Magnesium Hydroxide Slurry: A Safe, Cost Effective Solution for ...
Magnesium Hydroxide Slurry: A Safe, Cost Effective Solution for ...
Magnesium Hydroxide Slurry: A Safe, Cost Effective Solution for ...
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The Use of <strong>Magnesium</strong> <strong>Hydroxide</strong><br />
<strong>Slurry</strong> as a <strong>Safe</strong> and <strong>Cost</strong> <strong>Effective</strong><br />
<strong>Solution</strong> <strong>for</strong> H 2<br />
S Odor and Corrosion in<br />
Sanitary Sewer Systems<br />
Aileen Gibson<br />
Chris Knapp<br />
Steve Leykauf
Wastewater Treatment History<br />
• In 1977, the Clean Water Act Increased<br />
Requirements <strong>for</strong> Secondary Treatment<br />
• Categorical Pre-treatment Reduced Heavy Metals<br />
• Shift from Phosphate to Sulfur Based Detergents<br />
• More Centralized Treatment<br />
• Low Flow Plumbing Fixtures
DISSOLVED SULFIDE<br />
CONCENTRATION (mg/l)<br />
Corrosion Effect<br />
20<br />
DISSOLVED SULFIDE VS. TOTAL METALS<br />
15<br />
10<br />
10<br />
5<br />
Sulfides<br />
Metals<br />
Corrosion Threshold<br />
0<br />
0<br />
1980 1985 1990 1995<br />
TOTAL METALS<br />
CONCENTRATION (mg/l)
Effects on Municipalities<br />
• Hydrogen Sulfide (H 2 S) Formation Has Increased<br />
• Accelerated Biogenic Corrosion<br />
• Increased Sewer and Plant Odors<br />
• Grease Buildup (Fats, Oil and Grease – FOG)<br />
• Treatment Plant Upsets<br />
• Higher <strong>Cost</strong> of Treatment
Facts<br />
• U.S. Wastewater Infrastructure is Failing<br />
Faster than it is Being Replaced<br />
• Sanitary Sewer Overflows (SSO’s) are Very<br />
<strong>Cost</strong>ly Fiscally and Politically<br />
• Odor and FOG are Significant Problems<br />
Which Also Carry High Fiscal and Political<br />
Expense
Corrosion Chemistry<br />
• When Dissolved<br />
Oxygen Falls Below 0.1<br />
mg/l, Wastewater Turns<br />
Septic and Anaerobic<br />
• These Bacteria<br />
(SRB) Reduce Sulfate<br />
to Sulfide Producing<br />
the Rotten Egg Smell<br />
Called Sewer Gas<br />
H 2 S Gas H 2 S Gas<br />
D.O.
Corrosion Chemistry<br />
H 2 S<br />
H 2 S<br />
H 2 S Gas<br />
H 2 S<br />
H 2 S Gas H 2 S Gas<br />
SO<br />
2-<br />
4 HS - H 2 S<br />
• Hydrogen Sulfide<br />
Gas is the Principal<br />
Source of Odor and<br />
Corrosion<br />
• Evolution of H 2 S is a<br />
Function of Dissolved<br />
Sulfide Concentration,<br />
Water Temperature,<br />
Turbulence and pH
At pH 7 Roughly 50% of<br />
the Dissolved Sulfide<br />
Can Exist As Hydrogen<br />
Sulfide<br />
H 2 S<br />
H 2 S<br />
H 2 S Gas<br />
H 2 S<br />
H 2 S Gas H 2 S Gas<br />
6.00<br />
1200<br />
H 2 S (aq) and HS - in solution (mg/L)<br />
5.00<br />
4.00<br />
3.00<br />
2.00<br />
1.00<br />
H 2 S (g)<br />
HS -<br />
H 2 S (aq)<br />
1000<br />
800<br />
600<br />
400<br />
200<br />
H2S (g) in air (ppm)<br />
SO<br />
2-<br />
4 HS - H 2 S<br />
0.00<br />
0<br />
3 4 5 6 7 8 9 10<br />
pH
Corrosion Chemistry<br />
• In the Headspace H 2 S<br />
Gas is Biologically<br />
Converted to Strong<br />
Sulfuric Acid by<br />
Thiobacillus Bacteria<br />
• This Results in<br />
Corrosion of Sewage<br />
System Infrastructure<br />
Thiobacillus<br />
Acid Attacks<br />
Concrete<br />
H 2 S + O 2 = H 2 SO 4<br />
SO 4<br />
2-<br />
HS - H 2 S
<strong>Magnesium</strong> <strong>Hydroxide</strong> <strong>Slurry</strong><br />
Properties<br />
Properties<br />
Typical*<br />
Mg(OH) 2 Purity, % (dry basis) 98.8<br />
Median particle size, microns 3<br />
Dry solids, % 61.0<br />
Viscosity, cps 200<br />
pH 10.0<br />
* THIOGUARD ® <strong>Magnesium</strong> <strong>Hydroxide</strong> <strong>Slurry</strong>
How Does <strong>Magnesium</strong> <strong>Hydroxide</strong><br />
• Mg(OH) 2 Raises the<br />
Wastewater pH to 8.0-<br />
8.5<br />
Resulting In:<br />
Reduced Efficiency<br />
of SRB and Less<br />
Sulfide Production<br />
Reduced or<br />
Elimination of H 2 S<br />
Gas Production<br />
Reduced Corrosion<br />
Rate of Sewer Pipes<br />
<strong>Slurry</strong> Work<br />
H 2 S (aq) and HS - in solution (mg/L)<br />
6.00<br />
5.00<br />
4.00<br />
3.00<br />
2.00<br />
1.00<br />
H 2 S (g)<br />
H 2 S (aq)<br />
HS -<br />
0.00<br />
0<br />
3 4 5 6 7 8 9 10<br />
pH<br />
1200<br />
1000<br />
800<br />
600<br />
400<br />
200<br />
H2S (g) in air (ppm)
<strong>Magnesium</strong> <strong>Hydroxide</strong> <strong>Slurry</strong><br />
Benefits<br />
• Prevents Formation of H 2 S Odor & Corrosion in<br />
Municipal Collection Systems<br />
• Extends Life of Sewer System<br />
• Reduces FOG<br />
• Mg(OH) 2 Dosage Is Not Dependent On Sulfide<br />
Concentration
FOG (Fats, Oils & Grease)<br />
Be<strong>for</strong>e Mg(OH) 2 ….
