• Title/Summary/Keyword: 바이오매스에너지

Search Result 397, Processing Time 0.023 seconds

Status and Perspective of Biomass Co-firing to Pulverized Coal Power Plants (미분탄 석탄화력발전에서의 바이오매스 혼소 동향 및 전망)

  • Yang, Won
    • KEPCO Journal on Electric Power and Energy
    • /
    • v.2 no.4
    • /
    • pp.525-529
    • /
    • 2016
  • Biomass co-firing to existing thermal power plants is one of the most economical and efficient way to reduce $CO_2$ emission from the plant. There are several methods of co-firing and it can be categorized into (1) Parallel co-firing, (2) Indirect co-firing, and (3) Direct co-firing. Parallel co-firing is the most expensive way to high-ratio co-firing because it requires biomass dedicated boiler. Direct co-firing is widely used because it does not need high capital cost compared with the other two methods. Regarding the direct co-firing, it can be classified into three methods- Method 1 does not need retrofit of the facilities because it uses existing coal mills for pulverizing biomass fuels. In this case high-ratio co-firing cannot be achieved because of poor grindability of biomass fuels. Method 2 needs biomass-dedicated mills and revision of fuel streams for the combustion system, and Method 3 needs additional retrofit of the boiler as well as biomass mills. It can achieve highest share of the biomass co-firing compared with other two methods. In Korea, many coal power plants have been adopting Method 1 for coping with RPS(Renewable portfolio standards). Higher co-firing ratio (> 5% thermal share) has not been considered in Korean power plants due to policy of limitation in biomass co-firing for securing REC(Renewable Energy Certificate). On the other hand, higher-share co-firing of biomass is widely used in Europe and US using biomass dedicated mills, following their policy to enhance utilization of renewable energy in those countries. Technical problems which can be caused by increasing share of the biomass in coal power plants are summarized and discussed in this report. $CO_2$ abatement will become more and more critical issues for coal power plants since Paris agreement(2015) and demand of higher share of biomass in the coal power plants will be rapidly increased in Korea as well. Torrefaction of the biomass can be one of the best options because torrefied biomass has higher heating value and grindability than other biomass fuels. Perspective of the biomass torrefaction for co-firing is discussed, and economic feasibility of biomass torrefaction will be crucial for implementation of this technology.

Biochar for soil carbon sequestration (토양탄소격리를 위한 바이오차)

  • Woo, Seung Han
    • Clean Technology
    • /
    • v.19 no.3
    • /
    • pp.201-211
    • /
    • 2013
  • Biochar is charred materials generated during pyrolysis processes in the absence of oxygen using biomass, resulting in high carbon contents. In recent years, biochar has attracted more increasingly due to its potential role in carbon sequestration, renewable energy, waste management, soil amendment for agricultural use, and environmental remediation. Since biochar has a long-term stability in soil for thousands of years, biochar can be carbon negative compared to carbon-neutral biomass energy that decomposes eventually. Moreover, when biochar is applied to soil, crop production can be largely improved due to its high pH and its superior ability to retain water and nutrients. This paper review the research trends of biochar including the principles of carbon sequestration by biochar, its physico-chemical properties, and its applications on agricultural and environmental area.

Evaluation on the utilization possibility of waste mushroom logs as biomass resource for bioethanol production (바이오에탄올 생산을 위한 바이오매스 자원으로서 버섯골목의 이용 가능성 평가)

  • Lee, Jae-Won;Koo, Bon-Wook;Choi, Joon-Weon;Choi, Don-Ha;Choi, In-Gyu
    • 한국신재생에너지학회:학술대회논문집
    • /
    • 2006.06a
    • /
    • pp.485-488
    • /
    • 2006
  • In order to investigate the possibility of waste mushroom logs as biomass resource chemical and physical characteristics of normal woods and waste mushroom logs such as crystallinity value, energy consumption, total sugar yield after hydrolysis chemical compounds and molecular weight distribution after acid hydrolysis, were examined. In the results, crystallinity of waste mushroom logs which were three year passed after the inoculation was decreased drastically from 49% to 33% during the cultivation. Lignin contents as chemical compounds of normal woods and waste mushroom logs were 21.07% and 18.78%, respectively. By the results of measurement of energy consumption, the size reduction of normal woods required a significantly higher energy than that of waste mushroom logs. In the hydrolysis, total sugar yield by enzyme and acid hydrolysis were high in waste mushroom logs(53% 57.5%) than in normal woods(42.9%, 47.17%). According to the molecular weight distribution using GPC, low molecular weight compounds were distributed in waste mushroom logs. Based on these results, waste mushroom logs have enough potential as material for developing alternative energy because of easily conversion to sugar by various hydrolysis methods and requirement of low energy consumption during size reduction.

