Sciact
  • EN
  • RU

Catalytic Hydrotreatment of Fast-Pyrolysis Oil Using Non-Sulfided Bimetallic Ni-Cu Catalysts on a Al2O3 Support Научная публикация

Журнал Applied Catalysis B: Environmental
ISSN: 0926-3373
Вых. Данные Год: 2012, Том: 117-118, Страницы: 105-117 Страниц : 13 DOI: 10.1016/j.apcatb.2011.12.032
Авторы Ardiyanti A.R. 1 , Khromova S.A. 2 , Venderbosch R.H. 3 , Yakovlev V.A. 2 , Heeres H.J. 1
Организации
1 Chemical Engineering, University of Groningen, Nijenborgh 4, 9747 AG, Groningen, The Netherlands
2 Boreskov Institute of Catalysis, 5, pr. Akad. Lavrentieva, 630090 Novosibirsk, Russia
3 BTG Biomass Technology Group BV, Josink Esweg 34, 7545 PN Enschede, The Netherlands
Реферат: Fast pyrolysis oil from lignocellulosic biomass is an attractive energy carrier. However, to improve the product characteristics such as a reduced polarity and higher thermal stability, upgrading is required. We here report activities on the catalytic hydrotreatment of fast pyrolysis oil using bimetallic NiCu/-Al2O3 catalysts with various Ni/Cu ratios (0.32 to 8.1 w/w) at a fixed total metal intake of about 20 wt% with the objective to improve product properties for co-feeding applications in conventional oil refineries. Hydrotreatment reactions were initially carried out for a model compound (anisole, continuous set-up, 300 ◦C, 10 bar) and subsequently for fast pyrolysis oil (batch autoclave, 1 h at 150 ◦C followed by 3 h at 350 ◦C, at 100 bar initial pressure). Best results, i.e.the highest hydrodeoxygenation yield for experiments with anisole (75 mol%), and an upgraded oil with the most favorable properties for fast pyrolysis oil (high H/C ratio, low Mw of 500 g/mol, low thermogravimetric residue of 6.8 wt%), were obtained for a catalyst with a Ni to Cu wt% ratio of eight (16Ni2Cu). For this catalyst, hydrogen consumption was the highest (146 NL/kgPO). The findings were rationalized using a reaction network model earlier developed for Ru/C. Analysis of catalyst (ICP, HRTEM, XRD and TGA) before and after reaction showed the occurrence of leaching of both active metals (Ni and Cu) and support, as well as coke deposition on the support. The most active catalyst in the series (16Ni2Cu) also gave lowest leaching and coking levels in the series.
Библиографическая ссылка: Ardiyanti A.R. , Khromova S.A. , Venderbosch R.H. , Yakovlev V.A. , Heeres H.J.
Catalytic Hydrotreatment of Fast-Pyrolysis Oil Using Non-Sulfided Bimetallic Ni-Cu Catalysts on a Al2O3 Support
Applied Catalysis B: Environmental. 2012. V.117-118. P.105-117. DOI: 10.1016/j.apcatb.2011.12.032 WOS Scopus РИНЦ CAPlusCA OpenAlex Sciact
Даты:
Поступила в редакцию: 20 июн. 2011 г.
Принята к публикации: 22 дек. 2011 г.
Опубликована online: 12 янв. 2012 г.
Опубликована в печати: 1 мая 2012 г.
Идентификаторы БД:
Web of science: WOS:000303293300012
Scopus: 2-s2.0-84856360250
РИНЦ: 17975056
Chemical Abstracts: 2012:487611
Chemical Abstracts (print): 156:509778
OpenAlex: W2049962843
Sciact: 538
Цитирование в БД:
БД Цитирований
Scopus 242
OpenAlex 229
Альметрики: