membrane technology for water...
TRANSCRIPT
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TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Membrane technology for water treatment
J-C SCHROTTERMembrane Research Manager
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Brief History of Membrane Technology for Water Applications...
1956 - early 1980s : RO desalination, no commercial MF/UF fordrinking water
mid-1980 - early 1990s :Development of Memcor (MF), Aquasource(UF), clean waters & small capacities (1993 - Milwaukee- cryptosporidium crisis)
mid-1990 - 2002: Start of market growth, new competitors (Zenon, Xflow,Hydranautics, Pall, Ionics)with second generation membranes/modules) Use on not so clean waters Start of immersed MBR products
Now Large plants > 200000m3/dStrong growth of RO desalination market
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Global Membrane Market share 2004 (overall $6.46 Billion)
Wastewater 4.3%
Desalination 20.4%
Water 15.4%
Chemical 5.6%
Food&Bev. 12.9%
Pharmaceutical 10.4%
Mining 1.4% Oil&Gas 1.5%
Other industries 9.6%
Power 3.8%
Metals 4.9%
Pulp&paper 3.1% Refineries 1.4%
Semiconductor 5.1%
40% for water
Source : The McILVAINE COMPANY (2004)
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Background : a technical « revolution »in a tight economical context
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Use of membrane for water treatment
Water resource management
Water resourcemanagement
Drinkingwater
production
Drinking water distribution
Wastewater collection
Sludge treatmentand recycling
Wastewatertreatment
Treatment of industrial effluents
Odor control
Siteremediation
Drinkingwater
production
Processwater
production
Industrialwastewatertreatment
MunicipalWastewatertreatment
Brackish andSea water
Desalination
Raw Water quality varies from location. Treatment should be adapted according to needs
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
O&M and Inv. Cost of the water with a membrane treatment
General trends are: O&M Cost
River water0.05- 0.2 $/m3
Brackish water0.2-0.35 $/m3
Seawater0.53-1.3 $/m3
Investment Cost from $100 / m3/d to more than $2000 / m3/d
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Strigent water quality regulation
Example in UK for drinking water :
New regulations in 2003 for Cryptosporidium (>1 oocysts/10 litres)
New specifications have also been put in place onLead (25µ/L by 2014 and 10µ/L by 2024)Benzene (1µ/L)Nitrate (50mg/L)Nitrite (0.1mg/L)THM (Trihalomethanes) (100 µ/L)Bromate (10µ BrO3/L)Arsenic (10µ/L)
High standards required on Pesticides (0,5µg/l)Bacteries (5-6 Log removal)Viruses (4log removal)
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Microscopic view of a membrane surface
Membrane pore diameter 0.2 µm
Cryptosporidium : 3 à 6 µm
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Pollutant removal by membrane processes
OsmoseInverse
Nano-filtration
Ultra-filtration
Micro-filtration
0,0001µm
0,001µm
0,01µm
0,1µm
1µm
10µm
100 µm
.
Diamètre des pores des membranes
Streptocoque1 µm
Pseudomonas Diminuta0,28 µm
Virus de l’Influenza0,1 µm
Hémoglobine0,007 µm
Ion Sodium 0,00037 µm
Eau
0,0002
µm
Giardia Lamblia et
Cryptosporidium3 à 6 µm
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Differents kind of module
Spiralwoundedelement
Hollow fibers
tubular
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Different kind of systems
Rack
Tube
Block
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Reduction of membrane cost
10
100
1 000
10 000
100 1000 10000 100000 1000000
Cumulative membrane area - metres
Syst
em $
/kL/
day
inst
alle
d
1996
1992
1995
1990
1999
CMF "S"
M2 SeriesM1 Series
M10M10C
1985
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Membrane Operating conditions
Transmembrane pressure [bar]
Flux
[L/m
2 /h]
1
10
100
1000
0,1 1 10 100
MF / UF
NF OI
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Dead-end and cross-flow mode
Raw concentrate
Raw
Permeate Permeate
Cross-flow modeNF/OI
Dead end modeMF/UF
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TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
High pressure membraneHigh pressure membranesystems NF/OI
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
• Membrane
PolyamideMembrane
Polysulfonelayer
Polyestersupport
Basic principle of NF and RO systems
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
• Module spiralé : principe de fabrication
Glue
spacer
2 membrane sheets
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
MembranePermeate spacersglue
Feed spacers
Permeate collector
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
Collector with 3 sheets
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
• Module spiralé : principe de fabrication
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
Feed
Ions
Concentrate
Permeate
Cross-flow filtration with turbulence promotors (feed spacers) to limit polarisation concentration and fouling issues
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems• applied Minimum pressure should counter balance :
Pure Water
Brackichwater
membrane
:• Osmotic pressure• Longitudinal pressure drop• Permeate reservoir height
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
Osmotic pressure (Van’t Hoff Law)
Π = CRT
Avec :•Π = Osmotic pressure
•C = Ion concentration ( mol/m3 )
•R = perfect gas constant ( = 8,314 J/mol/K )
•T = Temperature ( °K )
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TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
•Osmotic pressure
100 ppm TDS ≈ 0,068 bar
1,000 ppm TDS ≈ 0,68 bar
