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Percentage of Israel’s drinking water:• 2014: 35% • 2015: 40% • 2050: 70%
Once unthinkable, Israel can now produce a surplus of fresh water with desalination, becoming one of the leading countries in the field.
DISADVANTAGES
• High cost
• Intensive energy consumption
• Direct environmental impact• Disposal of brine
ADVANTAGES
• Additional fresh water
• Does not depend on drought periods
• Produced close to consumption
• Environmental benefits
• Economical benefits
In wastewater treatment, brine waste is the super concentrated by-product that results from treating seawater.
WHAT IS BRINE?
SEAWATER BRINE
SALINITY 39.4 g/l 69 g/l
TEMPERATURE 24.5° 32°
The higher the salinity , the larger the density
The higher the temperature the lower the density
Find the best alternative that will balance
Economic and Environmental issues
OBJECTIVE OF THE PROJECT
Current Situation at Ashkelon
• No pipe or diffusers are used for current brine discharge of 21,000 m3/hour.
• Brine disposed directly to the sea
• Designed for ≈ 50 MCM/year
• Currently supplying ≈ 100 MCM/year
WE DESIGNED FOR 42000 m3/hr of BRINE
Our Suggestion to Improve
• Introduce a pipe with a
diffuser
• Improving the dilutionwith lower environmental impact at lowest cost
Real Data Desalination plant at Ashkelon :
• Brine salinity: 69 g/L
• Seawater density: 39.4 g/L
• Average slope: 0.02
Assumed Data:
Hazen-Williams coefficient 135
Pump Efficiency 85%
Pipeline lifespan 40 years
Pipe operation 24 hours/day
Hours pumping/ year 8760 hours
Energy cost 0.02 $/kWh
Annual Interest 4%
Alternative Pipe length
1 1 Km
2 1.5 Km
3 2 Km
Pipeline Cost Calculation
• Investment Cost• Energy Cost• Operation and Maintenance Cost
Pipeline Cost Calculation• Investment Cost
• Only market diameters were used
• Total Pipeline Investment Cost
• Annual repayment for pipeline investment ($/year)[ -PMT(I,n,PV) ]
1 Km = 1 Million $
Pipeline Cost Calculation• Energy Cost
• Dynamic head Loss (m) [Hazen Williams]
• Total head Loss (m)[Dynamic HL+ Static HL+ Pressure requirements]
Pressure requirement= 1 atm= 10 m
• Power required (KW)Efficiency of 85%
• Energy required per year (KWh/year)8760 hours of pumping a year (24 hours)Average cost of of 0.02$/kWh as assumed
• Cost of energy required per year ($/year)
DiffusersThe ending point of an outfall pipe is generally made of a diffuser
This device separates the effluent fluid into several jets, so as to favor the process of dilution
Cost=1.1* Pipeline Investment Cost
Equal outlet velocity in nozzles2 m/s <velocity< 5.5 m/s
Distance between nozzles = Y/5
Dilution Calculations
Near field dilution: It occurs near the outlet into the sea.
Far field dilution: It occurs further away from the effluent outlet.
Comparison 1 Comparison 2
Same number of nozzles in the diffuser
Same dilution So
Different dilutions So Different number of nozzles in the diffuser
3 alternatives 3 alternatives
COMPARISONS
COMPARISON 1- Same # nozzles
Alternative Lengthpipe[Km]
# nozzles
Outletvelocity
Ratio Diffuser/
main pipeline
Dilution So
Cost[c/m3/ye
ar]
1 1200
5.16 m/s 0.81 43.140.44
2 1.5 200 5.16 m/s 0.81 98.84 0.63
3 2 200 5.16 m/s 0.81 171 0.82
Alternative Lengthpipe[Km]
# nozzles
Outletvelocity
RatioDiffuser/
main pipeline
Dilution So
Cost[c/m3/ye
ar]
1 1 450 2.29 m/s 1.85 94.6 0.49
2 1.5 194 5.32 m/s 0.79 95.8 0.63
3 2 110 9.38 m/s 0.45 95.9 0.78
COMPARISON 2- Fixed Dilution
CONCLUSION
Alternative 2 gives us the most suitable result to get potable water,
diluting back to the environment our waste at the most economical price.
1.5 km long
200 nozzles
So= 98.8
Cost=0.63 cents/m3/year