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Compliance with the New Arsenic MCL Epping, NH

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Compliance with the New Arsenic MCL

Epping, NH

Introduction

• Speaker: Devon Smith, PE

• Employer: Underwood Engineers

• Position: Senior Project Engineer

2

Purpose

• Regulations

• Existing System

• Treatment Process

• Water Treatment Plant

• Questions

Epping

• A case study on the Epping water treatment plant and the arsenic removal process.

Agenda

3

Arsenic (As)What is it?

• Naturally occurring metalloid• Colorless, tasteless & odorless in

drinking water

Health Effects?• Cancer• Diabetes • Neurological disorders • Birth defects

4

Regulations

“The U.S. Environmental Protection Agency (EPA) typically sets MCLs for drinking water contaminants at a level at which a lifetime of exposure would result in one excess cancer in one million people exposed…The 10 ppb MCL for arsenic is associated with a far greater risk – 3,000 in a million (roughly 1 in 300)..”

• Current Maximum Contaminant Level (MCL) • 10 parts per billion (ppb) or micrograms per liter

• January 2006

• Federal Regulation

• Future Maximum Contaminant Level (MCL)• 5 parts per billion (ppb) or micrograms per liter

• Expected July 2021

• State Regulation

5

Existing Water Supply System – Epping NH

Pleasant Street Tank250,000 Gal.

Gauthier Tank300,000 Gal

Epping Crossing Well Field Pilot Plant, 100 gpm

Existing System

• Storage = 550K Gal.

• Capacity = 183 gpm

Well Fields

• Epping Crossing

• As = 19 ppb

• Hoar Pond

• As = 9 ppb

• Cannot meet future As regulation

Hoar Pond Wells83 gpm

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Epping Crossing Well Field

Pilot PlantCapacity = 100 gpm Well E1

PPV = 225 gpm

Well D2PPV = 210 gpm

NHDES Env-DW 404.01

• Capacity > MDF

• Capacity > ADF with largest well off

• Future Capacity = 210 gpm

• Permit Well F1

Well F1Expected Capacity = 80 gpm

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Existing Pilot Plant • Capacity

• 100 gpm

• Filters

• No. = 3

• Diameter = 3.5 ft

• Media

• Clack MTM

• Chemical Feed

• 40% Ferric Chloride

• 12.5% Sodium Hypochlorite

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Epping Crossing Well Field – Water Quality

> 10 ppb (soon to be 5)

> 0.3 mg/L (SMCL)

> 0.05 mg/L (SMCL)

Standard

EPA Health Advisory for Mn• 0.3 mg/L for infants

NHAGQS for Mn• 0.84 mg/L

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Arsenic Removal by Iron Removal Oxidation

• Convert inorganic soluble As (III) to insoluble As (V)

Adsorption & Co-Precipitation• As becomes entrapped within

growing Fe by inclusion, occlusion or adsorption.

Filtration• Greensand media acts as a catalyst

in oxidation reduction reaction for Fe and Mn.

Key Parameters• As to Fe ratio

• pH = 6.2 -8.5

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Treatment Process Selection

Additional Fe and lowering the pH is

necessary for optimal As removal

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Blue Leaf Piloting • 4 Pilot Parameters (Fe /pH)

• HH

• HL

• LH

• LL

• Results

• As = 0.7 – 3.6 ppb

• Mn = 0.006 - 0.015 mg/L

• Fe = 0.03 – 0.59 mg/L

• Backwash Run Times• 20 HRs – 48 HRs

• Backwash Triggers• Turbidity breakthrough

• Pressure differential

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13

Manganese Greensand Process• Filters

• No = 3• Diameter = 8 ft

• Greensand Plus Media • Loading Rate = 2-12 gpm/sf • Anthracite Cap

• Delays filter blinding

• Regeneration

• Backwash• Combined water and air scour• Flow = 10-12 gpm/sf• Volume = 10,000 gal. – 16,000 gal.

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= Influent

= BW Waste

= Effluent

= BW Influent= Filter to Waste

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Backwash Equalization Tanks• Limited sewer capacity • 26,400 Gal. useable storage

• Backwash performance requirement• Backwash recycle was not provided

Freeboard

Min. PumpSubmergence

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• Wetlands and Buffers

• Conservation Easement

• Well Protection Zone

Site Plan Wetland Boundary

Wetland Buffer

Conservation Easement

Well Protection Zone

Wetland Buffer

PilotPlant

Water TreatmentPlant

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Floor Plan

Capacity • 435 gpm (0.63 MGD)

Building Dimensions• 67’-4” x 37’-8• 2,536 sf

Building Materials• Wood Frame• Fiber Cement Siding• FRP Paneling • Asphalt Shingles

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Hydraulics

Static Head

• Min = 162.5 ft

• Max = 378.6 ft

EL =126.0 ft Static GWT

EL = -90.1 ft180 Day Drawdown

EL = 288.5 ftSystem HGL

HGL Diagram (Simplified) Well D2

Filter

Storage Tank

Submersible Well Pump Curve

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Project Status

• Contractor: PRB Construction

• Construction Cost: $3,046,000

• Percent Complete: 10% (7/2/20)

• NTP: 6/1/2020

• Sub. Completion: 5/26/21

• Final Completion: 7/25/2021

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Thank You and Questions?

Contact [email protected]

(603) 230-9898

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References

1. NHDES. December 2018. Review of the Drinking Water Maximum Contaminant Level (MCL) and Ambient Groundwater Quality Standard (AGQS) for Arsenic. Concord, New Hampshire.

2. U.S. EPA. April 2006. Design Manual Removal of Arsenic from Drinking Water Supplies by Iron Removal Process. Columbus, Ohio

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