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Synthesis of cost-effective polymeric membrane by phase-inversion
method and effect of sonication mode, coagulation time and cross-
linking time on its swelling.
Abstract: The preparation of cost-effective polymeric membrane with better tensile strength and
increased permeation flux is done via phase-inversion method using ethanol as coagulant by
adding 1 gm. NaCl and the effect of cross-linking with (continuous and pulse) and without
sonication, coagulation time and cross-linking time on the membrane swelling is done at a fixed
concentration of cross-linking agent,0.5% glutaraldehyde in Cross-linking solution. The Swelling
Test is performed by dipping the membrane in milli-pore water for different tome periods. 1 hr, 6
hrs, 12 hrs, 24 hrs, 48 hrs and 72 hrs. respectively. The result shows that the membrane swelling
is least when the cross-linking is done via continuous mode and is observed highest when done
without sonication, due to better penetration of the cross-linking solution with in the membrane
by transmission of continuous sound waves through sonifier, resulting in lesser swelling due to
better interaction of the membrane with cross-linking agent in continuous mode where as in
pulse(degas) mode the membrane interacts with the cross-linking solution in discontinuity
resulting in comparatively lesser penetration of the CLA in membrane. As a result PVA
Membrane Swelling depending upon the mode of cross-linking follows the order: Continuous
mode < Degas mode < Without Sonication which shows the advantage of using sonifier for
cross-linking and its specific (Continuous) mode. The swelling further increases with increase in
coagulation time for a given cross-linking time due to increase in phase-inversion time PVA
concentration at the membrane surface increases and so does the hydrophilicity of the PVA
Membrane at the surface which leads to more water absorption and thus increased swelling.
Introduction: The PVA Membrane 12% by weight alone lacks mechanical strength and breaks
easily upon slight load or expansion due to its lesser tensile strength. In order to enhance its
mechanical strength and castability 1 gm NaCl is mixed with 11gm PVA which further increases
the permeation flux of the polymeric membrane without decreasing the rejection property of the
membrane. Beyond 1% permeation flux increases but rejection property of the membrane also
starts decreasing simultaneously. NaCl modified PVA Membrane has a slightly lower swelling
and a little smaller contact angle of water than the KCl modified PVA Membrane when the mass
fraction of salts is the same. Polyvinyl alcohol (PVA) polymer seems attractive for the
preparation of membranes because of its high hydrophilicity and good film forming properties. It
is little affected by greases, hydrocarbons and is chemically stable against organic solvents. But
because of its higher solubility and intensive swelling in water, the modification of PVA is
necessary for industrial application. Heat-treatment, cross-linking, acetalization, blend etc are the
usual methods of modification. Glutaraldehyde, a linear 5-Carbon dialdehyde is the most suitable
cross-linking agent because of its commercial availability and low cost in addition to its high
reactivity and is more efficient than other aldehydes in generating thermally and chemically
stable crosslinks.
Literature-Review:
AL Ahmad, NM Yusuf, BS Ooi, 2011, studied the effect of adding glutardehyde as cross-
linking agent on the pore size distribution of the membrane and concluded that the pore size of
the membrane decreases with increasing cross-linking time. The sonication has been done
immediately after the preparation of 12% PVA solution before casting for the removal of trapped
bubbles. He further concluded that cross-linking decreases the hydrophilicity of the membrane
which is confirmed by the increase in contact angle of water for the prepared membrane and pure
water permeation flux is believed to have direct relationship with the permeation flux. Thus
Glutaraldehyde cross-linked PVA membrane are suitable for ultrafiltration for particle size
greater than 100nm.
Zhang Qrxiu and Qiu Yunren, 2003 studied the effect of adding alkali metal chloride on the
properties of modified PVA-CA blend ultrafiltration membrane prepared by the phase- inversion
method and concluded that on increasing the mass fraction of alkali metal salt in the PVA
solution till 1% the permeation flux of the membrane increases much more than that of
unmodified PVA-CA membrane without affecting the rejection property of the membrane but
when the mass fraction of salt is greater than 1.5%, the permeation flux increases much more
than that of unmodified PVA-CA membrane but the rejection property of the membrane also
decreases which is undesirable for the membrane Also with the increase of mass fraction of salt,
the contact-angle decreases and the swelling increases.
