20 – Guide to Significance of Concentration

Stormwater BMP Performance Series
Part 1 of 2

BMP Concentration Performance: Fundamentals, Nutrients, and Detention Systems

Stormwater BMP Performance Series  ·  Part 1: Concentration Fundamentals through Wet Pond Enhancements  ·  Compiled from source slide set


1. BMP Concentration Fundamentals

Source slides: 1, 2, 23, 24  ·  Core principles governing pollutant removal in any BMP

The fundamental premise underlying all BMP performance analysis is that the concentration of a pollutant in the influent stream is the primary driver of how much removal a practice can achieve. This relationship governs evaluation, permitting, and comparison of BMPs across every technology type — from simple swales to engineered media filters.

Influent Concentration as the Governing Variable

A BMP can only remove what is present in the water flowing into it. When influent concentrations are high, there is a large gradient available to drive removal processes — physical settling, biological uptake, chemical adsorption — and percentage removal rates appear strong. As influent concentrations decline toward background or irreducible levels, those same processes slow and eventual removal approaches zero regardless of the BMP design.

Core Principle

Removal rate decreases as influent concentration decreases. A BMP that achieves 70% removal at high influent concentrations may achieve 20% or less when treating already-clean runoff. Comparing BMPs by percentage removal without controlling for influent concentration produces misleading conclusions.

Minimum Achievable (Irreducible) Concentrations

Every BMP has a minimum achievable effluent concentration — sometimes called the irreducible minimum — below which it cannot reduce pollutant levels regardless of hydraulic residence time, media depth, or plant density. This floor concentration reflects the equilibrium between removal processes and internal pollutant sources within the BMP itself (sediment release, biological cycling, desorption). Understanding these floors is essential to setting realistic water quality targets and to avoiding over-design.

Design Implication

When an influent concentration is already at or near a BMP’s irreducible minimum, adding that BMP to a treatment train provides negligible benefit and may represent inefficient use of land or capital. Site-specific influent data must be evaluated against published irreducible minima before selecting a BMP.

First-Order Rate Kinetics

Pollutant removal in most BMPs follows first-order rate kinetics — the rate of removal at any given moment is proportional to the concentration remaining. This mathematical relationship has several important practical consequences:

  • Each successive unit of hydraulic residence time removes a smaller absolute mass of pollutant than the previous unit.
  • Diminishing returns set in rapidly once concentrations approach the irreducible minimum.
  • Doubling detention time does not double pollutant removal — the gain narrows exponentially.
  • Stacking multiple BMPs in series (treatment trains) is generally more effective per unit cost than enlarging a single BMP once its removal efficiency plateaus.

Field Data Requirements for Approval and Permitting

Because laboratory and modeled removal rates frequently differ from field performance, regulatory frameworks commonly require field-validated concentration data before a BMP design can be approved or credited toward a stormwater permit. This requirement reflects:

  • The dependence of removal on site-specific influent concentrations that cannot be assumed from generic land-use data alone.
  • The need to verify that irreducible minima claimed by manufacturers or researchers are achievable under actual operating conditions.
  • Recognition that BMP performance degrades over time with sediment accumulation, vegetative changes, and seasonal variation — making point-in-time lab results insufficient.

Regulatory Note

Field monitoring data collected from multiple storm events across a range of antecedent conditions is the standard for establishing a BMP’s performance curve. Single-event or dry-weather grab samples are not adequate substitutes for this dataset.


2. Residential Runoff Concentrations

Source slides: 3, 4, 5  ·  Characterizing nutrient loads from residential land uses and drainage system type

Residential catchments deliver a wide range of nutrient concentrations to stormwater systems depending on the drainage infrastructure used, irrigation practices, and whether reclaimed water is applied to lawns. Understanding these differences is critical for sizing BMPs correctly and for anticipating when regulatory requirements may create conflicts with water reuse programs.

