Technoeconomic Feasibility of a Sunflower Husk Fast Pyrolysis Value Chain for the Production of Advanced Biofuels.

Biofuels are required to reach the target set out by the European Commission's Transport mandate in the RED II (Renewable Energy Directive) for 2020-2030. To avoid indirect land use change, waste biomass resources such as sunflower husks can be used for advanced biofuel production. A process simulation and technoeconomic assessment of three fast pyrolysis plant scenarios were conducted. The nature of the waste feedstock has an effect on the value chain configuration, fast pyrolysis, and upgrading process design. Considering the difficulties with the transport and storage of biogenic waste due to low bulk density or hazardous and pathogenic content in case of transporting untreated sunflower husks, it is recommended to use a hub-and-spoke type of decentralized value chain configuration. The fast pyrolysis plants are located close to the feedstock, and the fast pyrolysis bio-oil (FPBO) is transported to a single upgrading facility, colocated at an existing refinery. The upgraded FPBO is then cofed into an FCC (fluidized catalyst cracker), where partially green biofuels such as gasoline and diesel are produced. For the fast pyrolysis process design, Scenario 2, treating 10 t/h of dry biomass with electricity and steam as coproducts, has the most favorable economic results with a total capital investment (TCI) of 78 million Euro and operating expenses (OPEX) of 6 million Euro.

Environmental Performance Assessment of a Novel Process Concept for Propanol Production from Widely Available and Wasted Methane Sources.

Currently, propanol production highly depends on conventional fossil resources. Therefore, an alternative production process, denoted as "C123", is proposed and evaluated in which underutilized and methane-rich feedstocks such as biogas (scenario BG), marginal gas (scenario MG), and associated gas (scenario AG) are converted into propanol. A first modular-scale process concept was constructed in Aspen Plus, based on experimental data and know-how of the C123 consortium partners. The environmental performance of the considered scenarios was compared at the life cycle level by calculating key performance indicators (KPIs), such as the global warming burden. The results showed that scenario BG is the least dependent on fossil fuels for energy use. Scenario AG seems the most promising one based on almost all selected KPIs when taking into account the avoided gas flaring emissions. The performance of the C123 process concept could be improved by applying heat integration in the process concept.

Process design and economic analysis of a biorefinery co-producing itaconic acid and electricity from sugarcane bagasse and trash lignocelluloses.

Itaconic acid has economic potential as a commodity biochemical for the sugar industry, but its production is limited due to high production costs. Using cheaper and alternative lignocellulosic feedstocks together with achieving higher product titres have been identified as potential strategies for viable IA production. Consequently the use of sugarcane bagasse and trash for the production of itaconic acid (IA) and electricity have been investigated for an integrated biorefinery, where the production facility is annexed to an existing sugar mill and new combined heat and power (CHP) plant. Three IA biorefinery scenarios were designed and simulated in Aspen Plus®. Subsequent economic analyses indicated that cheaper feedstocks reduced the IA production cost from 1565.5 US$/t for glucose to 616.5 US$/t, but coal supplementation was required to sufficiently lower the production cost to 604.3 US$/t for a competitive IA selling price of 1740 US$/t, compared to the market price of 1800 US$/t.