Further the NaCl modified PVA-CA membrane has slightly lower swelling than KCl modified
membrane when the mass fraction of alkali metal salt (NaCl/KCl) is same in PVA solution.
Experimental set-up and procedure:
Reagent: PVA with a degree of polymerization >98%, sodium chloride, absolute ethanol (
minimum 99.9%), Glutaraldehyde aqueous solution (50% by weight), dry Sodium Sulfate, conc.
Sulfuric Acid 98% are all of analytically pure grade.
Procedure: PVA Membrane Synthesis: 11 gm PVA and 1 gm NaCl is mixed with 88 ml milli-
pore water using a magnetic stirrer at 90 degree Celsius at 500 RPM for 2.5 hrs. It is then casted
on a glass plate using a casting knife to maintain a uniform thickness. The glass plate is then
immediately put under the tray filled with ethanol for the desired coagulation time which is
varied as 0.5 hr, 1 hr, 1.5 hrs, 2 hrs. The membrane is then put out of the coagulant and is left for
drying at room temperature for 12 hrs. The membrane is then cut into the shape of petri-dish and
is then put into the cross linking solution of the following composition, glutaraldehyde 0.5%,dry
sodium sulfate- 45 gms (to prevent the membrane getting soluble in water), conc. Sulfuric Acid
98% strength(0.5% in cross linking solution), milli-pore water 1000 ml. It is then cross-linked
via sonifier using both the modes continuous, pulse(degas) and without sonication by dipping
simply in a tray filled with cross-linking solution for different coagulation time 0.5 hr, 1 hr, 1.5
hr. & 2 hrs. It is then put out of cross-linking solution and put out on the glass plate till it gets
dried.
Swelling Test : 6 circular membranes of radius 1cm is cut from the dried cross-linked PVA
membrane and is dipped into milli-pore water for the following time-period (in hrs) respectively
1,6,12,24,48 & 72. The membrane is then weighed on a high precision electronic weighing
balance. The weight of the swollen Membrane (W s) is noted down. Swelling Degree is
calculated by dividing the weight of water absorbed by the original weight of the membrane (W
o) multiplied by 100.
% S.D. = [(W s- W o) / W o] *100
Results and Discussions: The graph between % swelling degree and swelling time(hrs) is
plotted for different coagulation and cross-linking time with various modes of cross-linking:
 Degas (pulse) mode
 Continuous mode
 No Sonication ( in bath) cross-linking
0.5 hr. Cross-link, 0.5 hr. Coagulation:
Swelling Time
% S.D.
Degas Continuous No Sonication
1 56.680 52.542 63.843
6 60.956 59.903 62.756
12 62.550 54.790 65.456
24 51.082 50,000 58.541
48 67.939 57.639 68.542
72 67.299 57.005 69.013
0
10
20
30
40
50
60
70
80
0 20 40 60 80
%S.D.
S.T.(hrs)
0.5hrcrosslink,0.5 hr. coagulation
Degas
Continuous
No Sonication
0.5 hr. crosslink, 1 hr. coagulation:
Swelling
Time(hrs) Degas Continuous No Sonication
1 68.421 54.642 70.431
6 61.29 44.156 65.239
12 66.842 62.974 68.417
24 54.315 61.173 65.418
48 58.723 67.638 67.697
72 68.966 63.393 71.734
0
10
20
30
40
50
60
70
80
0 20 40 60 80
%S.D.
S.T.(hrs)
0.5 hr. crosslink,1 hr. coagulation
Degas
Continuous
No Sonication
0.5 hr. crosslink, 1.5 hr. coagulation:
ST (hrs) Degas Cont. NS
1 69.423 56.473 71.432
6 66.487 52.418 69.173
12 66.932 57.134 66.834
24 60.487 51.278 63.132
48 59.483 50.132 62.139
72 70.127 57.183 73.127
0
10
20
30
40
50
60
70
80
0 20 40 60 80
%S.D.
S.T.(hrs)
0.5 hr crosslink, 1.5 hr. coagulation
Degas
Continuous
No Sonication
0.5 hr. crosslink, 2 hrs. coagulation:
S.T.(hrs) degas cont NS
1 68.123 52.135 70.132
6 67.943 54.193 65.431
12 68.327 58.163 69.437
24 63.126 54.324 72.136
48 60.132 51.394 66.147
72 73.143 58.432 74.351
0
10
20
30
40
50
60
70
80
0 20 40 60 80
%S.D.
