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A Study on the N2O Separation Process from Crude N2O (Crude N2O로부터 정제된 N2O 분리공정에 관한 연구)

  • Cho, Jungho;Lee, Taekhong;Park, Jongki
    • Korean Chemical Engineering Research
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    • v.43 no.4
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    • pp.467-473
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    • 2005
  • Liquid phase nitrous oxide ($N_2O$) contains air, carbon monoxide, water, carbon dioxide and NOx as main impurities. It is known to be very dangerous to obtain a very pure $N_2O$ product by using solidification at low temperature. In this study a new method to obtain a high purity of $N_2O$ product based on a continuous distillation process was introduced. For the modeling of the continuous distillation process to obtain a product having a purity over 99.999% of $N_2O$ stream, Intalox wire gauze packing- No. SCH-80S gauze packing column was used. Peng-Robinson equation of state was used for the modeling of the continuous distillation process and refrigeration system. Computational results performed in this work showed a good agreement with Aspen Plus simulation results.

Optimization Study for Pressure Swing Distillation Process for the Mixture of Isobutyl-Acetate and Isobutyl-Alcohol System (Isobutyl-Acetate와 Isobutyl-Alcohol 이성분계의 압력변환증류 공정 최적화 연구)

  • Cho, Sung Jin;Shin, Jae Sun;Choi, Suk Hoon;Lee, Euy Soo;Park, Sang Jin
    • Korean Chemical Engineering Research
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    • v.52 no.3
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    • pp.307-313
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    • 2014
  • In this study, an optimization process design has been performed to separate 99.9 mol% of Isobutyl Acetate from binary azeotropic mixture of Isobutyl Acetate and Isobutyl Alcohol system using a Pressure Swing Distillation (PSD). PSD is used to separate binary azeotropic mixtures using the difference between the relative volatilities and azeotropic compositions by changing the system pressure. Non-Random Two Liquid (NRTL) model for liquid phase and the Peng-Robinson equation for vapor phase are used. An optimization study for the reflux ratio and feed stage locations which minimize the total reboiler heat duties are studied. Since PSD process consists of two columns, i.e. high pressure and low pressure, the effect of column sequence on the optimum conditions is reported.

Solubility of Ibuprofen in Supercritical Carbon Dioxide (초임계 이산화탄소를 이용한 Ibuprofen의 용해도 측정)

  • Kim, Young Ae;Chu, Junho;Lim, Jong Sung;Kim, Hwayoung;Lee, Youn-Woo
    • Clean Technology
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    • v.11 no.3
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    • pp.147-152
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    • 2005
  • For estblishing the best technique for the micronization of Ibuprofen using supercritical fluids, the solubility should be known. The solubility of Ibuprofen in supercritical carbon dioxide was measured by observing the cloud point. The cloud point was observed using high pressure equipment equipped a variable volume view cell between temperature of 35, 40 and $45^{\circ}C$. The solubility data was correlated by the Peng-Robinson equation of state Solute physical properties, such as critical temperature (Tc), critical pressure (Pc) and acentric factor (${\omega}$) were estimated by the some group contribution method. As pressure was increased, the solubility increased at constant temperature. The retrograde phenomenon by a solute vapor pressure and a density of solvent was observed at the pressure of around 150bar. It was found that $CO_2$ can be used as a supercritical solvent in micronization of ibuprofen by RESS.

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High-pressure Phase Behavior of 1-propanol / Carbon Dioxide Binary System (1-Propanol / CO2 이성분계의 고압 상거동)

  • Han, Chang-Nam;Kang, Choon-Hyoung
    • Korean Chemical Engineering Research
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    • v.48 no.6
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    • pp.763-767
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    • 2010
  • High-pressure phase behavior for the binary mixture of 1-propanol with supercritical $CO_2$ has been measured by means of a high-pressure phase equilibrium apparatus equipped with a variable-volume view cell. The equilibrium loci of the pressure - composition and pressure - temperature were obtained for the binary mixture of 1-propanol + $CO_2$ system at 305.15 K, 313.15 K, 323.15 K and 333.15 K, and from 2 MPa to 11 MPa. The critical temperature of the mixture increased with the temperature. The pressure-composition line for the binary mixture of $CO_2$-1-propanol system showed a typical type-II phase behavior. The experimental P-x envelopes were correlated by using the Peng-Robinson equation of state in a satisfactory manner to obtain the parameters with $k_{ij}=0.116$ and ${\eta}_{ij}=-0.065$.