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Wet Scrubbers Do Not Remove Every Pollutant

Industrial wet scrubber tower during on-site installation and commissioning for industrial air pollution control and chemical gas treatment applications.

Wet scrubbers are often assumed to remove virtually any pollutant in industrial air pollution control — a belief that is both widespread and dangerous.

“If there is a wet scrubber, the pollutant will be removed.”

That is not how it works.

A wet scrubber is not a universal machine.
It is a gas–liquid mass transfer system.

And that means something very simple:

if the pollutant is not compatible with the physical or chemical absorption mechanism, the scrubber cannot operate effectively, regardless of its size.

The biggest misconception: gas-liquid contact does not automatically mean removal

Many systems are designed around a flawed assumption:

  • there is a tower,
  • there is water,
  • there is recirculation,
  • therefore the problem is solved.

In reality, a scrubber does not generically “capture” molecules.
A wet scrubber only works if at least one of the following conditions exists:

  • the pollutant is soluble in the liquid;
  • the pollutant chemically reacts in the liquid phase;
  • the pollutant is associated with particulate or aerosols that can be intercepted;
  • thermodynamic conditions favor mass transfer.

If these conditions do not exist, the contaminant simply passes through the system.

Some pollutants are naturally treatable

Compounds such as:

have properties that allow:

  • dissolution,
  • neutralization,
  • oxidation,
  • relatively efficient absorption.

In these cases, wet scrubbers can achieve very high removal efficiencies.
But that does not mean the same approach works for every contaminant.

VOCs: the reality is far more complex

Many volatile organic compounds (VOCs) have:

  • low solubility,
  • hydrophobic behavior,
  • high volatility,
  • unfavorable absorption kinetics.

In practical terms:

simple contact with water is often insufficient.

Yet it is still common to see scrubbers designed as if every VOC could simply be “washed out.”

It cannot.

Some solvents pass through the tower almost unaffected.
Others require:

  • specific reagents,
  • oxidation stages,
  • contact times incompatible with real tower geometry,
  • or completely different technologies.

Methane cannot be “scrubbed” either

Methane is one of the clearest examples.
It has:

  • extremely low solubility,
  • high chemical stability,
  • virtually no useful reactivity in conventional wet scrubbers.

For this reason:

methane is not treated effectively with traditional wet scrubbers or biofilters.

It must either be oxidized, diluted, or managed through completely different process strategies.

Believing that methane can be removed simply by increasing water flow or chemical dosage means misunderstanding the physics of the process itself.

Chemistry matters more than the machine

wet scrubber internal

One of the most common mistakes in air pollution control is treating the scrubber as a standardized product.

In reality:

pollutant chemistry comes before equipment selection.

Without understanding:

  • speciation,
  • actual concentrations,
  • temperature,
  • humidity,
  • aerosol presence,
  • process variability,

it is impossible to determine:

  • whether a scrubber will work,
  • which chemistry should be used,
  • what liquid-to-gas ratio is required,
  • what pressure drop is necessary,
  • or whether the selected technology is fundamentally wrong.

A scrubber does not create selectivity out of nowhere

Another common misconception is that adding:

  • more stages,
  • more chemicals,
  • more recirculation,
  • more complexity,

automatically allows treatment of any emission stream.

But no system truly “sorts” molecules.

Every compound has:

  • its own solubility,
  • its own kinetics,
  • its own chemical behavior,
  • its own equilibrium conditions.

Inside real industrial gas mixtures:

  • some pollutants are absorbed,
  • others pass through,
  • others interfere with each other.

This is why truly effective systems are not built from standard catalogs, but from a deep understanding of the upstream industrial process generating the emissions.

The real goal: designing around the machine instead of the process

Most failures originate here.
First, the equipment is selected:

  • “a scrubber,”
  • often because it is available,
  • inexpensive,
  • or already used elsewhere.

Only afterwards does the engineering attempt to adapt it to the actual pollutants.