S.T.(hrs)
0.5 hr. crosslink, 2 hr.coagulation
Degas
Continuous
No Sonication
1 hr. cross-link, 0.5 hr. coagulation:
0
5
10
15
20
25
30
35
40
45
50
0 20 40 60 80
%S.D.
S.T.(hrs)
1 hr. cross-link, 0.5 hr. coagulation
Degas
Continuous
No Sonication
S.T.(HRS) Degas Cont NS
1 46.147 21.417 43.451
6 43.132 29.132 46.421
12 39.134 36.432 44.342
24 38.132 33.132 41.367
48 44.576 31.432 43.321
72 25.326 21.438 39.453
1 hr. crosslink, 1 hr. coagulation:
0
10
20
30
40
50
60
0 20 40 60 80
%S.D.
S.T.(hrs)
1 hr. crosslink, 1 hr. coagulation
Degas
Continuous
No Sonication
Swelling
Time Degas Continuous
No
Sonication
1 43.076 23.118 49.035
6 30.844 20.957 36.432
12 26.102 19.171 32.564
24 31.522 22.9 33.651
48 28.417 23.57 29.954
72 26.897 22.716 41.043
1 hr. cross-link, 1.5 hr. coagulation:
0
10
20
30
40
50
60
0 20 40 60 80
%S.D.
S.T.(hrs)
1 hr. crosslink, 1.5 hr. coagulation
Degas
Continuous
No Sonication
Swelling
time(hrs) Degas Continuous
No
Sonication
1 47.703 26.443 51.094
6 39.016 33.188 43.541
12 31.164 32.075 35.076
24 25.978 33.739 35.762
48 35.86 29.434 39.834
72 36.88 35.354 43.652
1 hr. crosslink, 2 hr. coagulation:
S.T.(hrs) Degas Continuous
No
Sonication
1 46.69 28.459 53.452
6 29.186 27.873 45.432
12 16.23 32.458 36.683
24 48.648 23.243 48.742
48 47.51 35.452 50.541
72 45.16 39.432 52.659
0
10
20
30
40
50
60
0 20 40 60 80
%S.D.
S.T.(hrs)
1 hr. crosslink, 2 hr. coagulation
Degas
Continuous
No Sonication
1.5 hr. crosslink, 0.5 hr. coagulation:
S.T.(hrs) Degas Cont N.S.
1 40.132 31.37 45.312
6 39.136 29.437 47.132
12 43.129 33.432 46.146
24 39.438 31.637 41.489
48 42.326 29.426 39.132
72 36.432 28.126 48.174
0
10
20
30
40
50
60
0 20 40 60 80
%S.D.
S.T.(hrs)
1.5 hr. crosslink, 0.5 hr. coagulation
Degas
Continuous
No Sonication
1.5 hr. crosslink, 1 hr. coagulation:
0
10
20
30
40
50
60
0 20 40 60 80
%S.D.
S.T.(hrs)
1.5 hr. crosslink, 1 hour coagulation
Degas
Continuous
No Sonication
S.T.(hrs) Degas Continuous
No
Sonication
1 41.241 35.234 45.437
6 45 32.986 47.862
12 41.52 29.468 45.452
24 44.6 31.469 46.751
48 37.176 34.92 43.543
72 40.23 35.862 46.783
1.5 hr. crosslink, 1.5 hr. coagulation:
S.T.(hrs) Degas Continuous
No
Sonication
1 47.436 46.67 49.873
6 43.724 43.345 48.571
12 52.268 43.137 57.652
24 46.751 45.896 48.648
48 31.52 38.053 45.649
72 42.43 43.23 49.835
0
10
20
30
40
50
60
70
0 20 40 60 80
%SD
S.T.(hrs)
1.5 hr. crosslink, 1.5 hr.coagulation
Degas
Continuous
No Sonication
1.5 hr. crosslink, 2 hr. coagulation:
S.T.(hrs) Degas Continuous
No
Sonication
1 48.437 47.239 50.367
6 43.28 49.405 49.843
12 46.703 50.47 53.453
24 45.316 44.811 51.432
48 39.294 49.841 45.342
72 46.25 43.472 50.432
0
10
20
30
40
50
60
0 20 40 60 80
%S.D.
