• 한국재료학회:학술대회논문집
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• 한국재료학회 2012년도 춘계학술발표대회
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• pp.58.2-58.2
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• 2012

Heavy hydrocarbon reforming is a core technology for "Dirty energy smart". Heavy hydrocarbons are components of fossil fuels, biomass, coke oven gas and etc. Heavy hydrocarbon reforming converts the fuels into $H_2$-rich syngas. And then $H_2$-rich syngas is used for the production of electricity, synthetic fuels and petrochemicals. Energy can be used efficiently and obtained from various sources by using $H_2$-rich syngas from heavy hydrocarbon reforming. Especially, the key point of "Dirty energy smart" is using "dirty fuel" which is wasted in an inefficient way. New energy conversion laboratory of KAIST has been researched diesel reforming for solid oxide fuel cell (SOFC) as a part of "Dirty energy smart". Diesel is heavy hydrocarbon fuels which has higher carbon number than natural gas, kerosene and gasoline. Diesel reforming has difficulties due to the evaporation of fuels and coke formation. Nevertheless, diesel reforming technology is directly applied to "Dirty fuel" because diesel has the similar chemical properties with "Dirty fuel". On the other hand, SOFC has advantages on high efficiency and wasted heat recovery. Nippon oil Co. of Japan recently commercializes 700We class SOFC system using city gas. Considering the market situation, the development of diesel reformer has a great ripple effect. SOFC system can be applied to auxiliary power unit and distributed power generation. In addition, "Dirty energy smart" can be realized by applying diesel reforming technology to "Dirty fuel". As well as material developments, multidirectional approaches are required to reform heavy hydrocarbon fuels and use $H_2$-rich gas in SOFC. Gd doped ceria (CGO, $Ce_{1-x}Gd_xO_{2-y}$) has been researched for not only electrolyte materials but also catalysts supports. In addition, catalysts infiltrated electrode over porous $La_{0.8}Sr_{0.2}Ga_{0.8}Mg_{0.2}O_3-{\delta}$ and catalyst deposition at three phase boundary are being investigated to improve the performance of SOFC. On the other hand, nozzle for diesel atomization and post-reforming for light-hydrocarbons removal are examples of solving material problems in multidirectional approaches. Likewise, multidirectional approaches are necessary to realize "Dirty energy smart" like reforming "Dirty fuel" for SOFC.

• 한국연소학회지
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• 제14권4호
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• pp.25-32
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• 2009

In commercial combustion systems, heavy oil is one of main hydrocarbon fuel because of its economical efficiency. Regarding heavy oil combustion, due to increasing concerns over environmental pollutants such as carbon monoxide, unburned hydrocarbon and nitrogen oxides, development of low pollutant emission methods has become an imminent issue for practical application to numerous combustion devices. Also a great amount of effort has been tried to developed effective methods for practical using of biomass. It is also an important issue to reduce carbon tax. In this paper, an experimental study has been conducted to evaluate the effect of biomass reburning on NOx formation in a heavy oil flamed combustion furnace. Experiments were performed in flames stabilized by a multi-staged burner, which was mounted at the front of the furnace. Experimental tests were conducted using air-carried rice husk powder and LNG as the reburn fuel and heavy oil as the main fuel. The paper reports data on flue gas emissions and temperature distribution in the furnace for several kinds of experimental conditions. NOx concentration in the exhaust has decreased considerably due to effect of reburning. The maximum NOx reduction rate was 62% when the rice husk was used by reburn fuel, however it was 59% when the LNG was used by reburn fuel. The result shows the positive possibility of biomass reburning system for optimal NOx reduction.

• Journal of Advanced Marine Engineering and Technology
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• 제30권1호
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• pp.88-92
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• 2006

This study is intended to check the flame temperature to raise in burning grade C heavy fuel oil and emulsion fuel oil in a boiler and to measure the concentration of Dry Shoot(DS) and Soluble Organic Fraction(SOF) after collecting the Particulate Matters (PM). The flames temperature in boiler was measured by burning grade C heavy oil and oil-water emulsion (C heavy oil $70\%\;and\;30\%$ of water) Combustion characteristics of two fuels was also compared by trapping particulate matters (PM) in exhaust gas and measuring the generated quantities of DS and SOF in fuel gas.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2011년도 추계학술대회 초록집
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• pp.97.2-97.2
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• 2011

