• Title/Summary/Keyword: 전이에스테르화 반응

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Production of Biodiesel from Fleshing Scrap Using Immobilized Lipase-catalyst (Lipase-catalyst를 이용한 프레싱 스크랩의 바이오디젤 제조에 관한 연구)

  • Shin, Soo-Beom;Min, Byung-Wook;Yang, Seung-Hun;Park, Min-Seok;Kim, Hae-Sung;Kim, Baik-Ho;Baik, Doo-Hyun
    • Applied Biological Chemistry
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    • v.51 no.3
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    • pp.177-182
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    • 2008
  • This study was carried out to investigate the reaction of lipase-catalyst transesterification using animal fat recovered from fleshing scrap generated during leather making process. Transesterification reaction between fat and primary or secondary alcohol was carried out under the condition of immobilized enzyme catalyst. The conversion rate was the highest when 1.5 mole of methanol was injected by 4 times. As for lipase, Candida antarctica showed the highest conversion rate of 82.2% among the 4 different lipases. It was found that water contained in the fat causes lower conversion rate. The condition of 1.2wt. % of water in the fat decreased the conversion rate by 40%. It was considered that the resulted reactant, fatty acid ester could be used as raw material for biodiesel with the characteristics of not generating SOx and diminishing smoke.

Biodiesel Production Technology and Its Fuel Properties (바이오디젤 공정기술과 연료특성)

  • Hong, Yeon Ki;Hong, Won Hi
    • Korean Chemical Engineering Research
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    • v.45 no.5
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    • pp.424-432
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    • 2007
  • Biodiesel is gaining more attractive due to its eco-friendly and the fact that it is prepared from renewable sources. It is monoalkyl esters of long chain fatty acids derived from vegetable oils and animal fats via transesterification reaction with alcohol in the presence of catalyst. This paper will review briefly (1) the effect of reaction conditions such as catalyst type, amount of free fatty acid and moisture, molar ratio of alcohol and oil, alcohol type, reaction temperature and time and stirring intesity, (2) downstream process of biodiesel after transesterification reaction, and (3) potentialities of biodiesel as an alternative fuel based on its properties in diesel engines.

Pretreatment of Vegetable Oil Using Ion-exchange Resin and Biodiesel Production (이온교환수지를 이용한 식물유지의 전처리 및 바이오디젤 생산)

  • Hong, Yeon-Ki;Huh, Yun-Suk;Hong, Won-Hi;Oh, Sung-Woo
    • Clean Technology
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    • v.13 no.2
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    • pp.104-108
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    • 2007
  • Biodiesel is a fatty acid alkyl ester produced by chemical reaction of a vegetable oil or animal fat and an alcohol. It is getting attention as a clean alternative energy that can replace gas oils. In this study, strong acidic ion exchange resin was introduced in the pretreatment process of the used cooking oil and rapeseed oil to enhance the conversion of the oil to the biodiesel by removing FFA(free fatty acid). More than 90% FFA was removed. Dry resins showed higher FFA removal efficiency than wet resins. Using transesterification the conversion of triglyceride into fatty acid methyl ester was raised up to 98%. These results can be applicable to the pretreatment of biodiesel feedstocks having high acidic value.

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Transesterification for FAME production of Rapeseed Oil

  • Jeong, Gwi-Taek;Yun, Dae-Hyeon;Gang, Chun-Hyeong;Choe, Byeong-Cheol;Lee, Un-Taek;Park, Don-Hui
    • 한국생물공학회:학술대회논문집
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    • 2003.04a
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    • pp.164-168
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    • 2003
  • Fatty acid methyl esters (FAMEs) show large potential applications as diesel substitutes, and they are known as biodiesel fuel. Biodiesel fuel as a renewable energy is an alternative that can reduce energy dependence on petroleum and air pollution. Several processes for the production of biodiesel fuel have been developed. Transesterification process under alkali-catalysis and short-chain alcohol gives high level yield of methyl esters in short reaction times. In this research, transesterification of rapeseed oil was investigated to produce the FAMEs. Experimental reaction conditions included molar ratio of oil to alcohol, concentration of catalyst, types of catalysts, reaction time, and reaction temperature. The conversion ratio of rapeseed oil enhanced with the alcohol-oil mixing ratio and with the reaction temperature.

