By Eugene F. Douglass, MS, PhD Department of Chemistry Nazarbayev University, Astana, Kazakhstan &
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Transcript of By Eugene F. Douglass, MS, PhD Department of Chemistry Nazarbayev University, Astana, Kazakhstan &
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Development and characterization of compatible cellulose blend membranes using cellulose and other natural biopolymers using a novel solvent
systemBy
Eugene F. Douglass, MS, PhDDepartment of Chemistry
Nazarbayev University, Astana, Kazakhstan&
Richard Kotek, PhDTECS, College of Textiles
North Carolina State University, Raleigh, NC USA
June 28, 2010
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Objectives - Reviewing briefly the literature, and previous
work with this system. To summarize the recent work developing new fibers and membranes using our novel solvent system.
To show the development of biopolymer blend cellulose membranes, using previous work as a foundation.
To show the characterization of the membranes. To extend the preliminary goals of the research
into a new creative area, developing brand new materials that may have use in the membrane industry, and to characterize these new materials.
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Presented by
1 - Introduction
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Layer of material which serves as a selective barrier Barrier is between two or more phases Remains impermeable to specific particles, molecules or
substances Osmotic forces enable free flow of solvents Some components are allowed passage into permeate
stream Others are retained and remain in the retentate stream
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Cellulosic sources Cellulose most abundant naturally occurring
polymeric raw material – very cheap raw material Wood pulp, cotton, other plant fibers, or plant
waste
Figure 1- Molecular structure of cellulose.11
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ExamplesCellulosic fibers and membranes Natural cellulose fibers: cotton, linen, & flax Regenerated cellulose: rayon fiber and film, cellophane film Cellulose dissolved in a solvent: Lyocell fiber and film Cellulose derivatives: nitrocellulose, celluloid, cellulose acetate fibers and
films
Early solution methods – Regenerated cellulose: Cellulose xanthate is made, dissolved, then regenerate the cellulose chemically.
Viscose process Rayon Problems: dangerous solvent, toxicity of waste material
Recent solution methods – Dissolve cellulose in a solvent system Lyocell process – prime commercial process
Lyocell Problems: solvent instability issues, expensive
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Amine and counter ion dissolution
Zn+2 > Li+ > Ca+2 > Mg+2 > Ba+2 > Na+ > NH4+ > K+
SCN- > I- > PO4-3 > Br- > Cl- > NO3
- > SO4-2 > ClO3
-
Order of decreasing swelling of cellulose 2
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Figure 2 – Swollen cellulose – crystal structure
A) ac sin γ projection; B) ab projection 2
Amine and metal salt association Ionic interactions assisting dissolution
+< 20mol%
> 20mol%SCNK
+
NH2CH2CH2NH2
dissociation
association
EDA=
cell-OH
dissolutioncell-OH= cellulose
K+ SCN
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Figure 3 – Coordination of ED and KSCN in solution9 Frey
Presented by
2 - Development of cellulose blend membranes
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Previous work at North Carolina State UniversityHyun Lee12 – developed cellulose fibers from this optimized
solvent blend, and did some basic membrane investigation Possible porous membrane Severe yellowing upon aging
Problems: could not reproduce this structure using means described Used non-reproducible method of casting
Used tape layers on glass rods Draw down on glass plate, hard to remove
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Figure 4 – Porous cellulose membrane12
Development of new casting process for reproducibility
Reproducibility is required Casting table Uniform casting bar Cast on PET plastic film for ease of placing in coagulation
bath and removal of coagulated membranes Obtained casting table and bars from Byk-
Gardner Obtained casting PET film and drawdown panels
for sample membranes
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Objective: Dissolution of cellulose and other biopolymers (DP 450)
Simple setup for dissolution, paddle stirrer apparatus
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Figure 5 - 7% free flowing ED/KSCN cellulose (DP = 450) solution
Figure 6 – Dissolution apparatus
Microscopic views of dissolution
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Table 1 - Different swelling and dissolution mechanisms for cotton and wood fibers in NMMO – water mixtures at various water contents.3
Background of invention of new material
Cellulose and starch are polysaccharides Bond linkage of glucose units different Solvent for cellulose works, perhaps would work for starch. Discussion with Drs. Kotek, Venditti, and Pawlak: Can
starch make a membrane with this solvent system? No, could we do a blend??
Motivation Attempt blend with starch for membranes; success! Based on success with starch; chitosan, chitin and soy
protein were also tried. Both porous and nonporous membranes were obtained, this
section describes the development of cellulose blended with starch to form a useful membrane.
