were
obtained
module
with
over
those
the
helical
optimum
linear
(forward
for rhe
module. S.
rime,
Luque,
Gehlert,
H.
Mallubhotla,
R. Kuriyel,
S. Pearl,
G.
S. Dzengeleski,
G. Belfort:
(5
1999).
effect
facilitated
of
solvents
transport
acid
feed phase,
membrane
receiving
the
phase
phase
had
rhe
Applied
pressure,
0.7
With
and same
also
hydrophobic
that
wetted
0n
Ag’ and
was
The conraminarion
as the support.
The
solvent
fouling
with
in
rhe
membrane
0.5
correlated
well
wirh
rhe
operating
number had
(DN)
the
of the solvents
maximum
about
25
constants Ag’ and from
kcal/mol. of
complexes
DHA-Et
the
increased
rhe
kcal/mol,
that
is
\oIvent.
Ag-salt
form
the 19
precipitation
aqueous
showed
rhe
of DHA-Er
membrane.
prepared
in
When
x
60”(:.
two non-solvcnrs, solvenr traditional investigated.
from
membrane
membrane, factors
while
and
DHA-b-t
the
the
between
high of the
faciliration
selectivities
Nafion
ot
of
in glycerin
and
[he increaTe remprrature
of
the
experimental
were found
to enhance
permeances
because
larger membrane
swelling.
of
the
H. Matsuyama,
Y. Kitamura,
Y. Marsuba:
Tf Membrane Science
159(1-2)
_J l-10
Y. Doi,
wcrc
solid/liquid phase
different
morphologies de-mixing
obtained
by
<:eramic
emulsion
propanol,
respectively,
rhe co-solvent used
characteristics treafmrnl oiliwatel-
precipitating
wirh different
and
pore
were evaluated
of an
unsrable studies
10
invesrigare
through
size
contrast,
for the
as the
secondary
emulsion.
experimental underraken
it
The were the
showed
operating
proportional
These
eEecrs containing
rdfic
component.
Ill
rhe
composite
O-IO%
to
severe fluctuation any
feed
concenrracion
homogeneous ceramic W.H.
Hong,
wacel
No
range
Developments
a[ b)
mem-
Research Trends
_/. “f
latest
29-39
rapidly
and
cellular obtained
de-mixing.
when 2-propanol precipitation
In
was used
medium, de-mixing
it and
particulare formed.
of membrane
The
formarion
membrane
research
(1 July 1999).
precipitarfon a
and applications
around the world
support. Hong:
Membrane Science 159( l-2)
to precipirate
Features
around
PDMS
brane withour
When
operating
was observed
Y.K.
and
Contracts of
of IPA in feed mixture.
using
news
New product releases
of
case
with
Iwo
Industry trends Commercial
each
fl ucruarion
on the
month News
the
of
I’DMSiceramic
Next
effects
by measuring
permeation
(I luiy 1999).
capillary
and plasricising
were investigared
t la: ,/. (4‘ I-2) 4 l-4(,
C.L.
of
ro the
remperaturc.
coupling
Y.M. I.ec. S.Y. Nani,
Membrane .Sciewr 159(
of PDMS
rhat rhe selectivity
IPA is inversely
w.i\
at over Xi wt%i.
is dominant,
observed
were
were
mean\
of
watct
II’A in feed
2-
crystallisation-induced principles
20 wr%
ia
rhar
wa
live
feed II’A
by IPA. In
rhe ptasticisation
be
system,
morphologies
than
ratio,
showed
delayed
rhan
which
of water,
of PDMS
waler
the
liquid/liquid
dominant
plasricisarion
rates could
system. as
morphologies
membranes
distriburionc
using
condensation
temperarure,
and
mcmbranc
with irlct-rahing
maintained
pores, on selectivirie5
we,-c
flux through
I’ANilPAA~
decredbed
range, rhe effect
permeation
diagram.
ternary
Permeate
~dtel
100 u&,
.md
In rhis composirion
de-mixing the
grid
perme‘itc’
in the permeate
to relate the
morphologies
3OOgim’h
rhan
.m
concentratiorl
membrane,
de-mixing
mote
tlux in
respecrively. the
irk 30 wr”;rl
PAAc \howed that
‘1%~
with the PAAc
of tip
20 wt”! of IPA in rhe feed mixture.
at
of liquid/liquid
medium,
Oil/water treatment
0 I1 the diagram
about
watct
I’ANiiI’AAc
contalnillg
in
to
of the
white
condensarion
system,
based phase
Ir was attempted
membrane
was
(1 July 1939).
