• Applied Chemistry for Engineering
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• v.8 no.3
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• pp.357-364
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• 1997

The objective of this study was to find optimum nonionic surfactants for clean up of soils contaminated by hydrocarbon oils. PIT(phase inversion temperature) measurements in ternary systems containing pure hydrocarbons, pure nonionic surfactants, and water were carried out and interfacial tensions were measured as a function of time for n-hexadecane oil drops brought into contact with various mixtures of nonionic surfactant and water. Batch surfactant washing experiments were performed based on the measurement, results of PIT and interfacial tension and the results showed that maximum removal of n-hexadecane occurred at the PIT of the system. For the $C_{12}E_5(C_{12}H_{25}O(CH_2CH_2O)_5H)$ system, maximum n-hexadecane removal of 73.4% occurred at the PIT of $52^{\circ}C$. In contrast, n-hexadecane removal at $25^{\circ}C$ and at $60^{\circ}C$, each corresponding to the conditions of below PIT and above PIT of the system, was found to be 57.1% and 57.0% respectively. The maximum removal of a hydrocarbon at the PIT of a system, where the hydrophilic and hydrophobic properties are balanced, was found to be due to the existence of high oil solubilization into a middle-phase microemulsion and ultralow interfacial of the order of $10^{-2}$ to $10^{-3}$ dyne/cm between middle-phase microemulsion and excess oil phase.

• Resources Recycling
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• v.8 no.5
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• pp.34-43
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• 1999

An elecmc arc cracking reaclor is developed for the productiol~o f ieusuble fuel gas by the thennal destruction of waste oil. The churaclensucs of product gas and ~esiduesf rom arc crachng of wnste lubr~cat~nogil are sludird. Thc product gas is mainly coruposcd of hydrogen 135-4076), acetylene (13-4076), ethylene 13-476) and olher hgdrocnrbons. The contenr of carbon monomde, one or the main product in a conventional low-temperature Lhennal cracking umt, 1s very slnvll in lhis atc cracking expcnmcnt. Total calocctic wlue of product gas shows 11,000-13.000 kcizlkg, which is hiph cnough to use as a ~ L I I I Cga~ s . and the concentralions oC loxic gases arc well below the rcguliltury emission critena The GCIMS analysis of llquld-phase residues shows that the high rnalccular welgllt hydrocilrbons in the waste oil arc cracked into the low malecular weight hydrocarbons snd hydroem,. The dehydrogcnntion is found lo be Lhe main cracking rcacuon due lo the high temperalure ~ ~ ~ d ubcyc edle ctric arc. The average parucle size of soot as the solid-phase residue is 10 3 wm, and the conlents of cabon a ~ hdea vy metals are abovc 60% and under 0.01 ppm, respecttrely. Thc utllizvtion or sool, as industl-id1 rcsource seems lo he reasible aIter refimng.

• Applied Chemistry for Engineering
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• v.34 no.5
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• pp.507-514
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• 2023

The selective catalytic reduction (SCR) of nitrogen oxides (NO_x) was investigated in a catalyst (Ag/γ-Al₂O₃) packed dielectric barrier discharge plasma reactor. The intermittent generation of plasma in the catalyst bed partially oxidized the hydrocarbon reductant for NO_x removal to several aldehydes. Compared to using the catalyst alone, higher NO_x conversion was observed with the intermittent generation of plasma due to the formation of highly reductive aldehydes. Under the same operating conditions (temperature: 250 ℃; C/N: 8), the NO_x reduction efficiencies were 47.5%, 92%, and 96% for n-heptane, propionaldehyde, and butyraldehyde, respectively, demonstrating the high NO_x reduction capability of aldehydes. To determine the optimal condition for intermittent plasma generation, the high voltage on/off cycle was adjusted from 0.5 to 3 min. The NO_x reduction performance was compared between continuous and intermittent plasma generation on the same energy density basis. The highest NO_x reduction efficiency was achieved at 2-min high voltage on/off intervals. The reason that the intermittent plasma discharge exhibited higher NO_x reduction efficiency even at the same energy density, compared to the continuous plasma generation case, is that the intermediate products, such as aldehydes generated from hydrocarbon, were more efficiently utilized for the reduction of nitrogen oxides.