Swale vs. Curb-and-Gutter Drainage

The type of roadside drainage used in a residential subdivision significantly affects the nutrient concentration of runoff reaching any downstream pond or BMP. Swale-drained streets consistently produce runoff with lower phosphorus and nitrogen concentrations than curb-and-gutter systems serving comparable residential densities.

Swale Drainage

Lower P & N

Infiltration and biological uptake along swale length act as distributed pretreatment before runoff enters the pond system.

Curb & Gutter

Higher P & N

Rapid conveyance bypasses natural attenuation; full nutrient load from impervious surfaces reaches downstream BMPs without pretreatment.

This difference makes swales a form of passive pretreatment for downstream wet ponds and other BMPs. Developments that transition from curb-and-gutter to swale drainage during design can reduce the required treatment volume in downstream detention facilities, potentially lowering project costs while improving receiving water quality.

Effect of Reclaimed Water Irrigation

Reclaimed (reuse) water applied to residential lawns for irrigation contains residual nutrients — particularly nitrogen — from the wastewater treatment process. When this water runs off or percolates through soil and enters stormwater systems, it elevates the nutrient concentration of pond discharge above levels achievable from potable-water-irrigated or non-irrigated landscapes.

Regulatory Conflict

Elevated pond discharge concentrations driven by reuse irrigation can push a project’s stormwater BMP out of compliance with Stormwater Rule nutrient reduction requirements — even when the BMP is functioning correctly. This creates a direct conflict between water reuse mandates and stormwater quality regulations that must be resolved at the project or regulatory level before construction.

Projects relying on reuse irrigation should quantify the nutrient contribution from reclaimed water, incorporate that loading into pond sizing and BMP selection, and engage regulatory agencies early to determine whether credits, variances, or alternative compliance pathways are available. Floating wetland enhancements (discussed in Section 5) are among the options considered for reuse-impacted ponds.


3. Phosphorus and Nitrogen Species Fate

Source slides: 6, 7  ·  Removeable and non-removeable fractions of total phosphorus and total nitrogen

Total phosphorus (TP) and total nitrogen (TN) are each composed of multiple chemical species that behave very differently in a BMP environment. Understanding which fractions are amenable to removal — and which are not — sets realistic expectations for maximum achievable performance and explains why published removal efficiencies vary widely across studies.

Phosphorus Species Fractions

Approximately 70% of the total phosphorus in typical stormwater runoff is potentially removeable through conventional BMP mechanisms. The removeable fraction consists of:

  • Soluble reactive phosphorus (SRP) — inorganic ortho-phosphate available for biological uptake by algae and macrophytes, and for chemical adsorption to soils, media, and sediments.
  • Particulate phosphorus — phosphorus bound to suspended sediment or organic particles, removeable by gravitational settling or filtration.

The remaining ~30% is dissolved organic phosphorus — bound within organic molecules that are highly resistant to settling, adsorption, and direct biological uptake. Removal of dissolved organic phosphorus requires long biological detention times during which microbial mineralization can slowly convert it to reactive inorganic forms. In most practical BMP designs, this fraction passes through largely unchanged, establishing the ceiling on TP removal at approximately 60%.

Maximum TP Removal — Practical Ceiling

~60% of influent TP, assuming full removal of SRP and particulate fractions and negligible removal of dissolved organic P. Claims exceeding this ceiling in field conditions warrant careful scrutiny of influent characterization methods.

Nitrogen Species Fractions

Total nitrogen is more chemically complex than phosphorus. Approximately 48% of TN is potentially removeable through standard BMP processes. The removeable fraction includes:

  • Ammonia-N — directly available for biological uptake by plants and microorganisms; also removed by nitrification in aerobic zones.
  • Nitrate and nitrite (NOx-N) — removed via denitrification in anoxic zones (e.g., submerged sediments in wet ponds and wetlands) and by plant uptake.
  • Particulate nitrogen — nitrogen attached to settleable particles, removed by sedimentation.

