Dewvaporation Dewvaporation
“ “Carrier Carrier-
- Gas Enhanced Atmospheric
Dewvaporation Dewvaporation Carrier Carrier- -Gas Enhanced - - PowerPoint PPT Presentation
Dewvaporation Dewvaporation Carrier Carrier- -Gas Enhanced Atmospheric Gas Enhanced Atmospheric Pressure Desalination Pressure Desalination
Most common in the USA USA
Solvent forced through membrane membrane
Energy consumption from pressure from pressure
Susceptible to fouling, scaling and degradation scaling and degradation
Pressurized feed
Applied pressure > Osmotic pressure Osmotic pressure
Semi-
permeable membrane membrane
Incomplete salt removal (different rates) (different rates)
Membrane Module Pump Brine Pretreatment Post Treatment Saline Feed Pure Water
3
2SO
4
2.50 – – 4.00 $/1000gal of product 4.00 $/1000gal of product2
2
26 KWh/1000gal of product2
2
4.00 -
10.00 $/gal-
day2
2
Phase separation
Heat saline water/condense vapor water/condense vapor
Reduce pressure
Energy required for heat
Large energy costs, less common in USA common in USA
Evaporation / Condensation Column Brine Fresh water Pretreatment Saline feed Heat
80% of world’ ’s thermal s thermal desalination product desalination product
Energy needed for heat
Recycles heat
Two heat sources for incoming saline feed incoming saline feed
External
Heat of vaporization
Additional heat
Pressure released in first released in first chamber chamber
Water boils quickly quickly
Evaporation and condensation condensation
Heat Vapor Saline Feed Pure Water Waste Brine Pump Condensate Trays Heat Exchanger Tubes
Extra heat transfer layer
Reduces heat transferred
Reduces efficiency
Use stainless steel
56 KWh/1000gal of product2
2
Because of expensive energy, prices are in the range of $12 to $14 per 1000 gallons range of $12 to $14 per 1000 gallons5
5 in USA
in USA
Only economically feasible in regions like the Middle East, where fuel is cheap and water is Middle East, where fuel is cheap and water is scarce scarce
Air moves in a cycle
Works to recycle heat
P u r e w a t e r S a l i n e f e e d Inlet Air Ambient Air Outlet Air Added heat (Qboiler) Heat Condensing water Saline feed Air Evaporating water
Blower
d dz z z
+
dz T T hL dW h dT T GVh dT T Gh T GVh T Gh
d vap V a v a
) ( ) ( ) ( ) ( ) (
2 1 1 1 1 1
− + ∆ + + + + = +
Mass Balance: Heat Balance: dWd G, GVz G, GVz+dz FDz FDz+dz Region 1 Region 2
Can be added as steam
Adding steam keeps air saturated
1 2 3 4 5 Q to achieve T G, GVs
e
G, GVs
d
Humid Air Dry Air Humid Air Dry Air
Model considered credible if temperature profile was appropriate appropriate
Temperature of evaporation side air had to reach ambient air temperature (25 temperature (25º ºC) at bottom of column C) at bottom of column
Air flow rate (G) had the most dramatic effect on product flow and heating requirements flow and heating requirements
1 Humid Air 2 3 4 5 Dry Air G, GVs
e
G, GVs
d
T5
Temperature Down the Tower
0.00 10.00 20.00 30.00 40.00 50.00 60.00 70.00 80.00 100 200 300 400 500 600 700 800 Distance from Tower Top (cm) Temperature (deg. C) T Air Dewformation Side T Pure Water Product T Seawater/Brine T Air Evaporation Side
∆T
$0.79 $1,867.10 18.85 1123.76 1744200 6000 6 $1.00 $1,830.24 206.01 936.60 1453500 5000 5 $1.30 $1,773.35 393.29 749.33 1162800 4000 4 $1.81 $1,725.26 580.56 562.05 872100 3000 3 $4.27 $1,665.91 870.56 272.06 581400 2000 2 $5.86 $1,557.14 954.77 187.85 290700 1000 1 Operating Cost $/1000gallons FAC $ FB gal/day FD gal/day Qboiler J/hour G mol/h Design
Costs $/1000gallons vs. Flow Rate
0.00 5.00 10.00 15.00 20.00 25.00 200 400 600 800 1000 1200 Flow Rate (gallons/day) $/1000gallons
More air to heat
More expensive blower blower
Slightly higher tower
Energy Cost Vs. Air Flow
0.00 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90 1.00 1000 2000 3000 4000 5000 6000 7000 Flow Rate of Air Mol/hr Cost of Energy $/day
Equipment Cost vs. Air Flow
0.00 500.00 1000.00 1500.00 2000.00 2500.00 3000.00 3500.00 1000 2000 3000 4000 5000 6000 7000 Air Flow Mol/hr Equipment Cost $
FAC vs. Air Flow
1000.00 1100.00 1200.00 1300.00 1400.00 1500.00 1600.00 1700.00 1800.00 1900.00 2000.00 1000 2000 3000 4000 5000 6000 7000 Air Flow mol/hr FAC $
Dewvaporation is on the low is on the low end of costs for current end of costs for current desalination technologies desalination technologies
Flow rates similar to Beckman Beckman’ ’s had similar costs s had similar costs
This is in the $1.70 to $3.70/1000gallon range $3.70/1000gallon range
Most effective in places like Arizona where the air is dry Arizona where the air is dry