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4º BIOCOM - Avaliação técnico-econômica da implementação de um sistema de cul... - 0 views

  • a biomassa de microalgas tendo em vista as alternativas de oleaginosa disponíveis no mercado, o que contribuiria para a opção da não realização do projeto. O custo da tonelada de biomassa de microalgas produzida seria de R$ 3.155,61. A cultura de microalga poderia retirar, em 10 anos, até
    • Pannir selvam
       
      4º BIOCOM - Avaliação técnico-econômica da implementação de um sistema de cultivo de microalgas na usina termelétrica Barbosa Lima Sobrinho com vista à biofixação de CO2 http://www.abq.org.br/biocom/2011/trabalhos/76-9524.htm … @ufrngpec
selvamecobr

Energy-balance-of-algal-biogas-production.pdf - 0 views

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    algae biogas chp
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    algae biogas chp
selvamecobr

Energy-balance-of-algal-biogas-production.pdf - 0 views

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    algae biogas chp
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    algae biogas chp
selvamecobr

Energy-balance-of-algal-biogas-production.pdf - 0 views

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    algae biogas chp
selvamecobr

Energy-balance-of-algal-biogas-production.pdf - 0 views

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    algae biogas chp
selvamecobr

Energy-balance-of-algal-biogas-production.pdf - 0 views

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    algae biogas chp
selvamecobr

Energy-balance-of-algal-biogas-production.pdf - 0 views

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    algae biogas publicados
selvamecobr

Energy-balance-of-algal-biogas-production.pdf - 0 views

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    alga biogas trab publicados
biomassabr

Industrial Symbiosis for the development of Biofuel Production.pdf - 0 views

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    analise entrada saia
Pannir selvam

Catalytic steam reforming of model biogas - ScienceDirect - 0 views

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    Catalytic steam reforming of a model biogas (CH4/CO2 = 60/40) is investigated to produce H2-rich synthesis gas. Gas engines benefit from synthesis gas fuel in terms of higher efficiency and lower NOx production when compared to raw biogas or CH4. The process is realized in a fixed bed reactor with a Ni-based catalyst on CaO/Al2O3 support. To optimize the performance, the reactor temperature and the amount of excess steam are varied. The experimental results are compared to the theoretical values from thermodynamic calculation and the main trends of CH4 conversion and H2 yield are analyzed and verified. Finally, optimal reactor temperature is pointed out and a range of potential steam to methane ratios is presented. The experimental results will be applied to design a steam reformer at an existing anaerobic biomass fermentation plant in Strem, Austria.
Pannir selvam

http://jukuri.luke.fi/bitstream/handle/10024/540187/luke-luobio_33_2017.pdf?sequence=1 - 0 views

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    finsih micro algae
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