The remaining ~52% is dissolved organic nitrogen — complex organic molecules including humic substances, proteins, and amino acids. Like dissolved organic phosphorus, this fraction is highly resistant to rapid removal. Long biological detention times enable slow microbial mineralization, but in typical BMP hydraulic residence times this fraction largely exits in the effluent. The practical ceiling for TN removal is approximately 40–50%.

Maximum TN Removal — Practical Ceiling

~40–50% of influent TN, assuming full removal of inorganic N and particulate N fractions. The dissolved organic N fraction persists through most BMP designs. Extended wetland detention offers the best available pathway for marginal additional removal.

Design Implication

When stormwater regulations set TN or TP reduction targets above these practical ceilings, compliance cannot be achieved through BMP selection alone. Source controls reducing organic nitrogen and phosphorus contributions — fertilizer management, pet waste programs, organic debris removal — must be combined with structural BMPs to approach or exceed the removeable fraction limits.


4. Wet Detention Pond Performance

Source slides: 8, 9, 10, 11, 12  ·  Removal mechanisms, residence time relationships, and irreducible concentration floors

Wet detention ponds are among the most widely used stormwater BMPs and among the most thoroughly studied. Their performance depends on a combination of physical settling, biological nutrient cycling, and chemical sorption processes — all of which are governed primarily by the hydraulic residence time (HRT) available during and between storm events.

Residence Time and Removal Efficiency

Removal of both nitrogen and phosphorus in wet ponds is a direct function of how long water resides in the permanent pool and extended detention storage above it. Longer residence times allow:

  • Greater gravitational settling of particulate-bound nutrients.
  • More complete biological uptake by phytoplankton, periphyton, and rooted macrophytes.
  • More extensive denitrification in the anoxic sediment layer.
  • Greater sorption of SRP to sediment surfaces.

As residence time increases, each additional unit of detention produces smaller absolute gains in removal — the characteristic diminishing returns of first-order kinetics described in Section 1. Beyond a threshold residence time, the pond approaches its irreducible minimum effluent concentration and further enlargement yields negligible water quality benefit.

Irreducible Minimum Concentrations

Field data from wet detention ponds consistently demonstrate concentration floors below which even well-designed, well-maintained ponds cannot reduce nutrient levels. These floors reflect the equilibrium between removal processes and internal nutrient cycling within the pond ecosystem:

Irreducible TN

350–400 µg/L

Dominated by dissolved organic nitrogen fraction that resists biological processing at typical pond residence times.

Irreducible TP

10–15 µg/L

Residual dissolved organic phosphorus plus internal loading from accumulated sediments under anaerobic conditions.

Reduction Across All Nutrient Species

A well-designed wet detention pond reduces concentrations of all nitrogen and phosphorus species — not just the totals. Monitoring data confirm reductions in:

  • Ammonia-N — through nitrification and plant/algal uptake.
  • Nitrate/nitrite-N — through denitrification in anoxic sediment zones and uptake.
  • Particulate N and P — through gravitational settling.
  • SRP — through biological uptake and sorption to sediments; approaches its own irreducible floor around 10 µg/L.
  • Dissolved organic N and P — partial reduction via slow biological mineralization; the fraction most responsible for irreducible floors.

Inorganic Nutrients Near the Biological Uptake Limit

In ponds approaching their irreducible minima, inorganic nutrient concentrations (ammonia, nitrate, SRP) fall to levels near or at the limit of biological uptake — the minimum concentrations at which aquatic organisms can effectively assimilate nutrients against concentration gradients. Below these thresholds, plants and microorganisms cannot efficiently extract further nutrients from the water column. This biological uptake limit is a hard constraint that applies regardless of the biomass of aquatic plants present in or around the pond.

Multi-Process System

Wet detention pond performance should not be attributed to any single mechanism. Physical settling, biological uptake, nitrification-denitrification, and chemical sorption all contribute. Designs that compromise any of these mechanisms — for example, through inadequate depth for anoxic sediments, or excessive nutrient loading that promotes algal blooms and internal recycling — will underperform relative to the irreducible minima cited above.


