cross-linking and solvent treatment of pei membranes · 2017. 11. 18. · cross-linking results...

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Cross-Linking Results Cross-Linking and Solvent Treatment of PEI Membranes Connor Seacat · Griffin Karr · Michael Wales · Mary Rezac Background Membranes are used for separating gasses. The polymer that we are constructing our membranes from is polyetherimide (PEI). Solvent treatments intend to increase selectivity of the membranes and cross-linking prevents membranes from becoming plasticized. Plasticization occurs when gasses absorb into the membrane in large quantities and disrupt the packing of the polymer chains causing the membrane to lose its selective permeability. Research Objective Key Findings Methods XRD and FTIR data indicate that we effectively crosslinked the membranes. Most solvents negatively affected the membranes’ gas selectivity. 1-Heptanol and n-Amyl alcohol showed improvements to the selectivity of the membranes. GPU= %&’()* @-./ 01*2∗.4)*∗5**6 /1*77(1* Membranes were gas flux tested before and after each treatment. Gas permeability was calculated by: Peaks shifting right indicate decreased d-spacing due to cross- linking. Amorphous halo shifting left indicates swelling of polymer chains. 0 10 20 30 40 50 60 70 80 90 100 300 500 700 900 1100 1300 1500 1700 1900 Arbitrary Units cm-1 FTIR Data Of Ethylene Diamine 0 Hr 5 Hr 8 Hr Imide Amide Amide Imide Imide Imide bands: (1) 1770 cm -1 (2) 1700 cm 1 (3) 1340 cm 1 Amide bands: (1) 1645 cm -1 (2) 1530 cm -1 Solvent Treatment Results 0 20 40 60 80 100 120 140 160 0 1 2 3 4 5 6 7 8 9 10 He/N2 Selectivity Permeance He He/N2 Selectivity vs Permeance of He 1-Butanol n-Amyl 1-Heptanol 1-Octanol Hexadecane 0 20 40 60 80 100 120 140 160 0 1 2 He/N2 Selectivity Treatment He/N2 Selectivity vs Number of Solvent Treatments 1-Butanol n-Amyl 1-Heptanol 1-Octanol Hexadecane 0 0.005 0.01 0.015 0.02 0.025 1-Butanol n-Amyl 1-Heptanol 1-Octanol Hexadecane Mass Solvent/ Mass Polymer Vapor Sorption of PEI Film Gas Supply Gas Selector Feed Pressure Knob Feed Pressure Gauge Retentate Valve Membrane Holder Vacuum Valve Vacuum Pump Pressure Transducer Ballast Membranes were prepared by dissolving PEI in a solvent solution and then casting that solution onto a glass sheet. The membranes were then precipitated in a bath of acetone and dried. Use diamines to cross- link PEI membranes through vapor exposure and liquid baths in alcohol- diamine solutions. Treat PEI membranes with various solvents to heal imperfections and increase the selectivity of He to N 2 and He to O 2 gasses through the membranes. Determine most effective solvents and treatment styles. 0.00 1000.00 2000.00 3000.00 4000.00 5000.00 6000.00 7000.00 8000.00 10.00 15.00 20.00 25.00 30.00 35.00 40.00 45.00 Arbirtary Units 2 Theta (Degrees) 1,3-diaminopropane XRD Unmodified PEI 2 hr (T1) diaminopropane 2 hr (T2) diaminopropane 4 hr (T1) diaminopropane 4 hr (T2) diaminopropane 8 hr (T1) diaminopropane 8 hr (T2) diaminopropane 0.00 1000.00 2000.00 3000.00 4000.00 5000.00 6000.00 7000.00 8000.00 10 15 20 25 30 35 40 45 Arbitrary Units 2 Theta (Degrees) Ethylenediamine XRD Unmodified PEI 2 hr (T1) ethylenediamine 2 hr (T2) ethylenediamine 4 hr (T1) ethylenediamine 4 hr (T2) ethylenediamine 8 hr (T1) ethylenediamine 8 hr (T2) ethylenediamine 0 1000 2000 3000 4000 5000 6000 7000 8000 10.00 15.00 20.00 25.00 30.00 35.00 40.00 45.00 Arbitrary Units 2 Theta (Degrees) 1,3-Cyclohexanebis(methylamine) XRD Unmodified PEI 2 hr (T1) cyclohexanebis 2 hr (T2) cyclohexanebis 4 hr (T1) cyclohexanebis 4 hr (T2) cyclohexanebis 8 hr (T1) cyclohexanebis 8 hr (T2) cyclohexanebis 0.00 1000.00 2000.00 3000.00 4000.00 5000.00 6000.00 7000.00 8000.00 10 15 20 25 30 35 40 45 Arbitrary Units 2 Theta (Degrees) 1,3-diaminobutane XRD Unmodified PEI 2 hr (T1) diaminobutane 2 hr (T2) diaminobutane 4 hr (T1) diaminobutane 8 hr (T1) diaminobutane 8 hr (T2) diaminobutane 0 5 10 15 20 25 30 35 40 0 5 10 15 20 25 30 35 40 δh (δd^2 + δp^2)^.5 δh vs (δd^2 + δp^2)^.5 PEI methylene chloride (1) methylene chloride (2) water (1) water (2) methanol ethanol 1-propanol 2-propanol 1-butanol Heptane Toluene (1) Toluene (2) p-xylene (1) p-xylene (2) Solubility parameters and sorption data were used to predict the effects of the solvent. FTIR Data for Ethylene Diamine

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  • Cross-Linking Results

    Cross-Linking and Solvent Treatment of PEI Membranes Connor Seacat · Griffin Karr · Michael Wales · Mary Rezac

    Background

    Membranes are used for separating gasses.

