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

16 shows the cost comparison between SSP and conventional stabilization.

The cost comparison in 16 and financial model in 17 were based on utilizing a “high” percentage sidestream (10%) combined with “low” percentage CO2 recovery and re-use (10%), and an airstrip of the blended stream.

Based on the data shown in Table 16 and 17, even using assumptions that are detrimental to SSP (such as lifespan of 10 years, raised electricity costs for SSP, risk discount factor of 30% per annum, minimum required return of investment of 10% per annum and low percentage CO2 recovery), SSP still provides significant financial advantage over conventional lime/CO2 stabilization with a project payback period of 4.3 years, Net Present Value of R 2.7 million and Internal Rate of Return of 52% (De Souza et al., 2002).

Based on the financial assessment studies, direct comparison between the SSP and Simplified SSP is not possible due to the variations of chemical costs. The cost variation may be due to the quality of the chemicals, Rand exchange rate and the region to which the chemical is transported. In this case, it is due to conducting the studies at separate locations.

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