5. Wet Pond Enhancements

Source slide: 13  ·  Floating wetland islands and targeted applications for elevated nutrient conditions

Standard wet detention pond design achieves the irreducible minima described in Section 4 under normal residential loading conditions. When influent nutrient concentrations are elevated — due to reuse irrigation, high-density development, or other concentrated sources — enhancements can provide incremental additional removal beyond what the base pond design achieves.

Floating Wetland Islands

Floating wetland islands (FWIs) are buoyant platforms planted with emergent wetland vegetation that root into the water column rather than pond sediments. The plant roots and associated microbial biofilms create an active treatment zone within the open water of the pond. Their documented performance benefit in wet detention applications is approximately:

Incremental TP Reduction

~10%

Additional removal beyond baseline wet pond performance, applicable when influent SRP and inorganic N exceed biological uptake thresholds.

Applicability Thresholds

Floating wetland islands deliver meaningful performance gains only when the concentrations of inorganic nutrients in the pond are sufficient to support active plant uptake. Below the biological uptake limit, plant roots cannot assimilate nutrients efficiently and the incremental removal benefit disappears. Field data have established the following minimum concentration thresholds for FWI effectiveness:

Phosphorus Threshold for FWI Uptake

SRP must exceed 10 µg/L in the pond water column for floating wetland plant uptake to provide meaningful phosphorus removal. At SRP concentrations at or below this threshold — typical of well-performing base ponds — plant uptake becomes negligible and the ~10% incremental benefit is not realized.

Nitrogen Threshold for FWI Uptake

Inorganic nitrogen (ammonia + NOx) must exceed 130 µg/L in the pond water column for floating wetland plant uptake to be effective. Ponds receiving normal residential runoff without reuse supplementation often already approach or fall below this threshold, limiting the utility of FWI additions.

Best-Fit Application Scenarios

Given these threshold constraints, floating wetland islands are most appropriately applied in the following scenarios:

  • Reuse-impacted ponds — where reclaimed water irrigation elevates inorganic N and SRP above the biological uptake thresholds, creating conditions where FWI plant uptake is actively supported.
  • High-density residential or commercial catchments — where runoff carries elevated nutrient concentrations from intensive landscaping, impervious area washoff, or on-site wastewater influence.
  • Ponds with demonstrated nutrient concentrations above thresholds — confirmed by site-specific monitoring rather than assumed from land-use tables.

Caution

Adding floating wetland islands to a pond already operating at or near its irreducible minima (SRP ≤10 µg/L, inorganic N ≤130 µg/L) provides no measurable nutrient removal benefit. In this condition, FWIs are aesthetic amenities only, and should not be credited toward stormwater nutrient reduction compliance without supporting concentration data showing the thresholds are exceeded.


Topic 6: Adsorption Media BMPs

Slides 15–16 · Removal mechanisms, approved media types, and data requirements

How Adsorption Media Remove Nutrients

Adsorption media BMPs work through two physical-chemical mechanisms: adsorption onto solid surfaces and entrapment within the media matrix. As stormwater passes through or over the media, dissolved phosphorus and other nutrients bind to active sites on the media surface. This process is fundamentally different from biological uptake — no living organisms are required for the basic adsorption reaction, though biological communities may enhance performance in some media types.

Core Principle

Sorption is concentration-dependent. Media actively remove nutrients only when influent concentrations exceed a minimum threshold. Below that threshold, net removal stops — and the media may even release previously captured nutrients back into the water column. This threshold behavior is critical when evaluating whether a media BMP is appropriate for a given site.

Biosorption Activated Media (BAM)

Biosorption Activated Media — commonly abbreviated BAM — combines physical adsorption with a biological component. Microorganisms colonize the media surface and contribute to nutrient immobilization. However, BAM requires specific conditions to function as intended:

  • Adequate moisture retention to sustain the microbial community between storm events
  • Sufficient organic carbon to support biological activity
  • Influent concentrations high enough to drive active sorption
  • Periodic replacement or regeneration as active sites become saturated

When these conditions are not met, BAM performance degrades and may not justify the cost premium over conventional media.

