Deactivation of Catalysts and Reaction Kinetics for Upgrading of Renewable Oils
Doktorsavhandling, 2019

The transport sector is one of the main contributors of greenhouse gas emissions in the world. Advanced biofuels from renewable oils can play a decisive role in reducing carbon emissions from the transport sector. Advanced biofuels from waste streams like tall oil, used cooking oil etc. can lower the CO2 emissions in a range of up to 90% making our future and society more sustainable. Catalytic hydrodeoxygenation (HDO) is a process in which oxygen is selectively removed from renewable oils to produce advanced biofuels. These biofuels are drop-in hydrocarbons which can substitute fossil-based fuels without infrastructure or vehicle changes. This thesis focuses on aspects of catalyst deactivation and reaction kinetics during the production of such biofuels via HDO reactions.
Renewable oils can be sourced from varied streams like tall oil (paper industry residue), animal fats, used cooking oil etc. due to which their composition and innate contaminants can vary significantly. Phosphorus, alkali metals like potassium or sodium, iron, silicon, chlorides etc. are some of the common poisons present in renewable feedstocks which can cause catalyst deactivation during the upgrading process. In the first section of this thesis, the influence of iron (Fe), phosphorus (from phospholipid) and potassium (K) as poisons during HDO of fatty acids over molybdenum based sulfided catalysts was investigated. A range of concentration of poisons was evaluated to show that these poisons severely impacted the activity of catalysts. A change in selectivity was also seen, which is an important parameter to consider during the industrial production of biofuels. Different characterization techniques were employed to study the poison distribution on catalyst samples from lab experiments as well as from a refinery. It was suggested that Fe deposits preferentially near Ni-rich sites which deteriorated the ability of these catalysts to create active sites i.e. via sulfur vacancies. However, phosphorus resulted in irreversible phase transformation of the support to aluminum phosphate (AlPO4) which resulted in catalyst deactivation via pore blockage. In the comparative experiments, with spherical catalyst particles (1.8 mm), the Fe caused the strongest deactivation among P and K, based on the quantity added to feed oil. Although, considering the decrease in surface area per unit of deposited element after the experiment, then P caused the most deactivation. It was concluded that Fe deposited mostly near to the outer surface irrespective of concentration while P and K penetrated deeper in catalyst particles such that the distribution profile was dependent on the concentration.
Reaction kinetics of HDO of fatty acids provides critical knowledge which could be applied at the refining scale in process design and optimization. The activity and selectivity of NiMo catalyst during HDO of stearic acid was studied by varying reaction conditions like temperature, pressure, feed concentration and batch-reactor stirring rate and using intermediates like octadecanal and octadecanol. A deeper understanding of the reaction scheme and selectivities was developed based on the experimental results. A Langmuir–Hinshelwood-type mechanism was used to develop a kinetic model which well-predicted the changes in selectivities at varying reaction conditions.


Kinetic modeling

Catalyst deactivation


Advanced biofuels




Prakhar Arora

Chalmers, Kemi och kemiteknik, Kemiteknik, Kemisk apparat- och reaktionsteknik

Investigating the effect of Fe as a poison for catalytic HDO over sulfided NiMo alumina catalysts

Applied Catalysis B: Environmental,; Vol. 227(2018)p. 240-251

Artikel i vetenskaplig tidskrift

The role of catalyst poisons during hydrodeoxygenation of renewable oils - Prakhar Arora, Hoda Abdolahi, You Wayne Cheah, Muhammad Abdus Salam, Eva Lind Grennfelt, Henrik Rådberg, Derek Creaser, Louise Olsson

Kinetic study of hydrodeoxygenation of stearic acid as model compound for renewable oils

Chemical Engineering Journal,; Vol. 364(2019)p. 376-389

Artikel i vetenskaplig tidskrift

NiMoS on alumina-USY zeolites for hydrotreating lignin dimers: Effect of support acidity and cleavage of C-C bonds

Sustainable Energy and Fuels,; Vol. 4(2019)p. 149-163

Artikel i vetenskaplig tidskrift

Effect of Dimethyl Disulfide on Activity of NiMo Based Catalysts Used in Hydrodeoxygenation of Oleic Acid

Industrial & Engineering Chemistry Research,; Vol. 56(2017)p. 5547-5557

Artikel i vetenskaplig tidskrift

Investigation of the robust hydrothermal stability of Cu/LTA for NH3-SCR reaction

Applied Catalysis B: Environmental,; Vol. 246(2019)p. 242-253

Artikel i vetenskaplig tidskrift

Biofuels are fuels which are made from biomass or related materials.  They are classified as a form of renewable energy since biomass, i.e. the feedstock material, can be readily replenished without environmental impact. Several feedstocks, like agricultural residues (rice husk, wheat straw, cotton stalk etc.), residue from food processing (bagasse, non-edible oil seed cakes etc.), byproducts from the paper and pulp industry (tall oil etc.), used cooking oil from restaurants and forest residues could be used as feedstocks in the production of liquid biofuels. It should be noted that advanced biofuels like hydrogenated vegetable oils (HVO) are chemically similar to fossil-derived diesel, and thereby do not impair engine performance and mileage. The use of biofuels for the transport sector can reduce the emission of greenhouse gases (GHGs) by up to 90%. Thus, such biofuels are critical to reduce the unsustainable carbon emissions from the transport sector and to achieve the transition towards a sustainable society.

Fossil fuels like petrol, diesel, kerosene etc. are made up of different molecules containing carbon and hydrogen while biomass contains – carbon, hydrogen and oxygen. It is critical to remove the oxygen from these feedstocks before they can be used as fuels in the transportation sector. During a biofuel production process, via hydrodeoxygenation (HDO) reactions, these oxygen molecules are selectively removed while carbon and hydrogen remain. This is carried out in refineries using a catalyst to enable these reactions. These catalysts become deactivated which means their performance decreases with time during the production process. In this work, we studied how and what factors cause the deactivation of catalysts. We developed an understanding of deactivation mechanisms resulting from impurities present in renewable feedstocks. This knowledge could be beneficial for industry to prevent or delay catalyst deactivation and lead to biofuel production becoming even more efficient.

Alternativbränsleproduktion med användandet av biooljor från skogssektorn - Fundamentala studier av katalysatordeaktivering

Formas, 2014-01-01 -- 2018-12-31.


Hållbar utveckling






Kemiska processer

Annan kemiteknik




Doktorsavhandlingar vid Chalmers tekniska högskola. Ny serie: 4681


Chalmers tekniska högskola

Mer information

Senast uppdaterat