Abstract

Designing an effective intravenous membrane oxygenator requires selecting hollow fiber membranes (HFMs) which present minimal resistance to gas exchange over extended periods of time. To evaluate HFMs, we developed a simple apparatus and methodology for measuring HFM permeability in a gas-liquid environment which has the capability of studying a variety of fiber types in any liquid of interest, such as blood. Using this system, we measured the O 2 and CO 2 exchange permeabilities of Mitsubishi MHF 200L composite HFMs and KPF 280E microporous HFMs in water at 37°C. The membrane permeability measured for the MHF 200L composite fiber was 7.9 × 10 −6 ml/s/cm 2/cmHg for O 2 and 8.4 × 10 −5 ml/s/cm 2/cmHg for CO 2, and for the KPF 280E microporous fiber, 1.4 × 10 −5 ml/s/cm 2/cmHg for O 2 and 3.2 × 10 −4 ml/s/cm 2/cmHg for CO 2. The permeabilities of the microporous HFMs were over two orders of magnitude less than what would be measured in a gas-gas system due to liquid infiltration of the pores, emphasizing the importance of measuring permeability in a gas-liquid system for relevant applications such as intravenous oxygenation. Furthermore, both O 2 and CO 2 permeabilities of the microporous fiber were consistent with a liquid infiltration depth of only 1%. The O 2 permeability of the MHF fiber was found to be less than the overall exchange permeability ultimately required of our intravenous oxygenation device ( K ≈ 1 × 10 −5 ml(STP)/s/cm 2/cmHg). Consequently, the MHF 200L composite fiber appears unsuitable for intravenous oxygenation devices such as ours.

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