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Study on Production of Glycerol Derivative from Bioglycerol (바이오디젤 부산물인 폐글리세롤을 이용한 유도체 생산에 관한 연구)

  • Ryu, Young-Bok;Lee, Sun-Do;Lee, Man-Sig
    • Proceedings of the KAIS Fall Conference
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    • 2010.11a
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    • pp.298-300
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    • 2010
  • 화석 연료인 석유, 천연가스, 석탄의 점진적 고갈이 예상됨에 따라 전 세계는 석유와 유사한 성질을 갖는 바이오 오일을 에너지원 및 화학원료로 사용하려는 노력이 증가하고 있다. 바이오 오일 활용분야 중 가장 큰 부분을 차지하고 있는 것은 바이오 디젤로 식물성 오일과 알콜의 전이에스테르화 반응에 의하여 생산되며, 바이오 디젤 1톤당 100kg의 글리세롤이 부산물로 생성된다. 본 연구에서는 바이오 디젤 부산물인 폐글리세롤을 이용하여 다양한 유도체의 생산 및 그 유도체의 가능성에 대하여 살펴보았다.

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Biodiesel Production with KOH/NaX catalyst as various calcination temperature (KOH가 담지된 NaX 제올라이트 촉매의 소성온도에 따른 바이오디젤 합성 특성)

  • Kim, Min-Kyu;Kim, Jang-Mi;Chang, Duk-Rye
    • 한국신재생에너지학회:학술대회논문집
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    • 2009.11a
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    • pp.524-526
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    • 2009
  • 바이오디젤은 식물성 기름이나 동물성 지방과 같은 재생 가능한 원료로부터 전이에스테르화 반응을 통해 생산되는 대체 연료이다. 본 연구에서는 NaX 제올라이트 촉매에 염기성 물질인 KOH를 담지한 후 소성온도에 따라 제조된 촉매를 사용하여 바이오디젤 제조 특성을 조사하였다. 제조된 촉매의 결정구조와 성분을 분석하기위해 XRD, SEM 을 이용하였으며, 표면적을 측정하기 위해 BET 를 사용하였다. 실험결과 소성온도가 $500^{\circ}C$일 때 30wt% KOH/NaX 제올라이트 촉매내 K 함량이 가장 높았고, 이때 70%이상의 높은 바이오디젤 수율을 얻을 수 있었다.

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Study on Manufacturing Emulsion Oil Using Biodiesel Feedstock Oil Production By-product (바이오디젤 원료유 생산 부산물을 이용한 유화유 제조 연구)

  • Kim, Deogkeun;Jeon, Sanggoo;Yoon, Sangjun;Park, Soonchul
    • 한국신재생에너지학회:학술대회논문집
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    • 2010.11a
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    • pp.106.2-106.2
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    • 2010
  • 동식물성 기름과 메탄올의 전이에스테르화 반응에 의해 생산되는 바이오디젤은 환경친화성과 지속가능성이 인정됨에 따라 그 생산량이 급격히 증가하고 있어 대두유, 유채유, 팜유 등의 원료유 부족과 가격 상승, 수급 불안정 등의 문제가 대두되고 있다. 이를 해결하기 위한 방안으로 유리지방산 함량이 높은 저가유지 자원(폐식용유, 폐돈지, 폐우지, soapstock, trapped grease)과 새로운 오일 작물을 이용한 생산 기술 연구가 활발히 진행되고 있다. 본 연구에서는 비활용 해외 열대작물 씨앗에서 착유한 식물성 오일을 정제하여 바이오디젤 원료유를 생산하는 과정에서 발생하는 폐기물(폐유, 폐수)의 경제적 처리 방안으로 유화유 제조 원료(벙커C유, 물)와 유화유 제조 첨가제(무기계, 유기계)로 활용 가능성을 검토하였다. 열대작물 오일의 물성 분석 결과 고형물, 수분, 인지질(phospholipid), 유리지방산(free fatty acid) 함량이 기존 원료유보다 매우 높게 나타났다. 인지질은 바이오디젤 제조 반응후 에스테르와 글리세린의 층분리를 방해하고 유리지방산은 염기촉매와 결합하여 지방산염을 생성해 생산 수율을 감소시킨다. 고형물과 수분 역시 촉매반응에 악영향을 가지나 여과와 감압증발에 의해 쉽게 제거가 가능하다. 유리지방산은 산촉매 에스테르화 반응에 의해 제거가 가능하다. 인지질은 탈검(degumming) 과정을 통해 제거하며 탈검은 수용성 탈검, 산 탈검, 세정 공정으로 구성된다. 착유한 원료유의 고형물을 제거 후 물과 수세하여 수용성 인지질을 수화하여 층 분리해 제거하고 상층의 오일은 추가적인 산 탈검을 수행한다. 그 뒤 세정을 통해 사용된 탈검제인 산과 추가적으로 수화된 인지질을 제거하게 된다. 이러한 3단계의 탈검 과정에서 하층으로 오일과 물이 폐기물로서 배출되며 본 연구에서는 배출 폐기물을 다시 층분리하여 오일층과 물 층으로 구분하여 유화유 제조에 사용되는 벙커C유, 물, 그리고 기존 유기계 및 무기계 유화제의 대체 가능성을 조사하였다. 유화 연료유는 기름과 물을 균일한 분산상으로 혼합한 연료유로 연소시 오일계 성분의 미연분을 감소시켜 연료 효율 제고와 배출가스 성상을 개선하기 위해 개발되어 왔다. 본 발표에서는 다양한 종류의 상용 첨가제 및 바이오디젤 원료유 생산 폐기물을 활용해 유화 연료유를 제조하였으며 각 유화유의 장시간의 상(phase) 안정성을 비교하였다. 바이오 폐기물 중에는 천연 계면활성제(surfactant)인 인지질이 다량 함유되어 있어 기존의 무기계 및 유기계 유화제보다 상 안정성이 우수하게 나타났으며 바이오디젤 원료유 생산 공정의 폐기물인 폐유과 폐수의 활용이 가능한 것으로 나타났다.

