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Title: Water Issues at the Technion


1
Technion - Israel Institute of Technology Grand
Water Research Institute Rabin Desalination
Laboratory Chemical Engineering Department
  • Water Issues at the Technion
  • Prof. Raphael Semiat

2
UN Report
  • The Global Need for Water
  • Water shortage have reached crisis
  • Proportion in many parts of the world
  • Estimated 1.5 billion people do not have access
    to adequate supplies of safe water
  • Estimated 10,000 people die every day and
    thousands more suffer from a range of
    debilitating illnesses due to water related
    diseases
  • This includes estimated 2.2 million child death
    annually
  • Availability of fresh water resources is fixed
  • Per capita availability continues to decrease as
  • Population increases
  • Developing countries improve their quality of
    life and level of industrialization
  • Salinity levels in many fresh water aquifers
    increases

RDL GWRI Technion
3
Water deficiency 2004
3B
1.5B
2004 2025
2004
2025
Source Seckler et al, 2002
4
Middle East Desalination Research Center
5
Mountain Aquifer
6
Chloride year 2000
Coastal Aquifer salinization processes
Shore Basin
7
Desalination Sites
Large plants Shomrat ?? (30) Hadera (140) Soreq
(140) Palmahim (3010) Ashdod (100) Brackish
inland (50) Ashkelon (10020) Ktziot (3)
Tenders - BOOT projects for 25 years
7
8
Ashkelon Plant
On Sept 2006 completed first 100 Million m3
9
Lowest cost ever announced currently
0.56US/m3
The process And Cost Evaluation
VID IDE VIVENDY (VEOLIA) DELEK - DANKNER
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10
Spiral Wound Membranes
membranes thickness- 200 nm and down. Holes size
and size distribution, membrane properties
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Eilat Plants
  • Sabha A 25,500m3/day BW
  • Sabha B 10,000 BW
  • Sabha C 10,000 SW

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12


13
Operational Experience Saving on
chemicals. Eilat plants
13
14
Man made polluted waters Industrial, agriculture
and urban effluents
Straining
Modern Sewage Treatment
Sludge/ solids treatment
Adsorption
Secondary treatment
Energy
Compost
Micro/Ultra-Filtration
MBR
Polishing
Reverse-Osmosis or Nano-Filtration
Concentrate disposal
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16
Related Documents
Driving Forces for Water RD Need for
Water Global need, Industry, Agriculture, Remote
Locations, Desertification, Etc. Cost Difference
- (Industry/Urban - Agriculture) Cost Difference
- (Thermal Processes - Membrane
Processes) Technologies for Export
16
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17
  • Water Technologies - Innovation and Challenge
  • Grand Water Research Institute

The Stephen and Nancy Grand Water Research
Institute at the Technion operates as the Israeli
national institute for research in the science,
technology, engineering and management of water
resources The mission of the GWRI, established in
1993, is to be a center of excellence of
international caliber, the leading water research
institute in Israel The GWRI concentrates in
particular on topics of relevance and importance
to Israel
Water Treatment Desalination Treatment and reuse
of wastewater Preservation of water quality and
quantity in the sources Hydrology quantity and
quality Water and environmental
microbiology Management in and of the urban water
sector Water resources management and policy
57 members from 7 Faculties of the Technion 6
professors from other universities Cooperation
Other universities, research institutes,
agencies, government ministries, industry,
private sector
18
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19
  • Significant membrane properties
  • Main Characteristic properties
  • Selectivity
  • Permeability
  • Mechanical stability (creep and compaction)
  • Chemical Stability (Hydrolytic stability,
  • Organic material stability, pH,
  • Microbial resistance, Cl2 attack, etc.
  • Surface anti-fouling properties
  • (Phtalates, cellulose acetate, Chlorine in water,
    NaOH in cleaning,
  • Initial fluxes reduction, suspended materials and
    precipitants (CaCO3, CaSO4, SiO2, CaF2, SrSO4,
    BaSO4, etc.)

Membrane thickness, Permeability,
rejection, Size, size distribution Anti-fouling
treatment Catalitic reactivity.
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21
Performance of new membranes
22
Boron complexation using Manitol
23
Illustration of typical measurementsCaCO3
Run in which the membrane was not scaled
Run in which the membrane was scaled
Mechanism of AS?
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Effectiveness of various anti-scalants(Super-satu
ration level of CaSO4 3.5)
CaSO4
Induction time, t SHMP, 6 ppm tgt10 hr A, 12
ppm t4 hr B, 12 ppm t3 hr B, 6 ppm t1 hr A, 6
ppm tlt1 hr
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Antiscalants - Molecular Modelling
  • Requirements
  • effective antiscalents are molecules which
    inhibit growth of the crystals formed by the
    scalent
  • the antiscalent has to be capable of binding on
    all crystal faces
  • Modelling
  • modelling the interaction between the crystal
    lattice and the antiscalent can be performed by
    force field calcula-tions (e.g. with the
    Dreiding force field).
  • Example
  • Barium Sulfate

Coveney, P. V. , Davey, R. , Griffin, J. L. W. A
New Design Strategy for Molecular Recognition in
Hetero-geneous Systems A Universal Crystal-Face
Growth Inhibi-tor for Barium Sulfate J. Amer.
Chem. Soc., 2000, Vol. 122
26

Dynamic Bio Film Membrane Foulant
Yeast
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Particle deposition close to the spacer
28
Module view and sampling
Prof. Carlos Dozoretz
29
Nanofiltration of MF-MBR effluents
CLSM of a fully developed biofilm
CSLM Confocal Laser Scanning Microscope
30
Long term bacteria fouling
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Solar Desalination Aqaba Jordan Sept 2005
32
Degradation of Ethylene Glycol in "Fenton like"
process different concentrations of
nano-particles catalyst ?-250 PPM, ?-500 PPM,
X-1000 PPM, ?-1250 PPM
An important step in wastewater recovery
Nano particles Nano FeOx Catalysis
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35
High Supersaturation in concentrate pipes
Effect of silica super-saturation
GWRI Rabin Desalination Laboratory
36
Super-saturation Removal from concentrates
Conclusions
  • The most promising technique for precipitating
    CaSO4 is by adding a coagulant.
  • Alkali addition is an effective precipitation
    technique for both scaling salts but seems
    uneconomic.

