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8/2/2019 Ceramic Membranes in Energy And
1/19
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