• Korean Chemical Engineering Research
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• 제56권4호
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• pp.536-541
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• 2018

Excess molar volumes ($V_m^E$) of binary mixtures of 1-propanol or 2-propanol (1) + cyclohexane or n-hexane (2) were measured with V-shaped dilatometer at 303.15 K. The $V_m^E$ data for these mixtures varied as: 2-propanol > 1-propanol and were higher for cyclohexane than n-hexane for both propanol systems. The experimental data were correlated with Redlich-Kister polynomial. The $V_m^E$ data were interpreted qualitatively as well as quantitatively in terms of Flory-Treszczanowicz-Benson model and Prigogine-Flory-Patterson theory. Both models correctly described the sign and shape of $V_m^E$ vs $x_1$ curves. The values calculated by both the models agree well with the experimental data.

• Korean Chemical Engineering Research
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• 제48권6호
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• pp.763-767
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• 2010

본 연구에서는 가변부피 투시셀이 장착된 고압 상평형 장치를 사용하여 초임계 용매인 이산화탄소와 1-propanol의 기액 상평형 거동을 관찰하였다. 이산화탄소와 1-propanol 이성분계에 대하여 온도 305.15 K, 313.15 K, 323.15 K, 333.15 K와 압력 2~11 MPa 범위까지의 실험 결과를 압력-조성(P-x)과 압력-온도(P-T)의 평형 곡선으로 나타내었다. 온도가 증가함에 따라서 혼합물 임계압력도 증가하였고 이산화탄소와 1-propanol계 혼합물의 P-T 곡선은 전형적인 type-II의 유형을 나타내었다. Peng-Robinson 상태방정식을 이용하여 실험 결과를 적합하여 결정한 최적 파라미터 값은 각각 $k_{ij}=0.116$와 ${\eta}_{ij}=-0.065$이였으며 Peng-Robinson 상태방정식에 적용하여 계산된 예측치는 실험결과와 비교적 좋은 일치를 보였다.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1991년도 한국자동제어학술회의논문집(국내학술편); KOEX, Seoul; 22-24 Oct. 1991
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• pp.1085-1090
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• 1991

Chemical heat pump is a system to upgrade the low level energy such as industrial waste heat and solar energy by using coupled endothermic and exothermic chemical reactions. Dehydrogenation of 2-propanol can absorb heat near 80.deg. C and is transformed into acetone and hydrogen. Hydrogenation of acetone can liberate heat near 200.deg. C. Dehydrogenation of 2-propanol is difficult around 80.deg. C because .DELTA.G has positive value, but dehydrogenation reaction in liquid phase can overcome this problem because vaporized acetone and hydrogen can be rapidly eliminated. In this work, dehydrogenation of 2-propanol was investigated in liquid phase with Raney nickel catalyst. The energy efficiency of the chemical heat pump was estimated by computer simulation.

• Bulletin of the Korean Chemical Society
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• 제26권8호
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• pp.1246-1250
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• 2005

We have evaluated the hydroxyl group-solvent specific interactions by using a Lichrosorb RP18 stationary phase and by measuring the retention data of carefully selected solutes in 50/50, 60/40, 70/30, 80/20, and 90/10(v/v%) methanol/water eluents at 25, 30, 35, 40, 45, and 50 ${^{\circ}C}$. The selected solutes are 3 positional isomers of phenylpropanol, that is, 1-phenyl-1-propanol, 1-phenyl-2-propanol, and 3-phenyl-1-propanol. There exist clear discrepancies in ${\Delta}H^o$ (solute transfer enthalpy from the mobile to the stationary phase) and $T{\Delta}S^o$ (solute transfer entropy) among positional isomers. The difference in ${\Delta}H^o$ and $T{\Delta}S^o$ between secondary alcohols (1-phenyl-1-propanol and 1-phenyl-2-propanol)is negligible compared to the difference between the primary alcohol (1-phenyl-3-propanol) and secondary alcohols. The $T{\Delta}S^o$ values of 3-phenyl-1-propanol are close to those of butylbenzene while the $T{\Delta}S^o$ values of secondary alcohols are close to those of propylbenzene. The difference in ${\Delta}{\Delta}H^o$ (specific solute-mobile phase interaction enthalpy) between the primary alcohol and the secondary alcohol decreases with increase of methanol content in the mobile phase. A unique observation is an extremum for 1-phenyl-3-propanol in the plot of $T{\Delta}{\Delta}S^o$ vs. methanol volume %. The positive sign of $T{\Delta}{\Delta}S^o$ of 3-phenyl-1-propanol implies that the entropy of 3-phenyl-1-propanol is greater than that of the hypothetical alkylbenzene (the same size and shape as phenylpropanol) in the mobile phase.

• 청정기술
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• 제24권4호
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• pp.275-279
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• 2018

본 연구에서는 물과 이산화탄소의 상호 용해력을 높이기 위한 방법의 하나로, 계면활성제를 이용하여 물과 이산화탄소의 마이크로에멀션 형성하는 조건을 관찰하였다. 물과 이산화탄소의 마이크로에멀션을 형성시키기 위하여 계면활성제 2,2,3,3,3-Pentafluoro-1-propanol를 첨가하였다. 초임계 이산화탄소에 물과 계면활성제인 2,2,3,3,3-Pentafluoro-1-propanol 일정량을 첨가하여 이에 따른 마이크로에멀션의 구름점(cloud point) 변화와 경향을 살펴보았다. 계면활성제+이산화탄소 계의 경우 상전이 조건은 313.2 ~ 353.2 K 온도범위에서 8.35 ~ 12.69 MPa이였으며, 물+계면활성제+이산화탄소 계의 경우 온도범위 318.2 ~ 338.2 K에서 7.83 ~ 17.28 MPa에 이르는 압력 범위에서 구름점를 보였다.

