• Journal of Microbiology and Biotechnology
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• 제16권8호
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• pp.1255-1261
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• 2006

An alkaliphilic bacterium, Bacillus sp. strain BK, was found to produce extracellular cellulase-free xylanolytic enzymes with xylan-binding activity. Since the pellet-bound xylanase is eluted with 2% TEA from the pellet of the culture, they contain a xylan-binding region that is stronger than the xylan-binding xylanase of the extracellular enzyme. The xylanases had a different molecular weight and xylan-binding ability. The enzyme activity of xylanase in the extracellular fraction was 6 times higher than in the pellet-bound enzyme. Among the enzymes, xylanase had the highest enzyme activity. When Bacillus sp. strain BK was grown in pH 10.5 alkaline medium containing xylan as the sole carbon source, the bacterium produced xylanase, arabinofuranosidase, acetyl esterase, and $\beta$-xylosidase with specific activities of 1.23, 0.11, 0.06, and 0.04 unit per mg of protein, respectively. However, there was no cellulase activity detected in the crude enzyme preparation. The hydrolysis of agricultural residues and kraft pulps by the xylanolytic enzymes was examined at 50$^{\circ}C$ and pH 7.0. The rate of xylan hydrolysis in com hull was higher than those of sugarcane bagasse, rice straw, com cop, rice husk, and rice bran. In contrast, the rate of xylan hydrolysis in sugarcane pulp was 2.01 and 3.52 times higher than those of eucalyptus and pine pulp, respectively. In conclusion, this enzyme can be used to hydrolyze xylan in agricultural residues and kraft pulps to breach and regenerate paper from recycled environmental resources.

• Journal of the Korean Wood Science and Technology
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• 제16권2호
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• pp.50-61
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• 1988

접착제(接着劑) 제조(製造)를 위하여 펄프폐액(廢液)중의 리그닌을 이용(利用)하는 연구(硏究)가 1930년경(年傾)부터 진행(進行)되여 아황산펄프폐액(廢液)중의 Lignosulfonate의 경우는 페놀수지(樹脂)나 요소수지(要素樹脂)에 증량(增量)시키거난 반응(反應)시키는 연구(硏究)인데 비하여 kraft 리그닌을 이용(利用)하는 경우는 페놀수지(樹脂)의 보문(報文)이 주류(主流)를 이루고 있으나 요소계(要素系) 공축합수지(共縮合樹脂)는 아직 발표(發表)된 바 없으며 또한 아직까지 리그닌을 이용(利用)한 상업적(商業的)인 접착제(接着劑)가 제조(製造)되어 활용(活用)되지 못하고 있는 실정(實情)이다. 따라서 본(本) 연구(硏究)는 합판제조(合板製造)의 원가절감(原價節減), 폐액이용(廢液利用)의 환경보존관점(環境保存觀點)에서 Krfat Pulp 폐액(廢液)중의 리그닌접착제(接着劑)의 제조(製造)하고져 실시(實施)하였으며, Urea-Lignin 접착제(接着劑)의 도포량(塗布量)은 일반적(一般的)으로 합판(合板)에 도포(塗布)되는 요소수지(要素樹脂)의 량(量)(320g/$m^2$)과 동일(同一)하고 압축응력(壓縮應力)은 균일(均一)하게 12kg/$cm^2$으로 하여 열압조건(熱壓條件)(온도(溫度), 시간(時間))의 영향(影響))을 아울러 규명(糾明)하였다. Urea-Formaldehyde와 Kraft lignin의 혼합비(混合比)는 중량비(重量比)(N.V.C)로 7:3으로 합성수지(合成樹脂)를 만들어 합판제조(合板製造)를 통(通)하여 구명(究明)를 결과(結果) 다음과 같은 결론(結論)을 얻었다. 1. 본(本) 실험(實驗)의 결과(結果) 요소수지(要素樹脂)의 약(約) 30%가 krfat lignin으로 대체(代替)할 수 있음을 보여준 바, Pulping 공정(工程)의 부산물(副産物)로 얻어진 폐액(廢液)은 합판제조시(合板製造時) 접착제(接着劑)의 대체원(代替源)으로 유효(有效)하다. 2. 경제적관점(經濟的觀點)에서 합판제조(合板製造)를 위한 최적열압조건(最適熱壓條件)은 $160^{\circ}C$에서 3분(分)으로 압착(壓搾)하는 것이 적절(適切)하였다.(상태(常態)): 16.49kg/$cm^2$, 내수(耐水) : 18.56kg/$cm^2$, 내온수(內溫水) : 12.53kg/$cm^2$). 3. 요소-리그닌 접착제(接着劑)로 제조(製造)된 합판(合板)의 전단인장강도(剪斷引長强度)는 양호(良好)한 접착력(接着力)을 나타냈으며, 내수접착력(耐水接着力)($30^{\circ}C$에서 3시간(時間) 심적후(沈積後) 시험(試驗)은 상태접착력(狀態接着力)과 별차이가 없거나 더 높은 인장강도력(引長强度力)을 보여준 바, 내수합판용(耐水合板用) 접착제(接着劑)로 상당한 전망(展望)을 나타냈다.