Approved Media Types and User-Defined Options

Florida’s BMP framework recognizes seven approved adsorption media types. These media have undergone sufficient testing to receive credit in stormwater calculations without additional site-specific field data. In addition to these pre-approved options, the framework allows for user-defined media — proprietary or novel materials that a designer wishes to incorporate. User-defined media carry an important data requirement:

Data Requirement — User-Defined Media

Field-tested concentration data must be provided for any media not on the pre-approved list. This means real-world performance data collected under conditions representative of the proposed application — not laboratory bench tests or manufacturer-supplied data from different climate zones or influent matrices.

The distinction between laboratory and field performance is especially important for adsorption media. Lab conditions — controlled temperature, clean water matrices, steady-state flow — routinely overstate removal efficiency compared to field conditions with variable flows, competing ions, and biological fouling.


Topic 7: Wetland BMPs and Equilibrium

Slides 17–21 · Hardwood versus herbaceous wetlands, equilibrium concentrations, and nutrient dynamics

Hardwood Wetland Equilibrium

Hardwood (forested) wetlands are not effective nutrient sinks for stormwater treatment. Over time, these systems reach chemical equilibrium with their underlying anoxic soils. Once equilibrium is established, the wetland neither removes nor exports significant quantities of nutrients on a net annual basis — it simply passes water through at concentrations dictated by soil chemistry.

Equilibrium Concentrations — Hardwood Wetlands

Total Phosphorus: approximately 100 µg/L
Total Nitrogen: approximately 1,000–2,000 µg/L
These are the background concentrations that the wetland tends to produce regardless of influent concentration.

The Low-Concentration Problem

The equilibrium dynamic creates a counterintuitive hazard: if stormwater enters a hardwood wetland at concentrations below the wetland’s equilibrium point, the wetland will export nutrients rather than remove them. Water flowing in at, for example, 30 µg/L TP will exit at concentrations approaching 100 µg/L TP as the system equilibrates. This is the opposite of the intended treatment effect and represents a significant design pitfall.

Design Warning

Do not route pre-treated stormwater with low nutrient concentrations through a hardwood wetland. The wetland will act as a nutrient source, negating upstream treatment and worsening discharge quality.

Herbaceous Wetlands: A Different System

Herbaceous wetlands — dominated by emergent macrophytes such as cattails, bulrush, and pickerelweed — behave very differently from hardwood wetlands. The key distinction is biological productivity. Herbaceous wetlands support dense biological communities including macrophytes, periphyton, and diverse microbial assemblages. These communities actively assimilate nutrients into biomass, providing ongoing removal capacity rather than simple equilibrium buffering.

  • Macrophyte uptake sequesters phosphorus and nitrogen into plant tissue
  • Periphyton mats provide high-surface-area biological contact zones
  • Sedimentation of organic particles removes nutrients from the water column
  • Microbial denitrification converts nitrate-nitrogen to atmospheric nitrogen gas
  • Net result: additional nutrient uptake beyond what physical settling alone achieves

Because herbaceous wetlands achieve active biological removal rather than mere equilibrium, they can treat water at concentrations well below 100 µg/L TP — making them compatible with pre-treated stormwater in treatment train configurations.


Topic 8: Treatment Trains

Slides 20, 22 · Combining BMPs in sequence to achieve lower effluent concentrations

The Treatment Train Concept

A treatment train routes stormwater through two or more BMPs in sequence, with each stage further reducing pollutant concentrations before discharge. The combined system consistently outperforms any single BMP operating alone. The most effective configuration documented in Florida stormwater research pairs a wet detention pond with a downstream herbaceous wetland.