S.T.(hrs)
1.5 hr. crosslinking,2hr.coagulation
Degas
Continuous
No Sonication
As is clear from the graph, the continuous mode gives the least swelling after 72 hours of
swelling test while the highest swelling is observed when the cross linking is done without
sonication due to better interaction of the cross linking agent (0.5% glutaraldehyde) with the
membrane via continuous transmission of ultra-sonic vibrations in continuous mode and better
removal of air bubbles in cross-linking solution whereas in pulse(degas) mode the extent of
penetration and interaction of the cross-linking agent and the membrane comparatively reduces
due to irregularities in transmission of ultrasonic vibrations in the form of pulse. Moreover for a
given cross-linking time, the swelling degree increases with increase of coagulation time, as the
time required for phase inversion in coagulation bath increases resulting in enhanced PVA
concentration and reduced water concentration at the PVA- Ethanol interfacial surface which
results in the increased hydrophilicity of the PVA membrane at the surface facing coagulant
(ethanol). The other part of the PVA membrane with dense water concentration after
coagulation supported on glass plate is rendered less hydrophilic after getting cross-linked, thus
only the part of the membrane facing ethanol decides the trend of variation of % swelling degree
which increases with increase of coagulation time giving rise to more absorption of water and
hence greater swelling for a given cross-linking time.
CONCLUSION:
 For the same coagulation & cross-linking time, cross-linking by contiuous sonicaton
mode gives lesser swelling than the degas mode followed by No sonication(in bath cross-
linking) for same concentration of cross-linking agent; due to better penetration of the
cross-linking solution with in the membrane by transmission of continuous ultrasonic
waves through sonifier, resulting in lesser swelling due to better interaction of the
membrane with cross-linking agent, where as in pulse(degas) mode the membrane
interacts with the cross-linking solution in discontinuity resulting in comparatively lesser
penetration of the Cross-linking agent in membrane. As a result PVA Membrane
Swelling follows the order depending upon the mode of cross-linking : Continuous
mode < Degas mode < Without Sonication
 .% Swelling Degree. increases with increase of coagulation time irrespective of the
mode of crosslinking (degas, continuous or No sonication) mode for a given cross
linking time as follows: 0.5 hr. coagulation< 1 hr. coagulation< 1.5 hr.
coagulation< 2 hr. coagulation. as the time required for phase inversion in
coagulation bath increases resulting in enhanced PVA concentration and reduced
water concentration at the surface which results in the increased hydrophilicity of the
PVA membrane on its surface because of the hydrophilic nature of PVA giving rise
to more absorption of water for a given time period and thus greater swelling.
 For a given coagulation time, 1 hr. cross-linking gives the least swelling. The
swelling degree follows the order: 1 hr. crosslink < 1.5 hr. crosslink< 0.5 hr.
crosslink irrespective of the mode of sonication for a given coagulation time.
REFERENCE:
[1] S.-G. Kim, K.-H. Lee, Poly(vinyl alcohol) membranes having an integrally skinned
asymmetric structure, Mol. Cryst. Liquid Cryst. 512 (2009) 32–39.
[2] Y. Zhang, H. Li, H. Li, R. Li, C. Xiao, Preparation and characterization of modified
polyvinyl alcohol ultrafiltration membranes, Desalination 192 (2006) 214–223.
[3] M. Krumova, D. López, R. Benavente, C. Mijangos, J.M. Pereña, Effect of
crosslinking on the mechanical and thermal properties of poly(vinyl alcohol), Polymer 41
(2000)9265–9272.
[4] R. Ji-Won, Y. Choong-Kyun, K. Sun-Woo, Modification of poly(vinyl alcohol)
membranes using sulfur-succinic acid and its application to pervaporation separation of
water-alcohol mixtures, J. Appl. Polym. Sci. 68 (1998) 1717–1723.
[5] L.K. Pandey, C. Saxena, V. Dubey, Modification of poly(vinyl alcohol) membranes
for pervaporative separation of benzene/cyclohexane mixtures, J. Membr. Sci. 227
(2003)173–182.
