• 한국신재생에너지학회:학술대회논문집
• /
• 2007.06a
• /
• pp.598-601
• /
• 2007

셀룰로오스, 헤미셀룰로오스, 리그닌으로 구성된 목질계 바이오매스를 이용한 가스화의 경우 30%의 리그닌 성분이 열에 안정한 상태인 타르로 형성되면서 가스화 후단공정에서의 정제, 발전 등에 직접 사용하기 어려우며, 가스화 효율을 저하시키는 원인이 된다. 이의 문제 해결을 위하여 본 연구에서는 촉매를 이용한 수증기 개질 반응을 통하여 타르를 합성가스로 개질시킬 수 있는 방법을 모색하기 위하여 다양한 온도, 촉매, 스팀 주입량 및 촉매크기에 따른 전환율, 생성가스 특성을 알아보았다. 타르 대상 물질로는 타르 내 상당부분을 차지하고 있는 톨루엔을 이용하였다. 일반적으로 반응온도, 스팀 주입량이 증가할수록 수소 생성량이 증가하였으며, 지르코니아로 증진된 니켈 촉매의 경우 600$^{\cdot}C$ 에서도 100%의 높은 전환율을 보였다. 일반적인 가스화기에서 배출되는 타르의 농도보다 10배 높은 조건에서도 100%의 높은 전환율을 얻을 수 있었으며, 이를 통하여 실제 공정으로의 적용시에도 후단 공정의 부담을 줄일 수 있는 개질기로 적용 가능할 것으로 보인다.

• Proceedings of the KAIS Fall Conference
• /
• 2011.12a
• /
• pp.283-285
• /
• 2011

수소첨가 가스화반응 특성을 조사하기 위해 $800^{\circ}C$, 8 MPa에서 조업 가능한 회분식반응기를 이용하여 실험을 수행하였다. 실험에 사용한 플라스틱은 폴리에틸렌이었으며 바이오매스는 톱밥이었다. 반응기내 압력감소속도는 기상물 생성속도를 나타냄을 알 수 있었으며 이러한 결과는 반응시간에 따른 전환율 변화로부터 확인할 수 있었다. 기상물 생성량과 플라스틱-바이오매스 혼합물의 전환율은 플라스틱 함량비가 증가할수록 증가하였다.

• Korean Chemical Engineering Research
• /
• v.49 no.4
• /
• pp.470-474
• /
• 2011

Rice straw is the main grain straw and is produced in large quantities every year in Korea. Pretreatment of lignocellulosic biomass using soaking process was carried out mild conditions at atmospheric pressure and temperature of $60^{\circ}C$. We found enzymatic hydrolysis condition of pretreated biomass. In case of a rice straw, compared with previous lignocellulosic biomass, we found that hydrolysis time was a shorter than others. Hydrolysis of SAA-treated rice straw has shown conversion rate was higher at $50^{\circ}C$. Hydrolysis was ended between 40~48 hour. Glucose conversion rate was higher when enzyme loading is 65 FPU/ml and 32 CbU/ml. When substrate concentration was 5%(w/v), it was that conversion rate was 83.8% after hydrolysis for 72 hr. In simultaneous saccharification and fermentation(SSF) experiment about SAA-treated rice straw, ethanol productive yield was highest from $40^{\circ}C$. The yield of that time was 33.05% from 48 hour.

• 한국생물공학회:학술대회논문집
• /
• 2000.11a
• /
• pp.216-219
• /
• 2000

Pyrolysis products of woody biomass were consistedofvarious linear hydrocarbon, aromatics or condensed cyclic compounds. In order to obtain biomass pyrolysis products, more equipments and time were needed. But solvolysis of woody biomass with acetone easily obtained decomposition products and enhanced conversion rate(18.72%, max.) from woody biomass than pyrolysis of woody biomass. Beacause solvolysis with acetone improved conversion rate (26.64%, max.) of lignin. the whole conversion rate was improved. But above $300^{\circ}C$, lignin showed lower conversion rate, so the whole conversion rate decreased. Solvolysis products of woody biomass with acetone were same as pyrolysis products. Above $400^{\circ}C$, methoxy phenols were completely disappeared.

• Transactions of the Korean hydrogen and new energy society
• /
• v.29 no.5
• /
• pp.503-511
• /
• 2018

There have been many studies of combustion in the circulating fluidized bed. However, little study is available for combustion of wood pellet together fed with wood chip. The mixed ratio of two fuels is an useful information when thermal power company would receive the Renewable Energy Portfolio Standard (RPS) from government. In this study, the combustion behavior and kinetics of such biomass fuels are evaluated using fluidized bed reactor and thermogravimetric analyzers. The mixing ratio of wood chip relative to wood pellet was varied at different temperatures. The results show that a combustion reactivity changed significantly at the wood chip mixing ratio of 40%, particularly at low temperature condition.

