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Dare County Water Department 

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STUMPY POINT REVERSE OSMOSIS WATER TREATMENT PROCESS

Wells

Stumpy Point Well #1 is the remote well located approximately 1,000' from the plant site. It is drilled to a total depth of 200'. The well casing is Schedule 80 PVC six inches in diameter with a slot PVC screen from 170' to 190'. Stumpy Point Well #2 is the well located behind the water plant. It is drilled to a total depth of 230'. The well casing is Schedule 40 PVC four inches in diameter with a slot PVC screen from 170' to 190'.  Each of the well pumps is a Goulds, single stage submersible pump that is driven by a 5 horsepower Franklin submersible motor. They each deliver up to 70 gallons per minute.  The pumps are positioned 88' below the ground level. 

Pre-Treatment

The two submersible well pumps bring the brackish raw water to the plant for treatment through PVC piping. 

A scale inhibitor is fed to the raw water to minimize the formation of any precipitant on the membrane surface. The scale inhibitor in use at the Stumpy Point Plant is Spectraguard/SC used at 6.0 - 7.0 ppm.

The water, after chemical addition and mixing, is filtered using one 5.0 micron cartridge filter that will last from 6 to 9 months depending on the amount of water processed.  It will be replaced when the pressure drop exceeds 10 pounds per square inch.

The Reverse Osmosis (RO) Treatment

RO UnitOnce pre-treated, the water becomes feed water at the RO unit.  The unit consists of a feed header, 3 long tubes called pressure vessels (PVS), interstage and concentrate manifolds and a concentrate control valve.  In addition, there are various gauges and meters installed for analysis.  These three PVS house four membranes in series each.  The water enters the first two PVS where part of the total product is separated from the feed.  The remaining pressure vessel squeezes out the rest of the product in the second stage of treatment.  This plant operates on approximately 60% product recovery.  Better than one half of the feed water to the units eventually becomes product water.  The unit produces 60,000 gallons per day of product water.

The membranes used in the process are Aqua Pro eight inch TW-8040 membranes.  The average feed pressure to the units is 180 psi.  This is accomplished through the use of a Baldor pump with a 25 hp motor.

Post Treatment

After exiting the RO unit, post treatment chemicals are added to the product water.  These chemicals are sodium hypochlorite for disinfection with a 1.0 part per million (ppm) residual of free chlorine in the 10,000 gallon finished water tank, fluoride for dental care at 1.0 ppm, sodium hydroxide for stabilization and corrosion control and a zinc orthophosphate also for corrosion inhibition at 1-2 ppm.  The finished water contains about 40 ppm of total dissolved solids with 20 ppm being chlorides and 15 ppm sodium. Calcium chloride is used to bring the total hardness up on the finished water. The total hardness is two (2) before adding calcium chloride and twenty-five (25) after post treatment. This helps with corrosion control along with the other post treatment chemicals. 

Waste Discharge

The 40% of the feed water that is not product becomes a waste stream in which all of the dissolved minerals removed in the Reverse Osmosis process are disposed. This stream is discharged into the Stumpy Point
Bay. The Bay is under the scrutiny of the NC Division of Water Quality by way of an NPDES permit.

Computer Control

There is one SCADA (Supervisory Control and Data Acquisition) Workstation HMI (Human Machine Interface) located at the Stumpy Point Facility. It will be the primary point of operator interface at the facility. It will communicate directly to the Modicon PLC (Programmable Logic Controller) via Ethernet. An additional SCADA Workstation is provided for the Skyco Facility. It is identical to the primary station but also includes the WIN 911 Alarm Notification Software. The processor located at the Dare County Skyco Water Plant will be used for monitoring during hours that the Stumpy Point Plant is unmanned.

Page last updated February 24, 2004

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