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Table 2 -Types of starches used – all are blends
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Starch Amylose (%) Amylopectin (%)
Corn Starch ~26 ~74High Amylose starch >50 <50Waxy Maize Starch <5% >95%
Figure 7 - Amylose Figure 8 - Amylopectin
Presented by
3 - Characterization of porous cellulose blend membranes with
Starch
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SEM characterization of blend membranescellulose and corn starch
Cross sections of 50/50 cellulose and corn starch blend
membranes
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Figure 9 – 500x cellulose / corn starch blend membrane
Figure 10 – 5000x cellulose / corn starch blend membrane
Cross-sections of 50/50 cellulose and high amylose starch blend membranes
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Figure 11 – 500x cellulose / high amylose starch blend membrane
Figure 12 – 5000x cellulose / high amylose starch blend membrane
Cellulose and high amylose starchIncompatible
Cellulose and waxy maize starch
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Figure 13 – 500x cellulose / waxy maize starch blend membrane
Figure 14 – 5000x cellulose / waxy maize starch blend membrane
Cross-sections of 50/50 cellulose and waxy maize starch blend membranes
1000 nm pore size
Compatible!
TGA analysis of cellulose membrane and 50/50 cellulose / waxy maize starch membrane
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Figure 15 - Cellulose membrane: onset 332º C, end 371º C, ash
level about 28% Figure 16: Cellulose / wm starch blend membrane: onset 272º C, end 324º C, ash level about 20%
100
3030
100
Mass %
20o C
20o C 710o C
710o C
Wide Angle X-ray Scattering of blend membranesCellulose II structure Amorphous
structure Peaks at 16,17 and 23 2θ Broad peak at 20-22 2θ
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Cellulose / Waxy Maize Starch membrane
Figure 17 – cellulose membrane Figure 18 – cellulose / waxy maize starch membrane
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Table 3 - Tensile property comparison of cellulose and cellulose blend membranes
AuthorsTensile modulus
(kgf/mm2)
Failure stress
(kgf/mm2)
Failure strain
(%)
Khare2 NMMO 163.1 ± 61 6.62 ± 1.9 6.5 ± 1.5
Douglass nonporous cellulose 166.5 ± 16 5.36 ± 0.7 26.2 ± 10.1
Douglass porous cellulose 33.0 ± 9.3 0.59 ± 0.17 3.9 ± 1.4
Cellulose – wm starch blend 51.0 ± 15.2 1.06 ± 0.4 10.0 ± 5.3
Presented by
4 - Cellulose and proteins blended in solution to make
membranes
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Development of cellulose / soy protein blend membranes
Based on success with Starches, we thought protein might work First attempt with Brim Soy Protein isolate, received from USDA labs on
NCSU campus Two protein types in the Brim blend Dissolves well in solvent blend
ADM soy materials received from NC Soy Council SAF soy protein Archon F soy protein concentrate Profam 974 soy protein isolate (comparable to Brim)
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Sample blend membranes made from each protein, to determine best quality membranes. Brim and Profam 974 made best quality
membranes These were used for main
characterization Determine ideal mass ratios of Soy protein
to cellulose using Profam 974 at 40, 30 and 20% by characterization of each mass percent membrane.
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5 – Characterization of cellulose / soy protein blend membranes
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SEM cross section micrographs of 50/50 cellulose – soy protein blends – Compatible!
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Figure 19 – 50/50 Cellulose/brim membrane, 5000x
Figure 20 – 50/50 Cellulose/Profam 974
membrane, 5000x
TGA Analysis - cellulose membrane compared to cellulose/brim soy protein blend
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Figure 21 - Cellulose membrane: Onset 332º C, end
371º C, ash about 28% Figure 22 - Cellulose / brim blend membrane: Onset 241º C, end
342º C, ash about 28%
Mass %
20o C
20o C
710o C
710o C
100 100
30 30
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Figure 23 - Cellulose membrane: Onset 332º C, end 371º C, ash
level about 28%Figure 24 - Cellulose / Profam 974 blend membrane: Onset 284º C, end 344º C, ash level
about 9%
Mass %
20o C
20o C 710o C
710o C
100 100
30 30
TGA Analysis - cellulose membrane compared to cellulose/Profam 974 soy protein blend
Table 4 - Summary of TGA results for soy protein / cellulose blend membranes
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Table 8 - Comparison of TGA results between membranesMaterials Start temperature (ºC)
Onset temperature(s) (ºC)
Char level @ 710º C (%)
Cellulose fiber 242 350 11Cellulose
membrane 257 332 28Profam 974 189 276 27
Brim soy protein 193, 285 235, 310 25
Cellulose / Profam 974
mixed185 290, 362 18
Cellulose / Profam 974 membrane
200 283 9
Cellulose / brim mixed 201, 280 234, 355 19Cellulose /
brim membrane
178 241 28
Wide Angle X-ray Scattering of Profam 974 blend membraneCellulose II Structure Amorphous Structure Peaks at 16,17 and 23 2θ Broad Peak at 20-22 2θ
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Figure 25 – Cellulose membrane Figure 26 – Cellulose / Profam 974 membrane
Wide Angle X-ray Scattering of Stretched Soy Protein blend membranes Amorphous Structure Amorphous Structure
Peaks at around 14 and 21 2θ Around 14 and 21 2θ
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Figure 27 – Cellulose / Brim blend
Figure 28 – Cellulose / Profam 974 blend
Notice Notice
Tensile Properties Summary
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Table 5 – Comparison of Tensile properties for soy blend membranesSamples Tensile modulus
(kgf/mm2)Failure stress
(kgf/mm2)Failure strain
(%)Thickness
(mm)
Cellulose membrane 75 ± 12 2.5 ± 1.2 36 ± 12 0.047 ± 0.015
Cellulose / brim
membrane157 ± 52 3.2 ± 1.6 27 ± 12 0.029 ± 0.003
Cellulose / Profam 974 membrane
200 ± 75 4.7 ± 1.2 16 ± 8.0 0.026 ± 0.001
Cell / PF 40% 220 ± 53 5.0 ± 2.0 29 ± 12 0.026 ± 0.001
Cell / PF 30% 204 ± 74 4.3 ± 2.3 27 ± 12 0.031 ± 0.005
Cell / PF 20% 195 ± 69 2.4 ± 1.8 20 ± 12 0.034 ± 0.003
Presented by
6 – Later work at NCSU
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• Made blend fibers from cellulose / waxy maize, and cellulose / soy protein blends.