  • PDF

Technical Trends of Hydrogen Production (수소생산 기술동향)

  • Ryi, Shin-Kun;Han, Jae-Yun;Kim, Chang-Hyun;Lim, Hankwon;Jung, Ho-Young
    • Clean Technology
    • /
    • v.23 no.2
    • /
    • pp.121-132
    • /
    • 2017
  • The increase of greenhouse gases and the concern of global warming instigate the development and spread of renewable energy and hydrogen is considered one of the clean energy sources. Hydrogen is one of the most elements in the earth and exist in the form of fossil fuel, biomass and water. In order to use hydrogen for a clean energy source, the hydrogen production method should be eco-friendly and economic as well. There are two different hydrogen production methods: conventional thermal method using fossil fuel and renewable method using biomass and water. Steam reforming, autothermal reforming, partial oxidation, and gasification (using solid fuel) have been considered for hydrogen production from fossil fuel. When using fossil fuel, carbon dioxide should be separated from hydrogen and captured to be accepted as a clean energy. The amount of hydrogen from biomass is insignificant. In order to occupy noticeable portion in hydrogen industries, biomass conversion, especially, biological method should be sufficiently improved in a process efficiency and a microorganism cultivation. Electrolysis is a mature technology and hydrogen from water is considered the most eco-friendly method in terms of clean energy when the electric power is from renewable sources such as photovoltaic cell, solar heat, and wind power etc.

Biomass Gasification for Fuel Cell Combined-Heat-and-Power Systems (바이오매스 활용 연료전지 열병합발전시스템을 위한 연료화 공정)

  • Hong, Gi Hoon;Uhm, Sunghyun;Hwang, Sangyeon
    • Applied Chemistry for Engineering
    • /
    • v.33 no.4
    • /
    • pp.335-342
    • /
    • 2022
  • In the agricultural sector where the fossil fuels are primary energy resources, the current global energy crisis together with the dissemination of smart farming has led to the new phase of energy pattern in which the electricity demand is growing faster particularly. Therefore, the fuel cell combined heat and power system, coupling the environmentally friendly fuel cell to biomass treatment and feeding, can be regarded as the most effective energy system in agriculture. In this mini-review, we discuss the R&D trend of the fuel cell combined heat and power system aimed at utilizing agricultural by-products as fuels and highlight the issues in terms of the process configuration and interconnection of individual processes.

독일의 바이오가스 이용 현황 및 전망

  • O, Gwang-Seok;Jang, Jeong-Hui;Lee, Gyo-Seong;Kim, Gi-Dong;Jeong, Jin-Do
    • Journal of the KSME
    • /
    • v.50 no.9
    • /
    • pp.39-42
    • /
    • 2010
  • 바이오가스는 세계적으로 풍부한 바이오매스 자원에서 발생하고 지구온난화 문제에 대응할 수 있는 탄소중립 청정에너지원이다. 이 글에서는 유럽의 바이오가스 생산 및 시작동향 중에서도 EU 생산량의 35%를 차지하는 독일의 현황에 대해 살펴보고자 한다.

  • PDF

Biomass Carbon Emissions according to Conversion of Forest Land in Korea (산지전용에 따른 우리나라의 임목바이오매스 탄소배출량)