But the correct sequence is the opposite:

  • understand the industrial process;
  • identify the pollutants;
  • understand their physical and chemical behavior;
  • only then design the treatment system.

Conclusion

Wet scrubbers can be extremely effective technologies.

But only when:

  • the contaminant is compatible with the absorption mechanism,
  • the chemistry is correct,
  • mass transfer conditions are realistic,
  • and the system is designed around actual operating conditions.

because:

A scrubber does not remove “everything.”
Removing a pollutant first requires understanding it.

Industrial wet scrubber installation with quote about pollutant removal and process understanding, featuring a polypropylene scrubber tower during field assembly and maintenance.

Related Case Studies

  • |

    Air Pollution and Odour Control for Category 3 Animal By-Products Processing

    Technical summary

    Flow rate: 8,000 m³/h
    Industry: Animal by-product ABP transformation
    Technology: 1 Acidic + 1 Alkali/oxidative PC-1 single staged scrubbers
    Target pollutans: Odour, ammonia, VOC
    Process air temperature: 80°C

    Read More “Air Pollution and Odour Control for Category 3 Animal By-Products Processing”
  • | |

    Why Your Ammonia Scrubber Is Not Working

    On paper, ammonia removal with a wet scrubber looks simple.
    Add acid. Control pH. Remove NH₃.

    In reality, many industrial scrubbers fail to remove ammonia consistently — even when all “parameters” seem correct.

    If your ammonia scrubber is not working, the problem is rarely a single variable.
    It is almost always a process issue, not a component issue.

    The Real Problem

    Ammonia absorption is not just a chemical reaction.
    It is a mass transfer process limited by:

    You don’t have “a pH”.

    Most scrubbers fail because they are designed as equipment, not as process systems.

    Why It Happens

    1. pH control is not enough

    Lowering pH shifts ammonia (NH₃) into ammonium (NH₄⁺), which is soluble.

    But:

    • local pH ≠ bulk pH
    • poor mixing creates zones where ammonia is not absorbed

    You don’t have “a single pH value”.
    You have a distribution of pH conditions inside the tower.

    2. L/G Ratio Is Too Low

    Ammonia absorption requires sufficient liquid flow.

    If the liquid-to-gas ratio (L/G) is too low:

    • contact area is reduced
    • absorption capacity is limited

    Typical failure:

    Scrubber sized on airflow only → insufficient liquid phase

    3. Poor Liquid Distribution

    Even with correct flow rate:

    • uneven spray
    • asymmetric piping
    • clogged nozzles

    create preferential paths.

    poor liquid distribution in wet scrubber nozzle spray pattern
    • Gas bypasses the liquid
    • Efficiency collapses

    This is one of the most underestimated causes of failure.

    4. Buffering Systems in the Liquid

    This is where most engineers get it wrong.

    In real systems:

    • carbonates
    • bicarbonates
    • ammonium salts

    create buffer systems

    Result:

    • pH does not drop as expected
    • acid consumption increases
    • ammonia removal becomes unstable

    The problem is not dosing.

    The problem is chemistry equilibrium.

    5. Insufficient Contact Time

    Short towers, high velocity, or undersized packing:

    • reduce residence time
    • limit absorption

    Ammonia removal is not instantaneous

    It requires time + interface

    6. Gas Conditions Are Ignored

    Temperature and saturation matter.

    • hot air reduces solubility
    • low humidity limits absorption
    • low humidity limits absorption

    A scrubber designed for “nominal conditions” will fail in real operation.

    What Most Engineers Get Wrong

    • Designing based only on airflow
    • Assuming pH = performance
    • Ignoring liquid distribution
    • Treating ammonia as a “simple pollutant”
    • Oversimplifying chemistry

    What Actually Works

    An ammonia scrubber works when:

    • L/G ratio is correctly sized
    • liquid distribution is uniform
    • pH is controlled considering buffering systems
    • contact time is sufficient
    • process variability is included in design

    This is not about adding more acid.
    It is about designing the system as a whole.

