http://www.chemistrymag.org/cji/2000//022010nc.htm

  Feb.25, 2000  Vol.2 No.2 P.10 Copyright Instructions(Chinese)


Effect of post-treatment on the performance of the particle-filled PAN membrane

Ge Jijun, Yin Yan, Cui Yongfang , Zhang Zhiying, Zhou Hua
(Department of Material Science, Tianjin Institute of Textile Science and Technology, Tianjin, 300160, China)

Received Dec. 15, 1999

Abstract The post-treatment process of matrix PAN/SiO2 (PAN, Polyacrylonitrile) and its influence on the membrane performance are studied. The results show that the post-treated composite increases the heat-resistance. The post-treated flat membrane maintains higher flux without decreasing the retention.
Key words Polyacrylonitrile, particle-filled membrane, dynamic viscoelastic properties, water permeability

The polyacrylonitrile membrane has long been used as flat or hollow fiber. It is also used as layers of composite membrane because of its excellent capability to resist pollution and chemical reactions. Because of the porous and low glass transition temperature in wet condition, the membrane will shrink during dewatering or heating unless they are treated with special chemical or physical method[1]. Since most of the composite processes are carried out in a dry state at a high temperature, it is impossible to use the deformed membranes as matrix. A few articles about PAN matrix and its post-treatment are reported[2-5] , but some of them deal with SiO2 reinforcement. In order to overcome the disadvantage of "the membrane densification" in making composite membrane, the membrane matrix of PAN/SiO2 and its post-treatment are studied. The result shows that post-treated PAN/SiO2 can increase the ability of heat-resistance without deformation and loss of their performance.
1 RIMENTAL
1.1 Materials
The PAN (=30,000) is obtained from Qinhuangdao Factory of acrylon. Silica (used for chromatography) is imported from Germany.
1.2 Sample preparation
An amount of PAN is dissolved in DMF to form an 18%(wt.) solution. Then SiO2 is put into the solution and the solution of PAN/SiO2 is rapidly agitated for at least 3 hours. The solution is casted on glass and coagulated in water at 25
°C to form a smooth membrane. The membranes are kept in water for use. The draw and the heat treatment of membranes are carried out in boiling water respectively.
1.3 Instrumentation
The morphology of the membrane is scanned with a Hitachi S-450 scanning electron microscope. The dynamic viscoelastic curves are measured on a Rheovibron DDV-II-EA. Water flux and retention are evaluated with ultrafilter equipment made by Tianjin Institute of Membrane Technology.
2 RESULTS AND DISCUSSIONS
2.1 Water flux and retention

    The water flux increases markedly with the increase of draw ratio, as shown in Fig. 1. The fixed length heat-treatment causes the flux to reduce to only half of that of the untreated. But after the membranes are drawn, the water flux increases with draw ratio. Provided that the draw ratio is 250%, the flux rises up to four times that of the untreated one. Simultaneously, the retentions of the drawn membranes keep almost the same as the undrawn one. For example, the post-treatment membranes are used to determine the retention of ploy (ethylene glycol)(PEG, =10,000) and the results are listed in Table 1.
Fig.1 Relationship between draw ratio and flux

Table 1 The PEG retention of post-treatment membranes

Treatment
Conditions

Untreated

Fixed length heated

Drawn 150% heated

Drawn 200% heated

Drawn 250% heated

Retention

99.0%

98.7%

98.9%

99.0%

99.1%

2.2 Morphology
The surfaces of drawn membranes are observed by scanning electron microscope, as shown in Fig.2. The shapes of the surface pores of particle-filled PAN membranes are altered from round to ellipse. Inside the pores, there are some particles, which divide one pore into two. A great many of hypopores appear on the surface. The drawn membranes have a more porous area than that of the undrawn one. But the average size of a pore does not alter remarkably. This is why the drawn membranes have higher flux and remain constant retention.

0201003.jpg (25248 bytes) Fig.2 SEM micrograph of surface of PAN/SiO2 membrane with draw ratio of 2.24

2.3 Dimension stability
The untreated membranes are noticeably warped and become brittle in dry condition. This makes the membrane unfit for use. The effects of treatment temperature and draw ratio on the dimension stability of dry membranes are shown in Table 2.
Table 2 The effects of heat treatment and draw ratio on dimension stability

Treatment
Temperature

Fixed length
heated

Drawn 150%
heated

Drawn 200%
heated

Drawn 250%
heated

30°C

Smooth, brittle

Smooth, brittle

Smooth, flexible

Smooth, good flexible

40°C

Smooth, brittle

Smooth, brittle

Smooth, flexible

Smooth, good flexible

60°C

Lightly warped, brittle

Little warped,
brittle

Smooth, flexible

Smooth, good flexible

80°C

Warped, brittle

Warped, brittle

Lightly warped, flexible

Smooth, good flexible

Fig.3 The effect of the post-treatment on the elastic modulus.
    It can be seen that the membranes become more stable and flexible with the increase of the draw ratio. In order to explain the increase of dimension stability with draw ratio, the dynamic viscoelastic experiments are carried out and the results are shown in Fig. 3.
    This indicates that the elastic module of the membrane decreases with the increase of the draw ratio below the temperature of 400K. The smaller the draw ratio is, the more quickly the elastic modules of the membrane drop with the rise of the temperature. With a draw ratio of 250 %, the modules change slightly, which means that it is not sensitive to temperature. So, the drawn membranes possess more dimension stability in higher temperature, even at 80
°C(see Table 2).
3 CONCLUSION
The dimension stability of the membrane of PAN/SiO2 in dry conditions can be greatly improved by means of drawing and heating treatment.
REFERENCES
[1] Craig R, Bartels K K, Wachtel A. J. Membr. Sci., 1987, 32: 291-321.
[2] Yang M C, Chou M T. J. Membr. Sci., 1996, 116: 279.
[3] Cui Y F, Lin D S, Zhao Y H et al. Water Proc. Tech., 1993, 13: 19-24.
[4] Watanabe K, Kyo S.  J. Chem. Eng. Jpn., 1993, 1: 17-21.
[5] Heintx W S. J. Membr. Sci., 1994, 89: 153.

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