AS Dosage
Destabilization of AS
Concentrate Waste
Membrane

Precipitation vessel
Brackish Water
Slurry to waste
Pure Water
Recycle of concentrate of reduced hardness
  • Certain surfactants can induce rapid
    precipitation of CaCO3.
  • Seeding does not induce precipitation in the
    case of CaSO4 solutions but is very effective in
    the case of CaCO3.

37
CONTINUOUS FLOW PRECIPITATION STUDY EFFECT OF
RETENTION TIME ON PSD
  • The augmented retention time also acts to
    increase systematically the size of the
    precipitated particles.
  • The surface mean diameter D3,2 is seen to
    increase from 3 mm at t 1.1 hr to 10 mm at t
    8.75 hr.

38
Escherichia coli
Identification of specific virulent strains in
water Dr. Y. Kashi
Listeria
Bio Monitoring
39
Identification of specific virulent strains in
water Dr. Y. Kashi
Vibrio cholerae
Bacillus anthrax
Bio Monitoring
40
DNA Fingerprint
41
Bacterial Identification and Typing System
Input Unknown sample or bacterial colony
 
Reacting the bacterial DNA with a capillary
optical fiber
Bacterial genotype Database
Output Identified Bacteria
Pre-made DNA biosensor array with custom made
probes
42
Vibrio cholerae
43
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45
Chemical Detection Methods Large and complex
instruments Sensors / detectors Sensor
arrays Lab-on-a-chip
46
Suggested Techniques for Monitoring Particulate
Matter in Water


Laser Induced Breakdown Spectroscopy

47
On-Line Detection of Water-Terror Agents in
Aquatic Environments Prof. I. Schechter

Laser

  • The Technology
  • Laser Induced Breakdown Spectroscopy.
  • Sampling on the nm-mm range
  • - Direct detection in water

Cd

Zn


Spectrometer


Sample
48
Suggested Techniques for Monitoring Particulate
Matter in Water Prof. I. Schechter
TR-LIF Polymeric film sampling
49
Suggested Techniques for Monitoring Particulate
Matter in Water
Fourier Transform Spectroscopic Imaging
50
Energy usage in Desalination - comparison
51
Household Energy ConsumptionElectricity,
transportation and desalinated water
  • A small family, consumes water at a rate of 18
    m3/month,
  • 1200 KWh of electricity /month, Drives 1500
    km/month, consumes 160 liter gasoil/month
  • Energy consumption assuming only desalinated
    seawater used - 140 KWh/month (fuel value)
  • Energy consumption - driving a car - 1500
    KWh/month (fuel value)
  • Energy consumption - electricity - 1200/0.452667
    KWh/month (fuel value)
  • Energy for desalination/ energy for
    transportation - 9.3
  • Energy for desalination/ energy for electricity -
    2.6
  • Energy for desalination/ total energy consumption
    - 3.4
  • Can we save 3.4 in our household energy
    consumption?
  • Where we should put our energy for use? In water?
    In high energy consuming cars? In overused AC?

52
???? ??? ?? ????????? ????? ??? ?????
  • ???? ??????? 4X4 ?????? 5 ?"? ?????. ????
    ????? 300 ?"? 60 ???? ???
  • ????? ?????? ??????? ??????? ?- 15 ?"? ??-??
    ??????? ??????? ???? ????? ????? ???? ??? ???
    ?????? ?????!!!
  • ?? ????? ???? ???????

53
Desalination and proper water usageOther costs
should be included besides Energy
  • Cost of water in negligible for regular household
  • Cost of water is tolerable for most industries
  • Cost of water is significant in agriculture
  • Make better usage of water
  • Use of greenhouses
  • Use Drip-Irrigation save 30-90 of water
    consumption by other irrigation techniques
    reduce the cost problem

54
200-250 m2 are needed to make 1 m3 water a day!
55
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The dead sea problem
Bathymetric and Satellite Map of the Sea of
Galilee. Ben Avraham Zvi, Amit Gideon and Golan
Arik (contour interval 1 m)
57
Energy Canals Med Dead Red - Dead
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Water is needed in locations where agriculture is
still the basis for life. Simple agriculture
cannot afford even the currently relatively low
costs. It is a global question of the same type
as the usage of alternative energy sources to
solve environmental-pollution problems. The
future of mankind depends on finding the proper
answers to those questions, in addition to the
quest for global peace.
59
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60
Pushing the Limits of Desalination Reduction of
RO desalination process costs Main directions
for reducing desalination costs Membrane
improvement Permeability, rejection, resistance
to fouling Concentration polarization -
Flow Improvement of membrane modules Fouling and
scaling prevention Optimization of the water
recovery level The boron problem Pretreatment
MF, UF etc. Energy aspects Concentrates -
Environmental Process optimization
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Membrane Distillation Configuration
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