Slurry Hydrotreatment of Biomass Materials over Metal Sulfide-based Supported and Unsupported Catalysts
Doktorsavhandling, 2023

The scarcity of fossil feedstocks and the deterioration of the current global climate condition have prompted the search for reliable alternatives for fossil fuel replacement. Biomass feedstocks are abundant, carbon-rich, and renewable bioresources that can be used to produce renewable bio-oils that can fill the gap left by fossil-derived oils. Such bio-oils require an upgrading process, such as catalytic hydrodeoxygenation (HDO), to improve their quality for use as advanced biofuels and chemicals. Transition metal sulfides (TMS) are typically used in the traditional petroleum refining industry. In this thesis, we have explored the use of unsupported and supported metal sulfides in the hydrotreatment of Propylguaiacol (PG), a bio-oil model compound, Kraft lignin (KL), and pyrolysis bio-oil. In the recent work, the co-processing of the Kraft lignin and pyrolysis oil over the unsupported NiMoS was also performed.

Firstly, MoS2 supported on γ-Al2O3 catalysts and promoted by transition metals, such as Nickel (Ni), Copper (Cu), Zinc (Zn), and Iron (Fe) were evaluated for the HDO of PG in a batch reactor setup. The catalyst screening results showed that the sulfided Ni-promoted catalyst gave a 94% yield of deoxygenated cycloalkanes, however, 42% of the phenolics remained in the reaction medium after 5 h for the sulfided Cu-promoted catalyst A pseudo-first kinetic model that took into consideration the main side reactions was developed to elucidate the deoxygenation routes for the HDO of PG using sulfided catalysts. It was demonstrated that the activity of the transition metal promoters for the HDO of PG correlated to the yield of deoxygenated products from the hydrotreatment of KL. Further, the effect of the annealing treatment of a hydrothermally synthesized unsupported MoS2 dispersed catalyst was studied and evaluated for the HDO of PG. The annealing treatment of the as-synthesized catalyst under N2 flow at 400 °C for 2 h was found to enhance the HDO activity of PG. The annealed unsupported MoS2 demonstrated a high capacity for deoxygenation with a selectivity of 78.6% and 20.1% for cycloalkanes and aromatics from KL hydrotreatment, respectively. The results also indicate that a catalyst with high activity for deoxygenation and hydrogenation reactions can suppress char formation and favor a high lignin bio-oil yield.

The main hurdle during Kraft lignin liquefaction was the occurrence of repolymerization reactions during depolymerization that lead to the production of undesired solid char residues and subsequently cause low bio-oil yield. In this regard, the combination of NiMo sulfides with various ultra-stable Y zeolites (USY) for the KL hydrotreatment was studied. The use of the physical mixture of the unsupported NiMoS and the USY support was also studied to better understand the role of the catalyst components, and their interactions during lignin depolymerization, HDO, and also repolymerization of the reactive lignin intermediates. Further work was then extended to the co-hydrotreatment of KL and pyrolysis oil over the unsupported NiMo Sulfides. The synergistic effect between the complex feedstocks (KL and pyrolysis oil) was further explored by investigating the effect of supplementing various bio-oil monomers during KL liquefaction. It was found that the strategy of co-feeding bio-derived monomers and pyrolysis oil in the KL hydrotreatment presented an insight for co-processing and also the role of second co-feed was able to facilitate efficient lignin depolymerization increasing the desired bio-liquid yield and limiting lignin condensation. Further, a two-stage fast pyrolysis bio-oils (FPBO) processing concept that involves first a stabilization step in the slurry hydrocracker over an unsupported NiMoS and then followed by downstream fixed-bed hydrotreating producing renewable hydrocarbon was studied. The liquid products were thoroughly analyzed to understand their chemical and physical properties.

