• 임산에너지
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• 제18권1호
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• pp.17-24
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• 1999

액화목재는 목재 및 목질계 자원으로부터 신소재 개발을 위한 새로운 유효이용법의 하나이다. 이 액화목재의 주요 성분변화를 조사하기 위한 실험으로서 액화 전후의 리그닌의 구조적 변화를 알기 위하여 잣나무 KP리그닌과 리그닌설포산을 액화시켜서 유기용매로 분리하고, IR, 1H(13C)-NMR, GC-MS분석기기로 분석하였다. 액화리그닌 중에는 다수의 페놀성 물질들 즉, diguaiacol, acetic acid phenyl ester, phenol, 1-phenyl ethanone 등이 분석되었다.

• KEPCO Journal on Electric Power and Energy
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• 제2권3호
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• pp.447-452
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• 2016

It is imperative to develop an effective pathway to depolymerize lignin into liquid fuel that can be used as a bioheavy oil. Lignin can be converted into liquid products either by a solvent-free thermal cracking in the absence air, or thermo-chemical degradation in the presence of suitable solvents and chemicals. Here we show that the solvent-assisted liquefaction has produced promising results in the presence of metal-based catalysts. The supercritical ethanol is an efficient liquefaction solvent, which not only provides better solubility to lignin, but also scavenges the intermediate species. The concentrated sulfuric acid hydrolysis lignin (CSAHL) was completely liquefied in the presence of solid catalysts (Ni, Pd and Ru) with no char formation. The effective deoxy-liquefaction nature associated with scEtOH with aid hydrodeoxygenation catalysts, resulted in significant reduction in oxygen-to-carbon (O/C) molar ratio up to 61%. The decrease in oxygen content and increase in carbon and hydrogen contents increased the calorific value bio-oil, with higher heating value (HHV) of $34.6MJ{\cdot}Kg^{-1}$. The overall process is energetically efficient with 129.8% energy recovery (ER) and 70.8% energy efficiency (EE). The GC-TOF/MS analysis of bio-oil shows that the bio-oil mainly consists of monomeric species such as phenols, esters, furans, alcohols, and traces of aliphatic hydrocarbons. The bio-oil produced has better flow properties, low molecular weight, and high aromaticity.

• Journal of the Korean Wood Science and Technology
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• 제18권4호
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• pp.79-85
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• 1990

Many kinds of acetosolv lignin including ricestraw and spruce lignin were pyrolyzed. and liquefied in the autoclave reactor using 50% tetralin and m-cresol solution respectively as soluble solvent and Co-Mo as catalyst. In order to promote deoxyhydrogenolysis reaction $H_2$ gas was supplied into the reactor. The ratio between lignin and the soluble solvent are lg and 10cc. The reaction conditions are $200^{\circ}-700^{\circ}C$ of reaction temperature, 10-50 atms of reaction pressure and 100-500rpm of the reactor stirrer. By the deoxyhydrogenolysis liquefaction reaction, the main chemical structures of lignin which are aryl-alkyl-${\beta}$-0-4 ether, phenylcoumaran and biphenyl etc. are easily destroyed into liqufied aromatic compounds and aliphatic compunds linked with aromatic compounds. The percent yield of monomeric phenols on the weight bvase of lignin reacted reached to 12-14% by the chemical analytic GC-MS etc.

• Journal of the Korean Wood Science and Technology
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• 제25권1호
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• pp.1-7
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• 1997

Kraft oak lignin and ricestraw lignin from acetosolve pulping were dissolved in 50/50 mixture of tetralin/m-cresol solvent. The dissolved lignin was reacted in the pressurized autoclave which was operating at $350{\sim}500^{\circ}C$ of reaction temperature and 10~20 atms of reaction pressure respectively_Hydrogen pressure of 60~80kg/$cm^2$ was exercising into the pressurized autoclave reactor to create thermochemical hydrogenolysis reaction. It was identified by GLC, GC-MS and HPLC that the alkyl-aryl-${\beta}$-O-4 ether bond of lignin was cleaved and degraded into various smaller molecules of aromatic compound such as phenols and cresols under the reaction conditions around $300^{\circ}C$ and 10 atms of reaction temoerature and pressure. Hydrogenolysis reaction of lignin compound which was done above $500^{\circ}C$ of reaction temperature and 20 atms of reaction pressure showed that the amount of aromatic compound such as phenols and cresols degraded from reactant lignin was decreasing with newly present and increasing water out of product mixtures. It was supposed that new aliphatic compound of high molecular weight hydrocarbon is composed due to higher reaction temperature and pressure of hydrogenolysis reaction such as $500^{\circ}C$ and 20 atms, even though it was almost impossible, to identify what kind of degraded products it was by HPLC.