Pt-Ru and Pt-Ni bimetallic catalysts were prepared and tested for heavy hydrocarbon reforming. Metals were supported on CGO($Ce_{0.8}Gd_{0.2}O_{2.0-x}$) by incipient wetness method. The prepared catalysts were characterized by Temperature programmed reduction(TPR). Oxidative steam reforming of n-dodecane was conducted to compare the activity of the catalysts. The reforming temperature was varied from $500^{\circ}C$ to $800^{\circ}C$ at fixed $O_2$/C of 0.3, $H_2O$/C of 3.0 and GHSV of 5,000/h.Reduction peaks of metal oxide, surface CGO and bulk CGO were detected. Reduction temperature of metal oxide decreased over the bi-metallic catalysts. It is considered that interaction between metals leads to decrease interaction between metal and oxygen. On the other hands, reduction temperatures of surface CGO were dectected in the order of Pt-Ru > Pt-Ni > Pt. low reduction temperatures of surface CGO indicates the low activation energy for oxygen ion conduction to metal. Oxygen ion conduction is known as de-coking mechanism of ionic conducting supports such as CGO. In activity test, fuel conversion was in the same order of Pt-Ru > Pt-Ni > Pt. Especially, 100% of fuel conversion was obtained over Pt-Ru catalysts at $500^{\circ}C$.

• 대한기계학회논문집
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• 제19권12호
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• pp.3372-3381
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• 1995

An equilibrium analysis was carried out to determine principal species of heavy metals in waste incineration and their behaviors with variation of temperature, chlorine concentration, excess air ratio, and C/H ratio. The waste was assumed as a compound of hydrocarbon fuel, chlorine, and metals. Calculated results showed that the most important parameter to determine the principal species was temperature. Chlorine concentration also affected on mole fractions of the principal species. Generally principal species at high temperature were chlorides while there were some metals of which principal species were oxides. At low temperature mole fractions of the principal species increased, but at high temperature mole fractions of some metal species decreased. C/H ratio of the hydrocarbon fuel and excess air ratio had little effect on mole fractions of the metal species, compared to the temperature and chlorine concentration.

• Journal of Advanced Marine Engineering and Technology
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• 제28권2호
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• pp.292-299
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• 2004

This study is intended to check a temperature of the flame to raise by burning A heavy oil in a boiler. to measure the concentration of DS and SOF after collecting the PM(Particulate Matters). and to analyze the components ingredients of SOF by G.C Mass for presupposing the generation of particulate matters(soot). It is thought that the methyl(CH3) of the cyclic compound is changed to the materials of 2 cycles and 3 cycles after becoming CH by dehydrogenation and also mixing with the CH of a chain compound. form H-$\cdot$C=C$\cdot$-H that is mentioned before. in order to become Polycyclic Aromatic Hydrocarbon.

• 공업화학
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• 제27권4호
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• pp.343-352
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• 2016

지구상에는 1조 6880억 배럴의 원유매장량으로 현재 추세로 채굴하면 향후 53.3년 채굴 가능할 것으로 예측되고 있다. OPEC은 원유값이 10년 내에는 $100이 넘지 않을 것으로 예상하지만, 감산 정책의 정치적 이슈가 등장하면 원유값은 급격히 상승할 수도 있다. 따라서 일반 원유의 고갈에 대비해 비재래형 원유자원인 오일샌드나 비튜맨과 같은 중질유에 대한 관심이 높아지고 있다. 중질유는 일반적으로 레진이나 아스팔텐이라 부르는 탄소수가 60이 넘는 분자량이 높은 화합물 함량이 높아 점도가 높고 끓는점이 높다. 일반 원유를 감압 증류할 때 부생되는 감압잔사유(vacuum residue)는 물리화학적 물성들이 중질유와 비슷하다. 중질유의 채굴을 위해서는 점도를 낮추는 기술이 중요한데 본 리뷰논문은 상업적으로 사용되고 있는 aquathermolysis 기술을 검토하여 보았고 감압잔사유에 적용하여 보았다. 감압잔사유에는 니켈(Ni)과 바나듐(V)과 같은 전이금속이 함유되어 있는데, 이를 고도화하기 위해서는 전이금속 제거가 선행되어야 한다. 본 리뷰 논문에서는 감압잔사유로부터의 전이금속 제거 기술에 대한 최근 연구결과를 정리하여 보았다.

