Direct Addition for Odor Control
Magnesia chemicals are safe. They offer environmentally responsible solutions to problems related with acid neutralization, biological treatment and biosolids disposal and handling. Premier Chemicals produces over 300,000 tons of MgO and Mg(OH)2 products annually, developing and maintaining more grades of magnesia chemicals than any other producer.
Premier Chemicals is proud to offer the
Major Advantages
- Non-Hazardous
- Safe to Handle
- Environmentally safe
- Cost-effective
- Treats Odors, Corrosion and FOG (fats, oils, and grease)
- Positive plant benefits for Nitrification, biosolids production, digestor performance and chlorination
Direct Addition for Odor Control
Added directly to wastewater collection systems,
Crown Spray for Corrosion Control
Surfaces periodically sprayed with
Surface pH/Corrosion
H2S gas generated in the sewer system is converted by Thiobacillus bacteria residing on concrete and metal surfaces above the waterline to corrosive sulfuric acid. This acid attacks exposed concrete and metal surfaces.
A simple method to measure relative strength of the sulfuric acid and rate of decay of the infrastructure is surface pH testing, conducted with contact pH paper on the wetted surfaces inside wetwells, manholes and sewer lines.
The measured surface pH can then be used to correlate corrosion rate and subsequently, remaining years of useful life of a concrete structure.
The use of
Under some circumstances,
When
3 Distinct Phases make it unique among its alkaline peers, and highly suited to biological treatment systems
Phase I (Mg(OH)2):
Magnesium hydroxide as a particle has a solubility of 9 mg/L. While the solubility is considered relatively low, the particle, having a surface area of nearly 1 acre per gallon, is reactive and/or absorptive to acids, H2S, CO2, and some organics. The particle has a positive surface potential and is capable of improving flocculation and settling. In the collection system, it slowly dissolves as it reacts with H2S, CO2, acids, FOG, etc… At the plant, it usually enters the biosolids stream through Primary settling. That which passes through to Secondary processing is typically fully consumed by biogenic acids and CO2 produced during secondary treatment.
Phase II (MgOH+ + OH-):
This ionic phase is transitional from the particle phase to soluble phase and is indicative of magnesium hydroxide’s unique abilities to "buffer" both acids and bases. This species also explains why pH’s in a magnesium hydroxide supplemented stream do not accurately reflect the total amount of hydroxide present (neutralizing capability), since only the first ionized OH- contributes to the pH values. This is why pH, OH- and total alkalinity are critical measurements collectively rather than individually.
Phase III (Mg+2 + 2OH-):
This ionic phase is the result of complete dissolution of the Mg(OH)2 molecule. Complete dissolution occurs as a result of free proton (H+) acid neutralization or the formation of bicarbonate (HCO3-) from the reaction of OH- with CO2. Once dissociated, the divalent magnesium cation (Mg+2) aids wastewater treatment by 1) being utilized as a bridging particle for improved flocculation, settling and clarification in both Primaries and Secondaries and improved dewatering and densification in bio-solids processing 2) facilitating the transport and stabilization of P during ADP/ATP conversion and ATP hydrolysis, and 3) supplementing biological nutrients.
Residual OH- is reflected in pH readings. Since the reactive pH is 9, it "buffers" strongly in the pH range between pH 8 and 9, and most preferably near 8.4. As pH rises, magnesium shifts back towards Phases I and II. This is how magnesium hydroxide is extracted from brines and seawater for commercial production.

Odor Control
Odors occur when wastewater pH allows (H2S) hydrogen sulfide to evolve from liquid phase hydrosulfide (HS-).
First, sulfate reducing bacteria operate best at pH levels 6.8 to 7.2. Above this ideal pH range, less sulfide is produced and SRB growth rate is stunted.
so less sulfide is generated.
Second, H2S formation is extremely sensitive to pH. At pH levels < 7.0, the equilibrium reaction favors hydrogen sulfide (H2S) and odorous gas evolution. At pH > 7.0, the reaction favors hydrosulfide, (HS-).
Unlike other alkali choices,
Since
Treatment Plants
Direct addition of
- Odor Control
- Corrosion Control
- Nutrient Addition — Essential Element for Cell Metabolism
- Alkalinity Supplementation
- pH Control
Nitrogen compounds are the primary cause of pH/alkalinity degradation in treatment plants, with pH depletion being the major cause of activated sludge bulking, high SVI (Sludge Volume Index), and disinfection problems.
Digestion, Nitrification, Alkalinity and pH Control
Aerobic digestion and nitrification in the activated sludge process depletes natural alkalinity and can cause pH depression. A drop in pH can arrest second-stage nitrification and cause major upset conditions in the secondary clarifiers, resulting in effluent violations for BOD, TSS (Total Suspended Solids), ammonia, etc...Likewise, adequate alkalinity insures biological process stability and improves methane gas production of anaerobic digesters.
Secondary Clarifiers and SVI
Periodic pH problems interfere with the growth of floc-forming activated sludge. When this happens, sludge bulking and unwanted denitrification may cause SVI levels to increase.

Biosolids
These divalent cations and pH stability provided by
Chorine Disinfection
Incomplete nitrification allows nitrite (NO2-N) to pass through the clarifiers and into the chlorine contact tank, consuming chlorine at accelerated rates. Moreover, low pH and inadequate alkalinity can hinder rapid hydrolysis of Cl2 gas, reducing disinfection efficiency.
pH Control
Magnesium hydroxide slurry has long been used to maintain pH during nitrification. Because alkalinity is released slowly, there are no hot spots to kill Nitrosomonas or Nitrobacter bacteria.
And since the by-products of magnesium hydroxide reactions are soluble salts,
Summary
As sulfide levels have increased, many chemical options become ineffective or too costly.
The comparisons presented between
Selection of an appropriate odor control strategy is a complex process that must consider many factors. We believe