Bioenergy and full carbon dioxide sinking in sugarcane-biorefinery with post-combustion capture and storage: Techno-economic feasibility
Creators
- 1. Escola de Química, Federal University of Rio de Janeiro, CT, E, Ilha do Fundão, Rio de Janeiro, RJ, 21941-909 (Brazil)
Description
Highlights: • Sugarcane-biorefinery is retrofitted for bioenergy with carbon capture and storage. • 93% of CO2 from cogeneration and fermentation is captured for enhanced oil recovery. • Plantation CO2 uptake minus factory emissions gives 5.22 MtCO2/y negative emissions. • BECCS sugarcane-biorefinery is economically viable in some carbon-market scenarios. • Four studied scenarios of oil price, carbon tax, oil-CO2 ratio and cap-and-trade. -- Abstract: Sugarcane plantations promote impressive drainage of atmospheric carbon dioxide reaching 781 t/h for a 1000 t/h sugarcane-biorefinery. For first-generation bioethanol sugarcane-biorefineries, only 10% of sugarcane carbon dioxide equivalent leaves as hydrous-ethanol, while 90% return to atmosphere through bagasse-fired power cogeneration in steam-Rankine cycles. Thus, a sugarcane-biorefinery exports two bioenergy flows – electricity and hydrous-ethanol – and its impressive Bioenergy Carbon Capture and Storage potential is wasted. Capture of fermentation carbon dioxide merely means 5% of Bioenergy Carbon Capture and Storage efficiency. This work assesses a new sugarcane-biorefinery concept dramatically raising the Bioenergy Carbon Capture and Storage efficiency. With fermentation carbon dioxide already captured, it is advocated to implement 90% post-combustion capture of flue-gas carbon dioxide. Then, captured carbon dioxide is compressed and traded as Enhanced Oil Recovery agent transported to deep-water offshore oil fields via high-pressure pipelines counting on topographic gravitational effects to lower compression power. Aggregating pipeline/compression investment to the biorefinery, it is shown that such new Plantation-Biorefinery-Post-Combustion-Pipeline-Oil-Recovery enterprise is technically feasible for 5.22 MtCO2/y of Bioenergy Carbon Capture and Storage capacity and is economically feasible under certain conditions: (i) idle pipeline capacity rental to fossil carbon emitters at 10–20 USD/tCO2; (ii) recovered oil revenues traded at 1–2 bbl/tCO2 and 50–80 USD/bbl; (iii) carbon-taxation at 40–80 USD/tCO2; and (iv) carbon Cap-and-Trade at 30–70 USD/tCO2. Under such conditions the Plantation-Biorefinery-Post-Combustion-Pipeline-Oil-Recovery can attain 7 MMMUSD net value and 6 years payback-time.
Additional details
Identifiers
- DOI
- 10.1016/j.apenergy.2019.113633;
- PII
- S0306261919313200;
Publishing Information
- Journal Title
- Applied Energy
- Journal Volume
- 254
- Journal Page Range
- vp.
- ISSN
- 0306-2619
- CODEN
- APENDX
INIS
- Country of Publication
- United Kingdom
- Country of Input or Organization
- International Atomic Energy Agency (IAEA)
- INIS RN
- 55007737
- Subject category
- S09: BIOMASS FUELS; S25: ENERGY STORAGE;
- Descriptors DEI
- AFTERBURNERS; BAGASSE; BIOETHANOL; CARBON; CARBON DIOXIDE; CARBON SEQUESTRATION; COGENERATION; FERMENTATION; FLUE GAS; OILS; RANKINE CYCLE; SUGAR CANE
- Descriptors DEC
- AGRICULTURAL WASTES; AIR POLLUTION CONTROL; ALCOHOLS; BIOCONVERSION; CARBON COMPOUNDS; CARBON OXIDES; CHALCOGENIDES; CONTROL; ELEMENTS; EQUIPMENT; ETHANOL; GASEOUS WASTES; GRAMINEAE; HYDROXY COMPOUNDS; LILIOPSIDA; MAGNOLIOPHYTA; NONMETALS; ORGANIC COMPOUNDS; ORGANIC WASTES; OTHER ORGANIC COMPOUNDS; OXIDES; OXYGEN COMPOUNDS; PLANTS; POLLUTION CONTROL; POLLUTION CONTROL EQUIPMENT; POWER GENERATION; REEDS; SEPARATION PROCESSES; STEAM GENERATION; THERMODYNAMIC CYCLES; WASTES
Optional Information
- Copyright
- Copyright (c) 2019 Elsevier Ltd. All rights reserved.