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Molecular Dynamics Simulation Study of Lipase-catalyzed Esterification of Structural Butanol Isomers in Supercritical Carbon Dioxide (초임계 이산화탄소에서 리파아제-효소를 이용한 부탄올 구조이성질체의 에스테르화 반응의 분자 동역학 연구)

  • Kwon, Cheong-Hoon;Jeong, Jeong-Yeong;Song, Kwang Ho;Kim, Seon Wook;Kang, Jeong-Won
    • Applied Chemistry for Engineering
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    • v.18 no.6
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    • pp.643-649
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    • 2007
  • Lipase-catalyzed esterification of structural butanol isomers and n-butyric acid was investigated in supercritical carbon dioxide. The experiments were performed in a high pressure cell for 5 hrs with a stirring rate of 150 rpm at 323.15 K and 130 bar. The Candida Antarctica lipase B (CALB) was used in whole system as a catalyst. The experimental results were analyzed by GC-FID using a INNOWax capillary column. The conversion yield and the tendency of the esterification in supercritical carbon dioxide were compared with estimated results by molecular dynamics simulation. Based on the Ping-Pong Bi-Bi mechanism with competitive inhibition, each step of the reaction was optimized; using this result the transition state was predicted. Conformational preference of isomers was also analyzed using molecular dynamics simulations. This kind of approach will be further extended to the prediction of enzyme-catalyzed reactions using computers.

Study of Fuel Properties for Biodiesel Derived from Duck's Oil (오리기름으로부터 합성된 바이오디젤의 연료특성 연구)

  • Lim, Young-Kwan;Lee, Cheon-Ho;Jung, Choong-Sub;Yim, Eui-Soon
    • Applied Chemistry for Engineering
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    • v.21 no.6
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    • pp.653-658
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    • 2010
  • Biodiesel is well known for an eco-friendly alternative fuel for petrodiesel. But biodiesel has a disadvantage since it is derived from expensive food resource. In this study, we synthesized the biodiesel from duck's oil which was food trash via transesterification under base catalyst. After analytic result of density, kinematic viscosity, cold temperature characteristics, lubricity and cetane number which were main fuel characteristics, this duck's biodiesel has enough potential to use as fuel except only domestic winter season.

Characteristics of Transesterification Reaction of Soy Bean Oil by Acid Catalysts (산촉매에 의한 대두유의 전이에스테르화 반응 특성)

  • Shin, Yong-Seop
    • Journal of Environmental Science International
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    • v.18 no.2
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    • pp.231-238
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    • 2009
  • Characteristics of the transesterification reaction between triglycerides in soy bean oil and methanol were investigated in the presence of acid catalysts. such as sulfuric acid and PTS (p-toluene sulfonic acid). Concentrations of diglyceride and monoglyceride which were intermediates in the reaction mixtures, were far below 10% of triglyceride under any reaction conditions. Thus, conversion of the reaction could be determined from the concentration of triglyceride. Dried PTS had more superior catalytic power than sulfuric acid for transesterification reaction between soy bean oil and methanol. When transesterification reaction of soy bean oil was catalyzed by 1 wt% of PTS at methanol stoichiometric mole ratio of 2 and $65^{\circ}C$, final conversion reached 95% within 48 hours. If FAME (fatty acid methyl ester) was added into reaction mixture of soy bean oil, methanol and PTS catalyst, it converted reaction mixture into homogeneous phase, and substantially increased reaction rate. When reaction mixture was freely boiling which had equal volumetric amount of FAME to soy bean oil, methanol stoichiometric mole ratio of 2 and 1 wt% of PTS, final conversion achieved value of 94% and temperature approached to $110^{\circ}C$ within 2 hours.