[6] W.Y. Chuang, T.H. Young, W.Y. Chiu, C.Y. Lin, The effect of polymeric additives
on the structure and permeability of poly(vinyl alcohol) asymmetric membranes,
Polymer41(2000)5633–5641.
[7] B. Han, J. Li, C. Chen, C. Xu, S.R. Wickramasinghe, Effects of degree of
formaldehyde acetal treatment and maleic acid crosslinking on solubility and diffusivity
of water in PVA membranes, Chem. Eng. Res. Des. 81 (2003) 1385–1392.
[8] J.M. Yang, C.Y. Chiang, H.Z. Wang, C.C. Yang, Two step modification of
poly(vinyl alcohol) by UV radiation with 2-hydroxy ethyl methacrylate and sol–gel
process for the application of polymer electrolyte membrane, J. Membr. Sci. 341 (2009)
186–194.

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synthesis of poly

  • 1. Synthesis of cost-effective polymeric membrane by phase-inversion method and effect of sonication mode, coagulation time and cross- linking time on its swelling. Abstract: The preparation of cost-effective polymeric membrane with better tensile strength and increased permeation flux is done via phase-inversion method using ethanol as coagulant by adding 1 gm. NaCl and the effect of cross-linking with (continuous and pulse) and without sonication, coagulation time and cross-linking time on the membrane swelling is done at a fixed concentration of cross-linking agent,0.5% glutaraldehyde in Cross-linking solution. The Swelling Test is performed by dipping the membrane in milli-pore water for different tome periods. 1 hr, 6 hrs, 12 hrs, 24 hrs, 48 hrs and 72 hrs. respectively. The result shows that the membrane swelling is least when the cross-linking is done via continuous mode and is observed highest when done without sonication, due to better penetration of the cross-linking solution with in the membrane by transmission of continuous sound waves through sonifier, resulting in lesser swelling due to better interaction of the membrane with cross-linking agent in continuous mode where as in pulse(degas) mode the membrane interacts with the cross-linking solution in discontinuity resulting in comparatively lesser penetration of the CLA in membrane. As a result PVA Membrane Swelling depending upon the mode of cross-linking follows the order: Continuous mode < Degas mode < Without Sonication which shows the advantage of using sonifier for cross-linking and its specific (Continuous) mode. The swelling further increases with increase in coagulation time for a given cross-linking time due to increase in phase-inversion time PVA concentration at the membrane surface increases and so does the hydrophilicity of the PVA Membrane at the surface which leads to more water absorption and thus increased swelling.
  • 2. Introduction: The PVA Membrane 12% by weight alone lacks mechanical strength and breaks easily upon slight load or expansion due to its lesser tensile strength. In order to enhance its mechanical strength and castability 1 gm NaCl is mixed with 11gm PVA which further increases the permeation flux of the polymeric membrane without decreasing the rejection property of the membrane. Beyond 1% permeation flux increases but rejection property of the membrane also starts decreasing simultaneously. NaCl modified PVA Membrane has a slightly lower swelling and a little smaller contact angle of water than the KCl modified PVA Membrane when the mass fraction of salts is the same. Polyvinyl alcohol (PVA) polymer seems attractive for the preparation of membranes because of its high hydrophilicity and good film forming properties. It is little affected by greases, hydrocarbons and is chemically stable against organic solvents. But because of its higher solubility and intensive swelling in water, the modification of PVA is necessary for industrial application. Heat-treatment, cross-linking, acetalization, blend etc are the usual methods of modification. Glutaraldehyde, a linear 5-Carbon dialdehyde is the most suitable cross-linking agent because of its commercial availability and low cost