• Korean Chemical Engineering Research
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• 제61권4호
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• pp.561-569
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• 2023

푸르푸랄(furfural)은 리그노셀룰로오스 바이오매스(lignocellulose biomass)의 헤미셀룰로오스(hemicellulose) 성분 중 하나인 자일로스(xylose)로부터 생산되는 플랫폼 화학물질이다. 푸르푸랄은 페놀류 화합물이나 바이오 연료 등의 중요한 원료로 사용될 수 있다. 본 연구에서는 푸르푸랄 생산공정에서 일반적으로 사용되는 산 촉매인 황산(sulfuric acid)과 친환경적 촉매인 포름산(formic acid) 두 가지 촉매를 이용하여 회분식 반응 시스템(batch system)에서 자일로스로부터 푸르푸랄을 생산하기 위한 조건을 비교 및 최적화하였다. 자일로스의 초기 농도(10 g/L~100 g/L), 반응 온도(140~200 ℃), 황산 촉매(1~3 wt%), 포름산 촉매(5~10 wt%), 반응 시간에 따라 자일로스로부터 푸르푸랄 수율에 미치는 영향을 조사하였다. 촉매 종류에 따른 최적 조건은 다음과 같았다. 황산 촉매의 경우, 3 wt%의 촉매농도, 50 g/L의 초기 자일로스 농도, 180 ℃의 온도 10분의 반응시간에서 최대 58.97%의 푸르푸랄 수율을 얻었다. 포름산 촉매의 겨우, 5 wt%의 촉매농도, 50 g/L의 초기 자일로스 농도, 180 ℃의 온도, 150분 반응 시간에서 65.32%의 푸르푸랄 수율을 확보하였다.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.478-481
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• 2001

The spent petrochemical catalyst used in the manufacturing process of terephthalic-acid contains valuable metals such as cobalt and manganese. To recover these metals, sulfuric acid leaching was performed with hydrogen peroxide as a reducing agent. Low extractions of Mn, Co and Fe were obtained by sulfuric acid leaching without reducing agent. With adding hydrogen peroxide as a reducing agent, the high extraction of these metals could be obtained. Different from general leaching experiment, the extraction rates of metal components were decreased with increasing reaction temperature in this case. Under the optimum condition, the extraction rates of Mn, Co and Fe were 93.0%, 87.0% and 100% respectively.

• Bulletin of the Korean Chemical Society
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• 제28권10호
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• pp.1854-1856
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• 2007

• Journal of the Korean Wood Science and Technology
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• 제38권2호
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• pp.149-158
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• 2010

Organosolv pretreatments which utilized sulfuric acid, sodium hydroxide and ammonia as catalysts were conducted to screen the effective catalyst for organosolv pretreatment of Liriodendron tulipifera. The enzymatic hydrolysis was achieved effectively with sulfuric acid (74.2%) and sodium hydroxide (63.7%). They were thus considered as effective catalysts for organosolv pretreatment of L. tulipifera. The organosolv pretreatments with sulfuric acid and sodium hydroxide showed a different behavior on the reaction mechanism. The pretreatment with sulfuric acid increased the biomass roughness and pore numbers. On the other hand, the pretreatment with sodium hydroxide enhanced the surface area due to the size reduction and minor defiberization which were caused by hemicellulose degradation at an initial stage and more defiberization by lignin degradation at a later stage. The organosolv pretreatment with sodium hydroxide was performed at several different conditions to evaluate effectiveness of sodium hydroxide as a catalyst for organosolv pretreatment. According to the results of enzymatic digestibility, the changes of chemical composition and the morphological analysis of pretreated biomass, it was suggested that the pretreatment time impacted primarily on enzymatic hydrolysis. Increase in surface area during the pretreatment was a major cause for improvement in enzymatic digestibility when sodium hydroxide was used as a catalyst.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.432-436
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• 2001

In this study, calcium sulfate(gypsum) powder was obtained using waste sulfuric acid and stainless refinery sludge by- produced from chemical reagent and the iron industry, by the neutralization of waste sulfuric acid. As variables for the experiment the mole ratio of the H$_2$SO$_4$ : Ca(OH)$_2$, the pH, the reaction temperature and time, the amount of catalyst were used. The crystal shape and microstructure of obtained powder were observed by XRD and SEM, and the thermal property was investigated by DTA. As the NaCl is added 0~20wt% as a catalyst to the H$_2$SO$_4$ : Ca(OH)$_2$, system it can be found that the crystal shape goes through the processes as follows : gypsum dihydratlongrightarrowgypsum hemihydrate＋gypsum dihydratelongrightarrowgypsum hemihydrate. And gypsum hemihydrate is $\beta$-type as the result of DTA. As waste sulfuric acid and stainless refinery sludge were used, the pH of reacted solution (which was 0.8) was rapidly raised up to 8~9 by the addition of stainless sludge and gypsum dihydrate was produced as a by-product. Therefore, it was found that stainless refinery sludge is sufficiently applicable for the neutralization of waste sulfuric acid.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2006년도 추계학술대회
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• pp.541-543
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• 2006