• Journal of Energy Engineering
• /
• v.24 no.3
• /
• pp.1-5
• /
• 2015

This study is to investigate the effect of torrefaction on enzymatic hydrolysis of lignocellulosic biomass for bio-ethanol production. As a pretreatment, the torrefaction of lignocellulosic biomass was conducted in temperature of $250{\sim}350^{\circ}C$ in the absence of oxygen. Tween-80, nonionic surfactant, was tested to enhance saccharification efficiency by coping with hydrophobicity resulted from torrefaction. As a result, the glucose production from enzymatic hydrolysis of biomass pretreated by torrefaction was greater than that obtained from the non-pretreated biomass. Sugar conversion was higher when the biomass was saccharified with addition of tween-80. It was found that torrefaction can be applied as a preptreatment for lignocellulosic biomass and tween-80 is needed to enhance its enzyme saccharification.

• 한국생물공학회:학술대회논문집
• /
• 2000.11a
• /
• pp.733-736
• /
• 2000

Lignin is usable as fuels and heavy oil additives if depolymerized to monomer unit, because the chemical structures are similar to high octane materials found in gasoline. In this study, the solvent-phase thermal cracking(solvolysis) of lignin was performed at the various temperature and time in a laboratory tubular reactor. Conversion yield was measured for the properties of thermal cracking and liquefaction reaction of lignin. Highest conversion yield when acetone was used as thermal cracking solvent was 55.5% at $350^{\circ}C$, 50minutes and highest tar generation were $260{\sim}350mg/g\;{\cdot}\;lignin$ at $250^{\circ}C$, and highest conversion yield after tar removal was 76.88% at $300^{\circ}C$, 30minutes. Conversion yield, product compositions and amounts were determined by tar degradation yield.

• Korean Chemical Engineering Research
• /
• v.54 no.4
• /
• pp.448-452
• /
• 2016

This study is for the effective pretreatment and saccharification of lignocellulosic biomass for a transport fuel receiving attention. The waste water during the pretreatment of biomass is major factor for determining the price of biofuel. Therefore, we conducted high concentration of organosolv pretreatment for decline waste water and reusing the solvent. We confirmed effect of organosolv pretreatment by components analysis and enzymatic hydrolysis of pretreated biomass. The corn stover was used for and 99.5 wt% of ethanol as a organosolv pretreatment. The pretreatment condition was varied 130 to $190^{\circ}C$ during the designated reaction times and the effect of pretreatment was investigated by enzymatic hydrolysis. The highest glucose conversion was more than 68% the pretreatment condition of $190^{\circ}C$ for 70 min or more. The solid remaining was more than 70% and almost of cellulose and hemicellulose were survived.

• Journal of Korean Society of Environmental Engineers
• /
• v.36 no.10
• /
• pp.704-710
• /
• 2014

Biomass is considered an alternative energy which can solve an greenhouse gas problem like $CO_2$ which is a major contributor to global warming. The biomass can be converted to various energy sources through thermochemical conversion. In this study, a continuous gasifier was engineered for a wood biomass gasification. The biomass was used a waste wood. The experiments of $CO_2$ gasification were achieved as the gasification temperature, moisture content and input $CO_2$ concentration. The results showed that the yield of producer gas increased with an increasing the gasification temperature. The amount of the light tar increased due to the decomposition of gravimetric tar by the thermal cracking, and the char was confirmed pore development through the SEM analysis. The CO concentration was increased with an increased input $CO_2$ concentration from Boudouard reaction. Through the parametric screening studies, the hydrogen and carbon monoxide concentration were 32.91% and 48.33% at the optimal conditions of this test rig.

• Journal of Korean Society of Forest Science
• /
• v.96 no.4
• /
• pp.477-482
• /
• 2007

Forest biomass became a topic because we have growing interest in global environmental issues and environment-friendly energy resources. This study was carried out to estimate the forest biomass and develop a program for biomass information management in Korea. The total forest biomass (million ton) were 521 for gross forest, 403 for productive forest and 201 for commercial forest in 2005. Also, the annual biomass production in forest was 20 million ton which was equivalent to 94,290 Gkcal of heating value and about 9 billion won of paraffin oil. The biomass growing rate (every 10year) increased from 4.95% in 1985 to 5.30% in 1995 but turn down 4.46% in 2005. The factors that the forest stock could be converted to the forest biomass have developed according to forest type. Therefore, it is impossible to estimate the exact biomass by tree species. In this reason, the demands of the development of the factors by tree species was raised. In addition, it is on time to develop an equation for estimation of biomass by species using dbh and height as independent factors.