• Proceedings of the Membrane Society of Korea Conference
• /
• 2004.05a
• /
• pp.98-101
• /
• 2004

Utilization of biomass resources has considerable contribution to the reduction of carbon dioxide emission. Ethanol is one of the biomass products and is used as an additive to gasoline in several countries. Conventional process to produce ethanol involves energy-intensive azeotropic distillation. Pervaporation (PV) or vapor permeation (VP) is considered to be an alternative separation process to the conventional process.(omitted)

• Proceedings of the Membrane Society of Korea Conference
• /
• 1992.10a
• /
• pp.57-58
• /
• 1992

분리막을 이용한 물질의 분리는 최근 들어 많은 연구가 수행되어 일부 실용화 되고 있으나, 최근에 관심을 끌고 있는 Pervaporation 분리법에 의한 유기물의 분리는 여러가지 이유에서 아직 큰 성과를 올리지 못하고 있다고 생각된다. 그러나, 이 방법만이 갖는 잇점 때문에 국내.외에서 다방면으로 활발히 연구가 진행되고 있다. 한편 Pervaporation 분리법의 분리기구를 규명하는데는 많은 어려움이 있으므로 아직까지 명확히 밝혀지지 않고 있으나 언제인가는 밝혀져야 할 과제라고 생각된다. 따라서 본 연구에서는 투과현상을 좀 더 구체적으로 파악하므로써 분리기구를 해석하는 데 다소나마 기여하기 위하여 물 선택성 막은 Carboxy-methylcellulose(CMC) 막을 제작하여 알코올류, DMF, DMAc, Dioxane등의 유기 수용액의 분리실험을 하였으며, 투과 증기의 조성을 짧은 시간 간격으로 측정하므로써 분리특성과 아울러 투과현상을 파악하였다.

• Proceedings of the Membrane Society of Korea Conference
• /
• 1996.03a
• /
• pp.25-43
• /
• 1996

In general, membrane technology in Japan has remarkably developed in these 20 years. Especially, ones treating water is now in high level and seems to be matured. Water shortage of last summer was a new stimulus for promoting membrane research works. The researches are now extending to more precise separation of, for example, isomer and proteins. In such cases, not only polymeric materials but also ceramic or carbon ones are attempted. Concerning pervaporation (PV), water permselective membranes (GFT) are in practical use, PV research works are now concentrating on separation of new targeting substances. Here, I'd like to introduce, first of all, the outline of membrane technology in Japan (not limited to PV), and then of PV research works.

• Proceedings of the Membrane Society of Korea Conference
• /
• 2004.11a
• /
• pp.3-5
• /
• 2004

• Proceedings of the Membrane Society of Korea Conference
• /
• 1999.04a
• /
• pp.86-89
• /
• 1999

• Korean Chemical Engineering Research
• /
• v.49 no.5
• /
• pp.560-564
• /
• 2011

The objective of this study is to propose a mathematical model for a pervaporation process for concentrating hydrogen peroxide. The process was developed by NASA, which consists of a shell and membrane tubes, where a liquid hydrogen peroxide solution flows in the shell, and a sweep gas flows in the tubes countercurrent to each other. The liquid retentate is concentrated as more water molecules permeate and evaporate through the membrane than hydrogen peroxide. For this process, a mathematical model has been developed in the form of a system of nonlinear partial differential algebraic equations based on a sorption-diffusion mechanism for permeation, an Arrhenius relationship for the temperature dependency of the permeate flux, and mass and momentum balances for the liquid concentrations and flows in the membrane module. The dynamic behavior of the concentration of hydrogen peroxide in the retentate side has been simulated by solving a simplified version of the proposed model, and the result is compared with the experimental data reported in the NASA patent.

• Korean Chemical Engineering Research
• /
• v.52 no.6
• /
• pp.750-754
• /
• 2014

Quantitative risk analysis has been performed for a pervaporation process for production of high test peroxide. Potential main accidents are explosion and fire caused by a decomposition reaction. As the target process has a laboratory scale, the consequence is considered to belong to Category 3. An event tree has been developed as a model for occurrence of a decomposition reaction in the target process. The probability functions of the accident causes have been established based on the frequency data of similar events. Using the constructed model, the failure rate has been calculated. The result indicates that additional safety devices are required in order to achieve an acceptable risk level, i.e. an accident frequency less than $10^{-4}/yr$. Therefore, a layer of protection analysis has been applied. As a result, it is suggested to introduce inherently safer design to avoid catalytic reaction, a safety instrumented function to prevent overheating, and a relief system that prevents explosion even if a decomposition reaction occurs. The proposed method is expected to contribute to developing safety management systems for various chemical processes including concentration of hydrogen peroxide.

• Applied Chemistry for Engineering
• /
• v.4 no.4
• /
• pp.791-797
• /
• 1993

The application of the pervaporation process in biotechnology is rapidly growing. A two stage pervaporation process can be applied to the downstream processing of ethanol fermentation. In this paper, the second stage process in which the water-ethanol composition was 50:50 wt.% was investigated in more detail by using Nylon 4 and its blended membranes containing poly(vinyl alcohol) (PVA) and poly(acrylic acid) (PAA). Nylon 4 membranes were tested for compositions at 25, 30, and $35^{\circ}C$. Nylon 4 membranes had a separation factor of 4.18 with a permeability of $0.69kg/m^2hr$ at water-ethanol composition of 50:50 wt.%, while nylon 4-PVA blended membranes crosslinked by 5 Mrad gamma-ray irradiation showed a higher separation factor of 10.56 with permeability $0.55kg/m^2hr$ at the same composition. Nylon 4 also showed a high separation factor 27.8 at the ethanol-water azeotropic composition among the homopolymer membranes.

• Membrane Journal
• /
• v.12 no.4
• /
• pp.255-261
• /
• 2002

Poly(vinyl alcohol) (PVA) membranes crosslinked with poly(acrylic acid-co-maleic anhydride) (PAM) as a polymeric crosslinking agent were prepared to investigate the pervaporation performance for the dehydration separation of aqueous ethanol solution. The characteristics of the resulting membranes crosslinked(x) were analysed by FT-IR and water swelling test. The water swelling decreased with increasing crosslinking agent content. The crosslinked PVA membranes with PAM showed lower water swelling than those of PVA membrane crosslinked with glutaraldehyde and modified PVA membrane. The swelling of water molecules in the crosslinked PVA membranes is more restricted by both chemical crosslinking between PVA and polymeric crosslinking agent chains and physical crosslinking by the entanglement between the PVA and polymeric crosslinking agent chains. For the pervaporation of aqueous ethanol solution through the crosslinked membrane, as the contents of crosslinking agent increased, the separation factor increased while the permeation flux decreased. The separation factor slightly decreased and permeation flux increased with increasing feed water content. As a result it could be considered that PVA-PAM membranes suppressed the plasticization effect even in the range of high water concentration in fled.

• Membrane Journal
• /
• v.17 no.1
• /
• pp.14-22
• /
• 2007

This is the research about the concentration of trace Magnolia flavor components in water by pervaporation. We have investigated the change of selectivity depending on support membrane structure and active layer thickness using prepared PVDF/PDMS composite membrane. Through the pure water flux test for PVDF support membrane, we could indirectly confirm that as the coagulation temperature decreases and the polymer concentration increases, the surface porosity and pore diameter decreases. Appling these results to transport mechanism, we could explain the effect of support membrane structure for the composite membrane. The selectivity increases as the thickness of PDMS active layer increases. We could know that there is a limitation to describe the transport on the active layer by Fick's law through these results.