• Proceedings of the Korean Vacuum Society Conference
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• 2014.02a
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• pp.261.1-261.1
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• 2014

지구상에 존재하는 모든 생물에 의해 배출되는 이산화탄소는 온실가스로써 산업혁명 이후 급격한 농도 증가로 인해 지구 온난화 등의 다양한 환경문제를 초래하고 있다. 지구 온난화의 가시화로 인한 각종 기후 협약 및 탄소배출권 등에 규제로 온실가스 감축의무부과가 확실해져 탈 석유기반 사회로 전환을 위한 이산화탄소를 처리하는 다양한 연구가 각국에서 활발히 진행 중이다. 본 연구에서 마이크로웨이브 플라즈마 토치를 이산화탄소 분해에 이용하게 되었고 그 목적은 이산화탄소가스를 마이크로웨이브로 가열하여 순수한 이산화탄소 플라즈마 토치를 발생함으로서 지구 온난화의 주범인 이산화탄소를 생산적으로 이용하기 위한 것으로 전자파를 발진하는 마그네트론으로는 3kW, 2.45GHz의 주파수를 사용한다. 마이크로웨이브 플라즈마 토치를 이용한 이산화탄소의 분해 시 생성되는 물질을 확인하기 위하여 이산화탄소의 열역학적 평형을 계산하였으며 또한 이산화탄소의 분해 반응의 준 평형상태에서의 속도상수를 이용하여 각 분해반응생성물들의 밀도비율을 계산하였고, 이를 일반화시켜 도시하였다. 위 과정을 통해 고온의 이산화탄소 토치는 탄화수소 연료를 1기압에서 개질할 수 있음을 알 수 있다. 예를 들어 메탄개질은 $CO_2+CH_4{\rightarrow}2CO+2H_2$의 반응식이 된다. 이때 엔탈피와 엔트로피 변화는 각 각 ${\Delta}H=247kJ/mole$과 ${\Delta}S=257J/mole/deg.$이며 이 반응에 대한 gibbs 자유에너지는 $G={\Delta}H-T{\Delta}S$로서 개질 자발반응이 일어나는 온도는 $T={\Delta}H/{\Delta}S=961K$가 된다. 그리고 탄화수소 개질에 참여하는 산소와 CO 라디칼의 밀도가 대단히 높다. 따라서 메탄개질은 이산화탄소 토치를 통하여 1기압에서 쉽게 이루어진다.

• 한국신재생에너지학회:학술대회논문집
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• 2006.11a
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• pp.344-347
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• 2006

탄화수소 연료(LNG, LPG)를 개질하여 수소를 제조하는 연료 처리 공정 중, 탈황 기술은 촉매의 활성저하 및 전극의 피독을 방지하기 위한 필수 기술이다. 본 연구에서는 도시가스 및 액화석유 가스용 부취제로 사용되는 유기 황화합물(,DMS, THT, TBM)을 제거하기 위한 탈황제로서 Cu/ZnO계 흡착제를 개발하였다. 공침법을 이용하여 흡착제를 제조하여 각 부취제별로 상온 및 고온에서의 흡착탈황 성능을 조사하였으며 또한, 이의 특성분석을 행하였다. $Cu/ZnO/Al_2O_3$ 탈황제는 메탄으로부터 고온에서 TH, DMS, TBM+THT 등의 황화합물들을 매우 효과적으로 제거할 수 있었다. 특히, TBM+THT의 혼합가스에서 TBM에 대해 선택적인 흡착을 보였다. THT 흡착에서 흡착온도가 $300^{\circ}C$ 이상에서는, 흡착과정 동안 황의 상호작용으로 인해 금속황화물이 생성되었다.

• 한국신재생에너지학회:학술대회논문집
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• 2006.06a
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• pp.89-92
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• 2006

수소에너지는 화석연료 사용의 증가로 인한 환경오염 및 자원고갈의 문제점을 해결해 줄 수 있는 미래의 청정한 에너지이다. 현재 주 에너지원인 화석연료의 사용에 의하여 배출된 오염물질이 지구온난화와 같은 문제점들을 일으킨다. 이러한 문제점들을 없애줄 수 있는 대안 중 하나가 수소에너지이다. 수소에너지는 자원이 풍부하며 연소시에 오염물질이 배출되지 않는 장점이 있다. 수소에너지는 수소를 연소시켜서 얻는 에너지로써, 수소를 태우면 같은 무게의 가솔린 보다 3배나 많은 에너지를 방출한다. 수소를 생산하는 방법 중 가장 이상적인 방법은 물을 분해하는 방법이다. 그러나 이 방법은 수소를 대량으로 생산하기에는 아직 기술에 대한 확보가 되어있질 않으며, 경제성도 떨어진다는 단점이 있다. 현재 많이 쓰이는 방법 중 탄화수소류의 메탄을 수증기 개질하는 방법이 있다. 메탄 수증기 개질방법은 환경오염물질인 CO나 $CO_2$를 배출한다는 것과 높은 열원이 필요하다 본 연구에서는 C-H결합에너지가 낮아 메탄보다 분해하기 쉬운 부탄의 직접분해로 수소를 생산하고자 한다. 부탄 직접분해는 환경오염물질인 CO나 $CO_2$가 발생되지 않는 장점이 있다. 부탄 분해반응은 $500{\sim}1100^{\circ}C$의 범위에서 이루어 졌으며, 촉매는 탄소계인 카본블랙을 사용하였고, 촉매의 성능을 비교하기 위하여 열분해반응이 동시에 수행되었다.

