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Drinking Water Treatment Technology Unit Cost Models

Drinking Water Treatment Technology Unit Cost Models

Federal laws and executive orders require EPA to estimate compliance costs for new drinking water standards. The three major components of compliance costs are:

  • Treatment
  • Monitoring
  • Administrative costs

Treatment technologies remove or destroy pollutants (such as arsenic, disinfection byproducts, and waterborne pathogens).

To estimate treatment costs, EPA developed several engineering models using a bottom-up approach known as work breakdown structure (WBS). The WBS models:

  • Derive system-level costs
  • Provide EPA with comprehensive, flexible and transparent tools to help estimate treatment costs

Each WBS engineering model contains a work breakdown for a particular treatment process. Engineering equations estimate equipment requirements given user-defined inputs such as design and average flow. Each model has many design assumptions (such as redundancy requirements).  The models provide unit cost and total cost information by component.

The models also contain estimates of:

  • Add-on costs (such as permits, pilot studies and land acquisition)
  • Indirect capital costs (such as site work and contingencies)
  • Annual operation and maintenance costs

Figure 1 shows the structural features used to generate treatment costs in the WBS models.

This diagram displays the variables that are factored in to determining water treatment costs
Figure 1. Structural features used to generate treatment costs in WBS models

The WBS models integrate these features into a series of worksheets in a Microsoft® Excel workbook for each technology. An input sheet allows users to define parameters (such as system design and average flows, target contaminant, and raw water quality). Critical design assumptions generally reflect engineering practices. Users can revise these values to reflect site-specific requirements.

WBS cost models are available to the public for the following treatment technologies:

Granular Activated Carbon (GAC)

Packed Tower Aeration (PTA)

  • Packed Tower Aeration (PTA) (xlsm)
  • PTA Documentation (pdf) (119 pp, 4.81 MB)
  • PTA uses towers filled with a packing media to mechanically increase the area of water exposed to non-contaminated air. PTA reduces the concentration of volatile contaminants including:
    • volatile organic compounds
    • disinfection byproducts
    • hydrogen sulfide
    • carbon dioxide
    • other taste-and-odor-producing compounds

Multi-Stage Bubble Aeration (MSBA)

Anion Exchange (AE)

Cation Exchange (CE)

  • Cation Exchange (CE) (xlsm)
  • CE Documentation (pdf) (113 pp, 3.67 MB)
  • CE removes positively charged contaminants from water by passing it through a bed of synthetic resin. It is useful for removal of contaminants including:
    • barium
    • chromium-3
    • radium
    • strontium
    • hardness ions such as calcium and magnesium

Biological Treatment

Reverse Osmosis and Nanofiltration (RO and NF)

  • Reverse Osmosis and Nanofiltration (RO/NF) (xlsm)
  • RO/NF Documentation (pdf) (130 pp, 4.67 MB)
  • RO and NF are membrane separation processes that physically remove contaminants from water.
  • RO is useful for removal of contaminants including:
    • many inorganic contaminants (antimony, arsenic, barium, beryllium, cadmium, chromium, cyanide, mercury, nickel, nitrate, perchlorate, selenium)
    • dissolved solids
    • radionuclides
    • synthetic organic chemicals
  • NF is useful for removal of hardness, color and odor compounds, synthetic organic chemicals, and some disinfection byproduct precursors.

Nontreatment Options

Learn about Technologies

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