• 청정기술
• /
• 제25권1호
• /
• pp.81-90
• /
• 2019

프로페인($C_3H_8$)의 건식 개질($CO_2$ 개질)을 통한 합성 가스($H_2$와 CO 혼합물) 제조를 위해 $Ni-CeO_2/{\gamma}-Al_2O_3$ 촉매가 충진된 유전체 장벽 방전 플라즈마 반응기를 사용하였다. 열 또는 플라즈마에 의해 환원된 $Ni-CeO_2/{\gamma}-Al_2O_3$ 촉매를 사용하여 $C_3H_8/CO_2$ 비율 1/3, 총 유량 $300mL\;min^{-1}$에서 플라즈마-촉매 건식 개질을 수행하였다. 건식 개질에 대한 촉매 활성은 온도범위 $500{\sim}600^{\circ}C$에서 평가되었다. $Ni-CeO_2/{\gamma}-Al_2O_3$ 촉매 제조를 위해 전구물질 수용액(질산니켈, 질산세륨)으로 함침된 ${\gamma}-Al_2O_3$를 공기 분위기에서 소성시킨 후, $H_2/Ar$ 분위기에서 환원시켰다. 촉매 특성 조사에는 X-선 회절분석기(XRD), 투과전자현미경(TEM), 전계 방출 주사전자현미경(FE-SEM), 승온 탈착($H_2-TPD$, $CO_2-TPD$) 및 라만 분광기가 이용되었다. 열로 환원된 촉매와 비교하면 플라즈마 방전하에서 환원된 $Ni-CeO_2/{\gamma}-Al_2O_3$ 촉매가 개질 반응을 통한 합성 가스 생산에서 보다 우수한 촉매 활성을 나타내었다. 또한, 플라즈마로 환원된 $Ni-CeO_2/{\gamma}-Al_2O_3$가 개질 반응의 문제점인 탄소퇴적 관점에서 장기 촉매 안정성을 보여주었다.

• 한국환경과학회지
• /
• 제21권2호
• /
• pp.165-179
• /
• 2012

Indirect $CO_2$ effect due to non-methane volatile organic compound (NMVOC) emissions from solvent and product use and fugitive NMVOC emissions from fuels in the Republic of Korea and 13 Annex I countries under United Nations Framework on Climate Change were estimated and the proportions of them to total greenhouse gas (GHG) emissions ranged from 0.092% to 0.45% in 2006. Indirect greenhouse effect ($CO_2$, $CH_4$, and $O_3$) were estimated at 13 photochemical assessment monitoring sites in the Republic of Korea using concentrations of 8 NMVOCs of which indirect global warming potential (GWP) were available. The contribution of toluene to mixing ratio was highest at 11 sites and however, the contribution of toluene to indirect greenhouse effect was highest at nine sites. In contrast to toluene, the contributions of ethane, butane, and ethylene were enhanced. The indirect greenhouse effects of ethane and propane, of which ozone formation potentials are the lowest and the third lowest respectively among targeted 10 NMVOCs, ranked first and fourth highest respectively. Acetaldehyde has relatively higher maximum incremental reactivity and is classified as probable human carcinogen however, its indirect GWP ranked second lowest.

• Biomolecules & Therapeutics
• /
• 제18권1호
• /
• pp.99-105
• /
• 2010

The purpose of this study was to evaluate relative bioavailability of the coenzyme Q10 (CoQ10) in emulsion and three liposome formulations after a single oral administration (60 mg/kg) into rats. Emulsion formulation of CoQ10 was prepared by conventional method using Phospholipon 85G as an emulsifier, and three liposome formulations (neutral, anionic, and cationic) of CoQ10 were prepared by traditional lipid film hydration technique using Phospholipon 85G, cholesterol, and charge carrier lipids (1,2-dioleoyl-3-trimethylammonium-propane chloride salt for cationic liposome and 1,2-dimyristoyl-sn-glycero-3-phosphate monosodium salt for anionic liposome). Mean particle size of all CoQ10-loaded liposome was less than a micron, and size distribution of the liposome population was homogeneous. Bioavailability of CoQ10 in emulsion was 1.5 to 2.6-fold greater than liposome formulations in terms of $AUC_{0-24\;h}$. $T_{max}$ was 3 h when administered as emulsion while it was greater than 6 h in liposome formulations. Notably, it was approximately 8 h in cationic liposome. $C_{max}$ was highest in emulsion and was significantly decreased when administered as liposome. Charged liposome showed even lower $C_{max}$ than neutral liposome, especially in cationic liposome. In conclusion, therefore, it is suggested that clinicians and patients consider bioavailability issue a primary concern when choosing a CoQ10 product, especially when very high plasma level is required such as in the treatment of heart failure and Parkinson's disease.

