desalination by membrane technology – state of the art and future trends
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Desalination by membrane technology – state of the art and future trends. Dr. Matthias Rothe and Oliver Hentschel ProMinent GmbH Im Schuhmachergewann 5-11, D-69123 Heidelberg Tel. +49 (6221) 842-0, Fax. +49 (6221) 842-1900 [email protected] www.prominent.com. Content. - PowerPoint PPT PresentationTRANSCRIPT
Experts in Chem-Feed and Water Treatment
Desalination by membrane technology –state of the art and future trends
Dr. Matthias Rothe and Oliver Hentschel
ProMinent GmbH Im Schuhmachergewann 5-11, D-69123 Heidelberg
Tel. +49 (6221) 842-0, Fax. +49 (6221) [email protected] www.prominent.com
Experts in Chem-Feed and Water Treatment
Content
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 2
1. Basics and state of the art membrane filtration
2. Applications for desalination by membranes
3. Future trends for membrane desalination
Experts in Chem-Feed and Water Treatment
1. Basics and state of the art membrane filtration
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 3
Membrane filtration: removal of particles and salts ensuring lowest operating costs
physical process using semi-permeable membranes
4 technologies depending on the size of the particles/molecules to be removed
Microfiltration
Ultrafiltration
Nanofiltration
Reverse Osmosis
Experts in Chem-Feed and Water Treatment
Nanofiltration and Reverse Osmosis
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 5
Nanofiltration and Reverse Osmosis are the only membrane
technologies to remove ions/salts from water !
How does it work ?
Experts in Chem-Feed and Water Treatment
Osmosis
dilutedsolution
concentratedsolution
semipermeable membrane
water columncorrespondingto osmotic pressure
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 6
Experts in Chem-Feed and Water Treatment
Reverse Osmosis
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 8
pressure
dilutedsolution
concentratedsolution
semipermeable membrane
Experts in Chem-Feed and Water Treatment
Development of Reverse Osmosis Membranes
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 9
cellulose acetate membranes
lifetime about 6 months
pH range: 4 - 8
salt rejection:up to 90-95%
polyamide hollow fibre modules
lifetime about 5 years
pH range: 4 - 11
salt rejection:up to 96-98%
less sensitive against bacteria
thin film composite membrane
lifetime about 10 years
pH range: 2 – 11, for cleaning: 1 - 12
salt rejection: up to 99.8%
stability up to 45°C
sanitary membr. 90°C
less sensitive against bacteria/biofilm
1960 1970 1980 - 2014
Experts in Chem-Feed and Water Treatment
Thin film composite membrane
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 10
Polyamide ultrathin barrier layer (approx. 0.1-0.2µm)
Polysulfone micro-porous support (approx. 40µm)
Polyester non-woven web Carrier (approx. 120µm)
Experts in Chem-Feed and Water Treatment
Crossflow membrane filtration
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 11
Experts in Chem-Feed and Water Treatment
Thin film composite membrane module
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 14
http://www.youtube.com/watch?v=YlMGZWmh_Mw&feature=player_embedded
Experts in Chem-Feed and Water Treatment
Water temperature influence on reverse osmosis
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 15
increased water temperature
reduction of water viscosity
increased permeate production
but:decreased salt rejection
Experts in Chem-Feed and Water Treatment
Operation pressure influence on reverse osmosis
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 16
The salt rejection will be better, also
The higher the pressure the more permeate flow is produced
Experts in Chem-Feed and Water Treatment
Recovery of membrane systems
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 17
R
K
P
25% drain to waste
75% permeate100% raw water
Recovery [%] = Output : Input = (Permeate flow / raw water flow) x 100
Typical recoveries: 70-80% for desalination of tap water35-45% for desalination of sea water
Experts in Chem-Feed and Water Treatment
Typical reverse osmosis system
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 21
2 17
10
7/8
15
1913
13
20
13
2
11
12
13
1
2
3
54
1. particle filter2. pressure gauge3. solenoid valve incl. check valve4. pressure switch5. thermometer6. high-pressure pump7. pressure vessel8. membrane9. conductivity probe10. controller incl. conductivity measurement11. flow meter permeate12. 3-way valve
13. ball valve14. flow meter concentrate15. 3-way valve16. flow meter concentrate recycle17. sample valve18. cleaning tank19. cleaning pump20. check valve
616
9
11
18 10
16
Experts in Chem-Feed and Water Treatment
Typical reverse osmosis system
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 22
11
22
33
44
5566
