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NAMS 2002 Workshop - ICOM 2008

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Inorganic Membranes III – 1 – Keynote<br />

Friday July 18, 9:30 AM-10:15 AM, O’ahu/Waialua<br />

Silica Network Engineering For Highly Permeable Hydrogen Separation<br />

Membranes<br />

T. Tsuru (Speaker), Hiroshima University, Hiroshima, Japan - tsuru@hiroshima-u.ac.jp<br />

K. Yada, Hiroshima University, Hiroshima, Japan<br />

M. Kanezashi, Hiroshima University, Hiroshima, Japan<br />

Inorganic membranes are promising for possible application to high temperature<br />

separation systems and membrane reactor systems [1-3]. Metal membranes,<br />

which shows 100% selectivity to hydrogen and high permeances at<br />

temperatures, have several disadvantages such as expensive cost, degradation<br />

with hydrocarbon and acid gases, and hydrogen brittleness at low temperatures.<br />

On the other hand, amorphous silica, which can be derived from the sol-gel<br />

processing or CVD (Chemical vapor deposition), is a microporous material,<br />

consisting of silica network which allows the permeation of small molecules such<br />

as helium and hydrogen. In this paper, recent progress in the control and design<br />

of silica network by sol-gel processing will be discussed to develop highly<br />

permeable hydrogen separation membranes.<br />

The sol-gel process is divided into two main routes: the polymeric sol-gel route<br />

and the colloidal sol-gel route1). In the colloidal sol route where the hydrolysis<br />

and condensation reaction of alkoxide (tetraethoxysilane (TEOS) for SiO2<br />

membranes) is fast, the rapid condensation reaction causes particulate growth<br />

and/or the formation of precipitates. In the polymeric sol route, the hydrolysis<br />

reaction is slower, resulting in a partially hydrolyzed alkoxide and the formation of<br />

a linear inorganic polymer. Pore sizes can be controlled by the void spaces<br />

among the packed colloidal particles (i. e. interparticle pore) in the colloidal sol<br />

route and by the size of the gel network in the polymeric gel route, respectively.<br />

By controlling the preparation condition of silica sols (pH, temperature,<br />

concentration, aging time etc.), pore sizes of SiO2 membranes were found to be<br />

precisely tuned in the subnanometer range. SiO2 membranes showing highly<br />

hydrogen selectivity over nitrogen [3], as well as showing a large H2 permeation<br />

rate with low H2/N2 but high H2/SF6 separation factors, were successfully<br />

prepared [1].<br />

Another strategy to control silica network is the utilization of structured alkoxides,<br />

such as (EtO)3-Si-(CH2)n-Si-(OEt)3 (n=1-6). Since the silicone atoms are more<br />

distant with each other than the case of TEOS, due to the existence of -C2H4-,<br />

the silica network can be expected to be formed more loosely than the case of<br />

TEOS. Silica membranes prepared from bis(triethoxysilil)ethane (BTESE, n=2)

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