in addition to its high reactivity and is more efficient than other aldehydes in generating thermally and chemically stable crosslinks. Literature-Review: AL Ahmad, NM Yusuf, BS Ooi, 2011, studied the effect of adding glutardehyde as cross- linking agent on the pore size distribution of the membrane and concluded that the pore size of the membrane decreases with increasing cross-linking time. The sonication has been done immediately after the preparation of 12% PVA solution before casting for the removal of trapped bubbles. He further concluded that cross-linking decreases the hydrophilicity of the membrane which is confirmed by the increase in contact angle of water for the prepared membrane and pure
  • 3. water permeation flux is believed to have direct relationship with the permeation flux. Thus Glutaraldehyde cross-linked PVA membrane are suitable for ultrafiltration for particle size greater than 100nm. Zhang Qrxiu and Qiu Yunren, 2003 studied the effect of adding alkali metal chloride on the properties of modified PVA-CA blend ultrafiltration membrane prepared by the phase- inversion method and concluded that on increasing the mass fraction of alkali metal salt in the PVA solution till 1% the permeation flux of the membrane increases much more than that of unmodified PVA-CA membrane without affecting the rejection property of the membrane but when the mass fraction of salt is greater than 1.5%, the permeation flux increases much more than that of unmodified PVA-CA membrane but the rejection property of the membrane also decreases which is undesirable for the membrane Also with the increase of mass fraction of salt, the contact-angle decreases and the swelling increases. Further the NaCl modified PVA-CA membrane has slightly lower swelling than KCl modified membrane when the mass fraction of alkali metal salt (NaCl/KCl) is same in PVA solution. Experimental set-up and procedure: Reagent: PVA with a degree of polymerization >98%, sodium chloride, absolute ethanol ( minimum 99.9%), Glutaraldehyde aqueous solution (50% by weight), dry Sodium Sulfate, conc. Sulfuric Acid 98% are all of analytically pure grade. Procedure: PVA Membrane Synthesis: 11 gm PVA and 1 gm NaCl is mixed with 88 ml milli- pore water using a magnetic stirrer at 90 degree Celsius at 500 RPM for 2.5 hrs. It is then casted on a glass plate using a casting knife to maintain a uniform thickness. The glass plate is then immediately put under the tray filled with ethanol for the desired coagulation time which is
  • 4. varied as 0.5 hr, 1 hr, 1.5 hrs, 2 hrs. The membrane is then put out of the coagulant and is left for drying at room temperature for 12 hrs. The membrane is then cut into the shape of petri-dish and is then put into the cross linking solution of the following composition, glutaraldehyde 0.5%,dry sodium sulfate- 45 gms (to prevent the membrane getting soluble in water), conc. Sulfuric Acid 98% strength(0.5% in cross linking solution), milli-pore water 1000 ml. It is then cross-linked via sonifier using both the modes continuous, pulse(degas) and without sonication by dipping simply in a tray filled with cross-linking solution for different coagulation time 0.5 hr, 1 hr, 1.5 hr. & 2 hrs. It is then put out of cross-linking solution and put out on the glass plate till it gets dried. Swelling Test : 6 circular membranes of radius 1cm is cut from the dried cross-linked PVA membrane and is dipped into milli-pore water for the following time-period (in hrs) respectively 1,6,12,24,48 & 72. The membrane is then weighed on a high precision electronic weighing balance. The weight of the swollen Membrane (W s) is noted down. Swelling Degree is calculated by dividing the weight of water absorbed by the original weight of the membrane (W o) multiplied by 100. % S.D. = [(W s- W o) / W o] *100 Results and Discussions: The graph between % swelling degree and swelling time(hrs) is plotted for different coagulation and cross-linking time with various modes of cross-linking:  Degas (pulse) mode  Continuous mode  No Sonication ( in bath) cross-linking
