Ceramic Membranes in Energy And

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    CERAMIC MEMBRANES IN ENERGY ANDENVIRONMENT RELATED APPLICATIONS

    V.T. Zaspalis

    Research at the Center of Research and Technology-Hellas

    Center for Research and Technology-Hellas

    Chemical Process Engineering Research Institute

    Laboratory of Inorganic Materials

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    CONTENTS

    What is a membrane

    Low Temperature Applications :

    Separation of gas mix tures

    Water treatment

    High Temperature Applications:

    Environmental friendly combustion ofnatural gas

    Hydrogen from renewable sources

    CONCLUSIONS

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    What is a membrane

    A ceramic membrane is a thin semi-permeable film made of inorganicoxidic materials

    It can be porous so that selective transport takes place though the poresand through various mechanisms

    It can be non porous so that selective transport takes place throughcrystalline lattice diffusion

    It can be self-supported when is thick and strong enough, or supported onsubstrates when is thin and mechanically weak

    selectivity of permeating substances

    F l u x

    t h r o u g h

    porous systems

    dense systems

    research goals

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    34cm

    8mm 14mm

    What is a membrane

    n a n o p

    o r o u

    s l a y

    e r

    mesoporous bridgelayers

    m a c r o p o r o u

    s

    s u b s t r a t e

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    What is a membrane

    Ceramic membranes at CERTH are prepared:

    Step 1:Synthesis of stabilized nanoparticledispersions by metal-alkoxide hydrolysis

    Step 2:Membrane layer formation by dip-coating onporous substrates

    Step 3: Eventual further pore surface modification or size reduction by wet impregnation or vapor

    deposition techniques

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    Porous membranes, Separation of gas mixtures

    Scientific principle I: Knudsen law

    In simple words: At nanopore level small molecules move faster than large ones

    This principle can form the basis for the development of separationtechniques where mixtures of light (e.g. hydrogen) and heavy (e.g.hydrocarbons) components can be enriched in the light components

    L

    P

    RT

    vr A

    dx

    dC ADF mmk K K

    == 3

    2 M RT vm

    8=

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    Porous membranes, Separation of gas mixtures

    0.E+00

    5.E-09

    1.E-08

    2.E-08

    2.E-08

    3.E-08

    3.E-08

    4.E-08

    4.E-085.E-08

    5.E-08

    0.E+00 1.E+05 2.E+05 3.E+05 4.E+05 5.E+05 (Pa)

    F ( m o

    l s - 1 m - 1

    P a - 1

    )

    Hydrogen

    Helium

    Nitrogen

    Hydrogen Propane Mixture50/50

    M e m

    b r a n e

    Hydrogen Propane Mixture82/18

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    Porous membranes, Separation of gas mixtures

    Scientific principle II: Kelvin law

    Vapor pressure of liquid concave in a pore is lower than that of thesame liquid on a flat surface, it therefore condenses much earlier

    r P

    P

    M

    RT t

    cos2ln

    0=

    This principle can form the basis for the development of separationtechniques on mixtures containing a condensable and non-

    condensable and non-soluble component

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    Porous membranes, Separation of gas mixtures

    5

    5,5

    6

    6,5

    7

    7,5

    8

    20 30 40 50 60Temperature ( oC)

    S e p a r a

    t i o n

    f a c

    t o r

    0

    1

    2

    3

    4

    5

    6

    p e r m e a

    b i l i t y x

    1 0 1 5

    m o

    l / m

    / s / P a

    Propane C 3H8Propylene C 3H6

    Similar molecules very

    difficult to separate

    C 3H8: 50C 3H6: 50 C 3H8: 12

    C 3H6: 88

    C 3H8: 50H2: 50 C 3H8: 98H2: 2

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    Porous membranes, Separation of gas mixtures

    Scientific principle III : Activated microporous diffusion

    The pore is reduced down to the molecular dimensions and separation occurs bysieving

    Vapor deposition techniques

    H2: 50 CO 2: 50H

    2: 98.8 CO

    2: 1.2

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    Porous membranes, Water treatment

    0

    1

    2

    3

    4

    5

    6

    0,00010,0010,010,11

    d p ( m)

    Pure Water

    Monovalent ions

    Multivalent ions

    Viruses

    Bacteria

    Suspended solids

    3 layers

    1st

    2nd

    3 rd4 th

    4 layers 5 layers

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    Porous membranes, Water treatment