35,000 ppm TDS ≈ 24,1 bar
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
•Operating pressure
Membrane Operating application Pressure
(bar)
RO
SW (30 000 - 50 000 mg/l) 50-75BW (100-10 000mg/l) 10-40
Nanofiltration 5-15
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems• recovery factor
recovery factor = permeate flow rateFeed Flow rate
100%Feed
75%permeate
25% concentrate
1 Terminologie
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Transmembranepressure
Transmembraneosmotic pressure
Workingpressure
Permeate Flux (l/h/m2)
Permeability(l/h/m2/bar)
Recoveryfactor
∆ pp p
ptmf c
p=+
−2
∆ π π πtmf c
p=+
−2
tmtmw pp ∆−∆=∆
Qflowrate
Sp=
wp p
QL∆
=
YQQ
p
f
=
π
π
Basic principle of NF and RO systems
1 Terminologie
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
• Rejection : R
R = 1 - [%]cpcf
Rsystem < Rmodule
• Salt passage
P = 1 - R = [%] cpcf
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Example : performance of 1 module :•Recovery = 10%
•Salt rejection = 80%
•Flowrate = 100 m3/h
•TDS = 100 ppm
•Conc flowrate = 90 m3/h
•TDS = 109 ppm
•Perm flowrate = 10 m3/h
•TDS = 20 ppm
•Conc flowrate = 81 m3/h
•TDS = 116 ppm
•Perm flowrate = 19 m3/h
•TDS = 21 ppm
•Conc flowrate = 73 m3/h
•TDS = 121 ppm
•Perm flowrate = 27m3/h
•TDS = 22 ppm
Performance of NF and RO systems
Performance of the system :•Recovery factor = 27 %
•Salt rejection = 78 %
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Performance of NF and RO systems
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
0% 10% 20% 30% 40% 50% 60% 70% 80% 90% 100%
Salt
reje
ctio
n
Recovery factor
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
•Recovery Factor
Procédé RecoveryFactor (%)
ROSW (30 000 - 50 000 mg/l) 35 à 45 BW (100-10 000mg/l) 65 à 85
Nanofiltration 75 à 85
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Basic principle of NF and RO systems
• Design Flux
Membrane Design Application flux
(l/h/m2)
RO
SW (30 000 - 50 000 mg/l) 10 – 18
BW (100-10 000mg/l) 15 - 25
Nanofiltration 15 - 25
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Performance of NF and RO systems
Feed
2nd stage
1st stage
3rd Stage concentrate
Membrane module
Pressure vessel
permeate
• single pass
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
• Double pass
Performance of NF and RO systems
Double pass is necessary when
low salinity permeate water is needed
Boron should be treated for desalination application
(Boron EC = 1mg/l – WHO = 0,5 mg/l )
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Figure 1 Ortho Boric acid dissociation
0
10
20
30
40
50
60
70
80
90
100
7 8 9 10 11 12 13 14
pH
mol
e pe
rcen
t
H3BO3 H2BO3-
HBO3=
BO3-3
•Boron species vs pHBasic principle of NF and RO systems
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
NF and RO efficiency
Removal of :
saltsDOC (Dissolved Organic Carbons)pesticides microorganismsviruses
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Reverse Osmosis
Seawaterdesalination :10000-50000 mg/L
BrackishWater desalination
1000-10000 mg/L
Waste water reuse
< 1000 mg/L
applications
Natural ground or Surface water
< 1000 mg/L
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TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
applications
Nanofiltration
Desulfatationdes eaux de merForte salinité :
10000-50000 mg/L
Traitements d’affinage des Eaux douces
Salinité faible :< 1000 mg/L
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
NF/RO products
NF/RO products dominated by spiral wound elementsstandardized in 8-inch x 40-inchPrice went down over the last 20 years from 40$/m2 to 9$/m2
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
2003 RO/NF Membrane Sales by Competitors
Dow/filmtec34%
NittoDenko hydranautics
30%
Toray11%
GE Osmonics8%
TriSep4%
Others4%
Toyobo4%
Koch fluid Systems5%
Source : R.L Truby & Associates (2004)
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TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
LowLow pressure membrane pressure membrane systemssystems MF/UF
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Dominating membrane : Hollow fiber configuration
feedfeedPermeatePermeate
Fouling layer
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Fouling affects permeability
IrreversibleFouling
Chemicalreversible
Fouling
Physicalreversible
Fouling
Time
Perm
eabi
lity
Initial permeability
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Fouling removal
Physical Chemical
Action Fouling particulate Mineral and organic removal
Removal present at the membrane surface
Acid wash for mineral removalWater
Basic wash for organic removalProductsused
Air Oxidant for biomass removal
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Dead end filtration
Flux : 60 to 140 l/h/m²
Transmembrane pressure: 0,2 to 1,5 bar
Membrane lifetime : 5 years
Operating conditions
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Main differences between different type of UF/MF
1. Molecular Weight Cut Off 2. Inside-out or Outside-in Filtration3. Cleaning steps
Backwash water+airEnhanced Backwash (with chemicals)Cleaning In Place
4. Module surface area (Packing density)5. Module design6. Pressurized and suction (Submerged) type
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
pressurisedMF/UF systems
SubmergedMF/UF systems
0
20
40
60
80
100
Equipement
Membranes
Submerged systems
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Operating conditions of submerged type
Flux
(l/h
/m2 )
Pressure (bar)
Pure water
Critical flux
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Why monitor membrane integrity?