    When the System Cannot Work

    There are cases where:

    • tower is undersized
    • gas load is too high
    • variability exceeds design limits

    In these situations:

    • no adjustment will fix the problem
    • only a redesign or revamping will

    Can an Existing Scrubber Be Fixed?

    Sometimes, yes.

    Typical interventions:

    • increase liquid recirculation
    • redesign distribution system
    • introduce a second stage
    • modify chemical control strategy

    But:

    • not all systems are recoverable
    • and not all problems are “operational”

    Final Insight

    Ammonia removal is not difficult.

    But stable ammonia removal in real industrial conditions is.

    Is your ammonia scrubber underperforming?

    Contact us for a technical evaluation
  • |

    Odour Control for Biological Sludge Composting

    Technical summary

    Flow rate: 88,000 m³/h
    Industry: Biological sludge composting (municipal wastewater sludge + green waste)
    Technology: Multiventuri scrubber + two-stage packed column scrubber (acid + alkaline/oxidative)
    Target pollutants: Odour, ammonia, hydrogen sulphide, VOC
    Process air condition: Intermittent emissions with high odour load during loading/unloading phases

    Process-driven design for intermittent high-load emissions (88,000 Nm³/h)

    Application context

    Odour Control for Biological Sludge Composting requires a clear understanding of how emissions are generated during the composting of municipal wastewater biological sludge mixed with green waste.

    The plant treats approximately 88,000 Nm³/h of extracted air from:

    • Sludge unloading areas
    • Mixing and structuring phases
    • Composting tunnels
    • Mechanical handling operations

    The composting objective is to stabilise organic matter and produce agronomically valorisable compost through controlled aerobic degradation.

    When properly managed, composting itself does not necessarily generate severe continuous odour levels. The dominant issue lies elsewhere.

    Intermittent peak emissions during sludge unloading

    In biological sludge composting, emissions are predominantly intermittent rather than continuous.

    The highest odour peaks occur during:

    • Sludge unloading
    • Initial mixing with structuring green waste
    • Mechanical agitation of fresh material

    Fresh biological sludge may contain anaerobic microenvironments formed during storage and transport. When exposed to oxygen during unloading, rapid release occurs of:

    • Ammonia (NH₃)
    • Hydrogen sulphide (H₂S)
    • Reduced sulphur compounds
    • Volatile organic compounds
    • High humidity and bioaerosols

    Designing Odour Control for Biological Sludge Composting based on average conditions would underestimate these peak events.

    Engineering challenge at 88,000 Nm³/h

    The system had to manage:

    • High ammonia concentrations
    • Hydrogen sulphide spikes
    • Variable aerosol loads
    • Near-saturated humidity
    • Short-duration high-intensity emission events

    The primary design parameter was therefore peak load management, not nominal airflow alone.

    Multiventuri pre-conditioning stage

    Multiventuri scrubber for Air Pollution and Odour Control in biological sludge composting plant showing independent venturi stages and recirculation piping
    Multiventuri stage designed to manage intermittent high-load odour peaks during biological sludge unloading.

    A multiventuri stage was installed upstream of chemical scrubbing as structural gas conditioning.

    In Odour Control for Biological Sludge Composting, this stage provides:

    • Aerosol reduction
    • Gas homogenisation
    • Initial contaminant absorption
    • Peak concentration damping

    By distributing airflow across multiple venturi throats, the system avoids localised overload during unloading events and stabilises downstream chemical treatment.

    Compact dual chemical scrubbing system

    Following pre-conditioning, the gas enters two vertical scrubbers operating in sequence:

    Acid stage

    Dedicated to Ammonia neutralisation.

    Basic-oxidative stage

    Dedicated to hydrogen sulphide and reduced sulphur compound oxidation.

    Separating chemical environments ensures:

    • Stable pH control
    • Independent reagent dosing
    • Controlled reaction kinetics under variable load

    This sequential architecture is central to effective Odour Control for Biological Sludge Composting at high airflow rates.

