1
www.buffalo.edu Thiol-ene Polymer Networks for Reverse Osmosis Shawreen Shah, Kaipin Huang, Norman Ng and Haiqing Lin Department of Chemical and Biological Engineering, University at Buffalo (SUNY), Buffalo, NY 14260, USA Overview Conclusion and Future Work Drawback of Current RO Membranes Approach: Thiol-Ene Based Polymer Networks Conclusion : Highly crosslinked thiol-ene polymers and thin film composite membranes based on these polymers have been successfully prepared and characterized. Future Work : Optimize composite membranes and evaluate salt rejection using a dead-end filtration system and a crossflow filtration system. Laboratory of InNovative Membranes at UB Compositi on Density (g/cm 3 ) Fractional Free Volume Water Sorption Sol-Gel Percent Withou t solven t* With solven t* Withou t solven t* With solven t* Withou t solven t* With solvent * Withou t solven t* With solve nt* T1+E1 1.2 1.2 0.16 0.16 2.4% 2.6% 1.6% 0% T1+E2 1.3 1.3 0.12 0.12 2.2% 2.3% 1.2% 0% T2+E1 1.3 1.3 0.12 0.12 2.8% 2.7% 1.6% 0% T2+E2 1.3 1.3 0.15 0.15 1.9% 2% 0.2% 0% Reverse Osmosis (RO) system (Δp > Δ) Δp = pressure difference Δ = osmotic pressure difference Salt Rejection: C 2 : salt concentration in the permeate C 1 : salt concentration in the feed Current RO membranes are subjected to chlorine oxidation, leading to higher water flux and lower salt rejection. Thiol monomers T1: T2: Ene monomers E1: E2: Objective: To design and develop thiol-ene polymer based reverse osmosis membranes and study structure/property correlation. Advantage of Thiol-Ene Polymers: Highly crosslinked and homogenous Versatile with many choices of monomers Easy to prepare and immune from oxygen inhibition Approach: Novel polymers are prepared using multifunctional thiols and enes. Polymers are characterized using FTIR-ATR, density and fractional free volume measurements, and water sorption measurements. Thin film composite membranes are prepared on commercial microporous substrates for reverse osmosis applications. Flux evaluation: Thiol-ene polymer networks are immune to oxidation, and hence chlorine is not expected to degrade the membrane. A series of thiol-ene polymers were synthesized by UV photopolymerization. Monomers used: The reaction is initiated by exposure to UV light and proceeds via free radical polymerization. Thin Film Composite Membranes Thin film composite membranes were prepared by coating prepolymer solution on commercial microporous supports such as polyacrylonitrile (PAN). A dead end membrane filtration system was designed and built to test pure water flux across thin film composite membranes. Acknowledgement The selective layer of commercial RO membranes is comprised of highly crosslinked aromatic polyamide. We thank School of Engineering and Applied Sciences at University at Buffalo for their financial support. Greenlee, Lawler, Freeman, Marrot, Moulin, Water Res., 43 (2009) 2317-2348.. Ju, McCloskey, Sagle, Wu, Kusuma, Freeman, J. Membr. Sci., 307 (2008) 260-267 Characterization of Polymer Films Photo of a thiol- ene polymer film Fundamental of Reverse Osmosis Pore- penetratio n Increas e viscosi ty Decre ase thick ness PEO- Fill er DCM- Solve nt Ideal coating Thiol-ene reactions have fast polymerization rates, high conversion, network homogeneity and offer versatility in thiol and ene selection. Increasing the solvent content in the prepolymer solution increases the water permeance in the thin film composite membranes. SEM image of T1E2 + 0.35% PEO + 90% DCM Dense polymer structure on the surface. Membranes of thiol-ene polymers show hydrophilicity. Polymer network formation Salt * 50% Solvent content in prepolymer solutions * Lowe, Poly. Chem., 2010, 1, 17-36 * Wu, Liu, Yu, Liu, Gao, J. Membr. Sci., 352 (2010) 76-85 Lin et al., Ind. Eng. Chem. Res., 2013, 52 (31), 10820 0.8 0.85 0.9 0.95 1 0 500 1000 1500 2000 2500 N orm alized R ejection ppm .h chlorine ) ( p A J W 100 1 1 2 C C R 1000 1500 2000 2500 3000 Polym er Ene Thiol W avenum ber(cm -1 ) 0.8 1 1.2 1.4 1.6 0 500 1000 1500 2000 2500 N orm alized Flux ppm .h chlorine 0 10 20 30 40 50 60 70 80 C ontactA ngle T x E y + 0.1% PEO T x E y +0.35% PEO + 50% DCM T x E y +0.35% PEO + 90% DCM T1E2 T1E1 T2E1 T1E1 T1E2 T2E1 T1E2 T2E1 T1E1 PAN 30 0 0.2 0.4 0.6 0.8 1 0 5 10 15 20 Perm eance (L/m 2 x hrx bar) Pressure (bar) T1E1 + 0.35% PEO + 90% DCM T1E2 + 0.35% PEO + 90% DCM 0 0.005 0.01 0.015 0.02 0.025 0.03 0.035 0.04 0 5 10 15 20 Perm eance (L/m 2 x hrx bar) Pressure (bar) T1E1 + 0.35% PEO + 50% DCM T1E2 + 0.35% PEO + 50% DCM

North American Membrane Society Poster

Embed Size (px)

Citation preview

Page 1: North American Membrane Society Poster

www.buffalo.edu

0.8

0.85

0.9

0.95

1

0 500 1000 1500 2000 2500

Nor

mal

ized

Rej

ectio

n

ppm.h chlorine

Thiol-ene Polymer Networks for Reverse OsmosisShawreen Shah, Kaipin Huang, Norman Ng and Haiqing LinDepartment of Chemical and Biological Engineering, University at Buffalo (SUNY), Buffalo, NY 14260, USA

Overview

Conclusion and Future Work

Drawback of Current RO Membranes

Approach: Thiol-Ene Based Polymer Networks

Conclusion: Highly crosslinked thiol-ene polymers and thin film composite membranes based on these polymers have been successfully prepared and characterized.

