LIMESTONE CONTACTORS

 LIST OF CONTENTS

  Introduction

  Process Description

  Typical Contactor

  Design Criteria

  Photos, Plans & Specs

  Treatment Performance

  Operational Skills

  Automation Potential

  Advantages

  Limitations & Concerns

  Pilot Plant Objectives

  Costs 

  References

  Contacts & Facilities

 

TREATMENT PERFORMANCE - CONTINUED

According to the AWWA guidelines for copper corrosion mitigation, the bulk water pH must be in the range of 7.1 to 8.0 (Daniels et al., 2002). 13 shows the relationship between copper and pH levels at various sampling points in the Bredasdorp pipe network after limestone stabilization. The figure shows that the copper level remains fairly consistent throughout the pH range except for three samples. All these three samples had a pH value below 7.1. Daniels et al. (2002) further concluded that copper corrosion is not expected at pH above 7.1.

(D) Limestone Contactor Performance in Stellenbosch, South Africa

The effectiveness of a limestone contactor on copper reduction was also studied in Stellenbosch, South Africa by collecting pH and copper data at a household sampling point. According to Daniels et al. (2002), the limestone contactor was operated at a loading rate of 50% greater than its design capacity due to increased water requirements in Stellenbosch. The authors implied that this overloading caused the pH to be lower than desired and led to higher copper concentrations. The authors further implied that expanding the limestone contactor increased the pH and decreased the copper as shown in 14.

Using the data from 13 and 15, Daniels et al. (2002) concluded that the copper corrosion can be avoided at a pH of greater than 7.1.

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