• 한국막학회:학술대회논문집
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• 한국막학회 1999년도 춘계 총회 및 학술발표회
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• pp.75-77
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• 1999

• 한국세라믹학회지
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• 제41권12호
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• pp.933-938
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• 2004

[ $3CaO{\cdot}Al_{2}O_3$ ] 클링커 제조 원료로서의 굴 패각과 정유 폐 촉매의 사용 가능성과 이들 조합물의 클링커 소성성 및 광물 생성거동을 광물상과 미구조 관찰을 중심으로 확인하였다. 굴 패각에 함유된 불순물은 클링커의 합성에 영향을 미치지 않았고 이들 조합물은 비교적 저온에서 $12CaO{\cdot}7Al_{2}O_3$를 생성한 후 다시 CaO와의 반응으로 $3CaO{\cdot}Al_{2}O_3$를 생성하므로 $1400^{\circ}C$에서의 1회 소성으로 클링커 합성이 가능하였다. 그 이상의 온도에서는 분해용융이 진행되었으며 동일한 소성 조건에서 알루미나원으로 수산화알루미늄을 사용할 경우에는 $3CaO{\cdot}Al_{2}O_3$의 생성이 완료되기 전에 용융되어 클링커의 합성이 불가능하였다.

• 한국식생활문화학회지
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• 제20권5호
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• pp.627-631
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• 2005

대두유를 정제하는 과정에서 대두원유를 탈검-탈산-탈색-탈취의 일반적인 정제공정을 모두 거친 것과 이들 정제공정을 생략하고 협잡물만 제거한 후 그대로 탈취하여 고유의 색상을 갖는 독특한 대두유를 얻었다. 이 때의 차이는 Sample 1은 정상 탈취유, Sample 2, 3는 협잡물만을 제거한 다음 batch type deodorizer에 주입하여 진공도, 최고온도, stripping steam 주입량, 탈취시간 등을 차등화하여 3단계 탈취를 행하였다. 얻어진 탈취유의 이화학적 특성은 Sampl 1의 경우 산가 0.034, Lovibond color 9.1Y/0.9R, 과산화물가 0의 엷은 노란색 대두유였다. 그러나 Sample 2는 산가 0.078, Lovibond color 65.0Y/18.39R/4.2B/0.1N, 과산화물가 0.7의 밝고 투명한 녹색을 나타내었다. Sample 3은 산가 0.072, Lovibond color 37.3Y/3.8R/0.1B/0.1N, 과산화물가 1.6의 짙은 검붉은 갈색을 나타내어 차이를 보였다. 이러한 착색 탈취대두유는 앞으로 솔잎향미유, 들깻잎향미유 등의 다양한 향미유 제조의 원료유로 각광 받을 것으로 판단된다.

• 식품과학과 산업
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• 제50권4호
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• pp.65-81
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• 2017

In Korea, sesame oil has been used as a flavor source mainly by edible oil since ancient times, and it has been used by domestic screw pressing. In the 1960's, the demand for edible oils and fats increased significantly due to the improvement of national income and changes in food consumption patterns. In the early 1970's, a few edible oil manufacturing companies with modern solvent extraction and refining plants were established. In Korea, edible oil manufacturers account for more than 85% of employees with 50 or fewer employees. In Korea, there is a very shortage of raw materials for edible oils and fats, domestic production of edible oil is decreasing year by year and import volume is continuously increasing. While importing the edible oil bearing ingredients including soybean and extracted oil in the past, recently mainly imports crude oil and refines it in Korea. Soybean oil, palm oil and tallow account for 70~90% of total imported edible oils. Due to the recent well-being trend, the demand for olive, canola and grapeseed oils as household edible oil has increased and the production of blended oil has been greatly increased. Since the late 1980's, people have recognized edible oil and fat as a food instead of seasoning ingredient and have increased their edible oil and fat intake in Korea. Since the early 2000's, refined oil and fat products produced in Korea have been exported and is increasing every year.