  • 5. 0.5 hr. Cross-link, 0.5 hr. Coagulation: Swelling Time % S.D. Degas Continuous No Sonication 1 56.680 52.542 63.843 6 60.956 59.903 62.756 12 62.550 54.790 65.456 24 51.082 50,000 58.541 48 67.939 57.639 68.542 72 67.299 57.005 69.013 0 10 20 30 40 50 60 70 80 0 20 40 60 80 %S.D. S.T.(hrs) 0.5hrcrosslink,0.5 hr. coagulation Degas Continuous No Sonication
  • 6. 0.5 hr. crosslink, 1 hr. coagulation: Swelling Time(hrs) Degas Continuous No Sonication 1 68.421 54.642 70.431 6 61.29 44.156 65.239 12 66.842 62.974 68.417 24 54.315 61.173 65.418 48 58.723 67.638 67.697 72 68.966 63.393 71.734 0 10 20 30 40 50 60 70 80 0 20 40 60 80 %S.D. S.T.(hrs) 0.5 hr. crosslink,1 hr. coagulation Degas Continuous No Sonication
  • 7. 0.5 hr. crosslink, 1.5 hr. coagulation: ST (hrs) Degas Cont. NS 1 69.423 56.473 71.432 6 66.487 52.418 69.173 12 66.932 57.134 66.834 24 60.487 51.278 63.132 48 59.483 50.132 62.139 72 70.127 57.183 73.127 0 10 20 30 40 50 60 70 80 0 20 40 60 80 %S.D. S.T.(hrs) 0.5 hr crosslink, 1.5 hr. coagulation Degas Continuous No Sonication
  • 8. 0.5 hr. crosslink, 2 hrs. coagulation: S.T.(hrs) degas cont NS 1 68.123 52.135 70.132 6 67.943 54.193 65.431 12 68.327 58.163 69.437 24 63.126 54.324 72.136 48 60.132 51.394 66.147 72 73.143 58.432 74.351 0 10 20 30 40 50 60 70 80 0 20 40 60 80 %S.D. S.T.(hrs) 0.5 hr. crosslink, 2 hr.coagulation Degas Continuous No Sonication
  • 9. 1 hr. cross-link, 0.5 hr. coagulation: 0 5 10 15 20 25 30 35 40 45 50 0 20 40 60 80 %S.D. S.T.(hrs) 1 hr. cross-link, 0.5 hr. coagulation Degas Continuous No Sonication S.T.(HRS) Degas Cont NS 1 46.147 21.417 43.451 6 43.132 29.132 46.421 12 39.134 36.432 44.342 24 38.132 33.132 41.367 48 44.576 31.432 43.321 72 25.326 21.438 39.453
  • 10. 1 hr. crosslink, 1 hr. coagulation: 0 10 20 30 40 50 60 0 20 40 60 80 %S.D. S.T.(hrs) 1 hr. crosslink, 1 hr. coagulation Degas Continuous No Sonication Swelling Time Degas Continuous No Sonication 1 43.076 23.118 49.035 6 30.844 20.957 36.432 12 26.102 19.171 32.564 24 31.522 22.9 33.651 48 28.417 23.57 29.954 72 26.897 22.716 41.043
  • 11. 1 hr. cross-link, 1.5 hr. coagulation: 0 10 20 30 40 50 60 0 20 40 60 80 %S.D. S.T.(hrs) 1 hr. crosslink, 1.5 hr. coagulation Degas Continuous No Sonication Swelling time(hrs) Degas Continuous No Sonication 1 47.703 26.443 51.094 6 39.016 33.188 43.541 12 31.164 32.075 35.076 24 25.978 33.739 35.762 48 35.86 29.434 39.834 72 36.88 35.354 43.652
  • 12. 1 hr. crosslink, 2 hr. coagulation: S.T.(hrs) Degas Continuous No Sonication 1 46.69 28.459 53.452 6 29.186 27.873 45.432 12 16.23 32.458 36.683 24 48.648 23.243 48.742 48 47.51 35.452 50.541 72 45.16 39.432 52.659 0 10 20 30 40 50 60 0 20 40 60 80 %S.D. S.T.(hrs) 1 hr. crosslink, 2 hr. coagulation Degas Continuous No Sonication
  • 13. 1.5 hr. crosslink, 0.5 hr. coagulation: S.T.(hrs) Degas Cont N.S. 1 40.132 31.37 45.312 6 39.136 29.437 47.132 12 43.129 33.432 46.146 24 39.438 31.637 41.489 48 42.326 29.426 39.132 72 36.432 28.126 48.174 0 10 20 30 40 50 60 0 20 40 60 80 %S.D. S.T.(hrs) 1.5 hr. crosslink, 0.5 hr. coagulation Degas Continuous No Sonication
  • 14. 1.5 hr. crosslink, 1 hr. coagulation: 0 10 20 30 40 50 60 0 20 40 60 80 %S.D. S.T.(hrs) 1.5 hr. crosslink, 1 hour coagulation Degas Continuous No Sonication S.T.(hrs) Degas Continuous No Sonication 1 41.241 35.234 45.437 6 45 32.986 47.862 12 41.52 29.468 45.452 24 44.6 31.469 46.751 48 37.176 34.92 43.543 72 40.23 35.862 46.783
  • 15. 1.5 hr. crosslink, 1.5 hr. coagulation: S.T.(hrs) Degas Continuous No Sonication 1 47.436 46.67 49.873 6 43.724 43.345 48.571 12 52.268 43.137 57.652 24 46.751 45.896 48.648 48 31.52 38.053 45.649 72 42.43 43.23 49.835 0 10 20 30 40 50 60 70 0 20 40 60 80 %SD S.T.(hrs) 1.5 hr. crosslink, 1.5 hr.coagulation Degas Continuous No Sonication