Hydrotreatment

Kraft lignin

Transition metals

Slurry hydrocracking

Propylguaiacol

Advanced biofuels

MoS2

Reaction network

Pyrolysis oil

Unsupported TMS

KA
Opponent: Professor Anker Degn Jensen, Danmarks Tekniske Universitet i Danmark

Författare

You Wayne Cheah

Chalmers, Kemi och kemiteknik, Kemiteknik

Elucidating the role of NiMoS-USY during the hydrotreatment of Kraft lignin

Chemical Engineering Journal,; Vol. 442(2022)

Artikel i vetenskaplig tidskrift

Thermal annealing effects on hydrothermally synthesized unsupported MoS2 for enhanced deoxygenation of propylguaiacol and kraft lignin

Sustainable Energy and Fuels,; Vol. 5(2021)p. 5270-5286

Artikel i vetenskaplig tidskrift

Role of transition metals on MoS<inf>2</inf>-based supported catalysts for hydrodeoxygenation (HDO) of propylguaiacol

Sustainable Energy and Fuels,; Vol. 5(2021)p. 2097-2113

Artikel i vetenskaplig tidskrift

Y. W. Cheah, R. Intakul, M. A. Salam, J. Sebastian, P. Ho, P. Arora, O. Öhrman, L. Olsson, and D. Creaser, Slurry Co-hydroprocessing of Kraft lignin and pyrolysis oil over unsupported NiMoS catalyst: a strategy for char suppression

N. Bergvall, Y. W. Cheah, C. Bernlind, A. Bernlind, L. Sandström, L. Olsson, D. Creaser, and O. Öhrman, Upgrading of Fast Pyrolysis Bio-Oils to Renewable Hydrocarbons using Slurry- and Fixed Bed Hydroprocessing

The rising global atmospheric CO2 concentration caused by the combustion of fossil fuels has prompted the search for alternative renewable and sustainable energy sources. Sweden has set an ambitious goal to achieve net zero greenhouse gas (GHG) emissions by 2045 and further realize negative emissions. To achieve this, drop-in solutions are needed and also continuous joint efforts are required to improve existing renewable fuel production capabilities. Moreover, exploring and diversifying the existing renewable feedstocks portfolio is more than imperative to meet the current feedstock demand.

This thesis focuses on the use of bio-oil model compounds, Kraft lignin, and also pyrolysis oil as renewable sources for the production of fuel-like components via catalytic slurry hydrotreatment. This hydroprocessing technology selectively removes sulfur, nitrogen, and oxygen moieties and also impurities with hydrogen gas as a co-reactant and in the presence of sulfide-based catalysts in supported or unsupported form. One of the main hurdles for hydrotreating Kraft lignin is the production of undesired char residues that hamper process economy and its further upscaling. We developed an understanding of the causes of the undesired solid production by studying different reaction conditions and also exploring ways to mitigate char production. The concept of co-processing of renewable feeds was also tested in this work to better understand the role of a second reactant in the hydrotreatment system. Furthermore, a fast pyrolysis bio-oil (FPBO) derived from biomass residues was first hydrotreated into a more stabilized bio-intermediate in a slurry hydrocracker over an unsupported NiMo sulfide and then underwent a continuous hydrotreatment to produce renewable hydrocarbons. Moreover, the thesis also summarizes the current state of the art in terms of understanding of reaction networks, mechanisms, and catalytic materials deactivation for the catalytic upgrading of renewable feedstocks over metal sulfide catalysts that are widely used in fuel refineries. The major challenges involved with scaling up renewable feedstock hydrotreatment processes is discussed.

Renewable energies play an important role in the complex energy system while transitioning towards a circular economy. Renewable liquid fuels will remain one of the decarbonization measures for the foreseeable future, particularly for decarbonizing ‘hard-to-abate’ industries where electrification is still in an exploration phase, for instance, aviation and marine sectors.

Slurry hydrokrackning av biooljor i komplext raffinaderi

Energimyndigheten (41253-2), 2018-01-01 -- 2021-12-31.

Drivkrafter

Hållbar utveckling

Styrkeområden

Energi

Ämneskategorier

Kemiska processer

Organisk kemi

Infrastruktur

Chalmers materialanalyslaboratorium

ISBN

978-91-7905-867-8

Doktorsavhandlingar vid Chalmers tekniska högskola. Ny serie: 5333

Utgivare

Chalmers

KA

Opponent: Professor Anker Degn Jensen, Danmarks Tekniske Universitet i Danmark

Mer information

Senast uppdaterat

2023-06-16