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

17 shows that the use of a 20% sidestream leads to a 50% chemical cost saving of 2.63 c/kL (De Souza et al., 2002). In the case of a 100 ML/day treatment plant, this is equivalent in a savings of R 78,900 per month and R 959,950 per year (De Souza et al., 2002). The treatment cost using conventional lime/CO2 shows a constant trend throughout the range of the percent sidestream.

Cost comparison also shows that it was financially attractive to do the following:

a) Strip the excess CO2 after blending the sidestream and mainstream.
b) Accompany the partial stripping of the mainstream by adding lime.
c) Not strip the excess CO2 before blending the sidestream and mainstream.
d) Not strip the CO2 from the mainstream.

Financial assessment was carried out to investigate the viability of the Simplified SSP to stabilize the raw water of the Lesotho Highlands Scheme, South Africa. Financial evaluation of SSP was conducted by comparing its cost with the conventional methods (lime and carbon dioxide stabilization) treating the raw water from Katse Dam, South Africa. 15 shows the raw water characteristics.

The viability of the SSP was assessed using the computer model developed using JAVA and pilot plant operation.

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