2022
DOI: 10.1016/b978-0-323-95879-0.50120-x
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Macroalgae-based integrated biorefinery for hydrocolloids, chemicals and advanced biofuels production

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Cited by 2 publications
(5 citation statements)
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“…As the optimal pathway does not account for the PHB extraction and purification section (S4) or the diethyl ether and hydrogen conversion sections (bioethanol is not further processed), the associated heat exchangers for these sections remain unused. It should be noted that stream splitting is not considered since this operation is not always attractive from a practical point of view, as it was previously presented by Casoni et al 9 Different utilities, including low-pressure steam (LPS), medium-pressure steam (MPS), and high-pressure steam (HPS), are available for use. In the optimal configuration, HX4 and HX1 use LPS and HPS, respectively.…”
Section: ■ Results and Discussionmentioning
confidence: 99%
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“…As the optimal pathway does not account for the PHB extraction and purification section (S4) or the diethyl ether and hydrogen conversion sections (bioethanol is not further processed), the associated heat exchangers for these sections remain unused. It should be noted that stream splitting is not considered since this operation is not always attractive from a practical point of view, as it was previously presented by Casoni et al 9 Different utilities, including low-pressure steam (LPS), medium-pressure steam (MPS), and high-pressure steam (HPS), are available for use. In the optimal configuration, HX4 and HX1 use LPS and HPS, respectively.…”
Section: ■ Results and Discussionmentioning
confidence: 99%
“…As the optimal pathway does not account for the PHB extraction and purification section (S4) or the diethyl ether and hydrogen conversion sections (bioethanol is not further processed), the associated heat exchangers for these sections remain unused. It should be noted that stream splitting is not considered since this operation is not always attractive from a practical point of view, as it was previously presented by Casoni et al…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…El análisis se centrará en la obtención final de 600 t/a de biosolvente DMI . Este escenario se compara con el de obtención de 244 t/a de alginato de sodio y 322 t/a de DMI 2022). En ambos casos, se requieren 1864 t/a de macroalga para la obtención de productos.…”
Section: Materiales Y Métodosunclassified
“…La segunda etapa implicó la realización de un inventario de datos de cada uno de los recursos de entrada y salida que afectan al producto teniendo en cuenta los límites de la biorrefinería estudiada y la unidad funcional previamente establecida. Es importante mencionar que todos los flujos necesarios para llevar a cabo el LCA se obtuvieron a partir de los trabajos previamente publicados por Casoni et al (2020;2022). En esta etapa se cuenta con bases de datos que contribuyen a recopilación de informacion de manera confiable para diversos productos y procesos.…”
Section: Materiales Y Métodosunclassified