Dataset.

Supplementary data for An innovative ‘sea-thermal’ synergetic biorefinery for biofuel production: Co-valorization of lignocellulosic and algal biomasses using seawater under hydrothermal conditions [Dataset]

Digital.CSIC. Repositorio Institucional del CSIC
oai:digital.csic.es:10261/359908
Digital.CSIC. Repositorio Institucional del CSIC
  • Zhou, Yingdong
  • Remón, Javier
  • Ding, Wei
  • Jiang, Zhicheng
  • Pinilla Ibarz, José Luis
  • Hu, Changwei
  • Suelves Laiglesia, Isabel
Solvents (chloroform and ethyl acetate) were obtained from Scharlau chemical company. The seawater (supplied by Rioka del Cantábrico, S.L.) was taken from the Matxitxako cape at the Urdaibai biosphere reserve in the Cantabrian Sea (Spain). The microalgae Chlorella Vulgaris was acquired to Biotiva (Germany) as a fine dehydrated powder and used without additional treatment. Almond hulls were from Marcona-type almonds harvested in Spain.-- A stainless-steel batch autoclave (300 mL) equipped with a speed-controlled mechanical stirrer (Parker Autoclave Engineers) was used for the hydrothermal experiments.-- Under a Creative Commons license BY-NC 4.0., The proximate analysis of algae and almond hulls were analyzed by thermogravimetric analysis (ISO-18134:2016, ISO-18122:2016 and ISO-18123:2016). The elemental composition of the feedstocks was determined using an elemental analyzer. The biochemical composition of almond hulls was determined by chemical titration according to Hu et al, whereas biochemical composition was provided by the supplier.-- Table S1: Properties and composition of seawater. Table S2: Characterization results of C. vulgaris and almond hulls. Table S3: Processing conditions and experimental results for the co-HTT of C. vulgaris and almond hulls. Table S4: Relative influence of feedstock composition and processing conditions and interactions based on ANOVA analyses and cause-effect Pareto principle. Table S5: Detailed GC-MS peak area for biocrude (area%). Table S6: Process Optimization: Theoretical values vs. Experimental values., Peer reviewed
 
DOI: http://hdl.handle.net/10261/359908
Digital.CSIC. Repositorio Institucional del CSIC
oai:digital.csic.es:10261/359908

HANDLE: http://hdl.handle.net/10261/359908
Digital.CSIC. Repositorio Institucional del CSIC
oai:digital.csic.es:10261/359908
 
Ver en: http://hdl.handle.net/10261/359908
Digital.CSIC. Repositorio Institucional del CSIC
oai:digital.csic.es:10261/359908

Digital.CSIC. Repositorio Institucional del CSIC
oai:digital.csic.es:10261/359908
Dataset. 2024

SUPPLEMENTARY DATA FOR AN INNOVATIVE ‘SEA-THERMAL’ SYNERGETIC BIOREFINERY FOR BIOFUEL PRODUCTION: CO-VALORIZATION OF LIGNOCELLULOSIC AND ALGAL BIOMASSES USING SEAWATER UNDER HYDROTHERMAL CONDITIONS [DATASET]

Digital.CSIC. Repositorio Institucional del CSIC
  • Zhou, Yingdong
  • Remón, Javier
  • Ding, Wei
  • Jiang, Zhicheng
  • Pinilla Ibarz, José Luis
  • Hu, Changwei
  • Suelves Laiglesia, Isabel
Solvents (chloroform and ethyl acetate) were obtained from Scharlau chemical company. The seawater (supplied by Rioka del Cantábrico, S.L.) was taken from the Matxitxako cape at the Urdaibai biosphere reserve in the Cantabrian Sea (Spain). The microalgae Chlorella Vulgaris was acquired to Biotiva (Germany) as a fine dehydrated powder and used without additional treatment. Almond hulls were from Marcona-type almonds harvested in Spain.-- A stainless-steel batch autoclave (300 mL) equipped with a speed-controlled mechanical stirrer (Parker Autoclave Engineers) was used for the hydrothermal experiments.-- Under a Creative Commons license BY-NC 4.0., The proximate analysis of algae and almond hulls were analyzed by thermogravimetric analysis (ISO-18134:2016, ISO-18122:2016 and ISO-18123:2016). The elemental composition of the feedstocks was determined using an elemental analyzer. The biochemical composition of almond hulls was determined by chemical titration according to Hu et al, whereas biochemical composition was provided by the supplier.-- Table S1: Properties and composition of seawater. Table S2: Characterization results of C. vulgaris and almond hulls. Table S3: Processing conditions and experimental results for the co-HTT of C. vulgaris and almond hulls. Table S4: Relative influence of feedstock composition and processing conditions and interactions based on ANOVA analyses and cause-effect Pareto principle. Table S5: Detailed GC-MS peak area for biocrude (area%). Table S6: Process Optimization: Theoretical values vs. Experimental values., Peer reviewed




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