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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

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