1 pressure vessels incl. membranes2 switch cabinet with RO control unit3 cleaning tank4 flow meter permeate + concentrate5 particle filter6 conductivity sensor permeate
1 pressure vessels incl. membranes2 switch cabinet with RO control unit3 cleaning tank4 flow meter permeate + concentrate5 particle filter6 conductivity sensor permeate
Experts in Chem-Feed and Water Treatment
Overall design of a membrane system
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 23
Pre-treatment depending on the feed water‘s quality: filtration and chemical conditioning as a minimum
Pre-treatment depending on the feed water‘s quality: filtration and chemical conditioning as a minimum
Post-treatment depending on applicationPost-treatment depending on application
Experts in Chem-Feed and Water Treatment
Applications for desalination by membranes
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 24
Tap water desalination(typically up to 1.000 mg/l of feed water salinity)
Brackish water desalination(typically 1.500 – 8.000 mg/l of feed water salinity)
Sea water desalination(typically more than 35.000 mg/l of feed water salinity)
Experts in Chem-Feed and Water Treatment
Applications for Reverse Osmosis
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 26
industrial water desalination of tap water
• boiler water for steam production
• dilution water for juice- and softdrink production
• bottled water
• …
potable water production desalination of brackish and sea water reduction of nitrate reduction of fluoride reduction of arsenic
Experts in Chem-Feed and Water Treatment
Desalination of tap water (installation example)
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 27
3x tap water desalination 1.200 m³/day, total 3.600 m³/day,process water for paintshop of KIA motors
Experts in Chem-Feed and Water Treatment
Desalination of tap water (installation example)
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 28
3x tap water desalination 1.200 m³/day, total 3.600 m³/day,process water for paintshop of KIA motors
Experts in Chem-Feed and Water Treatment
Future trends for membrane desalination
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 32
nano-coating structures on the active membrane layer, advantages:
a. anti-fouling properties are improved
Experts in Chem-Feed and Water Treatment
Future trends for membrane desalination
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 33
b. Increase in permeability
• less energy is needed at improved salt rejection rates
• first membranes with nano-coating are commercially available now
http://www.nanoh2o.com/technology/video
Experts in Chem-Feed and Water Treatment
Future trends for membrane desalination
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 34
decreased energy consumption
• membrane desalination with renewable energies like solar power …
Experts in Chem-Feed and Water Treatment
Future trends for membrane desalination
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 35
… or wind energy:
Experts in Chem-Feed and Water Treatment
Future trends for membrane desalination
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 36
Combination of membrane technologies, e.g. Micro- and Ultrafiltration (MF/UF) as pre-treatment followed by reverse osmosis, advantages:
a. Smaller footprint of complete water treatment plant which leads to smaller buildings
b. Better quality water of pre-treatment e.g. in comparison to classical sand filters
c. Reverse osmosis after MF/UF can be designed much more aggressive because of higher filtrate quality. This saves investment and operation costs on the reverse osmosis downstream
Experts in Chem-Feed and Water Treatment
Future trends for membrane desalination
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 37
Energy recovery on sea water desalination systems has moved from turbines to pressure exchangers. They reduce energy consumption of a sea water desalination units by 50-60% !
Experts in Chem-Feed and Water Treatment
Cost considerations
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 38
Typical Pressure
Typical Recovery
Typical Energy Consumption for RO
PW 4 - 12 bar up to 80 % 0,4 – 0,75 kWh/m³
BW 10- 40 bar up to 60 % 1,2 – 2,00 kWh/m³
SW without ER
40 - 82 bar up to 30-50 % 4 – 8 kWh/m³
SW with PX 40 - 82 bar up to 30-50 % 1,8 – 3,5 kWh/m³
Energy consumption depend on: Salinity and permeate qualityRecovery RateFeed Water TemperatureMembrane Type and Aging (Fouling/Scaling)Pump Type and Configuration
Experts in Chem-Feed and Water Treatment
Energy consumption of large SWTP
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 39
Source: Watereuse: Seawater desalination Power consumption
Experts in Chem-Feed and Water Treatment
Typical Range of SWRO Facility Costs
Dr. Rothe, Oliver Hentschel, 24.01.2014, SANEPAR 40
Source: Watereuse: Seawater desalination Power consumption
Experts in Chem-Feed and Water Treatment
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