• Title/Summary/Keyword: composite hollow fiber membrane

Search Result 43, Processing Time 0.019 seconds

Assessing the Dehydration Pervaporation Performance for Purification of Industrially Significant 1, 2 Hexanediol/Water Mixtures Using Crosslinked PVA Membrane (가교된 PVA 분리막을 이용한 1, 2 hexanediol/water 혼합물의 투과증발 탈수 특성 연구)

  • Shivshankar Chaudhari;Se Wook Jo;Min Young Shon
    • Membrane Journal
    • /
    • v.33 no.6
    • /
    • pp.369-376
    • /
    • 2023
  • In this study, the alternative to the energy-intensive conventional vacuum distillation process, an eco-friendly and energy-efficient pervaporation separation was employed in 1,2 hexane diol/water (HDO/water) mixture. The crosslinked PVA-glutaraldehyde was coated inside the alumina hollow fiber membrane (Al-HF). In the HDO/IPA pervaporation separation, optimization of the membrane concerning PVA/GA ratio, curing temperature, and pervaporation operating condition were performed. In the long-term stability test, the sustainable pervaporation separation performance giving flux in the range of 1.90~2.16 kg/m2h, and water content in permeate was higher than 99.5% (separation factor = 68) was obtained from the PVA/GA (molar ratio = 0.08, curing temperature = 80℃) coated Al-HF membrane from HDO/water (25/75, w/w, %) mixture at 40℃. Therefore, this work provides potential and inspiration for PVA-based membranes to mitigate excessive energy requirements in HDO/water separation by pervaporation.

Pilot Test with Pervaporation Seperation of Aqueous IPA Using a Composite PEI/PDMS Membrane Module (IPA/물 혼합액의 PEI/PDMS 복합막 모듈을 이용한 투과증발 파일롯 분리특성)

  • Cheon, Bong Su;Cheong, Seong Ihl;Rhim, Ji Won
    • Membrane Journal
    • /
    • v.25 no.5
    • /
    • pp.385-390
    • /
    • 2015
  • To determine the pervaporation separation characteristics of IPA/water mixtures, PEI/PDMS hollow fiber membrane module commercialized by Airrane Co. was subjected to both lab and pilot tests. The flux of $0.52kg/m^2h$ and IPA concentration of 68.5% at $25^{\circ}C$ were obtained whereas the $1.368kg/m^2h$ and 61.2% were measured at $55^{\circ}C$. In order to realized the durability of the module, the long-term test (at $50^{\circ}C$) of 100 days has been conducted and as a result, the flux $1.03{\sim}1.15kg/m^2h$ and IPA concentration 61.8~62.5% were maintained with the initial values.

Hydrogen Permeation Performance of Pd, Pd/Cu Membranes Manufactured through Electroless Plating (무전해 도금을 이용해 제작한 Pd, Pd/Cu 분리막의 수소 투과 성능)

  • Jeong In, Lee;Min Chang, Shin;Xuelong, Zhuang;Jae Yeon, Hwang;Chang-Hun, Jeong;Jung Hoon, Park
    • Membrane Journal
    • /
    • v.32 no.6
    • /
    • pp.456-464
    • /
    • 2022
  • Hydrogen permeation performance was analyzed by manufacturing Pd and Pd-Cu membranes through electroless plating. As a support for the Pd and Pd-Cu membranes, α-Al2O3 ceramic hollow fiber were used. Pd-Cu membrane was manufactured through sequential electroless plating, and then annealing was performed at 500°C, for 18 h in a hydrogen atmosphere to make Pd and Cu alloy. After annealing, the Pd-Cu membrane confirmed that the alloy was formed through EDS (Energy Dispersive X-ray Spectroscopy) and XRD (X-ray Diffraction) analysis. In addition, the thickness of the Pd and Pd-Cu plating layers were measured to be about 3.21 and 3.72 µm, respectively, through SEM (Scanning Electron Microscope) analysis. Hydrogen permeation performance was tested for hydrogen permeation in the range of 350~450°C and 1~4 bar in hydrogen single gas and mixed gas (H2, N2). In a single hydrogen gas, Pd and Pd-Cu membranes have flux of up to 54.42 and 67.17 ml/cm2⋅ min at 450 °C and 4 bar. In the mixed gas, it was confirmed that the separation factors of 1308 and 453 were obtained under the conditions of 450 °C and 4 bar.