    Environmental outcome

    The installation was implemented to mitigate odour impact affecting surrounding residential areas.

    By addressing the intermittent and peak-driven nature of emissions, the system achieved stable odour mitigation despite variability in sludge composition and seasonal factors.

    Engineering insight

    In Odour Control for Biological Sludge Composting, understanding the biological origin of emissions is essential.

    The most critical emissions are:

    • Linked to anaerobic-to-aerobic transition
    • Triggered by sludge exposure
    • Concentrated during short operational windows

    Effective treatment at 88,000 Nm³/h requires architecture capable of absorbing shock loads and stabilising highly variable gas streams.

    Process-driven engineering, rather than average-based design, determines performance.

  • |

    Polypropylene Scrubbers: Real Limits in Industrial Applications

    What Are Polypropylene Scrubbers?

    Polypropylene scrubbers are widely used in industrial air pollution control systems due to their excellent chemical resistance and relatively low cost.
    A Polypropylene scrubber is typically used in wet scrubbing applications where corrosive gases, odours or pollutants must be removed from air streams.
    However, in real industrial environments, Polypropylene scrubbers are often selected based only on chemical compatibility. This is where most design mistakes begin.

    Why Polypropylene Scrubbers Are So Common

    The success of scrubbers made in Polypropylene comes from three main factors:

    • High chemical resistance
    • Cost-effectiveness compared to stainless steel
    • Ease of fabrication

    For many standard applications, a polypropylene scrubber is a reliable and efficient solution.

    But this is only part of the story.

    The Real Limit of Polypropylene Scrubbers

    The main limitation of scrubbers made in Polyptopylene is not chemical resistance.

    It is mechanical behaviour under temperature.

    Polypropylene has a high thermal expansion coefficient:

    • 0.15–0.20 mm/m·°C

    In industrial scrubbers, this means that even small temperature variations can generate significant structural movement.

    Thermal Expansion in Polypropylene Scrubbers

    Thermal expansion is often underestimated during design.

    In real operation, it leads to:

    • Misalignment between scrubber and piping
    • Stress on flanges and connections
    • Progressive deformation of the structure
    • Long-term mechanical fatigue

    These effects are not immediate, but they become critical over time.

    In constrained layouts, like long duct runs with fixed supports, thermal expansion cannot dissipate. It accumulates.

    Polypropylene duct in constrained installation showing potential thermal expansion stress in industrial system

    Why Polypropylene Scrubbers Fail in Operation

    When scrubbers made in Polypropylene fail, the cause is rarely chemical.

    Typical failure mechanisms include:

    • Rigid piping connected to the scrubber
    • Lack of expansion compensation
    • Poor mechanical support design
    • Temperature fluctuations not considered

    In many cases, the problem is attributed to installation errors, while the real issue is design-related.

    Polypropylene vs Other Materials

    Polypropylene is often compared with other materials such as HDPE or stainless steel.

    Each material behaves differently:

    • Polypropylene scrubbers → excellent chemical resistance, high thermal expansion
    • HDPE scrubbers → better mechanical resilience, similar expansion issues
    • Stainless steel scrubbers → low expansion, but limited chemical resistance in aggressive environments

    There is no universally “best” material. The correct choice depends on the process conditions.

    When Polypropylene Work Well

    Polypropylene perform reliably when:

    • Temperature varies significantly
    • Large structures are mechanically constrained
    • The system is rigid and over-constrained
    • Long-term dimensional stability is critical

    In these cases, alternative materials or different design approaches should be considered.

    Conclusion: Understanding Polypropylene Scrubbers

    Polypropylene scrubbers are not a bad choice. They are often a misunderstood one.

    The key is not only to evaluate chemical resistance, but to understand how Polypropylene scrubbers behave under real operating conditions.

    In industrial air treatment, material selection is not a chemical decision. It is an engineering decision.

