CO2 for pH Control

Using CO₂ for alkalinity control in cooling towers is effective, and in many cases, cost-competitive with acid feed (especially sulfuric).

 

Feature

CO₂

Sulfuric Acid

Cost

Higher

Lower

Corrosion risk

Low

High (can cause localized corrosion)

Safety

Safer (non-hazardous gas)

Hazardous, requires PPE and containment

pH control

Smooth, buffered

Easy to overshoot, sharp pH drops

Equipment

Needs gas handling, injectors

Needs acid tanks, pumps, safety systems

Environmental

No acid discharges

May require permits and spill containment

 

 

 

  1. How CO₂ Works in Cooling Towers
  2. CO₂ dissolves in water to form carbonic acid:
  3. CO₂ + H₂O → H₂CO₃ → H⁺ + HCO₃⁻
  4. This mild acid lowers pH and consumes alkalinity, similar to sulfuric acid, but with softer chemistry.
    1. You’re essentially rebalancing the carbonate system rather than adding strong mineral acids.
  5. Effectiveness
    1. Lowers pH effectively to the target range (usually 8.2–8.5)
    2. Reduces M-alkalinity over time by shifting carbonate equilibrium
    3. Reduces scale formation: Less carbonate = less CaCO₃ scaling
    4. Non-corrosive feed: Unlike sulfuric acid, CO₂ gas won’t cause localized corrosion or acid burns
    5. Self-buffering: Much harder to overshoot pH, making it safer
  1. Especially useful where alkalinity and calcium are both high, and you need to reduce scaling risk without over-acidifying.
  1. Cost Effectiveness

Typical Cost Comparison (US, 2024–2025 ballpark)

Chemical

Cost (delivered)

Notes

CO₂ (gas)

~$100–150/ton

Varies by volume, storage setup

Sulfuric Acid (93%)

~$150–200/ton

Cheaper per ton but more dangerous and corrosive

  1. Sulfuric acid is 50% to 66% less expensive than H2SO4 strictly on a chemical cost basis.
    1. But CO₂ is much safer, reduces corrosion risk, and provides gentler, self-buffering pH control.
    2. CO₂ becomes competitive:
  1. Where safety is a top concern
  2. In sensitive systems (e.g., stainless or aluminum components)
  • If operational downtime or acid handling costs are significant
  1. Efficiency Considerations
    1. CO₂ has lower acid strength per pound, so:
    2. You need more CO₂ by weight to neutralize the same amount of alkalinity
    3. But you reduce risks, corrosion, and handling costs
    4. Savings in safety, maintenance, and corrosion protection can offset higher volume requirements

 

  1. System Requirements
    1. CO₂ storage tank (bulk or cylinders)
    2. Gas flow control and injection system
    3. Often integrated with pH automation
  1. Initial capex is higher than sulfuric, but long-term OPEX + safety + maintenance costs can be better.
  1. When CO₂ is Most Cost-Effective
    1. High cycles → high pH/alkalinity → more acid demand
    2. Sites with strict safety regulations or acid-handling restrictions
    3. Systems prone to acid overdosing or corrosion
    4. Facilities with onsite CO₂ generation (e.g., breweries, food plants)
  1. CO₂ vs. Sulfuric Acid — Quick Comparison

Feature

CO₂

Sulfuric Acid

pH control

Gentle, buffered

Strong, sharp drops

Alkalinity removal

Effective (slower)

Fast, aggressive

Corrosiveness

Non-corrosive

Highly corrosive

Safety

Safer to handle

Hazmat precautions

Cost per unit

Higher

Lower

Control accuracy

Easier to fine-tune

Easier to overshoot

  1. CO₂ is very effective at reducing alkalinity and controlling pH gently
  2. Cost-effective in systems with:
    1. High cycles
    2. High alkalinity
    3. Safety or corrosion concerns
  3. Not always cheapest up front, but safer and often cheaper long term
  4. Best suited for systems where precision and non-corrosiveness matter
  1. Example Based on PHX 15 Make Up Water

Parameter

Value

pH

17.  7.69

M-Alkalinity

18.  156 ppm as CaCO₃

Target Cycles

19.  5

Target Tower pH

20.  ~8.4–8.5 (natural drift)

Target pH w/ CO₂

21.  ~8.2–8.3

  1. Let’s assume your goal is to:
  1. Reduce M-alkalinity in tower water from ~780 ppm (5× makeup) to ~500 ppm
  2. Lower pH from ~8.5 to ~8.2
  1.  
  2.  
  3. Chemical Demand Calculations
    1. CO₂
      1. 1 ppm alkalinity (CaCO₃) needs ≈ 0.88 ppm CO₂
    2. Sulfuric Acid (H₂SO₄, 92%)
      1. 1 ppm alkalinity (CaCO₃) ≈ 0.49 ppm 92% H₂SO₄