• 한국연소학회:학술대회논문집
• /
• 한국연소학회 1999년도 제19회 KOSCO SYMPOSIUM 논문집
• /
• pp.241-249
• /
• 1999

Soot particle temperatures in co-flow diffusion flames have been measured using a two-color pyrometry at the pressure of 0.2 MPa(2 atm). The measured soot particle temperatures along with the integrated soot volume fractions are analyzed to understand soot formation characteristics. At 0.2 MPa, the addition of small amount of air into ethylene do not change the soot particle temperature in soot formation regions. This result showed that the increase of soot formation with addition of air is mostly due to the chemical effect of the added air, such as the increased role of C3 chemistry during the early stage of soot inception process. The addition of sufficient air into ethylene, however, changes soot particle temperatures and the understanding of soot formation characteristics becomes complicated. Measured soot particle temperatures also showed that there is no significant temperature effect for the synergistic effect of ethylene/propane mixture on soot formation.

• 설비공학논문집
• /
• 제18권4호
• /
• pp.312-319
• /
• 2006

In this study, performance of 2 pure hydrocarbons and 7 mixtures was measured in an attempt to substitute HCFC22 used in air-conditioners and heat pumps. The mixtures were composed of R1270 (propylene), R290 (propane), HFC152a, and RE170 (Dimethyl ether, DME). The pure and mixed refrigerants tested have GWPs of $3{\sim}58$ as compared to that of $CO_2$ and the mixtures are all near-azeotropic showing the gliding temperature difference (GTD) of less than $0.6^{\circ}C$. Thermodynamic cycle analysis was carried out to determine the optimum compositions and actual tests were performed in a laboratory heat pump test bench at the evaporation and condensation temperatures of 7.5 and $45.1^{\circ}C$ respectively. Test results show that the coefficient of performance (COP) of these mixtures is up to 5.7% higher than that of HCFC22. While propane showed 11.5% reduction in capacity, most of the fluids tested had the similar capacity to that of HCFC22. Compressor discharge temperatures were reduced by $11{\sim}17^{\circ}C$ with these fluids. There was no problem with mineral oil since the mixtures were mainly composed of hydrocarbons. The amount of charge was reduced up to 55% as compared to HCFC22. Overall, these fluids provide good performance with reasonable energy savings without any environmental problem and thus can be used as long term alternatives for. residential air-conditioning and heat pumping application.

• Transactions on Electrical and Electronic Materials
• /
• 제2권2호
• /
• pp.5-15
• /
• 2001

The experiment established optimal conditions for over-carbonization. With the use of the electron microscopy and X-ray phase analysis the regularities of carbon deposit formation in process of methane and propane pyrolysis on the zeolites, Kazakhstan natural clays, chrome and bauxite sludge containing metal oxides of iron subgroup, have been studied. In process of over-carbonization the trivalent iron was reduced to metal form. In addition, the carbon tubes of divers morphology had been impregnated with ultra-dispersed metal particles. The kinetic parameters of carbon formation in process of methane decomposition on the zeolite - CoO mixture surface were investigated by method of thermo-gravimetric analysis. The morphology and structure of formed carbon fibrils, with the metal particles fixed at their ends, have been investigated, the formation of branched carbon fibrils pattern, so called octopus, being found. Also, the walnut shells and grape kernel carbonization, their immobilization by the cells of selective absorption of heavy metal and sulfur dioxide ions have been studied. The example of metal-carbon composites used as adsorbents for wastewater purification, C$_3$- C$_4$ hydrocarbon cracking catalysts and refractory materials with improved properties have been considered.

• 대한기계학회:학술대회논문집
• /
• 대한기계학회 2000년도 춘계학술대회논문집B
• /
• pp.453-458
• /
• 2000

The paper describes a study of the variation of the NO production emitted from turbulent propane flames established on a practical combustor where a primary and a secondary fuel lines are installed. The flowrate of the secondary fuel is pulsated or added in addition to that of the primary fuel which constrantly flows to the nozzle of the burner. Two modes depending on the positions of supplying the secondary fuel are performed; one is for its position to be placed at the center of the primary fuel tube and the other around the stabilization baffle. The mean concentrations of gas species, $O_2,\;Co\;CO_2,\;NO$, and HC(unburnt hydrocarbones) have been measured at the exit of the combustor. As equivalence ration $({\Phi})$ is increased the profile of the NO concentration on the latter mode rises slowly less than that on the former one. In the range of ${\Phi}=0.5$ to 0.54 the NO production is reduced by about 35% more on the latter mode than on the former one. The influence of pulsating the secondary fuel on the variation of the NO concentration doesn't appear at both modes.