• 농업과학연구
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• 제19권2호
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• pp.194-200
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• 1992

제지슬러지를 퇴비(堆肥) 등 유기물자원(有機物資源)으로이용하기 위하여 44점의(點) 제지슬러지를 제지회사에서 직접 채취하여 슬러지 중의 중금속 성분과 $PCB_s$ 함량을 조사하였고, 아울러 Kraft지슬러지와 판지(板紙)슬러지를 이용한 농가포장(農家圃場) 토양중의 중금속함량을 무시용(無施用) 토양과 비교하여 보았으며 중요한 결과는 아래와 같다. 1. 슬러지 중에서는 납이 평균(平均) 14.5-25.7ppm으로 비교적 높은 함량을 보였으며, Al, Cd, Cu, Fe, 및 Zn 등은 일반토양중 함량과 비교하여 큰 문제가 없는 수준이었으며, Cr과 Hg은 검출(檢出)되지 않았다. 2. Kraft지, 판지(板紙), 신문용지(新聞用紙)슬러지 중의 $PCB_s$ 함량을 조사해 본 결과, kraft지와(紙) 판지(板紙) 슬러지에서는 10ppb 이하로서 거의 무시할 수준이었으며, 신문용지 슬러지에는 다소간 존재하였으나 $PCB_s$ 총량(總量)을 정량하지는 못하였다. 3. 제지슬러지 시용토양중의 금속성분함량은 무처리토양과 비교하여 유의성있는 증가 양상을 보이지 않았으며, 전반적인 함량은 토양중 평균함량범위 이내였다. 4. 이상의 결과로 보아 제지슬러지의 토양환원은 현단계에서 부작용을 일으킬 우려가 없다고 평가할 수 있다.

• Journal of the Korean Wood Science and Technology
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• 제41권6호
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• pp.583-593
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• 2013

본 연구는 크라프트 리그닌의 염기 촉매 분해(Based Catalyst Depolymerization, BCD)반응에서 생성되는 반응물의 화학적 특성을 조사하였다. 초임계 메탄올을 용매로 하고 염기 촉매로 사용한 NaOH의 농도를 7.5, 3.25, 6.13%로 변화를 주었다. BCD 반응물에서 불용성 고형 부산물, 수용성 부산물과 각 부산물에서 diethyl ether로 추출하여 DEE-1, DEE-2를 얻었고 그 화학적 조성을 분석하였다. 실험 결과 염기의 농도가 높아질수록 불용성 고형 부산물이 많이 생성된 반면 수용성 분액분의 수율은 낮아졌으나 DEE 추출분의 수율은 차이가 없었다. 불용성 부산물에서 추출한 DEE-1은 GC/MS 분석 결과 BHT외에 페놀성 화합물은 검출되지 않았다. 대부분의 저분자 리그닌 분해 산물은 DEE-2에서 GC/MS를 사용하여 30개 이상의 피크가 관찰되었고 21개 성분이 확인되었다. 7.5와 3.25%의 NaOH를 사용한 반응의 DEE-2 주성분은 catechol (20.3, 17.7%), 4-methylcatechol (18.2, 15.6%), 3-methoxycatechol (9.6, 14.5%), syringol (8.9, 10.9%)등으로 주로 catechol 계열의 화합물이었다. 1.63%의 NaOH를 사용한 반응의 DEE-2 주성분은 syringol (22.3%), isovanillic acid (12.6%), 3-methoxycatechol(12.1%), 4-methylcatechol (11.7) 등으로 나타났다. 염기의 농도가 저분자 페놀성 화합물들의 전체적인 수율에는 영향이 없었지만 3.25와 1.63%의 농도를 경계로 성분 조성에 큰 영향을 주는 것을 관찰할 수 있었다.

