Electrophoretic protein transport in gold nanotube membranes

被引:92
作者
Yu, SF
Lee, SB
Martin, CR [1 ]
机构
[1] Univ Florida, Dept Chem, Gainesville, FL 32611 USA
[2] Univ Florida, Ctr Res Bionano Interface, Gainesville, FL 32611 USA
关键词
D O I
10.1021/ac020711a
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
Gold nanotube membranes are ideal model systems for exploring how pore size affects the rate and selectivity of protein transport in synthetic membranes. This is because these membranes have cylindrical, monodisperse pores (the nanotubes) with diameters that can be varied at will from tens of nanometers down to less than 1 nm. We report here on the effects of nanotube inside diameter, solution pH, and applied transmembrane potential on the rate and selectivity of protein transport in PEG-thiol-treated gold nanotube membranes. The transport properties of four proteins of differing sizes and pI values-lysozyme, bovine serum albumin, carbonic anhydrase, and bovine hemoglobulin-were investigated. In general, membranes containing larger diameter nanotubes showed higher fluxes and lower selectivities than membranes with smaller diameter nanotubes. Transmembrane electrophoresis can be used to augment the diffusive transport selectivity. For example, for proteins that are oppositely charged, a combination of a large transmembrane potential and a large nanotube diameter can be used to optimize both selectivity and flux. In addition to transmembrane potential and nanotube diameter, solution pH value plays an important role in determining the transport selectivity. This is because pH determines the net charge on the protein molecule and this, in turn, determines the importance of the electrophoretic transport term.
引用
收藏
页码:1239 / 1244
页数:6
相关论文
共 33 条
[1]  
ANFINSEN CB, 1985, ADV PROTEIN CHEM, V37, P176
[2]   Fractionation of BSA and lysozyme using gas-sparged ultrafiltration in hollow fiber membrane modules [J].
Bellara, SR ;
Cui, ZF ;
Pepper, DS .
BIOTECHNOLOGY PROGRESS, 1997, 13 (06) :869-872
[3]   Protein transport in nanoporous membranes modified with self-assembled monolayers of functionalized thiols [J].
Chun, KY ;
Stroeve, P .
LANGMUIR, 2002, 18 (12) :4653-4658
[4]   HINDERED TRANSPORT OF LARGE MOLECULES IN LIQUID-FILLED PORES [J].
DEEN, WM .
AICHE JOURNAL, 1987, 33 (09) :1409-1425
[5]   Fractionation of BSA and lysozyme using ultrafiltration: effect of pH and membrane pretreatment [J].
Ghosh, R ;
Cui, ZF .
JOURNAL OF MEMBRANE SCIENCE, 1998, 139 (01) :17-28
[6]   Protein purification by ultrafiltration with pre-treated membrane [J].
Ghosh, R ;
Cui, ZF .
JOURNAL OF MEMBRANE SCIENCE, 2000, 167 (01) :47-53
[7]   Membrane fouling during microfiltration of protein mixtures [J].
Guell, C ;
Davis, RH .
JOURNAL OF MEMBRANE SCIENCE, 1996, 119 (02) :269-284
[8]  
HINZ HJ, 1986, THERMODYNAMIC DATA B, P237
[9]   Measurement and theoretical modeling of protein mobility through membranes [J].
Ho, AK ;
Perera, JM ;
Dunstan, DE ;
Stevens, GW ;
Nyström, M .
AICHE JOURNAL, 1999, 45 (07) :1434-1450
[10]   Effect of membrane morphology on the initial rate of protein fouling during microfiltration [J].
Ho, CC ;
Zydney, AL .
JOURNAL OF MEMBRANE SCIENCE, 1999, 155 (02) :261-275