• Cross-linked cellulose and cellulose blend membranes to prevent falling apart in long term water contact.
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Presented by
7 – Coming work at Nazarbayev University
Brief Discussion
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ConclusionsNew dissolution process development: Using a special solvent system of ED/KSCN in a
65/35 mass % ratio, functional porous and non-porous membranes were produced that have comparable physical properties to other methods of making cellulose membranes.
New material development: Using the same solvent system, starch was
blended with cellulose in the solution and cast to make functional porous blend membranes, that are stronger than the cellulose porous membranes developed earlier, and very water absorbent.
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Conclusions Using the same solvent system, soy protein was
blended with cellulose to make functional non-porous blend membranes, that are strong and even more water absorbent than the blend membrane with starch.
The casting and drying processes were optimized to deal with issues of shrinkage that causes wrinkling and variable film thicknesses
Other polysaccharides (chitosan and chitin), and protein (keratin from hair) were also used to make functional blend membranes with cellulose, suggesting further applications for this system.
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Presented by
8 - References
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1. Ott . Cellulose and cellulose derivatives : Molecular characterization and its application. Burlington: Elsevier; 1954.
2. Khare VP, Greenberg AR, Kelley SS, Pilath H, Roh IJ, Tyber J. Synthesis and characterization of dense and porous cellulose films. J Appl Polym Sci 2007;105(3):1228-36.
3. Cuissinat C, Navard P. Swelling and dissolution of cellulose part 1: Free floating cotton and wood fibres in N-methylmorpholine-N-oxide-water mixtures. Macromolecular Symposia 2006;244(1):1.
4. Cuissinat C, Navard P. Swelling and dissolution of cellulose part II: Free floating cotton and wood fibres in NaOH-water-additives systems. Macromolecular Symposia 2006;244(1):19.
5. Fink H, Weigel P, Purz HJ, Ganster J. Structure formation of regenerated cellulose materials from NMMO-solutions. Progress in Polymer Science 2001 11;26(9):1473-524.
6. Swatloski RP, Spear SK, Holbrey JD, Rogers RD. Dissolution of cellulose with ionic liquids. J Am Chem Soc 2002;124(18):4974-5.
7. Zhang . 1-allyl-3-methylimidazolium chloride room temperature ionic liquid: A new and powerful non-derivatizing solvent for cellulose. Macromolecules 2005;38(20):8272.
8. Hafez MM, Pauls HW, inventors. Method for preparing thin regenerated cellulose membranes of high flux and selectivity for organic liquids separations. Exxon Research and Engineering Co., editor. 4496456. 1985 1/29/1985
9. Frey M, Li L, Xiao M, Gould T. Dissolution of cellulose in ethylene diamine/salt solvent systems. Cellulose 2006 04/29;13(2):147-55.
10. Cao Y. Preparation and properties of microporous cellulose membranes from novel cellulose/aqueous sodium hydroxide solutions. Journal of Applied Polymer Science [Internet]. [revised 2006;102(1):920.
11. Metzger J. Carbohydrate structures http://chemistry.gcsu.edu/~metzker/Common/Structures/Carbohydrates/
12. Lee HJ. Novel cellulose solvent system and dry jet wet spinning of Cellulose/ED/KSCN solutions. Raleigh, NC: North Carolina State University; 2007. Available from: unrestricted
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9- Acknowledgements North Carolina State University, College of Textiles
including Drs. Richard Kotek, Peter Hauser and Alan Tonelli Dr. Richard Venditti and Dr. Joel Pawlak, College of
Natural Resources Chuck Mooney, Birgit Anderson and Theresa White
Nazarbayev University, Astana, Kazakhstan seed funding to disseminate this work, and develop further work Drs. Kenneth Alibek SST, Sergey Mikhalovsky College of
Engineering
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