2013•Sugar IndustryRequires access

Energy efficiency improvement of cane sugar factories by drying of bagasse with superheated steam

Boris Morgenroth, Druce Batstone

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Abstract

Bagasse drying with superheated steam offers the advantage of producing approximately 15% more power than with a conventional co-generation plant. Based on a fibre content of 14% on cane a power export of up to 140 kWh/t cane is achievable compared to 122 kWh/t cane in case of a conventional highly efficient co-generation plant. The operational results of a 12 t/h bagasse drier in Australia are briefly described and a concept of integrating a bagasse steam drier system in a modern highly energy efficient cane sugar plant is explained. This encompasses changes in the boiler capacity, turbogenerators and evaparation plant lay-out. Based on power export prices in the range of USD50–85/MWh the payback period of a bagasse steam drier system can be estimated with 3–6 years.

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What this paper is about

Bagasse drying with superheated steam offers the advantage of producing approximately 15% more power than with a conventional co-generation plant. Based on a fibre content of 14% on cane a power export of up to 140 kWh/t cane is achievable compared to 122 kWh/t cane in case of a conventional highly efficient co-generation plant. The operational results of a 12 t/h bagasse drier in Australia are briefly described and a concept of integrating a bagasse steam drier system in a modern highly energy efficient cane sugar plant is explained. This encompasses changes in the boiler capacity, turbogenerators and evaparation plant lay-out. Based on power export prices in the range of USD50–85/MWh the payback period of a bagasse steam drier system can be estimated with 3–6 years.

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Available abstract

Bagasse drying with superheated steam offers the advantage of producing approximately 15% more power than with a conventional co-generation plant. Based on a fibre content of 14% on cane a power export of up to 140 kWh/t cane is achievable compared to 122 kWh/t cane in case of a conventional highly efficient co-generation plant. The operational results of a 12 t/h bagasse drier in Australia are briefly described and a concept of integrating a bagasse steam drier system in a modern highly energy efficient cane sugar plant is explained. This encompasses changes in the boiler capacity, turbogenerators and evaparation plant lay-out. Based on power export prices in the range of USD50–85/MWh the payback period of a bagasse steam drier system can be estimated with 3–6 years.

Key concepts: Bagasse, Cane, Superheated steam, Waste management, Boiler (water heating), Sugar cane, Pulp and paper industry, Electricity generation

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