Zobrazeno 1 - 10
of 36
pro vyhledávání: '"Richard J. French"'
Autor:
Calvin Mukarakate, Kristiina Iisa, Susan E. Habas, Kellene A. Orton, Mengze Xu, Connor Nash, Qiyuan Wu, Renee M. Happs, Richard J. French, Anurag Kumar, Elisa M. Miller, Mark R. Nimlos, Joshua A. Schaidle
Publikováno v:
Chem Catalysis. 2:1819-1831
Autor:
Joshua A. Schaidle, Stuart K. Black, Calvin Mukarakate, Earl Christensen, Richard J. French, Kathleen Brown, Michael B. Griffin, Thomas D. Foust, Kristiina Iisa, Kellene A. Orton, Scott E. Palmer
Publikováno v:
ACS Sustainable Chemistry & Engineering. 9:1235-1245
Catalytic fast pyrolysis (CFP) has been identified as a promising pathway for the production of renewable fuels and co-products. However, continued technology development is needed to increase proc...
Autor:
M. Brennan Pecha, Bruce D. Adkins, Joshua A. Schaidle, Thomas D. Foust, Kristiina Iisa, Michael B. Griffin, Peter N. Ciesielski, Richard J. French, Calvin Mukarakate, Meagan Crowley, Vivek S. Bharadwaj
Publikováno v:
Reaction Chemistry & Engineering. 6:125-137
Chemical reaction kinetics enable predictive scaling studies and process sensitivity analyses that can substantially accelerate commercial deployment of new catalytic transformation technologies. The absence of suitable kinetic parameters for catalyt
Autor:
Calvin Mukarakate, Kristiina Iisa, Naijia Hao, Arthur J. Ragauskas, Richard J. French, Himanshu Patel, Mark R. Nimlos, Kellene A. Orton
Publikováno v:
ACS Sustainable Chemistry & Engineering. 8:1762-1773
The impact of upgrading temperature and biomass-to-catalyst mass ratio on upgrading pine pyrolysis vapors over HZSM-5 was studied in a dual fluidized bed reactor system. Increasing the upgrading te...
Publikováno v:
Energy & Fuels. 32:12577-12586
Noble metal catalysts may be attractive for hydrotreating of catalytic fast pyrolysis (CFP) oils. Model mixtures of raw noncatalytic fast pyrolysis and CFP oils representative of upgrading over HZSM-5 were hydrotreated in a batch reactor at 250–360
Autor:
Kellene A. Orton, Earl Christensen, Abhijit Dutta, Joshua A. Schaidle, Kristiina Iisa, Nolan Wilson, Daniel A. Ruddy, Kurt M. Van Allsburg, Michael B. Griffin, Richard J. French, Hao Cai, Huamin Wang, Eric C. D. Tan, Connor P. Nash, Frederick G. Baddour, Daniel M. Santosa, Calvin Mukarakate
Publikováno v:
Energy & Environmental Science. 11:2904-2918
Catalytic fast pyrolysis (CFP) has emerged as an attractive process for the conversion of lignocellulosic biomass into renewable fuels and products. Considerable research and development has focused on using circulating-bed reactors with zeolite cata
Publikováno v:
Fuel. 207:413-422
Catalytic fast pyrolysis (CFP) bio-oils with different organic oxygen contents (4–18 wt%) were prepared in a bench-scale dual fluidized bed reactor system by ex situ CFP of southern pine over HZSM-5, and the oils were subsequently hydrotreated over
Autor:
Kristiina Iisa, Alexander R. Stanton, Kellene A. Orton, Richard J. French, Matthew M. Yung, Kimberly A. Magrini
Publikováno v:
Energy & Fuels. 30:9471-9479
Metal-impregnated (Ni or Ga) ZSM-5 catalysts were studied for biomass pyrolysis vapor upgrading to produce hydrocarbons using three reactors constituting a 100 000× change in the amount of catalyst used in experiments. Catalysts were screened for py
Autor:
Mark R. Nimlos, Matthew M. Yung, Kristiina Iisa, Watson Michael John, Jeroen ten Dam, Richard J. French, David K. Johnson, Kellene A. Orton
Publikováno v:
Energy & Fuels. 30:2144-2157
In situ and ex situ catalytic pyrolysis were compared in a system with two 2-in. bubbling fluidized bed reactors. Pine was pyrolyzed in the system with a catalyst, HZSM-5 with a silica-to-alumina ratio of 30, placed either in the first (pyrolysis) re
Autor:
Erica Gjersing, James Stunkel, Kristiina Iisa, Richard J. French, Michele D. Myers, Stuart K. Black
Publikováno v:
Energy & Fuels. 29:7985-7992
The effect of the catalyst type, hydroprocessing conditions, and feed preparation on the mild hydrotreating of biomass pyrolytic lignin was examined. Pyrolytic lignin oils were produced by water separation at 1:1 and 3:1 water/oil mass ratios. Hydrot