2013
DOI: 10.1016/j.biombioe.2013.01.033
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Thermal gasification or direct combustion? Comparison of advanced cogeneration systems in the sugarcane industry

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Cited by 77 publications
(46 citation statements)
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“…The most widely practised method of yielding surplus electric power production in traditional sugar mills is by introducing more efficient cogeneration systems. Most commonly, these are high pressure steam Rankine cycle cogeneration systems [3]. This method has been widely implemented in countries like Brazil [4], India [5], and Mauritius [5].…”
Section: Introductionmentioning
confidence: 99%
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“…The most widely practised method of yielding surplus electric power production in traditional sugar mills is by introducing more efficient cogeneration systems. Most commonly, these are high pressure steam Rankine cycle cogeneration systems [3]. This method has been widely implemented in countries like Brazil [4], India [5], and Mauritius [5].…”
Section: Introductionmentioning
confidence: 99%
“…The cogeneration inefficiency of traditional sugar cane mills is due to the fact that most of the traditional sugar mills are found in developing countries and were built up in remote rural areas where there is no national grid connection; thus, the cogeneration units of such mills are designed in such a way that they incinerate the majority of the produced bagasse in order to avoid disposal problems of the residue. Typical live steam parameters for such cogeneration units of sugar mills are in the range of 20-30 bar and 300-400°C [5][6][7], whereas modern cogeneration units of sugar mills operate with boilers having live steam parameters as high as 45-80 bar (just in few cases around 100 bar) and over 450°C [3]. This indicates that the boiler efficiencies in the modern cogeneration units will improve, and thus, there is a possibility of generating surplus power owing to the higher steam parameters of the live steam to be expanded in the power turbines.…”
Section: Introductionmentioning
confidence: 99%
“…Typically, plants require 400-550 kg of steam per ton of sugarcane, but, by using state of the art technology, sugar manufacturing and ethanol distillation would require only 280-300 kg-steam/tc (ton of sugarcane). This would imply a significant increase in the electrical power production [7]. Other possible layout configurations are based on gasification of the biomass.…”
Section: Introductionmentioning
confidence: 99%
“…Esse aproveitamento poderia se dar pela queima da palhada em caldeiras, como uma fonte de combustível adicional ao bagaço para a geração de energia (DESHMUKH, 2013 Atualmente, com a demanda de equipamentos para recolhimento de biomassa visando à produção de etanol de segunda geração e de energia elétrica, houve o desenvolvimento de equipamentos com maior capacidade, os quais poderiam reduzir o custo de recolhimento da palhada e, consequentemente, a redução do custo da energia elétrica produzida a partir dessa fonte.…”
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