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1.
Bioresour Technol ; 166: 508-17, 2014 Aug.
Artículo en Inglés | MEDLINE | ID: mdl-24950095

RESUMEN

The hemicelluloses fraction of black liquor is an underutilized resource in many chemical pulp mills. It is possible to extract and separate the lignin and hemicelluloses from the black liquor and use the hemicelluloses for biochemical conversion into biofuels and chemicals. Precipitation of the lignin from the black liquor would consequently decrease the thermal load on the recovery boiler, which is often referred to as a bottleneck for increased pulp production. The objective of this work is to techno-economically evaluate the production of sodium-free lignin as a solid fuel and butanol to be used as fossil gasoline replacement by fractionating black liquor. The hydrolysis and fermentation processes are modeled in Aspen Plus to analyze energy and material balances as well as to evaluate the plant economics. A mathematical model of an existing pulp and paper mill is used to analyze the effects on the energy performance of the mill subprocesses.


Asunto(s)
Biocombustibles , Fraccionamiento Químico/métodos , Citalopram/química , Papel , Aguas del Alcantarillado/química , Purificación del Agua/métodos , Adsorción , Citalopram/análisis , Conservación de los Recursos Energéticos , Cinética
2.
Bioresour Technol ; 161: 263-9, 2014 Jun.
Artículo en Inglés | MEDLINE | ID: mdl-24717319

RESUMEN

This paper presents a novel process for n-butanol production which combines a fermentation consuming carbon dioxide (succinic acid fermentation) with subsequent catalytic reduction steps to add hydrogen to form butanol. Process simulations in Aspen Plus have been the basis for the techno-economic analyses performed. The overall economy for the novel process cannot be justified, as production of succinic acid by fermentation is too costly. Though, succinic acid price is expected to drop drastically in a near future. By fully integrating the succinic acid fermentation with the catalytic conversion the need for costly recovery operations could be reduced. The hybrid process would need 22% less raw material than the butanol fermentation at a succinic acid fermentation yield of 0.7g/g substrate. Additionally, a carbon dioxide fixation of up to 13ktonnes could be achieved at a plant with an annual butanol production of 10ktonnes.


Asunto(s)
Butanoles/síntesis química , Fermentación , Ácido Succínico/metabolismo , Butanoles/economía , Catálisis , Ácido Succínico/economía
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