Drinking water regulationseg UK cryptosporidium rule: <1 oocyst in 10L of water
Membranes provide a physical barrier to these pollutantsThe ability of a membrane system to remove these pollutants depends on the state of this barrier
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
INTEGRITY TESTINGINTEGRITY TESTING
34 million fibres
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Integrity Test Theory
Air Pressure 100kPa
Air flow by diffusion
Defect Air flow through defect
( )defectthroughairQftime
P__=
∆
)( __ defectthroughairwater QfQ =
Pressure Decay Test (PDT)Detection level : Up to Log 5.3
Diffusive Air Flow Test (DAF)Detection level : > log 7
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Bubble point theory
dkP θγ cos4
=Bubble Point Pressure -where air will pass through the pores of a wetted membrane
P = Bubble point pressure (kPa)
K = corrected factor for irregular pores
γ = liquid surperficial tension
Θ = contact angle
d = pore diameter (microns)
diameter of the largest
pore
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Bubble point theory
For hydrophilic membranes, contact angle=0 thus d = 288/P
Pore diameter APPLIED PRESSURE
0,05 µm P = 57,6 bar
0,1 µm P = 28,8 bar
1 µm P = 2,88 bar
2,88 µm Current on site P =1 bar
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Identifies which Unit?
Pressure Decay Test (PDT)
Rate of decay Rate of decay ∝∝ log Reductionlog Reduction
>Log 4 Crypto Sensitivity>Log 4 Crypto Sensitivity
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
INTEGRITY TESTING
Integrity methods Integrity methods also check sealsalso check seals
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
INTEGRITY TESTING : Which Module ?
SonicAnalysis
Will detecta singlefibre break
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
INTEGRITY TESTING : Repairing Broken Fibres
Isolate and remove moduleImmerse in test vesselPass air through moduleLocate bubbles in broken fibreInsert pin in top of fibreCheck for no more bubblesRe-install modulePut module back on line
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TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
LowLow pressure membrane pressure membrane KeyplayersKeyplayers for for DrinkingDrinking water water
applicationsapplications
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Pressurized hollow fibresPressurized systems vs Submerged systems
Submerged systems (60% market Share)
Pressurized systems (40% market share)
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Pressurised membrane systems
NORITEstablished Players New Entrants
INGEPALL/ASAHI
POLYMEMKOCHDOW/OMEXELLAQUASOURCETORAYHYDRANAUTICS
MEMCOR (CMF)
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Submerged Membrane systems (60% Market share)
Established Players
ZENON
MEMCOR
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TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
LowLow pressure membrane pressure membrane KeyplayersKeyplayers for Municipal for Municipal wastewaste
water applications water applications
•re-use, •tertiary treatment, •MBR)
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Municipal waste water applications
MBR
RO
Raw water
WWTP
irrigationMF/UF
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Tertiary treatment and reuse key players
Hollow fibersMembranes
Established PlayersMemcorNoritZenon
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
MBR key players
Hollow fibersMembranes
Flat sheetmembranes
Established Players
Kubota Zenon
New EntrantsMemcorKochMitsubishi
Toray
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jean-christophe Schrotter
TRANSPORTS PROPRETE EAUSERVICES ENERGETIQUES
Hollow fibers Flat sheet+ Air consumption
S. solids tolerance ++ footprint
Flux +Membrane resistance +
+ Integrity testingPretreatment +
+ Membrane repairedSimplicity of the process +
la technologie la plus adaptée+ZEN
ON
M
EMC
OR
P
UR
ON
MIT
SUB
ISH
I H
YDR
AN
AU
TIC
S
KU
BO
TATO
RA
Y
Hollow fibers or flat sheet membranes ?