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JAEA-Review-2010-065.pdf:15.99MB - 日本原子力研究開発機構

JAEA-Review-2010-065.pdf:15.99MB - 日本原子力研究開発機構

JAEA-Review-2010-065.pdf:15.99MB - 日本原子力研究開発機構

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1-30<br />

Conductometric Analysis of Track Etching in<br />

Poly(vinylidene fluoride)<br />

T. Yamaki, H. Koshikawa, S. Sawada, S. Hasegawa, M. Asano and Y. Maekawa<br />

Environment and Industrial Materials Research Division, QuBS, <strong>JAEA</strong><br />

We have recently been working on ion-track membranes<br />

of poly(vinylidene fluoride) (PVDF) because they have<br />

attracted a renewed interest for their applications to fuel<br />

cells. Researchers previously employed a concentrated<br />

alkaline solution with a KMnO4 additive at high<br />

temperatures to produce visible tracks in the PVDF films.<br />

These severe conditions provided irreversible chemical<br />

damage all over the film including the non-irradiated part.<br />

On the other hand, we have attempted to prepare<br />

PVDF-based ion-track membranes efficiently without any<br />

oxidant additives 1-3) . The aim of this study is to investigate<br />

the formation of the PVDF track membranes in detail by<br />

conductometric analysis. Interestingly, instead of the<br />

oxidant agent-induced activation, high-voltage application to<br />

the conductometry cell was found to increase the etch rate,<br />

governing the pore sizes and shapes, which is indicative of<br />

4)<br />

pore development affected by the etching products .<br />

A 25 m-thick PVDF film was irradiated at room<br />

temperature with 450 MeV 129 Xe from the TIARA cyclotron.<br />

The fluence was fixed at 3 × 107 ions/cm 2 . Track etching<br />

was performed by mounting the irradiated film as a dividing<br />

wall in the conductometry cell made of Teflon containing a<br />

9 mol/dm 3 aqueous KOH solution at 80 ºC. The electrical<br />

conductance of the solution through the film, g(t), was<br />

monitored between two platinum electrodes as a function of<br />

the etching time under a sine AC voltage with a frequency<br />

of 1 kHz using an LCR meter. Assuming cylindrical pores,<br />

we calculated the effective pore diameter, deff, at any given<br />

time by<br />

deff = (4Lg(t)/KNS) 1/2 ,<br />

where L is the membrane thickness, K is the specific<br />

conductivity of the KOH etchant, N is the pore density<br />

generally corresponding to the ion fluence (corrected for the<br />

contribution of the microscopically-nonhomogeneous<br />

irradiation), and S is the area of the measured sample. The<br />

amplitude of the voltage between the electrodes was<br />

constant at either 0.3, 1.0 or 2.0 V.<br />

Figure 1 compares the conductometry results obtained at<br />

the different applied voltages. Basically, there were<br />

several characteristic regions during the course of the<br />

etching. In the beginning, the plateau at a nearly zero<br />

diameter represented the process of etchant penetration into<br />

tracks and approach of the etched cones from both sides of<br />

the film. As soon as these two approaching cones made<br />

contact with each other, the deff suddenly increased. The<br />

time associated with this contact is called the breakthrough<br />

time, TB. After the pore breakthrough, the deff increased, in<br />

other words, the pores grew in the transverse direction.<br />

Lastly, the rate of the deff increase became negligibly low,<br />

<strong>JAEA</strong>-<strong>Review</strong> <strong>2010</strong>-065<br />

- 34 -<br />

and eventually the curve reached the second plateau.<br />

Chemical etching in the unmodified area, that is, bulk<br />

etching occurred beyond the width of the latent track.<br />

As also seen in (a), a T B value is estimated to be 4.2 h at<br />

an applied voltage of 0.3 V. When the applied voltage was<br />

increased from 0.3 to 1.0 V, we did not see any significant<br />

change in the curve. When we further increased the<br />

voltage to 2.0 V, the curve exhibited a shorter T B and time<br />

taken until the d eff value started to level off, while it still<br />

showed an invariant growth rate and final d eff. In other<br />

words, the etching seemed to be accelerated at the higher<br />

voltages. Cornelius et al. 5) similarly found that the etch<br />

rate for the polycarbonate-based track membranes varied<br />

with the applied voltage. As a probable cause, they took<br />

into account the creation of dissolution products during the<br />

etching process which should attach to the pore walls and<br />

affect further etching. If the dissolved species are ionic or<br />

polar, they are possibly more efficiently pulled out of the<br />

pore due to electrophoretic migration, reducing the effect of<br />

their adsorption on the inner pore surface. That is, pore<br />

development will finally be activated by a concurrent<br />

decrease in the susceptibility of the materials to chemical<br />

attack, and this activating effect due to voltage application<br />

worked well for only the etching before the breakthrough.<br />

References<br />

1) T. Yamaki et al., Kobunshi Ronbunshu 65 (2008) 273.<br />

2) R. Rohani et al., Nucl. Instrum. Meth. Phys. Res. 267<br />

(2009) 554.<br />

3) T. Yamaki et al., GSI Sci. Rep. 2008 (2009) 350.<br />

4) N. Nuryanthi et al., Electrochemistry 78 (<strong>2010</strong>) 146.<br />

5) T.W. Cornelius et al., Nucl. Instrum. Meth. Phys. Res.<br />

265 (2007) 553.<br />

d eff (nm)<br />

200<br />

150<br />

100<br />

50<br />

0<br />

(b)<br />

(c)<br />

(a)<br />

0 5 10 15 20 25 30<br />

Etching time (h)<br />

Fig. 1 Plots of the d eff value as a function of the etching<br />

time. The voltage applied to the conductometry cell<br />

was (a) 0.3, (b) 1.0, or (c) 2.0 V.

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