  • | | |

    Scrubber Recirculation Pump Selection

    Why the scrubber recirculation pump is critical

    Choosing the right scrubber recirculation pump is one of the most critical decisions in wet scrubber design.

    • the actual liquid-to-gas ratio (L/G)
    • the stability of the system
    • the effectiveness of mass transfer
    • the long-term behavior under fouling, salts, and process variability

    Most scrubbers do not fail because of incorrect flow rate.
    They fail because the recirculation system becomes unstable over time.
    And the pump is the core of that system.

    Types of scrubber recirculation pumps

    In industrial wet scrubbers, three main types of wet scrubber recirculation pumps are commonly used:

    • Vertical centrifugal pumps in Polypropylene (PP)
    • Horizontal centrifugal pumps in Stainless Steel (AISI 316)
    • Magnetic drive (seal-less) pumps

    These technologies are often treated as interchangeable.
    In reality, they behave very differently under real operating conditions.

    Vertical polypropylene pumps for wet scrubbers

    vertical scrubber recirculation pump operating with solids and foam in industrial wet scrubber tank

    Configuration

    • Vertical shaft, immersed or semi-immersed
    • Wetted parts in polypropylene
    • Seal arrangement depending on pump design

    Advantages

    • Excellent resistance to aggressive chemicals (acids, alkalis, oxidants)
    • No external leakage to the environment, as the pump operates in immersed configuration
    • High tolerance to:
    • Solids
    • sludge
    • salt crystallization

    Limitations

    • Lower hydraulic efficiency
    • Limited head
    • Reduced structural rigidity compared to metal pumps

    Engineering perspective

    Vertical PP pumps are often the most reliable scrubber recirculation pumps in real industrial environments.

    They are not optimized for efficiency, but they are optimized for survival:

    • they tolerate contamination
    • they continue operating with unstable chemistry
    • they do not fail when solids or salts accumulate

    In systems with variable loads and dirty liquids, they are frequently the only pumps still operating after extended periods.

    Stainless steel (AISI 316) recirculation pumps

    ndustrial wet scrubber recirculation pump system with horizontal stainless steel pump and chemical resistant piping

    Configuration

    • Horizontal installation
    • Mechanical seal
    • Stainless steel construction

    Advantages

    • High hydraulic efficiency
    • Higher head capability
    • Strong mechanical structure

    Limitations

    • Mechanical seal is a critical failure point
    • Sensitive to:
    • crystallization
    • suspended solids
    • intermittent operation
    • Risk of leakage over time
    • Limited chemical resistance depending on process conditions

    Engineering perspective

    Stainless steel pumps perform well as scrubber recirculation pumps only under controlled conditions:

    • clean liquid
    • stable chemistry
    • predictable operation

    In real scrubber applications:

    • seals degrade
    • deposits form
    • leakage becomes a maintenance issue

    They are efficient, but not inherently robust.

    Magnetic drive pumps in scrubber applications

    Configuration

    • Seal-less design using magnetic coupling
    • No direct mechanical connection between motor and impeller

    Advantages

    • Zero external leakage
    • Suitable for hazardous or toxic fluids
    • Reduced maintenance on seals

    Limitations

    • Not tolerant to solids or particles
    • Sensitive to crystallization
    • Risk of overheating or magnetic decoupling
    • Higher cost

    Engineering perspective

    Magnetic drive pumps are often selected as scrubber recirculation pumps for safety reasons.
    However, they require:

    • clean fluids
    • stable operating conditions
    • controlled chemistry

    These conditions are rarely guaranteed in industrial scrubbers.

    When solids, salts, or variability are present, magnetic drive pumps tend to become unstable or fail.

    Which scrubber recirculation pump is best?

    The best scrubber recirculation pump is not the most efficient one.

    It is the one that:

    • tolerates solids
    • handles salt accumulation
    • remains stable under variable conditions

    In most real scrubber systems, this leads to a clear conclusion:

    Vertical polypropylene pumps provide the highest operational robustness.