• 한국신재생에너지학회:학술대회논문집
• /
• 한국신재생에너지학회 2005년도 제17회 워크샵 및 추계학술대회
• /
• pp.638-641
• /
• 2005

수소는 자원이 무한하고 청결한 에너지이다. 수소는 무공해 청정 대체연료로 사용될 수 있을 뿐만 아니라 풍부한 자원으로부터 얻을 수 있다. 수소에너지는 물을 분해하여 얻거나 화석연료를 수증기개질 또는 부분산화 시킴으로써 얻을 수가 있다. 수소에너지는 1차 에너지를 변환시켜 얻을 수 있는 2차 에너지로서 환경에 대한 부하가 거의 없어 향후 화석연료를 대체할 수 있는 가장 가능성이 높은 에너지이며, 연료전지의 상용화를 앞두고 있어 중요성이 더욱 증대되고 있다. 수소를 생산하는 방법 중 가장 이상적인 방법으로는 물분해함으로써 수소를 제조하는 방법이 있다. 그러나 물분해에 의한 수소생산은 제조비용이 비싸 경제성이 떨어진다는 점과 수소의 대량생산에 필요한 기술확보가 여의치 않아 어렵다. 그러므로 수소를 저 비용으로 대량 생산할 수 있는 수소 제조 기술의 확보가 선행되어야 할 것이다. 현재 상용화되어 있는 수소제조방법은 거의 석유나 천연가스의 수증기 개질에 의한 수소 제조 방법이다. 그러나 이러한 방법은 유해 환경 물질인 CO나 $CO_2$를 배출하는 단점을 지니고 있다. 이러한 단점을 보완키 위한 수소 제조공정의 대안 중 하나는 탄화수소연료의 수소와 탄소로의 직접분해에 의한 수소생산이다. 이 중 원하는 생성물인 수소 외에 부산물이 카본이 동시에 얻을 수 있는 메탄분해에 의한 수소생산방법은 생산된 수소의 약 15%만 연소시킴으로서 필요한 에너지를 공급할 수 있으며, 동시에 지구온난화의 주범인 CO 또는 $CO_2$가 생성되지 않는 장점이 있다. 하지만 메탄을 분해하기 위해서는 매우 높은 에너지가 필요로 하게 된다. 이에 반해 프로판은 메탄보다 낮은 열원에서 분해할 수 있는 장점을 지니고 있다. 본 연구에서는 메탄보다 분해하기 쉬운 프로판을 직접 분해하여 수소를 생산하고자 하였다. 프로판 직접분해반응는 $500\sim750^{\circ}C$의 온도 범위에서 이루어 졌으며, 촉매로서는 국내에서 생산되는 상용촉매인 카본블랙을 이용하였다.

• IMMUNE NETWORK
• /
• 제7권4호
• /
• pp.179-185
• /
• 2007

Background: Adenovirus (Ad) vectors have been widely used for many gene therapy applications because of their high transduction ability and broad tropism. However, their utility for cancer gene therapy is limited by their poor transduction into cancer cells lacking the primary receptor, coxsackievirus and adenovirus receptor (CAR). Methods: To achieve CAR-independent gene transfer via Ad, we pretreated Ad with 1,2-dioleoyl-3-trimethylammonium propane (DOTAP) and analyzed their transduction efficiency into cancer cells in vitro and in vivo comparing with the virus alone. Results: Treatment of DOTAP significantly increased adenoviral gene transfer in tumor cells in vitro. Moreover, DOTAP at an optimum dose $(10{\mu}g/ml)$ enhanced IL-12 transgene expression by fivefold in tumor, and twofold in serum after intratumoral injection of adenovirus expressing IL-12N220L (Ad/IL-12N220L). In addition, cotreatment of DOTAP decreased tumor growth rate in the Ad/IL-12N220L-transduced tumor model, finally leading to enhanced survival rate. Conclusion: Our results strongly suggest that DOTAP could be of great utility for improving adenovirus-mediated cancer gene therapy.

• 한국수소및신에너지학회논문집
• /
• 제34권2호
• /
• pp.226-233
• /
• 2023

In this study, we compared the performance of several refrigeration cycles using different refrigerants and utilizing the cold heat of liquefied natural gas (LNG) for the liquefaction of carbon dioxide. The final conditions for the liquefied CO₂ were set to -20℃ and 20 bar. The refrigerants used included R404a, ammonia, propane, and propylene using a vapor recompression refrigeration cycle. For the refrigeration cycle, the CO₂ at room temperature and pressure was compressed in a two-stage compression process with an intermediate cooling stage using a refrigeration unit. To compare with the liquefaction process using refrigeration, we compressed the CO₂ to 8 bar in a single compression stage and cooled it to around -50℃ using the cold heat of the LNG before liquefying it. Results showed that using ammonia as the refrigerant required the least amount of compressor power for the liquefaction process, and the heat transfer area of the evaporator was the smallest when using propylene as the refrigerant. Using the cold heat of LNG instead of refrigeration using R404a resulted in approximately 69% less energy consumption.