Life cycle cost and economic assessment of biochar-based bioenergy production and biochar land application in Northwestern Ontario, Canada
© The Author(s). 2016
Received: 31 May 2016
Accepted: 26 August 2016
Published: 14 September 2016
Replacement of fossil fuel based energy with biochar-based bioenergy production can help reduce greenhouse gas emissions while mitigating the adverse impacts of climate change and global warming. However, the production of biochar-based bioenergy depends on a sustainable supply of biomass. Although, Northwestern Ontario has a rich and sustainable supply of woody biomass, a comprehensive life cycle cost and economic assessment of biochar-based bioenergy production technology has not been done so far in the region.
In this paper, we conducted a thorough life cycle cost assessment (LCCA) of biochar-based bioenergy production and its land application under four different scenarios: 1) biochar production with low feedstock availability; 2) biochar production with high feedstock availability; 3) biochar production with low feedstock availability and its land application; and 4) biochar production with high feedstock availability and its land application- using SimaPro®, EIOLCA® software and spreadsheet modeling. Based on the LCCA results, we further conducted an economic assessment for the break-even and viability of this technology over the project period.
It was found that the economic viability of biochar-based bioenergy production system within the life cycle analysis system boundary based on study assumptions is directly dependent on costs of pyrolysis, feedstock processing (drying, grinding and pelletization) and collection on site and the value of total carbon offset provided by the system. Sensitivity analysis of transportation distance and different values of C offset showed that the system is profitable in case of high biomass availability within 200 km and when the cost of carbon sequestration exceeds CAD $60 per tonne of equivalent carbon (CO2e).
Biochar-based bioenergy system is economically viable when life cycle costs and environmental assumptions are accounted for. This study provides a medium scale slow-pyrolysis plant scenario and we recommend similar experiments with large-scale plants in order to implement the technology at industrial scale.
KeywordsLCA LCCA SimaPro Biochar Biomass Pyrolysis Bioenergy Wood Pellets
Biochar1-based bioenergy production through slow pyrolysis2 of sustainably produced biomass feedstock is one of the simplest and cheapest method among several carbon capture and storage (CCS) methods (Woolf et al. 2010). Production of biochar and bioenergy is gaining significant momentum worldwide over the last decade with a steady growth of 3 % per year (IEA 2015; IBI 2016). Growing worldwide attention towards combating the adverse impacts of climate change, and the future courses of actions towards climate related issues were willfully agreed during the recent (2015) climate conference in Paris by different nations. Canada made a further commitment to achieve 30 % reduction in CO2 from 2005 levels by 2030 which basically lies within the provincial jurisdictions as management of natural resources is a provincial affair in Canada. The Province of Ontario further targeted to reduce 37 % CO2 from 1990 levels by 2030 (Lyman 2015; MOECC 2015). As a forest resource rich province, Ontario has the best opportunity to utilize its forest-based biomass to reduce carbon emission by reducing its dependency towards much debated fossil fuel. A significant step towards this has already begun in Ontario as the province legally banned coal burning for the power generation.
Use of biomass-based feedstocks especially from agriculture and forestry has been popular in recent years. Northwestern Ontario (NWO), in particular, has a rich and sustainable source of woody biomass supply through the sustainable management of about 12 million ha of productive forest through 18 Forest Management Plans (MNRF 2015). Several previous studies (Wood and Layzell 2003; Hacatoglu et al. 2011; Kennedy et al 2011; Alam et al. 2012) have also indicated that the NWO forests are capable of sustainably supplying enough biomass feedstock to generate electricity from power-generating stations, which used coal as feedstock until 2014. One of the limiting factors in the use of biomass feedstock for power generation is the energy density and its vast variability within different types of woody biomass. To overcome this limitation and to continue a sustained supply of the feedstock, the wood biomass raw materials are being processed and pelletized. Atikokan generating station (AGS-200 MW) in NWO, a coal burning power plant recently converted to wood burning facility has already started using locally produced wood pellets to produce clean electricity. Although the production of bioenergy3 is a fairly established technology, it is not economically competitive compared to the production of energy using fossil fuel, because of its high cost of production (Klinar 2016). The other secondary issue related to bioenergy production that is gaining momentum is landfilling with wood ash, which may contain heavy metals. If these issues are not properly addressed, bioenergy production may lose its competitive edge as a clean energy producing technology. Co-production of biochar with bioenergy, and applying biochar back to the land from where the biomass feedstock originated is suggested as one of the most feasible solutions for GHG emissions and waste management issues (Lehmann and Joseph 2009). Several life cycle analysis studies including our study (Homagain et al. 2015) have shown GHG emissions reduction with co-production (Winsley 2007; Roberts et al. 2010; McElligott et al. 2011; Sohi 2013). However, there is no study to our knowledge, which conducts a comprehensive life cycle cost assessment of the biochar-based bioenergy system, and accounts for every step of the production and use cycle.
