Abstract

The purpose of the research was to identify the effect of time and microwave torrefaction power to heat value, water content, and ash content to recognize the maximum condition of the selected variables. Biomass waste and garbage can be one energy resource alternatives. The real exploitation of biomass resulted from forestry and estate activity waste that has been widely adopted is found in the production of briquette and charcoal. We adopted sugarcane bagasse and dry leaves mixture was to generate greater contents of cellulose and lignin to get higher heat value. One of the methods commonly adopted in briquette productions is microwave torrefaction. The process in the research covered raw material drying, slicing, microwave torrefaction, proximate analysis, data processing, and research finding discussion. The torrefaction process was activated by reacting to the raw materials, i.e.: sugarcane bagasse and dry leaves into a microwave under 230'C through 280oC in airtight condition and in a short time. The variables in the research were microwave power and torrefaction time. The microwave power was set at 80 W, 400 W, and 800 W, while the ten faction time set 5 minutes, 15 minutes, and 25 minutes. Based on the results of the research it was concluded that the most optimum variables were microwave power of 800 W and torrefaction time of 25 minutes.

Highlights

  • Biomass and waste can be an alternative energy source

  • Biomass torrefaction uses microwaves as renewable energy to replace the depletion of coal usage, thereby reducing high carbon energy

  • The purpose of this study was to determine the effect of time and microwave torrefaction power on the heating value, moisture content, and ash content and to determine the maximum conditions for the selected variables

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Summary

Introduction

Biomass and waste can be an alternative energy source. Agricultural waste, which is biomass, is an abundant alternative energy source, with relatively large energy content. Biomass torrefaction uses microwaves as renewable energy to replace the depletion of coal usage, thereby reducing high carbon energy. The pre-treatment torrefaction process with a mild reaction was shown beforehand until the final destination. It is known that a relatively low reaction temperature is in the range of 200-300 C in the oxygen-free environment and a heating rate of less than 50 C is minimal. The torrefaction reaction can be improved by the substance's heating value, energy density, C / O ratio, and biomass humidity. The torrefaction reaction can occur between 200-250 C or 250-300 C. The decomposition of hemicellulose, cellulose and lignin occurs at the reaction temperature and with the reaction time and the result is volatile gases (Himawanto, 2005)

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