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1.
Bioresour Technol ; 136: 78-86, 2013 May.
Artigo em Inglês | MEDLINE | ID: mdl-23562773

RESUMO

Biodiesel production from cotton-seed cake (CSC) and the pretreatment of the remaining biomass for dark fermentative hydrogen production was investigated. The direct conversion to biodiesel with alkali free fatty acids neutralization pretreatment and alkali transesterification resulted in a biodiesel with high esters content and physicochemical properties fulfilling the EN-standards. Blends of cotton-seed oil methyl esters (CME) and diesel showed an improvement in lubricity and cetane number. Moreover, CME showed good compatibility with commercial biodiesel additives. On the basis of conversion of the remaining CSC to sugars fermentable towards hydrogen, the optimal conditions included removal of the oil of CSC and pretreatment at 10% NaOH (w/w dry matter). The extreme thermophilic bacterium Caldicellulosiruptor saccharolyticus showed good hydrogen production, 84-112% of the control, from NaOH-pretreated CSC and low hydrogen production, 15-20% of the control, from the oil-rich and not chemically pretreated CSC, and from Ca(OH)2-pretreated CSC.


Assuntos
Biocombustíveis/análise , Biotecnologia/métodos , Gossypium/química , Hidrogênio/metabolismo , Sementes/química , Ácido Acético/metabolismo , Bactérias/metabolismo , Biocombustíveis/microbiologia , Biomassa , Óleo de Sementes de Algodão/química , Ésteres/análise , Fermentação , Ácido Láctico/biossíntese , Lubrificação , Oxirredução , Padrões de Referência
2.
Bioresour Technol ; 99(11): 5037-42, 2008 Jul.
Artigo em Inglês | MEDLINE | ID: mdl-17951052

RESUMO

The use of a heterogeneous catalyst, in the transesterification reaction of refined and acidic cottonseed oil for the production of methyl-esters (biodiesel) has been studied. The basic Mg-Al-CO3 hydrotalcite catalyst used showed a high activity for methanolysis and esterification reactions in a refined and an acidic cottonseed oil as well as in a representative high water content animal fat feed. The experiments were performed in a temperature range between 180 and 210 degrees C, in a batch reactor. The methanol to vegetable oil molar ratio was 6 to 1, while the catalyst concentration was fixed at 1 wt.% of the oil mass. Non-calcined and calcined forms of the catalyst were tested. The activity of the calcined catalyst was lower than the initial activity of the non-calcined catalytic system but it appeared the same with the reused non-calcined system.


Assuntos
Hidróxido de Alumínio/metabolismo , Hidróxido de Magnésio/metabolismo , Óleos de Plantas/metabolismo , Triglicerídeos/metabolismo , Catálise , Esterificação , Ácidos Graxos/metabolismo , Glicerol/metabolismo , Óleos de Plantas/química , Água
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