• The Korean Journal of Petroleum Geology
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• v.6 no.1_2 s.7
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• pp.25-36
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• 1998

Organic geochemical analyses were carried out in order to characterize organic matter (OM) in the sediments recovered from Korea/japan Joint Development Zone (JDZ V-1, V-3, VII-1 and VII-2) which is located in the northern end of the East China Sea Shelf Basin. Late Miocene sediments from the JDZ V-1 and V-3 wells generally contain less than $0.5\%$ of total organic carbon (TOC). However, early Miocene and Oligocene sediments show TOC values of $0.6-0.8\%$. Middle to late Miocene sediments are rich in TOC up to $20\%$ from JDZ VII-1 and JDZ VII-2 wells. The reason for this rich TOC might be attributed to the presence of coaly shales. Kerogens in the Tertiary sediments from the JDZ series wells are mainly composed of terrestrially derived woody organic matter. Elemental analyses indicate that OM from these wells can be compared to type III. Low hydrocarbon potential and hydrogen index reflect the type of OM. According to the biomarker analyses, the input of the terrestrial OM is prevalent. Oxidizing condition is also indicated by Pristane/Phytane ratio. Samples from the JDZ V-1 and V-3 wells obtain maturities equivalent to the oil generation zone around total depth, and organic matter below 3600 m from JDZ VII-1 and VII-2 wells reached dry gas generation stage. Oligocene sediments below 3500 m in the JDZ VII-1 and JDZ VII-2 wells may have generated limited amount of hydrocarbons, showing a progressive decrease in hydrogen index with depth, due to thermal degradation with increased burial. Gas shows and finely disseminated gilsonite may indicate the generation and migration of the hydrocarbons.

• Journal of Korean Society of Environmental Engineers
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• v.39 no.1
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• pp.34-39
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• 2017

The recent gradual increase in the energy demand is mostly met by fossil fuel, but the research on and development of new alternative energy sources is drawing much attention due to the limited fossil fuel supply and the greenhouse gas problem. This paper assesses the feasibility of producing fuel energy from a dewatered sewage sludge by microwave-induced pyrolysis with sludge char and graphite receptor. Both receptors produced gas, char, and tar in order from product amount. The gas produced for the sludge char receptor contained mainly hydrogen and methane with a small amount of light hydrocarbons. The graphite receptor generated higher gravimetric tar and generated higher light tar. Through the results, the product gas from the microwave processes of wet sewage sludge might be possible as a fuel energy. But the product gas has to be removed the condensable PAH tars.

• Journal of the Korean Professional Engineers Association
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• v.12 no.4
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• pp.26-31
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• 1979

The Natural Gas and petroleum have the same Origin, Namely, Ocean bottom deposits of the marine plant, plankton which are subdued to the biological action of the bacterium under the anaerobic circumstance, and changed to the hydrocarbon gas and oils. and such resources are appeared in the aqueous sedimentary rocks in the tertiary. There are three types of gas field, which are oil well gas field, structural gas field and water soluble gas field.

• Journal of the Korean Society of Propulsion Engineers
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• v.14 no.2
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• pp.71-79
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• 2010

As hypersonic flight speeds and engines efficiencies increase, heat loads on an aircraft and it's engine increase. Because the temperature of the air flow is too high to cool the aircraft structure at hypersonic flight speeds, it is essential to use the aircraft fuel as the primary coolant. Endothermic fuels are liquid hydrocarbon aircraft fuels which are able to absorb the heat loads by undergoing endothermic reactions, such as thermal and catalytic cracking. The endothermic reactions are improved by catalysts which change the extent of reaction and product distribution. At high temperature, liquid hydrocarbons would lead to coke formation that can reduce the effectiveness of heat exchanger and cause rapid degradation of the catalyst, thus endothermic capacity of endothermic fuels is limited to the temperature at which coke doesn't form. In this study, the essential cooling technologies by applying endothermic fuels and the properties of the endothermic fuels are described.