Carbon mass balance in sugarcane biorefineries in Brazil for evaluating carbon capture and utilization opportunities
被引:21
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作者:
Noel Simas Barbosa, Larissa de Souza
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机构:
Univ Sao Paulo, Luiz de Queiroz Coll Agr, BR-13418900 Piracicaba, Brazil
Finland Ltd, VTT Tech Res Ctr, POB 20, FI-53851 Lappeenranta, FinlandUniv Sao Paulo, Luiz de Queiroz Coll Agr, BR-13418900 Piracicaba, Brazil
Noel Simas Barbosa, Larissa de Souza
[1
,3
]
Hytonen, Eemeli
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机构:
Finland Ltd, VTT Tech Res Ctr, POB 1000, FI-02044 Espoo, FinlandUniv Sao Paulo, Luiz de Queiroz Coll Agr, BR-13418900 Piracicaba, Brazil
Hytonen, Eemeli
[2
]
Vainikka, Pasi
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机构:
Finland Ltd, VTT Tech Res Ctr, POB 20, FI-53851 Lappeenranta, FinlandUniv Sao Paulo, Luiz de Queiroz Coll Agr, BR-13418900 Piracicaba, Brazil
Vainikka, Pasi
[3
]
机构:
[1] Univ Sao Paulo, Luiz de Queiroz Coll Agr, BR-13418900 Piracicaba, Brazil
[2] Finland Ltd, VTT Tech Res Ctr, POB 1000, FI-02044 Espoo, Finland
[3] Finland Ltd, VTT Tech Res Ctr, POB 20, FI-53851 Lappeenranta, Finland
Sugarcane biorefineries, despite their contribution to sustainable transportation fuels and mitigation of carbon emissions in the mobility sector, produce a large amount of carbon dioxide in their conversion processes. According to the Paris climate agreement, a carbon neutral energy system has to be launched in the years to come, and in this scenario, greenhouse gases emission free industrial processes and alternative carbon sources will be needed. Therefore, this paper presents the evaluation of carbon mass balance of a typical Brazilian ethanol mill to better understand its potential for energy and carbon yield improvement. Due to the fact that Brazilian sugarcane mills are evolving from first generation to integrated first and second generation plant, four different scenarios were analysed. For a first generation plant without (S-I) and with conversion of straw to electricity (S-II) and for the integrated plant (S-III), results of carbon mass balance showed that the harvested sugarcane carbon was mainly converted into CO2 and in a smaller proportion into ethanol. In the modelled cases S- I to S- III the conversion of sugarcane carbon into CO2 and ethanol ranged from 41% to 53% and 17%-22%, respectively. Because this carbon amount in the CO2 flows provides an interesting platform to both increase the bioenergy produced and the harvested carbon-to-fuels ratio, a fourth scenario (S-IV) that studies the integration of power-to-gas (PtG) technologies into the mill was also considered. PtG can increase the sugarcane fuels energy content from 9.3kW/ha to 33.6 kW/ha using 1361.3 MWe of electricity, increasing the amount of sugarcane carbon transformed into sugarcane based fuels to 54% and converting CO2 into a high value added product. (C) 2017 Elsevier Ltd. All rights reserved.
机构:
Univ Malaya, Fac Sci, Inst Biol Sci, Kuala Lumpur 50603, MalaysiaUniv Malaya, Fac Sci, Inst Biol Sci, Kuala Lumpur 50603, Malaysia
Cheah, Wai Yan
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机构:
Ling, Tau Chuan
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Juan, Joon Ching
Lee, Duu-Jong
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机构:
Natl Taiwan Univ, Dept Chem Engn, Taipei 10764, TaiwanUniv Malaya, Fac Sci, Inst Biol Sci, Kuala Lumpur 50603, Malaysia
Lee, Duu-Jong
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机构:
Chang, Jo-Shu
Show, Pau Loke
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机构:
Univ Nottingham, Fac Engn, Dept Chem & Environm Engn, Malaysia Campus,Jalan Broga, Semenyih 43500, Selangor Darul, Malaysia
Univ Nottingham, Fac Engn, Ctr Food & Bioprod Proc, Mfg & Ind Proc Div, Malaysia Campus,Jalan Broga, Semenyih 43500, Selangor Darul, MalaysiaUniv Malaya, Fac Sci, Inst Biol Sci, Kuala Lumpur 50603, Malaysia