The feasibility of biodiesel production from soapstock by acid catalyst was tested. The water content of soapstock was more than 40%. Before the esterification of soapstock, the pre-treatment of soapstock was conducted adding potassium hydroxide and sulfuric acid. The pre-treated soapstock contained 99.6wt% of free fatty acid. When the free fatty acid was esterified with methanol, the fatty acid methyl ester content became 91.7wt% under the solid acid catalyst, Amberlyst-15. When this biodiesel was distilled the methyl ester content was 98.1wt% which satisfied the biodiesel Standard. Amberlyst-15 could be recovered easily because it was the soliid catalyst. When sulfuric acid was used as the acid catalyst, the fatty acid methyl ester content was 91.0wt%. From the results, it was possible to produce biodiesel efficiently from soapstock after pre-treatment. Because soapstock is very cheap, it will become good feedstock for biodiesel product ion.

• 자원리싸이클링
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• 제10권2호
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• pp.20-26
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• 2001

석유화학 폐촉매의 유가금속을 회수하기 위하여 과산화수소를 환원제로 사용하여 코발트, 망간, 철의 황산침출거동을 조사하였다. 유가금속의 침출은 반응시작 30분 이내에 모두 이루어졌으며, 고액농도 10 g/L, 0.5N $H_2$$SO_4$, $25^{\circ}C$, 30분 300 rpm에서 과산화수소를 0.027mol/L 첨가한 경우가 첨가하지 않은 경우에 비해 망간, 코발트, 철의 침출율이 24.9%, 20.6%, 30.1온에서 93.0%, 87.0%, 100%로 각각 향상되었다 황산농도가 0.5N H2s04까지 증가함에 따라 각 금속들의 침출율은 증가하였으며, 그 이상의 농도에서는 일정한 침출율을 나타내었다 한편, 반응온도가 증가할수록 망간, 코발트, 철의 침출율이 감소하는 경향을 보였다

• Bulletin of the Korean Chemical Society
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• 제31권4호
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• pp.981-983
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• 2010

The condensation of several aromatic/heteroaromatic aldehydes with 2-aminothiophenol catalyzed by silica sulfuric acid under microwave irradiation afforded 2-arylbenzothiazoles in high yields and short reaction times under solvent-free conditions. The major advantages of the present method are good yields, ecofriendly, reusable catalyst, mild and solvent-free reaction conditions.

• Journal of the Korean Wood Science and Technology
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• 제23권2호
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• pp.88-93
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• 1995

Acid-catalysts were used to accelerate the liquefaction of wood with phenol. Sulfuric acid was quite excellent as a acid-catalyst of liquefaction of wood. It's proper dose was 3% of oven-dried weight of wood to get the 10% of target degree of residue, when the reaction time was 2 hours. The liquefaction of wood catalyzed with sulfuric acid was easily carried out at low temperature of 140$^{\circ}C$, but the degrees of residue decreased gradually with the increase of reaction temperature. The behaviors of liquefaction of oak and radiata pine were nearly same.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.472-477
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• 2001

Spent catalysts containing platinum were generated in petroleum refinery and other chemical industries. The reclamation of precious metals from such wastes has long been attempted in view of their rare, expensive and indispensable nature. In this study, the recovery of platinum from petroleum catalysts was attempted by a method consisting mainly of dissolving alumina substrate with sulfuric acid thereby concentrating insoluble platinum. Also, platinum dissolved partially in sulfuric acid was recovered by a cementation method using aluminum metal as a reductive agent. The effect of temperature, time, concentration of sulfuric acid. and pulp density on the dissolution of substrate was investigated. When the substrate of platinum catalyst was ${\gamma}$-AI$_2$O$_3$ about 95% alumina was dissolved in 6.0M sulfuric acid at 10$0^{\circ}C$ for 2 hours. When the substrate was the mixture of ${\gamma}$-A1$_2$O$_3$and $\alpha$-A1$_2$O$_3$about 92% was dissolved after 4 hours. As a result, more than 99% of platinum could be recovered by this method and aluminum sulfate was obtained as byproduct.