• 공업화학
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• 제24권1호
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• pp.10-17
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• 2013

중질탄화수소를 부가가치가 높은 경질탄화수소로 전환하는 업그레이딩 공정은 기존 정유공정에서 사용되고 있는 기술이다. 최근 석유자원의 한계로 비재래형 에너지(Non conventional energy)기술 개발의 중요성이 증가하고 되었고, 그 생산기술이 점차 상용화되어 기존 정유제품의 수요를 대체하고 있다. 향후 자원 부국과의 경쟁입지를 확보하기 위해서는 이러한 비재래형 에너지를 이용하기 위한 기술개발이 매우 중요하다. 대표적인 비재래형 에너지로는 오일샌드 (oil sands), 초중질유(extra heavy oil), 셰일가스(shale gas) 등이 있으며, 이 중 오일샌드 및 초중질유는 원유를 대체할 수 있는 비재래형 에너지원으로, 이들 이용기술은 캐나다 및 베네수엘라에서 상업적으로 개발되었다. 특히, 비튜멘 (bitumen) 및 GTL (Gas-To-Liquid) 합성공정의 중간산물인 FT (Fischer-Tropsch) wax는 업그레이딩(upgrading) 혹은 정제 (refining) 공정을 거쳐 가솔린이나 디젤유과 같은 고부가가치 정유 제품으로 생산된다. 이러한 업그레이딩 공정은 기존 원유 정제공정에서 이루어지고 있는 저급 중질탄화수소의 고도화 공정에 해당되는 기술이다. 비튜멘은 상온에서도 유동성이 없는 고점성의 초중질유와 비슷한 물성을 가진 물질로 기존 정유플랜트에서 처리하기 어려운 성분들이 다량 포함되어 있어, 원유 정제 기술의 고도화 설비와는 차별화된 기술의 적용이 필요하다. 또한, 생산, 수송 및 판매에 많은 비용과 기술적 제한 사항이 존재하며, 특히 비튜멘 생산과 고부가화 합성원유 생산을 위해 필요한 많은 에너지 비용과 플랜트 건설 투자비용은 오일샌드 개발의 큰 장애 요소로 작용되고 있다. 그러나 비튜멘의 생산, 수송, 고부가화 부문의 기술적, 사업적 발전 방향에 대한 연구, 검토가 기존 정유사업 고도화와 연계하여 활발히 진행 중에 있다. 오일샌드의 경우, 비튜멘의 일반적인 시장 판매 방법으로 단순히 희석제와 혼합하여 판매하는 방법이 있고, 업그레이딩을 통하여 합성원유의 형태로 판매하는 방법이 있다. 전자의 경우엔 원유가 대비 희석 비튜멘의 가격차가 커지고, 희석제의 가격이 올라가는 시장상황에서는 불리하다. 또한, 플랜트의 용량이 증가하면, 더욱 경제성이 없어진다. 그래서 처리용량에 맞는 업그레이딩의 적용은 이러한 시장 환경 변화에 대한 대비라 할 수 있다. 이러한 비재래 에너지원의 고부가화(upgrading) 기술에 대하여 알아보고자 한다.

• 한국항해학회지
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• 제22권4호
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• pp.1-14
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• 1998

There are three basic modes of operation of ships: liner, tramp and industrial operations. Industrial operations, where the owner of the cargo, i.e. the industrial carrier controls the ships, abound in the shipment of bulk commodities, such as oil, chemicals and ores. Industrial carriers strive to minimize the shipping cost of their cargoes. This paper is concerned with the operational optimization problem of a fleet owned by major international oil company. The major oil company is a holding corporation for a group of oil producing, transporting, refining, and marketing companies located in various countries throughout the world. The operational optimization problem of the fleet is divided into two-phases. The front end corresponds to the optimization of transporting crude oil, product mix, and the distribution of product oil to meet market demand. The back end tackles the operational optimization problem of the fleet to meet the transportation demand derived from the front end. A case study is carried out with the H major oil company problem composed by reflecting the practices of an international major oil company. The results are summarized and examined in the point of optimization for the total operation of the H major oil company and the operational optimization problem of the fleet. The paper concludes with the remark that the results of the study might be useful and applicable in practices of these related decision problems.

