고 가축분뇨 처리비용도 절감할 수 있을 것으로 판단된다. 그러나 본 연구는 biomass 매년수확구의 식재당년의 결과이며, 식재한 묘목의 수령이 증가하고 입지환경에 적응되면 바이오매스 생산량도 대폭 증가할 것이므로 이와 같은 연구가 반복적으로 수행되어야 보다 확실한 결과를 얻을 수 있을 것으로 생각된다.

Production of mass microorganisms by using simple liquid culture facility to fit the field scale test.

  • Hong, Yeon-Kyu;Jung, Won-Kwon;Song, Seok-Bo;Hyun, Jong-Nae;Park, Sung-Tae;Kim, Soon-Chul
    • 한국식물병리학회:학술대회논문집
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    • 한국식물병리학회 2003년도 정기총회 및 추계학술발표회
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    • pp.107.1-107
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    • 2003
  • The fermentation process and subsequent processing determine the efficacy of a bioherbicide propagule. Large batches of biomass of the mycoherbicide agent for white clover, Sclerotium sp.(BWC98-105) was produced in simple liquid fermentator in 5 gallons vessels(Model No. 8087, Dabo Inc., Korea) with oxygen supply(DPH16000, FineTech Inc., Korea) simulating industrial conditions by utilizing commercially available, inexpensive ingredients (10 % rice bran), The maximum biomass yield of Sclerotium sp.(BWC98-105) was obtained after 5 days of air pumped incubation at room temperature condition(22-28$^{\circ}C$). By using this simple facility, it could get fragmented or proliferated greatly and attained maximum mycelia biomass. The biomass of mycoherbicide agent consisted of hyphae devoid of spores. Biomass mycelia of the fungus 99% survival at room temperature after 2 me. A thorough understanding of the effects of fermentation and formulation on viability and virulence is required to guide these processes. After an economical yield level of bioherbicide propagule has been achieved in a fermentation process, formulation becomes a critical factor which influences product efficacy. Because the fermentation must be stopped at a point when virulence/viability are optimum, the live bioherbicide propagule must be stabilized, formulated, and packaged.

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Enhancing the Absorption Properties of Biomass-based Superabsorbent Terpolymer

  • Kim, Jung Soo;Kim, Dong Hyun
    • Elastomers and Composites
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    • 제55권4호
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    • pp.249-256
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    • 2020
  • Superabsorbent polymers (SAPs) can absorb and retain ten to thousand times their dry mass of water because of their three-dimensional hydrophilic structures. Conventional SAPs are mainly composed of poly(acrylic acid sodium salt) derived from petrochemicals. The present work is aimed at limiting the use of the petrochemical component by replacing it with a biomass-based material. First, the core-SAP was prepared via the terpolymerization of itaconic acid, vinylsulfonic acid, and cellulose, and the optimum conditions in terms of material input ratio were determined. Following this, the core-SAP was surface-crosslinked by esterification with butane diol to improve its liquid permeability and absorbency under load (AUL). The liquid permeability was measured according to the amount of 0.9 wt.% NaCl solution passing between the swollen SAP particles under a given pressure, and the AUL was estimated from the weight of this solution absorbed under 0.3 psi pressure.

펜톤산화에 의한 바이오매스 분해향상과 펜톤산화 용액 재사용 평가 (Improvement of Biomass Degradation by Fenton Oxidation and Reusability of the Fenton Oxidation Solution)

  • 정소연;이재원
    • 신재생에너지
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    • 제16권4호
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    • pp.83-91
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    • 2020
  • In this study, the reusability of the Fenton oxidation solution was evaluated to reduce the cost of the pretreatment process. Biomass was sequential subjected to Fenton oxidation-hydrothermal treatment and enzymatic hydrolysis to produce monosaccharides. The liquid solution recovered after Fenton oxidation contained OH radicals with a concentration of 0.11 mol/L. This liquid solution was reused for a new Fenton oxidation reaction. After Fenton oxidation, hydrothermal treatment was performed under the same conditions as before, and 9.34-13.63 g/L of xylose was detected. This concentration was slightly lower than that of a fresh Fenton oxidation solution (16.51 g/L) but was higher than that obtained by hydrothermal treatment without Fenton oxidation (2.72 g/L). The degradation rate during hydrothermal pretreatment involving Fenton oxidation was 36.02%, which decreased (29.24-31.05%) slightly when the liquid solution recovered after Fenton oxidation was reused. However, the degradation rate increased compared to that measured from hydrothermal treatment without Fenton oxidation (15.21%). Moreover, the yield after enzyme hydrolysis decreased in the following order: fresh Fenton oxidation-hydrothermal treatment (89.64%) > Fenton oxidation with reused solution-hydrothermal treatment (74.84%) > hydrothermal treatment without Fenton oxidation (32.05%).

국내 주요도시 주변의 바이오매스 에너지 잠재량 분석 (Analysis of Biomass Energy Potential around Major Cities in South Korea)

  • 국진우;이시훈
    • 공업화학
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    • 제26권2호
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    • pp.178-183
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    • 2015
  • 바이오매스 자원은 고체, 액체, 기체 등의 다양한 형태의 에너지 자원으로 전환되어 이용될 수 있기 때문에 필수적인 재생에너지 자원으로 여겨지고 있다. 더불어 바이오매스는 화석 연료의 고갈과 지구 온난화를 해결할 수 있는 방법으로도 각광을 받고 있다. 바이오매스 에너지 전환 플랜트의 규모를 결정하고 경제성을 분석하기 위해서는 지역 내의 바이오매스 에너지 잠재량과 에너지 밀도에 대한 정보가 유용하게 이용될 수 있다. 농업 폐기물, 임업 폐기물, 축산 폐기물, 도시생활 폐기물 등의 국내 에너지 잠재량과 에너지 밀도를 정부 및 연구 기관들이 발표한 최신 자료를 수집하여 분석되었다. 바이오매스 자원을 확보하기 위한 지역이 증가할수록 에너지 잠재량은 증가하나 에너지 밀도는 감소하는 것으로 나타났다.