  • Kwon, Soon-Duk;Seo, Jeong-Ho;Son, Yeong-Mo;Park, Young-Kyu
    • Journal of Korea Foresty Energy
    • /
    • v.24 no.2
    • /
    • pp.10-15
    • /
    • 2005
  • This study was achieved by purpose to measure carbon emissions by conversion of forest land in Korea to correspond to UNFCCC. The conversion of forest land data extracted in forest basis statistical data during the latest 5 years from 2000 to 2004, and biomass carbon emissions used biomass extension factor by forest types and carbon conversion factor. During the latest 5 years, the forest land of the annual means about 7,200ha was conversed as other expenditure and tree volume of the annual mean about $212,000m^3$ was felled. It was calculated that total biomass carbon emissions by conversion of the forest land emits annual mean 105,000tC during the latest 5 years. Biomass carbon emissions by forest types was calculated that coniferous forest emits 54,000tC and deciduous forest emits 51,000tC. It was calculated that carbon emissions per ha by conversion of the forest land emits annual mean 14.4tC/ha during the latest 5 years. Seeing by forest types, coniferous forest emits 13.3tC/ha and deciduous forest emits 18.5tC/ha. Therefore, it was shown that deciduous forest emits more carbon per unit area than coniferous forest.

  • PDF

Enzymatic saccharification of rice straw, a lignocellulosic biomass by the extracellular enzyme from KMU001 (KMU001 조효소에 의한 목질계 바이오매스, 볏짚의 효소당화성에 관한 연구)

  • Kim, Yeong-Suk;Lee, Young-Min;Cha, Chang-Jun;Yoon, Jeoung-Jun
    • 한국신재생에너지학회:학술대회논문집
    • /
    • 2008.05a
    • /
    • pp.225-228
    • /
    • 2008
  • This study shows that lignocellulosic biomass saccharification work has been carried out with rice-straw by the extracellular enzyme from KMU001, and the enzymes produced in 5%(w/v) wood biomass were characterized by protein and various enzyme activity measurements. Several cellulases such as Endoglucanase(EG), $\beta$-D-1,4-Glucosidase(BGL), Cellobiohydrolase(CBH), and $\beta$-D-1,4-Xylanase (BXL) were detected. Saccharification of rice-straw by the enzyme yielded about 233mg/g of glucose after 48hrs.

  • PDF

Enhancing Enzymatic Saccharification by Aqueous Ammonia Soaking Pretreatment on Several annual plants (일년생 바이오매스(옥수수 줄기, 담배 줄기, 대마 목부)의 암모니아 침지 전처리가 효소 당화에 미치는 영향)

  • Shin, Soo-Jeong;Yu, Ju-Hyun;Park, Jong-Moon
    • 한국신재생에너지학회:학술대회논문집
    • /
    • 2009.06a
    • /
    • pp.418-421
    • /
    • 2009
  • Effects of aqueous ammonia soaking to three annual plants (hemp woody core, tobacco stalk and corn stover) awere investigated to focus on the enzymatic saccharification characteristics change by this treatment. At two different levels of treatment ($90^{\circ}C$-16 h and $45^{\circ}C$-6 days), higher temperature treatment led to more enzymatic saccharification of cellulose to glucose by commercial cellulase mixtures (Celluclast 1.5L and Novozym 342 from Novozyme Korea). Difference among annual plants were significant. corn stover was the best response to enzymatic saccharification of cellulose and xylan by comercial enzymes all treatment conditions but tobacco stalk was the worst response to all of them. chemical composition or physical structure difference may brought this difference.

  • PDF

The effect oxidizer temperature and steam addition on caloric value in biomass gasification process (공급공기의 온도 변화와 수증기가 바이오매스 가스화 과정에서 전환가스의 발열량에 미치는 영향)

  • Ahn, Seong-Yool;Mun, Cheol-Eon;Choi, Gyung-Min;Kim, Duck-Jool
    • 한국신재생에너지학회:학술대회논문집
    • /
    • 2007.06a
    • /
    • pp.606-609
    • /
    • 2007
  • An experimental study was carried out to investigate the heat value change by various conditions of wood sawdust gasification in the 1-dimensional downdraft flow fixed bed gasifier. The preheated air and steam were used as a gasifying agent. The components of syngas were influenced increasing residence time of supplied agent. The operating parameters, the supplied agent temperature and steam addition were used. The oxidizer temperature was varied from 500K to 620K. The gasification process was monitored by measuring temperature at three points near the biomass using R-type thermocouples and the syngas composition was analyzed by gas chromatograph. We get the sample gas at the end of gasifier. Finally, the amount of hydrogen and methane were increased widely as increasing the oxidizer temperature and adding steam.

  • PDF