Future Work: • Optimize composite membranes and evaluate salt rejection using a dead-end

filtration system and a crossflow filtration system.

Laboratory of InNovative

Membranes at UB

Composition

Density(g/cm3)

Fractional Free Volume

Water Sorption Sol-Gel Percent

Without solvent*

With solvent*

Without solvent*

With solvent*

Without solvent*

With solvent*

Without solvent*

With solvent*

T1+E1 1.2 1.2 0.16 0.16 2.4% 2.6% 1.6% 0%

T1+E2 1.3 1.3 0.12 0.12 2.2% 2.3% 1.2% 0%

T2+E1 1.3 1.3 0.12 0.12 2.8% 2.7% 1.6% 0%

T2+E2 1.3 1.3 0.15 0.15 1.9% 2% 0.2% 0%

Reverse Osmosis (RO) system(Δp > Δ)

Δp = pressure differenceΔ = osmotic pressure difference

Salt Rejection:

C2: salt concentration in the permeateC1: salt concentration in the feed

)( pAJW

10011

2

CCR

Current RO membranes are subjected to chlorine oxidation, leading to higher water flux and lower salt rejection.

Thiol monomers T1: T2:

Ene monomers E1: E2:

Objective: To design and develop thiol-ene polymer based reverse osmosis membranes and study structure/property correlation.

Advantage of Thiol-Ene Polymers: • Highly crosslinked and homogenous• Versatile with many choices of monomers• Easy to prepare and immune from oxygen inhibition

Approach: • Novel polymers are prepared using multifunctional thiols and enes. • Polymers are characterized using FTIR-ATR, density and fractional free

volume measurements, and water sorption measurements.• Thin film composite membranes are prepared on commercial microporous

substrates for reverse osmosis applications.

Flux evaluation:

• Thiol-ene polymer networks are immune to oxidation, and hence chlorine is not expected to degrade the membrane.

A series of thiol-ene polymers were synthesized by UV photopolymerization.

Monomers used:

The reaction is initiated by exposure to UV light and proceeds via free radical polymerization.

Thin Film Composite MembranesThin film composite membranes were prepared by coating prepolymer solution on commercial microporous supports such as polyacrylonitrile (PAN).

A dead end membrane filtration system was designed and built to test pure water flux across thin film composite membranes.

Acknowledgement

The selective layer of commercial RO membranes is comprised of highly crosslinked aromatic polyamide.

We thank School of Engineering and Applied Sciences at University at Buffalo for their financial support.

• Greenlee, Lawler, Freeman, Marrot, Moulin, Water Res., 43 (2009) 2317-2348..• Ju, McCloskey, Sagle, Wu, Kusuma, Freeman, J. Membr. Sci., 307 (2008) 260-267

Characterization of Polymer Films

Photo of a thiol-ene polymer film

Fundamental of Reverse Osmosis

1000 1500 2000 2500 3000

PolymerEneThiol

Wavenumber (cm -1)

Pore-penetrationIncrease viscosity

Decrease thickness

PEO-Filler

DCM-Solvent

Ideal coating

0.8

1

1.2

1.4

1.6

0 500 1000 1500 2000 2500

Nor

mal

ized

Flu

x

ppm.h chlorine

• Thiol-ene reactions have fast polymerization rates, high conversion, network homogeneity and offer versatility in thiol and ene selection.

0

10

20

30

40

50

60

70

80

Con

tact

Ang

le

TxE

y + 0.1% PEO

TxE

y+0.35% PEO

+ 50% DCMT

xE

y+0.35% PEO

+ 90% DCM

T1E2T1E1 T2E1 T1E1 T1E2 T2E1T1E2T2E1 T1E1PAN 30

Increasing the solvent content in the prepolymer solution increases the water permeance in the thin film composite membranes.

SEM image of T1E2 + 0.35% PEO + 90% DCMDense polymer structure on the surface.

Membranes of thiol-ene polymers show hydrophilicity.

Polymer network formation

Salt

* 50% Solvent content in prepolymer solutions

* Lowe, Poly. Chem., 2010, 1, 17-36

* Wu, Liu, Yu, Liu, Gao, J. Membr. Sci., 352 (2010) 76-85

0

0.2

0.4

0.6

0.8

1

0 5 10 15 20

Perm

eanc

e (L

/m2 x

hr x

bar

)

Pressure (bar)

T1E1 + 0.35% PEO + 90% DCM

T1E2 + 0.35% PEO + 90% DCM

0

0.005

0.01

0.015

0.02

0.025

0.03

0.035

0.04

0 5 10 15 20

Perm

eanc

e (L

/m2 x

hr x

bar

)

Pressure (bar)

T1E1 + 0.35% PEO + 50% DCM

T1E2 + 0.35% PEO + 50% DCM

Lin et al., Ind. Eng. Chem. Res., 2013, 52 (31), 10820