(620d) Optimal Biochar Catalyst Screening for Upgrading Pyrolysis Products | AIChE

(620d) Optimal Biochar Catalyst Screening for Upgrading Pyrolysis Products

Authors 

Hughes, M., Georgia Institute of Technology
Tong, Y., Stantec Inc.
Zhou, J., Shanghai University
Cortes Lopez, H., California State University, Bakersfield
Singer, S., Marquette University
Zitomer, D., Marquette University
McNamara, P., Marquette University
Kreutter, W., Marquette University
Bio-oil and pyrolysis gas (py-gas) are two major energy products generated from pyrolysis. However, all pyrolysis technologies produce bio-oil with undesired properties such as high viscosity, water content, acidity, and corrosiveness that requires special equipment for direct combustion or costly upgrading to produce drop-in-grade fuel. In contrast, py-gas can more easily be used in conventional power generators such as internal combustion engines. Thus, processes that improve py-gas yield while minimizing bio-oil production can be beneficial for convenient on-site energy recovery. Catalytic pyrolysis, specifically, could be an efficient means to reduce bio-oil production while increasing py-gas yield and maintaining biochar production. Therefore, biochar was assessed as a cost-efficient catalyst to reduce bio-oil production and increase py-gas production.

Biochars derived from six industrial carbonaceous wastes were evaluated for the first time in terms of their catalytic abilities during pyrolysis. Catalytic performance of these biochar catalysts was also compared to two popular mineral catalysts, calcined dolomite and sintered olivine, which have been extensively studied for tar reduction during thermochemical conversions. Paper mill sludge (p-sludge) biochar was the optimal catalyst based on its high py-gas production and py-gas energy, low catalyst loading, and long catalyst life. The p-sludge biochar catalyst approximately doubled py-gas yield compared to the control test. In addition, p-sludge biochar significantly decreased bio-oil yield (e.g. reduced by 40% at 800°C) and improved bio-oil quality by decomposing heavy hydrocarbons. The bio-oil catalyzed by p-sludge biochar contained fewer organic constituents based on GC-MS and GC-FID analyses. The catalytic activity of p-sludge biochar was stable and the majority of energy inherent to the products shifted from bio-oil to py-gas over four cycles of catalyst use. The p-sludge biochar had a high calcium content (e.g. 39% dry weight basis of 800°C biochar) which likely played an important role in upgrading pyrolysis products.