Influent

Untreated

Runoff TP
typically >100 µg/L

Stage 1

Wet Pond

Discharge TP
~35 µg/L

Stage 2

Herbaceous Wetland

Effluent TP
~15 µg/L

Discharge

Receiving Water

57% further reduction
from pond effluent

Wet Pond + Herbaceous Wetland Performance

The wet pond performs the bulk of initial nutrient removal through sedimentation, biological uptake in the water column, and algal assimilation. Pond effluent TP typically reaches approximately 35 µg/L — a substantial reduction from raw runoff, but still above drinking water standards and the thresholds for many sensitive receiving waters. The herbaceous wetland then reduces this further to approximately 15 µg/L TP, representing an additional 57% reduction from the pond discharge concentration.

Why the Combination Works

The wet pond reduces TP to concentrations below the herbaceous wetland’s equilibrium threshold, ensuring the wetland continues to remove rather than export nutrients. Each stage is operating in a concentration range where it performs optimally — this complementarity is the essence of effective treatment train design.

Hardwood Wetland After Pond: Avoid This Configuration

Routing wet pond effluent (~35 µg/L TP) through a downstream hardwood wetland is counterproductive. Because the pond has already reduced TP below the hardwood wetland’s equilibrium concentration (~100 µg/L), the hardwood wetland will release nutrients back into the water, raising effluent TP rather than reducing it. This configuration should be explicitly avoided in treatment train design.

Design Rule

Wet Pond → Herbaceous Wetland: Approved. Concentrations decrease at each stage.
Wet Pond → Hardwood Wetland: Avoid. Concentrations increase at the second stage, negating upstream treatment investment.


Topic 9: Evaluating Manufacturer Claims

Slides 14, 23–24 · Critical analysis of removal efficiency data and performance claims

Why Reported Removal Efficiencies Are Often Misleading

Manufacturers of proprietary stormwater treatment devices frequently report nutrient removal efficiencies — often expressed as percentage reduction — that appear impressive but are methodologically unreliable. The core problem is straightforward: removal claims are often based on tests conducted at artificially elevated influent concentrations. Because removal is concentration-dependent, high influent concentrations mechanically inflate the percentage removed, even if the effluent concentration is not particularly low.

Test Scenario A

Influent: 1,000 µg/L TP
Effluent: 500 µg/L TP

50%

removal — sounds good

Stormwater Reality

Influent: 100 µg/L TP
Effluent: ~90 µg/L TP

~10%

removal — same device

Concentration Ratio

Wastewater nutrients are approximately

10×

higher than stormwater

The Wastewater-to-Stormwater Transfer Problem

Many proprietary treatment devices were originally developed and validated for municipal wastewater treatment, where nutrient concentrations are an order of magnitude higher than in stormwater. A technology that achieves strong percentage removal in wastewater — removing nutrients from 10,000 µg/L down to 1,000 µg/L — may provide essentially no benefit when applied to stormwater at 100–200 µg/L, because the driving concentration gradient is insufficient to activate the removal mechanism.

  • Adsorption media that saturate slowly at wastewater concentrations may never reach their operative range in dilute stormwater
  • Biological processes optimized for high-strength wastewater may be carbon- or nutrient-limited in stormwater
  • Manufacturer-cited removal efficiencies from wastewater trials are not transferable to stormwater applications
  • Regulatory credit should not be awarded based on wastewater performance data alone

What to Ask for Instead

The most important data point when evaluating any nutrient removal technology is not the percentage removal efficiency — it is the minimum achievable effluent concentration under realistic stormwater conditions. This single metric reveals whether the technology can achieve the effluent quality required for the receiving water, regardless of how impressive the percentage reduction appears.

Evaluation Checklist — Manufacturer Claims

✔ What is the minimum achievable effluent concentration (not just % removal)?
✔ Were tests conducted with actual stormwater or synthetic/wastewater matrices?
✔ What were the influent concentrations used in the published studies?
✔ Is there field performance data from comparable climates and land uses?
✔ Has the technology been tested under variable flow conditions typical of stormwater events?
✔ Are independent third-party data available, or only manufacturer-supplied results?

