Pretreatment
Pretreatment Selection
1. Remove
suspended solids.
2. Control
calcium scaling.
* Antiscalant Injection
* Softening
* pH Adjustment (Acid Injection)
3. Other
treatment as dictated by water analysis and desired recovery.
Particulate | 10 to 25 micron cartridge filter. Sand or diatomaceous earth filter (Optional) |
pH correction | Acid addition to lower pH to about 6. Membrane hydrolysis function of pH |
Calcium Carbonate | pH adjustment prevents precipitation |
Calcium Sulfate | Precipitation inhibited with scale inhibitors |
Iron & Manganese | Soluble state no problem, but dander is oxidation to insoluble form at or near membrane. Oxidation, reduction, scale inhibitor possible methods |
Colloids | Coagulation/Flocculation; Ultrafiltration |
Organic Deposits | Filtration, Activated Carbon, Polyelectrolytes |
Microbiological Organisms | Chlorination |
Silica | Dependent on form, soluble, crystalline amorphous |
Temperature | Product flux ยต temperature; 1 to 1.5% per degree |
Pretreatment Techniques
Feed Water Characteristics | Potential | Treatment |
Turbidity (Suspended solids) | Forms Deposits in lines and equipment | Coagulation, settling, filtration |
Color | Stains and causes foaming | Coagulation, filtration absorption |
Odor (see dissolved gases) | Chlorination, Absorption | |
Taste | Chlorination, Absorption | |
Chemical Characteristics | Potential | Treatment |
Hardness (Ca and Mg salts) | Forms Scale | pH, softening, conversion control |
Minerals (Na, K, CI, SO4, HCO3) | Contribute to TDS | RO |
Mn++ | Forms Deposits | Oxidation |
Fe++ | Upon Oxidation | Filtration |
Silica | Forms Scale | Lime softening process |
Gases (O2 , H2 S, CO2 , NH3) | Cause Corrosion | Aeration Degasification |
Biological Characteristics | Potential | Treatment |
Bacteria | Forms organic | Chlorination |
Algae | Deposits | UV Irradiation |
Viruses |
Summary of Pretreatment Options
This table summarizes the pretreatment options when specific risks for scaling and fouling are present. It is a quick reference for "possible" and "very effective".Dechlorination
-
Sodium Bisulfite (Na H SO3)
-10% Solution
-3 Lbs. of Na H SO3 per lb. of Cl2
-
Activated Carbon
-1 million PPM gallons per cubic ft.
-
Solution life of Sodium Bisulfite
SODIUM
BISULFITE SOLUTION
WEIGHT %
|
MAXIMUM
SOLUTION LIFE
|
2
|
3 Days
|
10
|
1 Week
|
20
|
1 Month
|
30
|
6 Months
|
Activated Carbon
-
1 cubic foot of Carbon will remove 1 ppm of Chlorine from 1 million gallons of water
-
Design Flow Rate
-Chlorine 15 gpm/ft2
-Organics 6 gpm/ft2
Removal of Suspended Solids
Technique | Equipment Options |
Gravity Separation |
Primary
Sedimentation
Secondary Sedimentation
Chemical
Sedimentation
Flotation
Clarification
Settler
|
Physical Straining Process |
Screening
Diatomaceous Earth Filtration
Ultrafiltration
|
Granular Media Filtration |
Upflow
Sand Filters
Downflow
Sand Filters
Green
Sand Filters
Multi
Media Filters
Special
Design Filters
|
Granular-Media Deep-Bed Filtration
Table V. Minimum Fluidization Velocities for Various Uniform-Sized Media
(Observed
Empirically)9
Between U.S. Std. Sieves
Passing | Mm | Retained | Size | Mean Flow Rate to Achieve 10% | ||
(mm) | Expansion at 25°C, gpm/ft2 | |||||
Coal | Sand | Garnet | ||||
7
|
2.830
|
8
|
2.59
|
37.0
|
||
8
|
2.380
|
10
|
2.18
|
30.0
|
||
10
|
2.000
|
12
|
1.84
|
24.0
|
41.0
|
|
12
|
1.680
|
14
|
1.54
|
20.0
|
33.0
|
|
14
|
1.410
|
16
|
1.30
|
15.7
|
27.0
|
49.0
|
16
|
1.190
|
18
|
1.09
|
12.5
|
21.0
|
40.0
|
18
|
1.000
|
20
|
0.92
|
9.9
|
16.4
|
32.0
|
20
|
0.841
|
25
|
0.78
|
8.4
|
12.6
|
27.0
|
25
|
0.707
|
30
|
.65
|
7.0
|
9.0
|
22.0
|
30
|
0.595
|
35
|
0.55
|
6.3
|
18.0
|
|
35
|
0.500
|
40
|
0.46
|
5.4
|
13.7
|
|
40
|
0.420
|
45
|
0.38
|
4.0
|
11.3
|
|
50
|
0.297
|
60
(.25mm)
|
0.27
|
6.3
|
||
Specify
Gravity
|
1.7
|
2.65
|
4.1
|
|||
Table VI.
Temperature Correction: Approximate Correction Factors to be Applied for
Temperatures Other Than 25°C
Temperature (°C)
|
Multiply
the 25°C Value by
|
30
|
1.09
|
25
|
1.00
|
20
|
0.91
|
15
|
0.83
|
10
|
0.75
|
5
|
0.68
|
Typical Pressure Filter Media Beds For RO Pretreatment
A. SAND FILTERS
Top Layer
-12” to 24” fine sand
-0.45 to 0.6 mm e.s.
Middle Layer
-6” to 12” coarse sand
-0.8 to 1.2 mm e.s.
Bottom Layer
-4” find gravel
-1/4” to 1/8” diam.
B. DUAL - MEDIA
FILTERS
Top Layer
-6” to 24” No. 1 anthrafilt -0.65 to
0.76 mm e.s.
Layer
-12” to 18” fine sand
-0.45 to 0.6 mm e.s.
Layer -6” coarse sand
-0.8 to 1.2 mm e.s.
Bottom Layer
-4” fine gravel
-1/4” to 1/8” diam.
C. MANGANESE
ZEOLITE FILTERS
Top Layer
-0 to 6” No. 1 anthrafilt
-0.65 to 0.76 mm e.s.
Layer
-12” to 18” manganese zeolite -0.27 to 0.37
mm e.s.
Layer
-4” to 6” fine sand
-0.45 to 0.6 mm e.s.
Layer
-0 to 6” coarse sand
-0.8 to 1.2 mm e.s.
Bottom Layer
-4” fine gravel
-1/4” to 1/8” diam
NOTE:
Bed depths will depend on available height of pressure filter and at least 50%
of bed depth should be allowed as free board for bed expansion.
Deep Bed Filtration - Design Recommendations
DUAL MEDIA
Recommended
Depth:
Coal 18” - 24”
Sand 15” - 18”
FILTRATION
RATE
5
Gallons/Minute/Square Foot Dual Media
15
Gallons/Minute/Square Foot Multi Media
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