    How to choose the right scrubber recirculation pump

    Choose a vertical PP pump if:

    • solids are present
    • salt buildup is expected
    • operating conditions are variable

    Choose a stainless steel pump if:

    • the liquid is “clean”
    • higher head is required
    • maintenance can be managed

    Choose a magnetic drive pump if:

    • zero leakage is mandatory
    • the fluid is “clean”
    • operating conditions are stable

    Common mistakes in scrubber pump selection

    A frequent error in selecting a scrubber recirculation pump is focusing on:

    • efficiency
    • brand
    • initial cost

    Instead of:

    • process variability
    • fouling potential
    • long-term operation

    Most articles about scrubber recirculation pumps focus on materials and performance curves.

    Very few address what actually matters:

    how the pump behaves when the system is no longer ideal.

    Ignoring this leads to:

    • unstable L/G ratios
    • reduced removal efficiency
    • increased maintenance and downtime

    Conclusion

    A scrubber recirculation pump should not be evaluated based on nominal performance.

    It should be evaluated based on:

    • behavior over time
    • tolerance to real process conditions
    • ability to operate without constant intervention

    The real question is not:

    Which pump is the most efficient?

    but:

    Which pump keeps working when the process stops being ideal?

  • | | |

    Scrubber foam problem: root causes

    Scrubber foam problem: context

    In many industrial wet scrubbing systems, foam formation is often dismissed as a secondary or cosmetic issue. In reality, persistent foam is almost always the visible symptom of a deeper process inconsistency.
    This insight originates from real operational evidence: a recirculation tank completely filled with stable foam, generated during normal plant operation.

    What foam really indicates

    Foam inside a scrubber is not random. It is the result of a combination of physical and chemical conditions:

    • Presence of surfactants or organic compounds
    • High gas velocities and turbulence
    • Unstable liquid chemistry (pH, oxidation state, salinity)
    • Accumulation of reaction by-products

    When these factors align, foam transitions from transient to persistent.
    At that point, it stops being a nuisance and becomes a process variable.

    Why Foam Is a Problem

    The consequences are rarely limited to aesthetics:

    • Loss of effective liquid–gas contact
    • Carryover of droplets and contaminants
    • Unstable pressure drop
    • Reduced mass transfer efficiency
    • Risk of downstream fouling
    • Cavitation of recirculation pump

    In extreme cases, the scrubber continues to operate, but no longer performs its intended function.

    The Typical Reaction (and Why It Fails)

    The most common response is the addition of antifoam agents.
    This approach is appealing because it is immediate and simple.
    However, it rarely addresses the root cause.
    Antifoam acts on the symptom, not on the mechanism that generates foam. As a result:

    • Consumption increases over time
    • Performance becomes inconsistent
    • Operating costs rise without solving the instability

    Engineering Perspective: Treat the Cause, Not the Symptom

    Foam must be interpreted within the broader process context.
    The correct approach requires asking fundamental questions:

    • What compounds are actually present in the gas phase?
    • Is the chemical regime (acid/base/oxidative) coherent with those compounds?
    • Is the liquid recirculation accumulating by-products?
    • Is the hydraulic design promoting local imbalances?

    Only by reconnecting the scrubber to the upstream process can the issue be solved.

    Design Implications

    Persistent foam often reveals deeper design limitations:

    • Systems designed for steady-state conditions operating under variable loads
    • Lack of pollutant speciation during the design phase
    • Oversimplified assumptions about liquid chemistry
    • Inadequate purge and make-up strategies

    In other words, the problem is not the foam itself.
    The problem is that the system was never designed to handle the real process conditions.

    Key Takeway

    A scrubber does not fail when foam appears.

    It fails when foam is treated as an isolated issue.

    Understanding and controlling the origin of the emission is the only way to restore performance.

    Final note

    Visible phenomena in industrial systems are rarely superficial.
    They are signals.
    Ignoring them — or masking them with quick fixes — only delays the real engineering work.