Most of the related studies in literature focus on economic assessment of biochar systems (McCarl et al. 2009; Pratt and Moran 2010; Roberts et al. 2010; Galinato et al. 2011; Shackley et al. 2011; Yoder et al. 2011). These studies typically found that the potential economic profitability of biochar production systems varies depending on the feedstock used (Roberts et al. 2010; Cleary et al. 2015), the conversion technology employed (Pratt and Moran 2010; Bruun et al. 2011), or the inclusion of carbon sequestration subsidies or carbon credits1 4 reflecting the social value of GHG mitigation (Pratt and Moran 2010; Roberts et al. 2010; Galinato et al. 2011; Shackley et al. 2011). One study, modeling the trade-off between product yield and product quality as conversion temperature increases, has explored the implications of different production techniques and resulting variations in biochar properties for overall system performance (Yoder et al. 2011). Recent techno-economic assessments of slow-pyrolysis biochar and heat production (Klinar 2016; Patel et al. 2016) also showed that the biochar system can be profitable provided it is customized into the local production system. The size and scale of the biochar system affects the cost and its economic viability. Studies that compared the life cycle costs of different scale bioenergy systems with (Kulyk 2012) and without (Roberts et al. 2010; Cleary et al. 2015) biochar land application found that production cost of large-scale plant is lower than smaller scale plant but the GHG mitigation cost for large-scale plant is very high as compared to the smaller plant. For the purpose of this paper, we define ‘biochar-based bioenergy’ as the energy (char, syngas and bio-oil) produced by slow pyrolysis of woody biomass in a pyrolysis plant in the absence of oxygen. Bio-oil and syngas are then converted into electricity and biochar is applied in the same forest land where the raw material was collected. In this paper we assess the life cycle cost of producing biochar-based bioenergy and its land application with high and low availability scenario of biomass feedstock in NWO, Canada.
Life cycle cost analysis is a combination of life cycle environmental assessment, life cycle costing and economic analysis. We used a combination of LCA outputs, collected cost information for each analysis steps and scenario, created LCCA spreadsheet calculation tool, calculated net present value for each analysis scenario and conducted break-even analysis.
LCCA system boundary, study area and analysis scenarios
The study area lies in NWO Canada, where the Atikokan Generating Station (AGS) has been converted from coal to biomass (wood pellet) feedstock (OPG 2012). NWO has a vast amount of forest based woody biomass which can sustainably supply biomass feedstock to recently converted powerplant. Although AGS plans to use the combustion process for energy generation, our study uses different scenarios where biomass feedstock is converted into bio-oil, syngas and biochar using the normally available slow-pyrolysis machine in order to illustrate the cost assessment of biochar-based bioenergy production. The input-output data for the system boundary and unit processes were obtained directly from published literature, the NWO regional forest management units, forest management plans, and personal communications with harvesters, transporters and other professionals.
Life cycle cost assessment scenarios
Feedstock transportation distance (km)
Biochar land application
Project period (year)
1. Biochar Low
More than 200
2. Biochar High
Less than 200
3. Land Application Low
More than 200
50 t · ha−1 at 300 km
4. Land Application High
Less than 200
50 t · ha−1 at 100 km
Same average transportation distance (300 km for low availability and 100 km for high availability) for biochar land application is used as feedstock transportation. Biochar land application rate is used as 50 tonne per ha which was set during the life cycle assessment in SimaPro® assumption (See Homagain et al. 2015 for details).
Life cycle costing and net present value
Description of specific cost information
Total life cycle cost (LCC)
LCC t = MSC t + FCC t + TC t + SPC t + PC t + LAC t
Machine and Setup Cost (MSC)
• Planning—Feasibility study
• Environmental Impact Assessment (EIA) and development services
• Detailed Engineering Design
• Industry renewal fee
• Plant site Construction costs and maintenance in every 5 years.
• Equipment base price and delivery
• Plant Set Up and maintenance
MOECC 2015; PowerMax 2015, Pers. Comm.
Feedstock Collection Cost (FCC)
• Forest Harvest Residue (FHR)
• FHR-Labor—and related
• Saw Mill Residue (SMR)
• SMR-Labor- and related
• Underutilized trees (UTS)
• UTS-Labor- and related
Transportation Cost (TC)
• Feedstock Transportation to Storage
• Transportation from storage to Pyrolysis Facility
• Biochar Transportation to Land
• Bio-oil Syngas Transportation to market
AAFC 2008; Alam et al. 2012, Pers. Comm.
