Jose Luis Pinilla
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Jose Luis Pinilla has a total of 147 co-authors. Here are the top co-authors by number of shared publications:
- Isabel Suelves
Instituto de Carboquímica, CSIC, Miguel Luesma Castán 4, 50018 Zaragoza, Spain
54 shared publications R. Moliner
32 shared publications- Daniel Torres
Instituto de Carboquímica, CSIC, Miguel Luesma Castán 4, 50018 Zaragoza, Spain
29 shared publications - Maria Jesus Lázaro
Instituto de Carboquímica, CSIC, Miguel Luesma Castán 4, 50018 Zaragoza, Spain
29 shared publications Isabel Suelves
21 shared publications- Marcos Millan
Department of Chemical Engineering, Interdisciplinary Research Center for Refining and Advanced Chemicals, King Fahd University of Petroleum and Minerals
14 shared publications
Latest Publications
- Open Access
- 9 November 2026
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 291
Acid-Base Hydrothermal Pretreatments to Improve the Catalytic Activity of Low-Grade Hematite Iron Ore in Methane Cracking: Role of CaO and MgO Impurities
- 9 November 2026
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 291
Open AccessAcid-Base Hydrothermal Pretreatments to Improve the Catalytic Activity of Low-Grade Hematite Iron Ore in Methane Cracking: Role of CaO and MgO Impurities
- Open Access
- 26 February 2026
- Published by Elsevier in SSRN Electronic Journal
In-situ hydrogen sources for the continuous catalytic hydroconversion of waste cooking oil to green diesel
Hydrotreatment of waste cooking oil (WCO) offers a cleaner route than transesterification for producing diesel-range transportation biofuels, primarily C15-C18 linear paraffins (green diesel). This work evaluates the H2-free hydrotreatment of WCO using methanol, isopropanol and formic acid as in-situ hydrogen donors over a Mo2C/CNF catalyst. This catalyst delivered an 86 % C15-C18 yield at 350 ºC with complete conversion using external H2. Reactions were performed in a continuous trickle-bed reactor at 350 ºC and 70 bar. Additionally, donor decomposition was also studied under N2 at 70 bar and 250-350 ºC to monitor H2 formation in the absence of WCO. Gas-phase analysis demonstrates that hydrogen was supplied exclusively via in-situ H2 formation, with no evidence supporting a dominant catalytic transfer hydrogenation pathway. The catalyst selectively converted WCO to diesel-range hydrocarbons without promoting significant cracking. Under an initial WCO/donor ratio of 70/30 v/v, hydroconversion was limited for all donors, but formic acid produced the highest C15-C18 fraction and the most hydrogenated product slate. Increasing formic acid to 45 vol.% raised diesel yield to ~60 mol %, approaching the performance obtained with external H2. Liquid products were characterised by GC-MS and GC-FID, and, to improve separation and semi-quantitative assessment of complex fractions, including compounds lacking chromophores or with poor UV absorption (saturated hydrocarbons, olefins), High-Performance Thin-Layer Chromatography (HPTLC) was incorporated as a complementary analytical technique, obtaining a repeatable and informative profiling of products. Beyond performance assessment, this study provides mechanistic insight into donor decomposition and hydrogen generation under continuous operation, constituting the first systematic comparison of multiple in-situ hydrogen sources for the continuous upgrading of a real waste-derived feedstock and demonstrating a practical pathway toward H2-free WCO hydrotreatment.
- 26 February 2026
- Published by Elsevier in SSRN Electronic Journal
Open AccessIn-situ hydrogen sources for the continuous catalytic hydroconversion of waste cooking oil to green diesel
Hydrotreatment of waste cooking oil (WCO) offers a cleaner route than transesterification for producing diesel-range transportation biofuels, primarily C15-C18 linear paraffins (green diesel). This work evaluates the H2-free hydrotreatment of WCO using methanol, isopropanol and formic acid as in-situ hydrogen donors over a Mo2C/CNF catalyst. This catalyst delivered an 86 % C15-C18 yield at 350 ºC with complete conversion using external H2. Reactions were performed in a continuous trickle-bed reactor at 350 ºC and 70 bar. Additionally, donor decomposition was also studied under N2 at 70 bar and 250-350 ºC to monitor H2 formation in the absence of WCO. Gas-phase analysis demonstrates that hydrogen was supplied exclusively via in-situ H2 formation, with no evidence supporting a dominant catalytic transfer hydrogenation pathway. The catalyst selectively converted WCO to diesel-range hydrocarbons without promoting significant cracking. Under an initial WCO/donor ratio of 70/30 v/v, hydroconversion was limited for all donors, but formic acid produced the highest C15-C18 fraction and the most hydrogenated product slate. Increasing formic acid to 45 vol.% raised diesel yield to ~60 mol %, approaching the performance obtained with external H2. Liquid products were characterised by GC-MS and GC-FID, and, to improve separation and semi-quantitative assessment of complex fractions, including compounds lacking chromophores or with poor UV absorption (saturated hydrocarbons, olefins), High-Performance Thin-Layer Chromatography (HPTLC) was incorporated as a complementary analytical technique, obtaining a repeatable and informative profiling of products. Beyond performance assessment, this study provides mechanistic insight into donor decomposition and hydrogen generation under continuous operation, constituting the first systematic comparison of multiple in-situ hydrogen sources for the continuous upgrading of a real waste-derived feedstock and demonstrating a practical pathway toward H2-free WCO hydrotreatment.
- Open Access
- 22 December 2025
- Published by Elsevier in Biomass and Bioenergy
- Vol. 208
Tuning hydroconversion performance of n-hexadecane over Ni/silica-alumina catalysts: Role of Si/Al ratio and nickel loading
- 22 December 2025
- Published by Elsevier in Biomass and Bioenergy
- Vol. 208
Open AccessTuning hydroconversion performance of n-hexadecane over Ni/silica-alumina catalysts: Role of Si/Al ratio and nickel loading
- Open Access
- 19 November 2025
- Published by Elsevier in Bioresource Technology
- Vol. 442, 133659
From waste to fuel: catalytic conversion of waste cooking oil in batch and continuous modes
- 19 November 2025
- Published by Elsevier in Bioresource Technology
- Vol. 442, 133659
Open AccessFrom waste to fuel: catalytic conversion of waste cooking oil in batch and continuous modes
- Open Access
- 20 June 2025
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 146, 149723
Blueish hydrogen production via methane pyrolysis and remote CO2 capture and storage
- 20 June 2025
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 146, 149723
Open AccessBlueish hydrogen production via methane pyrolysis and remote CO2 capture and storage
- 24 February 2025
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 111, 83-94
High-energy milling of iron ore into an efficient catalyst for cracking of methane and biogas
- 24 February 2025
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 111, 83-94
High-energy milling of iron ore into an efficient catalyst for cracking of methane and biogas
- Open Access
- 15 November 2024
- Published by Elsevier in Biomass and Bioenergy
- Vol. 191
Hydroprocessing of waste cooking oil to produce liquid fuels over Ni-Mo and Co-Mo supported on carbon nanotubes
- 15 November 2024
- Published by Elsevier in Biomass and Bioenergy
- Vol. 191
Open AccessHydroprocessing of waste cooking oil to produce liquid fuels over Ni-Mo and Co-Mo supported on carbon nanotubes