    Purified water product

    As: 1ppm

    Fe 2O 3 nanoparticles

    cad e

    Qt K QQ

    ln1

    ln =

    0

    1

    2

    3

    4

    5

    6

    7

    0 20 40 60 80 100 120 140Contact time, min

    l n ( 1 / ( Q

    e - Q

    ) )

    Removal of toxic metals (As, Cr) from w ater

    0,01

    0,1

    1

    feed product

    A s

    i o n c o n c e n t r a

    t i o n

    ( p p m

    )

    Current maximum allowablelimit 50ppb

    Fe: 2000 ppm Fe: 0,001 ppm

    25nm 25nm

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    Dense Membranes, Hydrogen from renewable sources

    One of the most promising and long-term sustainable routesfor the production of energy is:

    H2O H 2 + 0.5 2

    The process currently under intensive research is the so-

    called RedOx process hydrogen production

    0 1 2

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    Dense Membranes, Hydrogen from renewable sources

    Our research-proposal is based on a dense oxygen conducting membrane reactor

    H2O

    H2

    Membrane

    Mixed Conductor

    Vo, e

    O o

    c o m p a r t m e n

    t 1

    c o m p a r t m e n

    t 2

    O 2

    ..Ooo21..2

    Dense Membranes Hydrogen from renewable sources

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    0.0E+00

    5.0E-09

    1.0E-08

    1.5E-08

    2.0E-08

    2.5E-08

    3.0E-08

    0 5000 10000 15000 20000

    Time (s)

    H 2

    I o n

    C u

    r r e n

    t ( A )

    0 1 2 3 4 5 6

    Time (hr)

    I n a c

    t i v e s t a

    t e

    Hydrogen in compartment 1, T=900 oC, P 1=P 2=1bar

    CO in (compartment 2)

    CO off

    (activation)

    baseline (0 mmol H 2 m -2 hr -1)

    steady state (~13 mmol H 2 m -2 hr -1)H2O 1/2O 2+H 2

    CO +H 2O CO 2+H 2steady state: (~39 mmol H 2 m -2 hr -1)

    Dense Membranes, Hydrogen from renewable sources

    Dense Membranes Environmental friendly combustion of natural gas

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    Dense Membranes, Environmental friendly combustion of natural gas

    H2O

    H2

    Membrane

    Mixed Conductor

    Vo, e

    O o

    c o m p a r t m e n

    t 1

    c o m p a r t m e n

    t 2

    O 2

    .. Ooo2

    1..2

    Air Methane (CH 4)

    CH 4+2O 2 CO 2+2H 2O + Energy

    pure CO 2 STORAGE

    Dense Membranes, Environmental friendly combustion of natural gas

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    Dense Membranes, Environmental friendly combustion of natural gas

    -50

    0

    50

    100

    150

    200

    0 20 40 60 80 100 120

    Reactor loop number O x y g e n a

    v a i l a b l e i n t h e s o

    l i d f o r r e a c t

    i o n

    C H 4

    p i c k s u p o x y g e n

    A i r

    d e l i v

    e r s o x y

    g e n

    La 0.7 Sr 0.3 Cu 0.05 Fe 0.95 O3Material:

    T=980 oC

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    CONCLUSIVE REMARKS

    Porous ceramic membranes (specially modified to the nanoporous region) cangive high separation factors and give rise to the development of efficient process,

    in particular for the separation of hydrogen

    Porous ceramic membranes can provide technological solutions to many water treatment case-problems. The technology is quite mature to leave the laboratories

    Dense oxygen conducting membranes can give rise to the development of greenhigh temperature processes towards either hydrogen production from renewable

    sources or CO 2-capture oriented combustion of natural gas

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    ACKNOWLEDGEMENTS

    Research staff of the Laboratory of Inorganic Materials

    L. Nalbandian

    S. Sklari

    A. Evdou

    A. Pagana

    Technical staff of CERTH:T. Tsilipiras

    N. Georgiou

    A. Moudiotis

    The vapor deposition modifications of the membranes are being done incooperation with:

    Prof. G. Sakellaropoulos, dr. S. Kaldis and S. Koutsonikolas

    of the department of Chemical Engineering

    of the Aristotle University of Thessaloniki