  • 16. 1.5 hr. crosslink, 2 hr. coagulation: S.T.(hrs) Degas Continuous No Sonication 1 48.437 47.239 50.367 6 43.28 49.405 49.843 12 46.703 50.47 53.453 24 45.316 44.811 51.432 48 39.294 49.841 45.342 72 46.25 43.472 50.432 0 10 20 30 40 50 60 0 20 40 60 80 %S.D. S.T.(hrs) 1.5 hr. crosslinking,2hr.coagulation Degas Continuous No Sonication
  • 17. As is clear from the graph, the continuous mode gives the least swelling after 72 hours of swelling test while the highest swelling is observed when the cross linking is done without sonication due to better interaction of the cross linking agent (0.5% glutaraldehyde) with the membrane via continuous transmission of ultra-sonic vibrations in continuous mode and better removal of air bubbles in cross-linking solution whereas in pulse(degas) mode the extent of penetration and interaction of the cross-linking agent and the membrane comparatively reduces due to irregularities in transmission of ultrasonic vibrations in the form of pulse. Moreover for a given cross-linking time, the swelling degree increases with increase of coagulation time, as the time required for phase inversion in coagulation bath increases resulting in enhanced PVA concentration and reduced water concentration at the PVA- Ethanol interfacial surface which results in the increased hydrophilicity of the PVA membrane at the surface facing coagulant (ethanol). The other part of the PVA membrane with dense water concentration after coagulation supported on glass plate is rendered less hydrophilic after getting cross-linked, thus only the part of the membrane facing ethanol decides the trend of variation of % swelling degree which increases with increase of coagulation time giving rise to more absorption of water and hence greater swelling for a given cross-linking time. CONCLUSION:  For the same coagulation & cross-linking time, cross-linking by contiuous sonicaton mode gives lesser swelling than the degas mode followed by No sonication(in bath cross- linking) for same concentration of cross-linking agent; due to better penetration of the cross-linking solution with in the membrane by transmission of continuous ultrasonic waves through sonifier, resulting in lesser swelling due to better interaction of the membrane with cross-linking agent, where as in pulse(degas) mode the membrane
  • 18. interacts with the cross-linking solution in discontinuity resulting in comparatively lesser penetration of the Cross-linking agent in membrane. As a result PVA Membrane Swelling follows the order depending upon the mode of cross-linking : Continuous mode < Degas mode < Without Sonication  .% Swelling Degree. increases with increase of coagulation time irrespective of the mode of crosslinking (degas, continuous or No sonication) mode for a given cross linking time as follows: 0.5 hr. coagulation< 1 hr. coagulation< 1.5 hr. coagulation< 2 hr. coagulation. as the time required for phase inversion in coagulation bath increases resulting in enhanced PVA concentration and reduced water concentration at the surface which results in the increased hydrophilicity of the PVA membrane on its surface because of the hydrophilic nature of PVA giving rise to more absorption of water for a given time period and thus greater swelling.  For a given coagulation time, 1 hr. cross-linking gives the least swelling. The swelling degree follows the order: 1 hr. crosslink < 1.5 hr. crosslink< 0.5 hr. crosslink irrespective of the mode of sonication for a given coagulation time. REFERENCE: [1] S.-G. Kim, K.-H. Lee, Poly(vinyl alcohol) membranes having an integrally skinned asymmetric structure, Mol. Cryst. Liquid Cryst. 512 (2009) 32–39. [2] Y. Zhang, H. Li, H. Li, R. Li, C. Xiao, Preparation and characterization of modified polyvinyl alcohol ultrafiltration membranes, Desalination 192 (2006) 214–223. [3] M. Krumova, D. López, R. Benavente, C. Mijangos, J.M. Pereña, Effect of crosslinking on the mechanical and thermal properties of poly(vinyl alcohol), Polymer 41 (2000)9265–9272.
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