• 한국지하수토양환경학회지:지하수토양환경
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• 제12권5호
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• pp.54-63
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• 2007

중질유로 오염된 토양의 생물학적 정화에 있어 amendment의 처리효과를 보고자 포장에서 pilot 규모로 105일간 실험을 수행하였다. 실험기간 중 주기적으로 토양시료를 채취하여 유류성분과 생물학적 활성과 관련된 분석을 수행하였는데 퇴비의 처리구들에서 쌀겨+무기양분처리구에 비하여 유류성분의 분해활성이 현저하게 증가함을 확인할 수 있었다. 105일 경과 후 amendment 처리구들에서는 초기농도 $6,205{\pm}173mgkg^{-1}$의 $33{\sim}45%$가 소실된 반면 무처리구에서는 8%만이 분해된 것으로 나타났다. 퇴비처리구들에서 무처리구 및 쌀겨처리구에 비해서 높은 중질유 분해활성을 관찰할 수 있었는데 실험기간 중 모니터링한 생물학적 지표들 중 soil respiration, dehydrogenase, lipase, urease 등의 효소활성이 쌀겨처리구에 비해 현저하게 높은 활성이 관찰되었고 이들 미생물학적 지표들과 중질유의 분해정도 사이에는 높은 상관관계가 존재하였다(p < 0.01).

• 대한기계학회논문집B
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• 제34권4호
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• pp.417-422
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• 2010

1.7L 커먼 레일 직접 연료분사 디젤엔진과 초저유황 스웨덴 디젤 연료를 이용하여 연료분사시기 8.5CA BTDC~0.5CA BTDC 와 배기가스 재순환률 37%, 43%, 48% 영역에서 실험을 수행하였다. 각각의 배기가스 재순환률에 대하여 연료분사시기가 지각됨에 따라 매연과 질소산화물이 동시에 저감되나 탄화수소와 일산화탄소는 증가하는 저온 디젤 연소영역에 있음을 확인하였다. 탄화수소를 가스크로마토그래프와 불꽃 이온 검출기를 사용하여 종 분석을 수행하였으며, 연료분사시기가 지각될수록, 그리고 배기가스 재순환률이 증가할수록 Partially burned HC, 알켄의 비율이 증가하였다. Partially burned HC 중에서 에텐이, 그리고 Unburned HC 중에서 노말 운데케인이 가장 많이 배출되었다. 이 두 개의 탄화수소 종은 촉매 연구에 사용되는 벤치 플로우리액터 시험에서 대표적인 탄화수소 종으로 사용할 수 있다.

• Applied Biological Chemistry
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• 제13권1호
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• pp.43-50
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• 1970

석유탄화수소 이용미생물연구의 일환으로서 미생물에 의한 세포단백질생산의 목적으로 전국각지 135 개지역에서 주유소 세차장의 유침(油浸)토양을 비롯 석탄, 논밭, 하천토양등 242종을 수집하고 이시료로부터 석유탄화수소를 유일한 유기탄소원으로 이용하는 효모 468균주를 분리하였고 분리된 효모균주의 증식율(增殖率)을 screening 하여 우수균주를 선정하였다. 선정된 효모에 대하여 동정(同定) 및 배양 최적 조건의 검토 그리고 효모균체의 성분분석을 한 결과 다음과 같다. 1) 석유탄화수소 이용효모중 90.8%가 주유소및 세차장등 유침토양에서 나머지 10%가 석탄, 작토(作土) 하천토양에서 분리되였다. 2) 분리선정된 가장 우수한 효모균주는 주유소의 유침토양에서 분리됐고 Candida curvata HY-69-19로 동정되었다. 3) 분리선정된 Candida curvata HY-69-19는 optimum pH 5.0, optimum temperature $28^{\circ}C$, aerobic condition에서 균증식율이 컸다. 4) Candida curvata HY-66-19는 유기탄소원으로 petroleum fraction 중 비중이 0.8654이고 비점이 $268.9^{\circ}C$ 이상의 fraction인 heavy gas oil을 잘이용하며 무기질소원으로$(NH_2)_2CO$가 증식율과균체세포생산에 최적임을 알었다. 5) 분리선정된 이효모는 heavy gas oil 배지에서 lag phase 18시간, logarithmic growth phase 24시간${\sim}$42시간 사이며 이 때의 generation time은 3.8${\sim}4.5$시간이었다. 6) 분리선정된 이 효모는 heavy gas oil 및 $(NH_2)_2CO$ 배지로 54시간 pH 를 6시간마다 조정하면서 진탕배양하여 300mg/ml. H.G,0.의 건조균체를 생산하였다. 7) Candida curvata HY-69-19의 균체성분은 조단백질 40.25%, 조지방 14.81%,탄수화물 24.32% 회분 10.63%이었다.