Storage/Processing Cost (SPC)
• Grinding/Pelletization Cost
Pyrolysis Cost (PC)
• Cost of plant operation
• Skilled labour/ Product Testing
• Pyrolyzed Products storage
Land Application Cost (LAC)
• Material handling, tractor and fuel costs
• Transportation and skilled labour costs
• Other incidental cost (2 %)
Pers. Comm. with independent applicators
Ten year averages of real interest and inflation rates were used (Bank of Canada 2013). Year 2013 is considered the base year for the project for all four scenarios, defined in Table 1, and all future costs and revenues are discounted for this year. Value of carbon sequestration is considered as one of the important dependent variable for the net present value calculation of the system. We also conducted a sensitivity analysis of different values of carbon credit and used CAD 60 for each equivalent tonne of carbon sequestered, while biochar is applied to the soil.
Biochar based bioenergy production is a costly investment. Our LCCA analysis shows that it warrants at least about a million dollar investment each year for a 25 year project. However, we noticed some thoughtful observation in our results.
Pyrolysis has the highest (36 %) share of total cost
Pyrolysis is the most costly stage among all production stages in the life cycle of bioenergy production and accounts for 36 % of the total cost of the system. Although pyrolysis is an old and established technology, there is a need to develop highly efficient and optimized machines. When producing biochar, bio-oil and syngas, the pyrolyzer consumes large amounts of energy and requires more skilled work force as compared to other stages. The average annual cost for the 1-MWh pyrolyzer in our study is slightly more than a similar half-capacity portable pyrolyzer (Coleman et al. 2010), but is cheaper than bio-oil pyrolysis system used in the UK (Rogers and Brammer 2012).
In a study on carbon market investment criteria for biochar projects conducted by California Energy Commission (CEC 2014), the authors also found that pyrolysis may be one of the most energy/resource expensive investments for biochar production. Although, pyrolysis biochar is becoming popular, it is still in research and development stage. If the demand for bioenergy production increases due to its environmental benefits, there will be more emphasis on developing highly efficient and cost effective system, thereby reducing the cost of pyrolysis.
Feedstock collection cost (12 %) is higher than transportation cost (9 %)
Our study uses three types of feedstock: forest harvest residue, saw mill residue and underutilized trees that are available in the study area of NWO. Collection of these materials would be a relatively new business and there are no established companies that can provide a sustainable supply of feedstock. On the other hand, there is an established forestry raw material transportation service provided by contractors on a competitive basis in the study area. Collection of these vast amounts of scattered feedstock is relatively labour and time intensive, and costs more than transportation. However, in other studies (Simon et al. 2010; Zhang 2010; Kung et al. 2013; Ronsse et al. 2013; Kaliyan et al. 2015) where the feedstock was mainly agriculture or municipal waste, the transportation cost was always found to be more than raw material collection cost.
Land application cost (14 %) is higher than feedstock collection and transportation cost (9 %)
Biochar land application would be completely new business in the area. Land application in forest lands or in recently harvested area is a cumbersome job as compared to homogenous agriculture farming field. Our study used a rate of 50 t · ha−1 which is almost half of what is suggested in the cropping field (Major 2010). Land variability, distance and rate of application may have contributed to the high cost of land application. However, land application is considered as paying carbon back to the nature for a long-term sequestration so the carbon credit accrued from the sequestration ultimately offsets this cost in the long run.
Land application scenarios have early break even and more return
Both land application scenarios with high and low feedstock availability have early break even periods (12 and 13 years) as compared to non-land application scenarios where break-even is after 17 years. This is because of the revenue generated through the carbon credits earned through the land application of biochar and the cost associated with the application is low as compared to the cost of land application.
Limitation of the study
Biochar-based bioenergy is a new socio-economic intervention in the area where fossil fuel has been contributing in the past. Social dimensions of bioenergy system especially macro-economic demand and supply side effects cannot be ignored while evaluating life cycle carbon and costs of the individual projects. This study did not consider this area, nor it did anything on the local job creation scenarios (direct, indirect and induces) as there are highly visible displacement effects and local job creation functions of the biochar-based bioenergy system.
This study was conducted during 2011–2013 (3 year span) when most of the wood market was relatively slow and energy prices (especially petroleum) were high as compared to 2014 onwards. Collection of cost information in a longitudinally spanned time frame may have caused some deviations in the total costs but all the future values are discounted with national real and 10-year average inflation rates.
All other related costs above and beyond the system boundary (Fig. 1) is assumed to be constant throughout all study period and across all scenarios.