Optimization and Evaluation of Organic Acid Recovery from Kraft Black Liquor Using Liquid-Liquid Extraction

  • Kwon, Hee Sun;Um, Byung Hwan
    • Korean Chemical Engineering Research
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    • 제54권6호
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    • pp.753-761
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    • 2016
  • Liquid-liquid extraction (LLE) can be used for the recovery of acetic acid from black liquor prior to bioethanol fermentation. Recovery of value-added chemicals such as acetic-, formic- and lactic acid using LLE from Kraft black liquor was studied. Acetic acid and formic acid have been reported to be strong inhibitors in fermentation. The study elucidates the effect of three reaction parameters: pH (0.5~3.5), temperature ($25{\sim}65^{\circ}C$), and reaction time (24~48 min). Extraction performance using tri-n-octylphosphine oxide as the extractant was evaluated. The maximum acetic acid concentration achieved from hydrolyzates was 69.87% at $25^{\circ}C$, pH= 0.5, and 36 min. Factorial design was used to study the effects of pH, temperature, and reaction time on the maximum inhibitor extraction yield after LLE. The maximum potential extraction yield of acetic acid was 70.4% at $25.8^{\circ}C$, pH=0.6 and 37.2 min residence time.

Treatment of High Concentration Organic Wastewater with a Sequencing Batch Reactor (SBR) Process Combined with Electro-flotation as a Solids-liquid Separation Method

  • Choi, Younggyun;Park, Minjeong;Park, Mincheol;Kim, Sunghong
    • Environmental Engineering Research
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    • 제19권4호
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    • pp.395-399
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    • 2014
  • Operation characteristics of the sequencing batch reactor (SBR) process with electro-flotation (EF) as a solid liquid separation method (EF-SBR) were investigated. EF-SBR process showed excellent solid-liquid separation performance which enabled to separate biosolids from liquid phase within 30 min and to extend cyclic reaction time. Although influent organic loading rate was increased stepwise from 5 to 15 g COD/day, food to microorganisms (F/M) ratio could be maintained about 0.3 g COD/g VSS/day in EF-SBR because biomass concentration could be easily controlled at desired level by EF. However, it was impossible to increase biomass concentration at the same level in control SBR (C-SBR) process because solid-liquid separation by gravity settling showed a limitation at higher mixed liquor suspended solids (MLSS) concentration with 60 min of settling time. Total chemical oxygen demand (TCOD) removal efficiency of EF-SBR process was not decreased although influent organic loading rate became 3 times higher than initial value. However, it was seriously deteriorated in C-SBR process after increasing the rate over 10 g COD/day, which was accounted for insufficient organic removal by relatively higher food to microorganisms (F/M) ratio as well as biosolids wash-out by a limitation of gravity sedimentation.

Compilation of liquefaction and pyrolysis method used for bio-oil production from various biomass: A review

  • Ahmad, Syahirah Faraheen Kabir;Ali, Umi Fazara Md;Isa, Khairuddin Md
    • Environmental Engineering Research
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    • 제25권1호
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    • pp.18-28
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    • 2020
  • In this paper the authors provide comparative evaluation of current research that used liquefaction and pyrolysis method for bio-oil production from various types of biomass. This paper review the resources of biomass, composition of biomass, properties of bio-oil from various biomass and also the utilizations of bio-oil in industry. The primary objective of this review article is to gather all recent data about production of bio-oil by using liquefaction and pyrolysis method and their yield and properties from different types of biomass from previous research. Shortage of fossil fuels as well as environmental concern has encouraged governments to focus on renewable energy resources. Biomass is regarded as an alternative to replace fossil fuels. There are several thermo-chemical conversion processes used to transform biomass into useful products, however in this review article the focus has been made on liquefaction and pyrolysis method because the liquid obtained which is known as bio-oil is the main interest in this review article. Bio-oil contains hundreds of chemical compound mainly phenol groups which make it suitable to be used as a replacement for fossil fuels.

Ionic Liquid Pretreatment of Lignocellulosic Biomass

  • Han, Song-Yi;Park, Chan-Woo;Kwon, Gu-Joong;Kim, Nam-Hun;Kim, Jin-Chul;Lee, Seung-Hwan
    • Journal of Forest and Environmental Science
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    • 제36권2호
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    • pp.69-77
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    • 2020
  • Lignocellulosic biomass has recalcitrant characteristics against chemical and biological conversion due to its structural heterogeneity and complexity. The pretreatment process to overcome these recalcitrant properties is essential, especially for the biochemical conversion of lignocellulosic biomass. In recent years, pretreatment methods using ionic liquids (ILs) and deep eutectic solvents (DESs) as the green solvent has attracted great attention because of their advantages such as easy recovery, chemical stability, temperature stability, nonflammability, low vapor pressure, and wide liquids range. However, there are some limitations such as high viscosity, poor economical feasibility, etc. to be solved for practical use. This paper reviewed the research activities on the pretreatment effect of various ILs including DESs and their co-solvents with organic solvents on the enzymatic saccharification efficiency of lignocellulosic biomass and the nanocellulose preparation from the pretreated products.