@article{ford_immer_lamb_2012, title={Palladium Catalysts for Fatty Acid Deoxygenation: Influence of the Support and Fatty Acid Chain Length on Decarboxylation Kinetics}, volume={55}, ISSN={["1572-9028"]}, DOI={10.1007/s11244-012-9786-2}, number={3-4}, journal={TOPICS IN CATALYSIS}, author={Ford, Jeffrey P. and Immer, Jeremy G. and Lamb, H. Henry}, year={2012}, month={May}, pages={175–184} }
 @article{immer_kelly_lamb_2010, title={Catalytic reaction pathways in liquid-phase deoxygenation of C18 free fatty acids}, volume={375}, ISSN={["1873-3875"]}, DOI={10.1016/j.apcata.2009.12.028}, abstractNote={The liquid-phase deoxygenation of stearic, oleic, and linoleic acids employing a 5 wt% Pd/C catalyst was investigated using on-line quadrupole mass spectrometry (QMS). Catalytic deoxygenation of stearic acid (SA) under He occurs primarily via decarboxylation; the liquid products are n-heptadecane and heptadecenes. On-line QMS revealed concomitant CO2 and H2 evolution which can explain the greater than expected heptadecene yields at low to intermediate conversions. After essentially complete SA conversion, hydrogenation of heptadecenes via hydrogen transfer from the dodecane solvent results in 98% n-heptadecane yield. The initial rate of SA decarboxylation under 10% H2 is lower than under He; however, by avoiding the formation of unsaturated products the reaction requires much less time to reach completion. The SA decarboxylation rate under 10% H2 is 6-fold slower in heptadecane than in dodecane. This apparent solvent effect is explained by the lower vapor pressure of heptadecane resulting in greater H2 inhibition of the decarboxylation reaction. Our results demonstrate that the unsaturated C18 free fatty acids, oleic and linoleic, must be hydrogenated to SA before decarboxylation can proceed at a significant rate. Oleic acid (OA) deoxygenation under He occurs very slowly and primarily via decarbonylation. In contrast, OA deoxygenation under 10% H2 occurs facilely via hydrogenation to SA followed by decarboxylation. Since hydrogenation is complete during heating to reaction temperature, the decarboxylation kinetics and product yields are not affected by the initial unsaturation of the reactant.}, number={1}, journal={APPLIED CATALYSIS A-GENERAL}, author={Immer, Jeremy G. and Kelly, M. Jason and Lamb, H. Henry}, year={2010}, month={Feb}, pages={134–139} }
 @article{immer_lamb_2010, title={Fed-Batch Catalytic Deoxygenation of Free Fatty Acids}, volume={24}, ISSN={["1520-5029"]}, DOI={10.1021/ef100576z}, abstractNote={Fed-batch catalytic deoxygenation of C18 free fatty acids (FFAs) to n-heptadecane was demonstrated in a 50 mL stirred autoclave reactor with continuous FFA injection via a high-pressure syringe pump. High selectivity to the hydrogen-neutral decarboxylation pathway was achieved using a 5 wt % Pd/C catalyst at 300 °C under 5% H2 (15 atm total pressure); the maximum quasi-steady-state deoxygenation rate under these conditions was 0.46 mmol gcat−1 min−1 [0.083 s−1 turnover frequency (TOF)] with 95% CO2 selectivity. In a separate experiment, quasi-steady-state SA deoxygenation activity was maintained for >24 h at 0.29 mmol gcat−1 min−1 (0.053 s−1 TOF) with 92% CO2 selectivity. When higher H2 partial pressures were employed, an abrupt switchover in reaction pathway and product selectivity from decarboxylation (CO2) to decarbonylation (CO) was observed. Higher CO selectivity leads to increased H2 consumption because of hydrogenation of heptadecenes, the primary products of the decarbonylation pathway. We infer t...}, number={10}, journal={ENERGY & FUELS}, author={Immer, Jeremy G. and Lamb, H. Henry}, year={2010}, month={Oct}, pages={5291–5299} }