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Google Translate desenvolviimento de projetos - 0 views

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nptel india projeto gestão mooc curse producao pdf

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desenvolvimento de projetos

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Gestao de projeto, plano e producao - 1 views

GESTÃO DE PROJETOS (16 palestras) UMA VISÃO GERAL (1 palestra) 1. Gerenciamento de projetos: uma visão geral SELEÇÃO DE PROJETOS (4 palestras) 2. Identificação e triagem do projeto 3. Avaliaçã...

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Google Translate - 0 views

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Google Tradutor curso tecnologia produto natural - 0 views

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Google Tradutor lab virtual - 0 views

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secador lab simulacao projeto fluxograma

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Cogumelo Champignon - estruturas de produção e sistemas de cultivo | Cursos a... - 0 views

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Cogumelo Champignon - estruturas de produção e sistemas de cultivo | Cursos a Distância CPT https://www.cpt.com.br/cursos-agroindustria-cogumelos-comestiveis/artigos/cogumelo-champignon-estruturas-de-producao-e-sistemas-de-cultivo

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Catalytic steam reforming of model biogas - ScienceDirect - 0 views

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projeto gestão vapou reforma biogas

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Pannir selvam on 17 Mar 18

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.

<div class="cArrow"> </div><div class="cContentInner">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.</div>

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

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Gestao tecnologia (Miniempresa e Econegocio) - Google+ - 0 views

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Gestao tecnologia (Miniempresa e Econegocio) - Google+ - 0 views

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Gestao tecnologia (Miniempresa e Econegocio) - Google+ - 0 views

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producao limpas ecologia industrial SGA PmaisL

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producao limpas e ecologia industrial

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Gestao tecnologia (Miniempresa e Econegocio) - Google+ - 0 views

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producao limpas ecologia industrial SGA PmaisL

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producao limpas e ecologia industrial 2

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