The Field Testing Requirement

Laboratory and pilot-scale tests are useful for initial screening but are not sufficient for regulatory credit or design reliance. Field testing under actual conditions is essential because stormwater treatment performance is sensitive to factors that laboratory tests cannot replicate: episodic high-flow events that bypass or short-circuit treatment zones, organic loading from debris and sediment, temperature variation, wet-dry cycling that affects biological communities, and the full matrix of competing ions present in real runoff. A technology that performs well in the laboratory but has not been validated in the field should be treated as unproven for design purposes.

Bottom Line for Practitioners

When a manufacturer presents removal efficiency data, the first question should be: “What were the influent concentrations, and where was the testing done?” High-percentage removal from high influent concentrations tells you almost nothing about whether the product will perform in your stormwater application. Request minimum concentration data and field validation under conditions comparable to your site before incorporating any proprietary device into a treatment design or permit application.


Appendix: Quick-Reference Cards

Summary reference cards for all topics covered in this module (Parts 1 and 2)

Topic 1 — Removal Mechanisms

Four mechanisms: Sedimentation · Biological uptake · Adsorption · Chemical precipitation

Key insight: Mechanism determines minimum achievable concentration

→ Match BMP type to target mechanism

Topic 2 — Concentration Dependence

Rate ∝ concentration: Removal slows as concentrations fall

Threshold: Each mechanism has a minimum below which it ceases

→ % removal overstates performance at low concentrations

Topic 3 — Wet Detention Ponds

Primary mechanism: Sedimentation + algal uptake

Typical effluent TP: ~35 µg/L

Internal loading risk: Anoxic sediments release stored P

→ Size for hydraulic residence time, not just volume

Topic 4 — Dry Retention & Filtration

Dry retention: Infiltration removes dissolved nutrients via soil adsorption

Filtration: Removes particulate fraction; limited dissolved nutrient removal

→ Media selection critical for dissolved nutrient credit

Topic 5 — Swales & Bioretention

Swales: Effective for TSS; limited dissolved nutrient removal without check dams

Bioretention: Soil/plant uptake removes N and P; requires amended media

→ Under-drain design affects nitrogen removal pathway

Topic 6 — Adsorption Media BMPs

Mechanism: Surface adsorption + entrapment

BAM: Biological + adsorption; requires proper moisture and carbon

7 pre-approved types; user-defined media need field data

→ Below threshold = zero or negative removal

Topic 7 — Wetland BMPs & Equilibrium

Hardwood equilibrium TP: ~100 µg/L  |  TN: ~1,000–2,000 µg/L

Low inflow < equilibrium: Wetland exports nutrients

Herbaceous wetlands: Active biological uptake, no equilibrium ceiling

→ Herbaceous = treatment; hardwood = pass-through or source

Topic 8 — Treatment Trains

Best configuration: Wet pond → Herbaceous wetland

Pond effluent TP: ~35 µg/L → Wetland effluent TP: ~15 µg/L

Avoid: Wet pond → Hardwood wetland (concentrations rise)

→ Each stage must operate in its effective concentration range

Topic 9 — Evaluating Manufacturer Claims

Red flag: % removal at high influent concentrations

Wastewater ≠ stormwater: Concentrations ~10× higher in wastewater

Ask for: Minimum achievable concentration + field data

→ Field validation under actual conditions is required

Reference — Key Concentration Values

Wet pond effluent TP: ~35 µg/L

Treatment train effluent TP: ~15 µg/L

Hardwood wetland equilibrium TP: ~100 µg/L

Hardwood wetland equilibrium TN: ~1,000–2,000 µg/L

Typical stormwater TP: 100–300 µg/L

Wastewater vs. stormwater ratio: ~10×


Florida Stormwater Management — BMP Nutrient Removal

Part 2 of 2 · Topics 6–9: Adsorption Media, Wetlands, Treatment Trains, and Evaluating Claims

Based on FDEP / SFWMD course material

For educational use · Verify against current regulatory guidance