~‘1s
non-solvent
of the membrane
ternary-
influence
different
pair,
rhe co-solvenr
sIructureb, complex
and
the
using
in rhe range from 0 to
by IPA in rhe feed
in which rhey are mixed
to produce
60°C.
DHA-Er
heat-rreatment
membrane
proportion
two
selectiviries
with operating
The
formation
‘fhe
and the prediction
rhe complexation Ag’ and
was pool-. The
the
was
ro ethyl ester of oleic acid
were low because abiliry
in Na
of rhe high swelling
increased
resulrs
rhc
increareti ratio
conccnIrdtion
composire
mixtures
solvenr/non-solvent
for rhe membrane
the permeance
However,
of PAAc towards flus
30 u t%
operating
bccauhc
affinity
mixing
wt%.
inLreased
water
Membrane\
inversely
flux
of
of w;1
in the 9’
concenlration,
more
as d co-
content
rnembl-ane
g/m%
membrane a
support,
PL)MS/ceramic
more
replacing
200
membrane
ceramic
immersion-
serving
system,
abour
using
PDMS
in ceramic
use of
was d
of IPA in rhe pervaporation
co-solvent by
permeate
membrane.
temperarure.
water-2-propanol
were
DMF, DMA and TBP were used as
because
composire pervaporarion,
was rhen higher
from
causeti
disordered
the
dc~.~-e~~sc~Ito
while
(PDMS)/
ro
membranes
When
1PA
using
by
of IPA were
poly(ethylenr-co-vinyl
rhe solvent, salt
out
poly(dimerhylsiloxane)
selectiviries
membranes
(EVAL)
mixture
proporGonal
(1 July 1999).
Crystalline
of
(isopropanol)/warer
of capillary
constants,
DN of about
pcrmeance
pervaporation
the
E. Julien, Y. Aurelle:
membrane\‘
permeate
using
Moreover,
I’ANi
and
i h alns
20 w&0, water conccnudtion
I I-20
alcohol)
the
luiy
.i\ ‘1%‘.
hirrdrancc 01. PAAc
structure\.
(1
high
Xlo}“~~.d
mernbrdll0.
bulkinecs
J, of’Membrzne
Ceramic supports
without
were larger
hc
PAAL in the doped
/. of‘ Membrane Science 159( I-2)
of
I .-Y.
21-27
when
pressure.
EVAL polymer
Hsieh,
1999).
obtained
wirh
melhanoI
Y.-S. Huang:
temperature
membrane
an
(Ihen,
P Srijaroonrat,
of DN
C.-c:.
homogeneou\
consrant
and the stability
Young,
For
membrane.
rhe sizes of oil droplers
110[1-
dehydration
because
pores.
capillary
;I
.mcl cxhibltcd \t.it>illtb
conformation
7-H.
between
rhe solvent
highest
rhan
to
solverilirlon-solvenr-potylilrl-
ceramic
induced
of rhe permearc
pressure
(0
membrane
From the balance on
pm
enough
cxrrnded
than in rhe feed.
equilibrium
The stability
effects
swelling
of
the
be
Stability
with the decrease
of rhe solvents. two
were
extraction
experiments.
and
ar a DN
of
oil was observed
contents
donor
and
can
carried
hydrophobic
surf:lce
more
used
membranes,
the
membrane
than
(N?/ll’i.
oxidation
The
rhe oil was easily
was
membrane
membranes,
hydrophilic
indicating
flux.
pyrrolidone a high
a II
rhe
to be lower
solvenr. The carrier of DHA-Et Nafion
on
sysrems
non-s~)lvenr/solvent-l~ot~ltller
Science 159(1-2)
and feed have
influence
flux was found
to be
respecrivcly.
velocity
tar rhe rcrnary
with
system.
reverse
found
\,
feed
oprimum
and
were
and
with
where
established
the best
‘l‘hr
time
1 min
important
(DHA-Et)
in the system
flux. filtration
filtration
and
to obtain
concenrrarion
of ethyl ester of
docosahexaenoic was studied
on
conditions
velocity
concentrarion) forward
Influence of solvents on facilitated transport The
pressure,
permeate
Hiotecbnolo~
& Hioengineering 65(3) 243-257 November
operating
and reverse back-flushing
Patents
Pervaporation of waterlisopropanol mixtures Polyaniline by
wirh
(PAAc) aqueous membranes solurion
membrane
patents
(PANi) was synrhesised
oxidarive
doped
World, US and European
for
polymerisation poly(acrylic pervaporarion isopropanol. were
blending
NetScope The best membrane
of
sites
I’ANi
prepared with
and acid)
by
/v-methyl
.-m-
Membrane Technology No. 118