• Archives of Pharmacal Research
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• 제13권3호
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• pp.282-284
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• 1990

By saponification and extraction of corn oil foots abandoned as waste during oil refining, a mixture of phytosterols was obtained, and its major components were determined as .betha.-sitosterol, campesterol and stigmasterol by gas chromatographic analysis. The mixture is very cheap and regarded as an excellent substrate for direct fermentation of C-17 keto steroid intermediate for various steroid pharmaceuticals.

• 한국수산과학회지
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• 제19권5호
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• pp.436-445
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• 1986

As the second part of the studies on the utilization of polyunsaturated lipids in sardine oil as nutritional or medical supplement, the conditions of lipid extration and concentration, refining, and storage stability of EPA-condensed sardine oil were investigated. In extraction of lipids, solvent ratios of chloroform-methanol mixture(2:1 v/v) affected the final content of unsaturated lipid in extracted oil and recovery. Stepwise solvent fractionation method at various low temperatures was effective to concentrate polyenoic acids like EPA and DHA when acetone or acetone-methanol mixture, added in the ratio of 1:5 (v/v) was applied step by step to different temperatures at 0 to $-35^{\circ}C$. Addition of 1 to $5\%$ (v/v) of water to acetone was also benefit to raise EPA content but that resulted in reducing the yield of condensed oil from $65\%\;to\;28\%$. Concentration rate of polyenoic acids by solvent fractionation in lipid-actone solution (1:5, v/v) at 0 to $-30^{\circ}C$ seemed limited to $5{\sim}8\%$ in fatty acid composition depending on the initial content of those polyenoic acids in the sardine oil. During the extraction, concentration, and alkaline treatment, oxidation was rapidly induced but oxidation products could be thoroughly removed on the process of deceleration and peroxide elimination. To stabilize the reactive polyenoic acid condensed oil during the storage, stuffing nitrogen gas was essential to expel dissolved oxygen in oil or to seal the oil from open air, and the addition of antioxidative agents as BHA and tocopherols were greatly helpful to extend the storage life.

• 한국수산과학회지
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• 제22권2호
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• pp.95-101
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• 1989

For the utilization of polyunsaturated fatty acids in sardine (Sardinops melanosticta) oil, mainly as a source for dietary supplement of eicosapentaenoic acid(EPA) and docosahe-xaenoic acid(DHA), the effects of refining and storage, conditions, and addition of stabili-zing agents on the storage stability of EPA condensed and refined sardine oil were tested. Refined, sardine oil deacidified, decolored, and deodorized, was more stable to autoxidation than crude or partially purified oils such as deacidified or/and decolored. The refined sardine oil must be kept at $5^{\circ}C$ or lower temperture for longer than two month storage. The addition of $0.018\%\;\alpha-tocopherol$ or BHT could enhance the stability to autoxidation, and EDTA or citric acid was useful as synergist. Especially the addition of $0.02\%$ citric acid to the oil still hot after deodorizing process ($125^{\circ}C$) was of benefit to stabilize the refined oil.

• Mass Spectrometry Letters
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• 제2권2호
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• pp.41-44
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• 2011

Molecular compositions of two types of heavy oil were studied using positive atmospheric pressure photoionization (APPI) Fourier transform ion cyclotron resonance mass spectrometry (FT-ICR MS). Vacuum gas oil (VGO) was generated from vacuum distillation of atmospheric residual oil (AR), and slurry oil (SLO) was generated from catalytic cracking of AR. These heavy oils have similar boiling point ranges in the range of 210-$650^{\circ}C$, but they showed different mass ranges and double-bond equivalent (DBE) distributions. Using DBE and carbon number distributions, aromatic ring distributions, and the extent of alkyl side chains were estimated. In addition to the main aromatic hydrocarbon compounds, those containing sulfur, nitrogen, and oxygen heteroatoms were identified using simple sample preparation and ultra-high mass resolution FT-ICR MS analysis. VGO is primarily composed of mono- and di-aromatic hydrocarbons as well as sulfur-containing hydrocarbons, whereas SLO contained mainly polyaromatic hydrocarbons and sulfur-containing hydrocarbons. Both heavy oils contain polyaromatic nitrogen components. SLO inludes shorter aromatic alkyl side chains than VGO. This study demonstrates that APPI FT-ICR MS is useful for molecular composition characterization of petroleum heavy oils obtained from different refining processes.