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

 

EXAMPLE OF CONSTRUCTION AND O&M COSTS - CONTINUED

It was estimated that the yearly cost of limestone replacement at Mars Hill, Maine is US$200 compared to US$2,500 for soda ash (Spencer, 2000). 16 and 12 show comparison of cumulative cost between limestone, lime and sodium carbonate over a 10-year period for the Makwane Plant in South Africa. The figure and table demonstrate a significant savings when using limestone contactor over lime and sodium carbonate that more than offset higher capital costs.

Financial assessment was carried out by CSIR to investigate the viability of the Simplified SSP to stabilize the typical raw water in Stellenbosch, South Africa. The viability of the Simplified SSP was determined theoretically using the computer model developed using JAVA, STASOFT and WATCHEM described earlier.

Comparison of operating costs was made between each Simplified SSP variation and between the Simplified SSP and conventional stabilization (based on achieving the same final water quality). The operating costs were determined using the required chemical dosages and chemical costs. 17 shows cost comparison between the Simplified SSP and conventional lime/CO2 stabilization. Both were based on treating the raw water characteristics as shown in 13 until a final alkalinity of 50 mg/L and a CCPP of zero were achieved. The chemical prices were based on the current cost at Stellenbosch, South Africa in November 1999 shown in 14.

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