After Mg(OH) 2
<strong>Magnesium</strong> <strong>Hydroxide</strong> <strong>Slurry</strong><br />
Additional Benefits<br />
• Due to pH Buffering Ability of Mg(OH) 2 , Less<br />
Feed Points Are Required<br />
• No Sludge Is Formed As With Iron Salts<br />
• Non-Hazardous and Non-Corrosive<br />
• Improves Downstream Wastewater Treatment<br />
Operations
Biological<br />
Biological<br />
Treatment<br />
Treatment<br />
Secondary<br />
Secondary<br />
Clarifier<br />
Clarifier<br />
Digestion<br />
Digestion<br />
Effluent<br />
Effluent<br />
Conditioning<br />
Dewatering<br />
Conditioning<br />
Conditioning<br />
Dewatering<br />
Dewatering<br />
Primary<br />
Primary<br />
Treatment<br />
Treatment<br />
Collection<br />
Collection<br />
System<br />
System<br />
Disinfection<br />
Disinfection<br />
Biological<br />
Biological<br />
Treatment<br />
Treatment<br />
Primary<br />
Treatment<br />
Conditioning<br />
Dewatering<br />
Biosolids<br />
Conditioning<br />
Conditioning<br />
Dewatering<br />
Dewatering<br />
Biosolids<br />
Biosolids<br />
Digestion<br />
Digestion<br />
Secondary<br />
Secondary<br />
Clarifier<br />
Clarifier<br />
Collection<br />
Collection<br />
System<br />
System<br />
Effluent<br />
Effluent<br />
Disinfection<br />
Disinfection<br />
Total System Treatment<br />
Benefits<br />
Mg(OH) 2<br />
<strong>Slurry</strong>
Case Study: Canton, OH<br />
• Using Mg(OH) 2 at Stark County (Canton, OH)<br />
–High H 2 S at Plum Street Manhole in Waynesburg, OH<br />
– Inject 2 Miles Upstream in Magnolia Wetwell<br />
Injected Tg<br />
H 2 S Reduction<br />
Lowered<br />
Feed Rate
Case Study: Summit County, OH<br />
Begin Tg Feed<br />
Intentionally Terminate Tg Feed
Case Study: Akron, OH<br />
Started feeding<br />
Thioguard at 2:15pm<br />
4-18-06<br />
Start Seeing Effects<br />
of Thioguard<br />
Addition
Case Study: Lagrange, IN<br />
350<br />
300<br />
Injected Tg<br />
Hourly Average<br />
Hourly Maximum<br />
250<br />
H2S PPM at LS #6<br />
200<br />
150<br />
Terminated Tg<br />
100<br />
50<br />
0<br />
5/14/07 0:00 5/16/07 0:00 5/18/07 0:00 5/20/07 0:00 5/22/07 0:00 5/24/07 0:00 5/26/07 0:00
Case Study: Steuben Lakes, IN<br />
80<br />
70<br />
THIOGUARD<br />
Feed Starts<br />
H2S PPM<br />
60<br />
50<br />
40<br />
Start Seeing<br />
THIOGUARD<br />
Effects Here<br />
Hourly Maximum<br />
Hourly Average<br />
30<br />
20<br />
10<br />
0<br />
2/27/2007 2/28/2007 2/28/2007 3/1/2007 3/1/2007 3/2/2007 3/2/2007 3/3/2007 3/3/2007 3/4/2007 3/4/2007 3/5/2007
Mg(OH) 2 <strong>Slurry</strong> Handling<br />
• <strong>Slurry</strong> Requires Periodic Agitation to Keep<br />
Solids in Suspension<br />
• Maintain Minimum Line Velocity Through<br />
Feed Lines<br />
• Recommend Peristaltic or Progressive Cavity<br />
Pumps <strong>for</strong> Metering<br />
• With 0 o C Freezing Point, Need Freeze<br />
Protection On Equipment
Mg(OH) 2 <strong>Slurry</strong> Equipment<br />
• Bulk Storage and Feed System<br />
– 2500-Gallon Tank<br />
With Heat Pads<br />
– Peristaltic Feed<br />
With VFD<br />
– Control Panel<br />
With Power and<br />
Control Signal<br />
Connections
Mg(OH) 2 <strong>Slurry</strong> Equipment<br />
• Tote Storage and Feed<br />
System<br />
• Agitator<br />
• 275-Gallon Day Tank<br />
• Control Panel<br />
• Flow Meter<br />
• Air-Driven Transfer<br />
Pump<br />
• Progressive Cavity Feed<br />
Pump
Compared To Other Treatment Options<br />
<strong>Magnesium</strong> <strong>Hydroxide</strong> <strong>Slurry</strong> Is…<br />
• Less Expensive, Particularly At High Sulfide<br />
Concentrations<br />
• More <strong>Effective</strong> For Odor and Corrosion Control<br />
• Non-Hazardous and Non-Corrosive<br />
• Can be Used System-Wide<br />
• Solves More Problems
Thank You.<br />
Any Questions