Role of temperature in the biomass steam pyrolysis in a conical spouted bed reactor

Autor: Maite Artetxe, Javier Bilbao, Gartzen Lopez, Martin Olazar, Maider Amutio, Laura Santamaria, Enara Fernandez, Aitor Arregi

Publikováno v: Addi. Archivo Digital para la Docencia y la Investigación
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[EN] The steam pyrolysis of pinewood sawdust has been conducted in a bench scale plant provided with a conical spouted bed reactor (CSBR). This process is of uttermost relevance for the in-line valorisation of pyrolysis volatiles, specifically for th

Externí odkaz: https://explore.openaire.eu/search/publication?articleId=doi_dedup___::b580bbf724cec5d35ac1e84212fadff9
http://hdl.handle.net/10810/55115

Sorption enhanced ethanol steam reforming on a bifunctional Ni/CaO catalyst for H-2 production

Autor: Chunfei Wu, Leire Olazar, Martin Olazar, Gartzen Lopez, Laura Santamaria, Maria Cortazar, Shuzhuang Sun, Enara Fernandez, Maite Artetxe

Publikováno v: Addi. Archivo Digital para la Docencia y la Investigación
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Cortazar, M, Sun, S, Wu, C, Santamaria, L, Olazar, L, Fernandez, E, Artetxe, M, Lopez, G & Olazar, M 2021, ' Sorption enhanced ethanol steam reforming on a bifunctional Ni/CaO catalyst for H 2 production ', Journal of Environmental Chemical Engineering, vol. 9, no. 6, 106725 . https://doi.org/10.1016/j.jece.2021.106725

[EN]The activity and stability of a 10 wt%NiO/CaO catalyst were tested in the sorption enhanced ethanol steam reforming (SEESR) in a fluidized bed reactor. The effect of temperature in the 600-750 degrees C range was analyzed and the performance of t

Externí odkaz: https://explore.openaire.eu/search/publication?articleId=doi_dedup___::bb3fe47821cab89023fde7581636a3fc
http://hdl.handle.net/10810/54485

Contributors

Autor: H Abbhijith, Farah Binti Ahmad, Iftikhar Ahmad, Mohd Hatta Maziati Akmal, Khalideh Al bkoor Alrawashdeh, Farman Ali, Nisar Ali, Shahid Pervez Ansari, Graziella C. Antonio, Aitor Arregi, Maite Artetxe, Abdullah M. Asiri, Saira Attique, Linda Barelli, Pietro Bartocci, Madeeha Batool, Gianni Bidini, Muhammad Bilal, Pietro Elia Campana, Caio H.S. Cenedese, M. Chakravarthy, Arunkumar Chandrasekaran, Prem Kumar Chaurasiya, Ja Young Cho, Maria Cortazar, Umberto Desideri, G. Nandhini Devi, Kelly C.R. Drudi, Francesco Fantozzi, Enara Fernandez, P Ganeshkumar, Hamid Raza Godini, Oliver Goerke, Eid Gul, Amal I. Hassan, Asif Hayat, Alia Tasnim Hazmi, Firzanah Hisham, Md. Faruque Hossain, Ahmad Husain, Hafiz M.N. Iqbal, Muhammad Rizwan Javed, Hyun Yi Jung, Anish Khan, Imran Khan, Mohammad Mujahid Ali Khan, Rafaqat Khurshid, Joong Kyun Kim, Nan Young Kim, Juliana Tófano C. Leite, Hailong Li, Gartzen Lopez, Katherine B.B. Marana, Joseph John Marshal S, Sikandar I. Mulla, Prerana Nashine, Martin Olazar, Santiago Orozco, Pankaj Pathak, M Karthic Raja, Upendra Rajak, Sakthivel Rajamohan, R Sakthivel, Hosam M. Saleh, Shimon Yohan Samuel, Laura Santamaria, Asma Tufail Shah, Mohd Urooj Shariq, Thokchom Subhaschandra Singh, Sweta Sinha, G. Srisowmeya, Senthilmurugan Subbiah, Kondru Gnana Sundari, Ikram Uddin, Tikendra Nath Verma, Jinyue Yan, Haiping Yang, Qing Yang

Externí odkaz: https://explore.openaire.eu/search/publication?articleId=doi_________::871b2911ed3c7ed59137fe9ade02f9bf
https://doi.org/10.1016/b978-0-323-90150-5.00034-0

Conditioning the volatile stream from biomass fast pyrolysis for the attenuation of steam reforming catalyst deactivation

Autor: Enara Fernandez, Laura Santamaria, Maite Artetxe, Maider Amutio, Aitor Arregi, Gartzen Lopez, Javier Bilbao, Martin Olazar

Publikováno v: Fuel. 312:122910

Externí odkaz: https://explore.openaire.eu/search/publication?articleId=doi_________::620b305f099278a5f8e8ce058e00db7a
https://doi.org/10.1016/j.fuel.2021.122910

In line upgrading of biomass fast pyrolysis products using low-cost catalysts

Autor: Laura Santamaria, Maite Artetxe, Gartzen Lopez, Maider Amutio, Enara Fernandez, Martin Olazar, Javier Bilbao, Aitor Arregi

Publikováno v: Fuel. 296:120682

Biomass pyrolysis and the in-line catalytic cracking of the pyrolysis volatile stream has been approached in this study. The pyrolysis step was carried out in a conical spouted bed reactor at 500 °C, whereas the inert sand or the cracking catalysts

Externí odkaz: https://explore.openaire.eu/search/publication?articleId=doi_________::2a13932be2e4570109ddd78ddb21d67a
https://doi.org/10.1016/j.fuel.2021.120682