• 한국세라믹학회지
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• 제40권5호
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• pp.488-493
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• 2003

유기용매를 함유하는 염화니켈 수용액으로부터 Ni 미분말을 제조하였고 Ni 분말형성에 미치는 유기용매 첨가의 영향을 검토하였다. 모든 생성물들은 0.1~l.0 $\mu\textrm{m}$ 범위의 구형입자들이었고 입자들간의 응집은 관찰되지 않았다. 1-propanol이 40 vol% 첨가된 경우 분말의 입경감소와 균일성이 현저하였다. 이들 분말에 대한 평균입경과 비표면적은 각각 0.3 $\mu\textrm{m}$와 16.4 m$^2$/g이었다. 1-propanol의 첨가량이 증가함에 따라 hydrazine에 의한 환원반응시간은 감소하였고, 1-propanol이 40 vol%가 첨가된 경우 환원시간은 약 5분이었다. Ni 합성 분말은 32$0^{\circ}C$ 부근에서 산화되었고, 30$0^{\circ}C$ 부근에서의 중량 감소는 Ni(OH)$_2$의 탈수에 기인한 것이다.

• 한국화재소방학회논문지
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• 제27권5호
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• pp.64-69
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• 2013

가연성 혼합물의 최소자연발화온도는 가연성액체의 안전한 취급을 위해서 중요한 지표가 된다. 본 연구에서는 ASTM E659 장치를 이용하여 가연성 혼합물인 n-Propanol과 Formic acid 계의 최소자연발화온도와 발화지연시간을 측정하였다. 2성분계를 구성하는 순수물질인 n-Propanol과 Formic acid의 최소자연발화온도는 각 각 $435^{\circ}C$와 $498^{\circ}C$로 측정되었다. 그리고 측정된 n-Propanol과 Formic acid 계의 최소자연발화온도는 제시된 식에 의한 예측값과 작은 평균절대오차에서 일치하였다. 그리고 n-Propanol과 Formic acid 계는 일부 혼합 조성에서 두 개의 순수물질 가운데 낮은 AIT보다 낮게 측정된 최소자연발화온도거동(MAITB, Minimum Autoignition Temperature Behavior)을 보이고 있다.

• 한국화재소방학회논문지
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• 제21권2호
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• pp.48-53
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• 2007

혼합물의 인화점에 대한 지식은 산업 현장에서 화재화재 예방 및 방호를 위해서 매우 중요하다. 본 연구에서는 water+2-propanol 계의 인화점을 Tag 개방식 장치(ASTM D1310-86)를 이용하여 측정하였다. 실험값은 Raoult의 법칙, Van Laar 모델식과 NRTL 모델식에 의해 계산된 값들과 비교되었다. 그 결과, Van Laar 모델식과 NRTL(non random two liquids) 모델식에 의한 예측값이 Rauolt의 법칙에 의한 예측값 보다 실험값에 더욱 근접하였다. 이는 water+2-propanol 계와 같은 비이상용액의 활동도 계수값을, Van Laar 및 NRTL 모델식이 Raoult의 법칙보다 정확하게 계산하기 때문이다. 또한, Van Laar 모델식의 실험값에 대한 모사성이 NRTL 모델식의 그것 보다 우수하였다.

• Journal of Microbiology and Biotechnology
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• 제11권3호
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• pp.369-375
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• 2001

Urushiol, a natural monomeric oil, was used to prepare a detergentless micro-emulsion with water and 2-propanol The formation of micro-emulsion was verified by conductivity measurements and dynamic light scattering. The conductivity data showed phase change dynamics, a characteristics of micro-emulsions, and subsequent dynamic light scattering study further confirmed the phenomenon. Average water droplet diameter was 10 nm to 500 nm when the molar ratio of 2-propanol ranged from 0.40 to 0.44 . Earlier studies were performed on toluene and hexane, in which the insoluble substrate in water phase was added to the solvents to be reacted on by enzymes. However, in the present urushiol system, urushiol was used as both solvent and substrate in the laccase polymerization of urushiol. The laccase activity in the system was examined using polymerization of urushiol. The laccase activity in the system was examined using syringaldezine as a substrate, and the activity increased rapidly near the molar ratio of 2-propanol at 0.4, where micro-emulsion started. The activity rose until 0.46 and fell dramatically thereafter. The study of laccase activity in differing mole fractions of 2-propanol showed the existence of an ‘optimal zone’, where the activity of laccase was significantly higher. In order to analyze urushiol polymerization by laccase, a bubble column reactor using a detergentless micro-emulsion system was constructed. Comparative study using other organic solvents systems were conducted and the 2-propanol system was shown to yield the highest polymerization level. The study of laccase activity at a differing mole fraction of 2-propanol showed the existence of an ‘optimal zone’ where the activity was significantly higher. Also, 3,000 cP viscosity was achieved in actual urushi processing, using only 1/100 level of laccase present in urushi.

• 한국산업융합학회 논문집
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• 제7권1호
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• pp.97-105
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• 2004

The Vapor-liquid equilibrium data for the binary system of 2-methyl-2-propanol-2-butanone are measured at subatmospheric pressure of 100, 200, 300, 400, 500, 600, 700 and 760 torr. This study shows that the relations between logarithmic values of relative valatility(log ${\alpha}$)and liquid phase composition(${\chi}$) in the above binary systems are expressed as a linear function. When the linear relationships of between logarithmic values of relative volatilities and liquid phase compositions in the binary systems of various pressure intersect at a point, this empirical equation can be applied to the systems of this kind. From these relations the vapor-liquid equilibrium data are estimated and compared with the measured values to be in a good agreement with in accuracy ${\pm}0.0021$ for the various pressure.