    The polymer that we are constructing our membranes from is polyetherimide (PEI).

    Solvent treatments intend to increase selectivity of the membranes and cross-linking prevents membranes from becoming plasticized. Plasticization occurs when gasses absorb into the membrane in large quantities and disrupt the packing of the polymer chains causing the membrane to lose its selective permeability.

    Research Objective

    Key Findings

    Methods

    XRD and FTIR data indicate that we effectively crosslinked the membranes.

    Most solvents negatively affected the membranes’ gas selectivity. 1-Heptanol and n-Amyl alcohol showed improvements to the selectivity of the membranes.

    GPU= %&'()*@-./01*2∗.4)*∗5**6/1*77(1*

    Membranes were gas flux tested before and after each treatment.

    Gas permeability was calculated by:

    Peaks shifting right indicate decreased d-spacing due to cross-linking.

    Amorphous halo shifting left indicates swelling of polymer chains.

    0

    10

    20

    30

    40

    50

    60

    70

    80

    90

    100

    30050070090011001300150017001900

    ArbitraryUnits

    cm-1

    FTIRDataOfEthyleneDiamine

    0Hr

    5Hr

    8HrImide

    Amide

    Amide

    Imide

    Imide

    Imide bands:(1) ≈1770 cm-1(2) ≈1700 cm−1(3) ≈1340 cm−1

    Amide bands: (1) ≈1645 cm-1(2) ≈1530 cm-1

    Solvent Treatment Results

    0

    20

    40

    60

    80

    100

    120

    140

    160

    0 1 2 3 4 5 6 7 8 9 10

    He/N

    2Selectivity

    PermeanceHe

    He/N2SelectivityvsPermeanceofHe

    1-Butanol

    n-Amyl

    1-Heptanol

    1-Octanol

    Hexadecane

    0

    20

    40

    60

    80

    100

    120

    140

    160

    0 1 2

    He/N

    2Selectivity

    Treatment

    He/N2SelectivityvsNumberofSolventTreatments

    1-Butanol

    n-Amyl

    1-Heptanol

    1-Octanol

    Hexadecane

    0

    0.005

    0.01

    0.015

    0.02

    0.025

    1-Butanol n-Amyl 1-Heptanol 1-Octanol Hexadecane

    MassS

    olvent/M

    assP

    olym

    er

    VaporSorptionofPEIFilm

    GasSupply

    GasSelector

    FeedPressureKnob

    FeedPressureGauge

    RetentateValve

    MembraneHolder

    VacuumValve

    VacuumPump

    PressureTransducer

    Ballast

    Membranes were prepared by dissolving PEI in a solvent solution and then casting that solution onto a glass sheet.The membranes were thenprecipitated in a bath of acetone and dried.

    Use diamines to cross-link PEI membranes through vapor exposure and liquid baths in alcohol-diamine solutions.

    Treat PEI membranes with various solvents to heal imperfections and increase the selectivity of He to N2 and He to O2 gasses through the membranes.

    Determine most effective solvents and treatment styles.

    0.00

    1000.00

    2000.00

    3000.00

    4000.00

    5000.00

    6000.00

    7000.00

    8000.00

    10.00 15.00 20.00 25.00 30.00 35.00 40.00 45.00

    Arbirta

    ryUnits

    2Theta(Degrees)

    1,3-diaminopropaneXRD

    Unmodified PEI 2hr(T1)diaminopropane 2hr(T2)diaminopropane

    4hr(T1)diaminopropane 4hr(T2)diaminopropane 8hr(T1)diaminopropane

    8hr(T2)diaminopropane

    0.00

    1000.00

    2000.00

    3000.00

    4000.00

    5000.00

    6000.00

    7000.00

    8000.00

    10 15 20 25 30 35 40 45

    Arbitra

    ryUnits

    2Theta(Degrees)

    EthylenediamineXRD

    Unmodified PEI 2hr(T1)ethylenediamine 2hr(T2)ethylenediamine

    4hr(T1)ethylenediamine 4hr(T2)ethylenediamine 8hr(T1)ethylenediamine

    8hr(T2)ethylenediamine

    0

    1000

    2000

    3000

    4000

    5000

    6000

    7000

    8000

    10.00 15.00 20.00 25.00 30.00 35.00 40.00 45.00

    Arbitra

    ryUnits

    2Theta(Degrees)

    1,3-Cyclohexanebis(methylamine)XRD

    Unmodified PEI 2hr(T1)cyclohexanebis 2hr(T2)cyclohexanebis

    4hr(T1)cyclohexanebis 4hr(T2)cyclohexanebis 8hr(T1)cyclohexanebis

    8hr(T2)cyclohexanebis

    0.00

    1000.00

    2000.00

    3000.00

    4000.00

    5000.00

    6000.00

    7000.00

    8000.00

    10 15 20 25 30 35 40 45

    Arbitra

    ryUnits

    2Theta(Degrees)

    1,3-diaminobutaneXRD

    Unmodified PEI 2hr(T1)diaminobutane 2hr(T2)diaminobutane

    4hr(T1)diaminobutane 8hr(T1)diaminobutane 8hr(T2)diaminobutane

    0

    5

    10

    15

    20

    25

    30

    35

    40

    0 5 10 15 20 25 30 35 40

    δh

    (δd^2+δp^2)^.5

    δhvs(δd^2+δp^2)^.5

    PEI

    methylenechloride(1)

    methylenechloride(2)

    water(1)

    water(2)

    methanol

    ethanol

    1-propanol

    2-propanol

    1-butanol

    Heptane

    Toluene(1)

    Toluene(2)

    p-xylene(1)

    p-xylene(2)

    Solubility parameters and sorption data were used to predict the effects of the solvent.

    FTIR Data for Ethylene Diamine