• Journal of the Korean Wood Science and Technology
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• 제23권2호
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• pp.19-25
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• 1995

This research was carried out to investigate the methods of liquefaction with Pinus koraiensis, and chemical components of the liquefied wood by FT-IR analysis and pyrolysis-GC/MS. Acetylated wood powder was liquefied above 90% in phenol or m-cresol when treated at about 150$^{\circ}C$ for 30min., using some catalysts. Untreated wood powder was liquefied above 90% in phenol or m-cresol when treated at about 200$^{\circ}C$ for 60min., using some catalysts. The results of FTIR analysis, carbohydrates were terribly disintegrated, the other side lignin peaks were occurred in liquefied wood, particulary. The results of pyrolysis-GC/MS, the liquefied wood have clear four peaks, phenol, guaiacol, o-cresol and m-/p-cresol, due to degradation of lignin, particulary.

• Journal of the Korean Wood Science and Technology
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• 제32권1호
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• pp.9-16
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• 2004

본 연구는 폐지로부터 용액화물을 제조하고, 제조된 용액화물의 성분 분리 및 성상분석을 통해 용액화물의 효율적인 이용방안을 위한 기초자료 제공에 그 연구 목적이 있다. 폐지의 액화에 있어 건식해리된 폐지보다 습식해리된 폐지의 액화가 비교적 용이하였으며, 이러한 이유는 습식해리된 폐지의 약품 침투가 비교적 용이하기 때문으로 판단된다. 폐지의 최적 액화조건은 폐지 1 g에 대해 크레졸 2 ㎖, 물 4 ㎖, 인산 0.5 ㎖로 첨가하여 190℃에서 60분간 액화 시킨 조건이 가장 우수하였다. 폐지 액화물 중 리그닌은 용제인 크레졸 층으로, 탄수화물은 수층으로 용해되어 각각 분리되며, 두 성분의 분리·회수는 비교적 용이하였다. 액화 폐지 중의 리그닌은 80% 이상 회수되었고, 회수된 리그닌의 분자량은 1,000 정도의 저분자량을 나타냈었다.

• 태양에너지
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• 제18권3호
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• pp.161-167
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• 1998

석탄액화시 나무, 리그닌, 흑액 등 바이오매스계 첨가제의 효과를 실험식적 규모의 고온, 고압 반응기에서 고찰하였다. 석탄액화시 리그닌계의 첨가는 석탄의 분해를 돕고, 액체생성물의 질을 높여준다. $400^{\circ}C$에서는 나무를 첨가하게 되면, 액체생성물이 8%정도 증가하지만, 그이상의 온도에서는 기체생성물의 증가로 액체생성물 수율이 줄어든다. 흑액은 액화수율을 증대시키기는 하지만, 그 증가율은 NaOH만을 첨가시킨 경우보다 낮았으며, $OH^-$의 존재 때문에 흑액중의 리그닌이 주는 효과가 그리 크지 않은 것으로 보인다.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 추계학술발표대회 및 bio-venture fair
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• pp.733-736
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• 2000

목질계 바이오매스의 구성성분 중 건조중량으로 약 $18{\sim}33%$를 차지하고있는 리그닌은, 기본적 단위물질이 가솔린의 성분물질과 화학적으로 유사한 구조를 형성하고 있기 때문에, 분해하여 저분자물질로 전환시킨다면 연료 또는 연료첨가제로 사용될 수 있다. 본 연구에서는 실험실용 관형반응기를 사용하여 반응온도 $250{\sim}450^{\circ}C$, 반응시간 $20{\sim}80$분의 범위에서 용매상 열분해 ${\cdot}$ 액화반응을 수행하였으며 리그닌의 열분해 ${\cdot}$ 액화반응특성을 조사하기 위하여 전환율을 측정하였는데 아세톤을 열분해 용매로 사용한 경우 가장 높은 전환율은 $350^{\circ}C$, 50분의 55.5%로 측정되었으며, 타르의 발생량은 $250^{\circ}C$의 경우 $260{\sim}350mg/g\;{\cdot}\;lignin$으로 가장 높게 나타났다. 타르성분을 제거한 후 전환율을 측정한 경우 가장 높은 전환율은 $300^{\circ}C$, 30분의 76.88%로 측정되어 열분해시 일차적으로 생성되는 타르의 분해도에 따라 전환율 값이 좌우되며 생성물의 조성과 생성량이 좌우됨을 확인할 수 있었다.

• Journal of the Korean Wood Science and Technology
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• 제19권4호
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• pp.80-84
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• 1991

Lignocellulosic biomass including acetosolv ricestraw and spruce lignin were liquefied and converted into liquid hydrocarbons by catalytic hydroliquefaction reaction. These experimental works were carried out in 1-liter-capacity autoclave using 50% tetralin and m-cresol solution respectively as soluble solvent and Ni. Pd. Fe and red mud as catalyst. $H_2$ gas was supplied into the reactor for escaltion of deoxhydroenolysis reaction. Catalyst concentrations were 1 % of raw material based on weight. The ratio between raw materials and soluble solvent are 1g and 10cc. The reaction conditions are 400-$700^{\circ}C$ of reaction temperature, 10-50 atms of reaction pressure. The highest yield of hydrocarbon, so called "product oil" showed 32% and 5.5% of lowest char formation when red mud was used as catalyst. The product oil yields from those of other catalysts were in the range of 20-29%. The influence of different initial hydrogen pressures was examined in the range d 30-50 atms. A minimum pressure of 35 atms was necessary to obtain a complete recovery of souble solvent for recycling.