• 펄프종이기술
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• 제36권5호
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• pp.69-77
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• 2004

Degradations of pine, yellow poplar and sweet gum by two fungi, Pycnoporus cinnabarinus and Trichophyton rubrum LSK-27 were investigated. P. cinabarinus degraded pine block samples much faster than T rub rum LSK-27, whereas P. cinnabarinus and T rubrum LSK-27 degraded yellow poplar and sweet gum at almost the same rate. In an effort to get a better understanding of how fungi degrade lignin in wood, contents of various functional groups were analyzed. After three-months of degradation of pine flour by these fungi, the following changes were observed: an increase in condensed phenolic OH group and carboxylic acid group content, a decrease in the guaiacyl phenolic OH content, and little change of aliphatic OH group content. Further studies in the degradation of pine flour by P. cinnabarinus indicated that the increase in condensed phenolic OH group content and the decrease in guaiacyl phenolic OH group content occurred in the first month of the degradation. The changes of functional group contents in the degradation of unbleached softwood kraft pulp by P. cinnabarinus had the same trends as those in the degradation of pine flour. That is, structural alteration of lignin due to the kraft pulping process had little effect on how P. cinnabarinus degraded lignin.

• 정보관리학회지
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• 제12권1호
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• pp.87-97
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• 1995

부울 검색 시스템은 구현이 용이하고 빠를 검색 시간을 제공하기 때문에, 오늘날 정보 검색 분야에서 가장 널리 사용되고 있다. 그러나 순수한 부울 검색 시스템은 문서값을 계산할 수 없기 때문에, 검색된 문서들을 질의를 만족하는 정도에 따라 정렬 할 수 없다. 부울 검색 시스템에 순위 결정 기능을 부여하기 위하여 퍼지 집합, Waller-Kraft, Paice, P-Norm, Infinite-One과 같은 확장된 부울 모델들이 개발되어 왔다. 이들 모델에서 부울 연산자 AND와 OR에 대한 계산식은 순위 결정의 성능을 결정하는 중요한 요소이다. 본 논문에서는 부울 연산자 계산식의 수학적 특성을 제시하고, 이들이 검색효과에 미치는 영향을 분석한다. 분석 결과는 P-Norm 모델이 높은 검색 효과를 얻기에 가장 적합함을 보여준다.

• 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.

• Journal of the Korean Wood Science and Technology
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• 제25권2호
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• pp.100-109
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• 1997

The objectives of this study was to decrease pollutions of bleaching effluent and was to enhanced brightness of non-chlorine bleached pulps by xylanase treatments. Xylanase cloned Esherichacoli(E. coli) capable of each of endo, exo-xylanase and acetyl-esterase were obtained from Bacillus stearothermophillus. These xylanase was maintained high activity in alkali and high temperature. Especially endo-xylanase would be more active in $60^{\circ}C$ and pH 11. Xylanase pretreatment(X) of unbleached pulp increased brightness, and decreased the degree of delignification. The degree of increase in brightness of pulp due to xylanase pretreatment was similar to non-enzyme treated pulp, regardless of the amount of enzyme added. Therefore, the addition of xylanase of 2 unit was recommended when considering costs of enzyme. The pulp bleached XO sequence had higher brightness and lower Kappa no, than O bleached pulp, while pulp bleached XP sequence had similar brightness and Kappa no. with P bleached pulp. In XOC/D, XOZ and XOP bleaching sequences, brightness and degree of delignification were improved. The C/D and Z stage bleached pulp was good effect on rate of raise in brightness and Kappa no., but P stage bleached pulp had similar level in non-enzyme treated bleaching sequence.

• 펄프종이기술
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• 제47권3호
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• pp.47-54
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• 2015

In this study, effects of kneading treatment on the properties of hardwood bleached kraft pulp (HwBKP), softwood bleached kraft pulp (SwBKP) and hardwood bleached chemi-thermo-mechanical pulp (HwBCTMP) were elucidated with a laboratory two-shaft kneader. Kneading treatment was performed at 30% (w/w) of pulp concentration and the number of passes through the kneader was adjusted from 0 to 10 passes. Then, changes in properties of pulp fibers were evaluated. It was found that fiber characteristics were influenced by kneading treatment. Fiber length was decreased with kneading while other morphological properties such as fiber width, curl and kink became increased as the number of passes through the kneader increased from 0 to 5 passes. The magnitude of changes in the morphological properties of softwood chemical pulp was the largest, followed by hardwood chemical pulp. The morphological properties of HwBCTMP were little influenced by kneading treatment. Swelling of fiber measured by WRV was increased with kneading except of HwBCTMP.

• 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.