Canada has committed to achieving 30 % reduction in CO2 emissions from 2005 levels by 2030, while the province of Ontario in Canada has further committed to reducing CO2 emissions by 37 % from 1990 levels by 2030. As a result, Ontario has banned the use of coal and is utilizing its forest-based biomass instead for energy production. However, the slow pyrolysis process of biochar-based bioenergy production has not been tested so far in Ontario due to its uncertain environmental and economic impacts. In this study we conducted a comprehensive life cycle cost and economic assessment analysis of biochar-based bioenergy production and biochar land application in Northwestern Ontario, Canada using LCA assumptions from our previous study (Homagain et al. 2015). Within the biochar-based bioenergy production system boundary and study assumptions, we found that pyrolysis process accounts for the highest share of 36 % cost in the production system; whereas land application accounts for 14 %, feedstock collection for 12 %, and transportation cost for 9 % of the total production cost. Land application scenarios are economically viable with 12 to 13 years of break-even time, when carbon sequestration is credited for at least CAD 60 per tonne of CO2e. Therefore, if biochar and bioenergy are co-produced, these can not only provide an economic alternative to fossil fuel energy production, but also help in sequestering stable carbon for longer periods of time. However, utilization of forest biomass may warrant an improvement in the regional biomass harvesting policy.
Biochar is a highly porous and stable carbon-rich co-product of pyrolysis that has many uses including soil amendments and long term carbon sequestration. Although chemically similar, biochar differs from charcoal in the sense that it is not used as fuel (Lehmann and Joseph 2009).
Pyrolysis is defined as a thermochemical decomposition process occurring in the absence of oxygen (Spokas et al. 2012).
In this paper we deal with biochar produced from woody biomass in a bioenergy plant using the slow pyrolysis technique, a process that maximizes production, at 300–500 °C with a vapour residence time of 5–30 min (Please see details in Homagain et al. 2015).
Bioenergy is the energy derived from the conversion of biomass where biomass may be used directly as fuel, or processed into liquids and gases.
A carbon credit (often called a carbon offset) is a financial instrument that represents a tonne of CO2 (carbon dioxide) or CO2e (carbon dioxide equivalent gases) removed or reduced from the atmosphere from an emission reduction project, which can be used, by governments, industry or private individuals to offset damaging carbon emissions that they are generating.
Agriculture and Agri Foods Canada, a federal department
Atikokan Generating Station. A 200 MWh power generating station owned by OPG. This is the largest wood pellet burning station in North America as of 2014 when it was converted from lignite coal burning to wood pellets
Carbon capture and storage
California Energy Commission
- CO2 :
Carbon dioxide equivalent, is a standard unit for measuring carbon footprints to express the impact of each different greenhouse gas in terms of the amount of CO2 that would create the same amount of warming. Carbon footprints of different greenhouse gases can be expressed as a single number as CO2e
Environmental Input and Output Life Cycle Assessment, a software developed by GDI
Feedstock collection cost
Green Design Institute. Developer of EIOLCA
International Biochar Initiative, USA
International Energy Agency, an autonomous intergovernmental organization established in the framework of the Organisation for Economic Co-operation and Development (OECD) in 1974 in the wake of the 1973 oil crisis
International Renewable Energy Agency
Land application cost
Total life cycle cost
Life cycle cost assessment
Ministry of Natural Resources and Forestry, Ontario, Canada
Ministry of Environment and Climate Change, Ontario, Canada
Machine and setup cost
Net Present Value. It is the difference between the present value of total revenue (cash inflows) and the present value of total cost (cash outflows) discounted for the entire investment period
National Renewable Energy Laboratory of USA
Northwestern Ontario. A big section of Province of Ontario covering about 52 million ha area
Ontario Power Generation, a crown corporation owned by Province of Ontario
- Pers. Comm.:
Return on investment. It is the most common profitability ratio of a project which is usually expressed as a percentage of net profit and is typically used for financial decisions, to compare the efficiency of different investments
A LCA software developed by Pre Consultants, the Netherlands
Storage and processing cost
Wood Pellet Association of Canada
Financial contributions from (1) Natural Sciences and Engineering Research Council of Canada through Industrial Postgraduate Scholarships (NSERC-IPS), (2) Ontario Graduate Scholarship (OGS) and (3) Ontario Power Generation (OPG) for this study are highly acknowledged.
KH as a first author conducted all analyses, interpreted results and wrote and revised the manuscript. CS as a principal supervisor and NL & MS as academic committee members made substantial contributions to the layout and design of the study and interpretation of the results. All authors read and approved the final manuscript.
KH is a recent PhD graduate from Faculty of Natural Resources Management of the Lakehead University and currently working with Ontario Ministry of Natural Resources and Forestry (MNRF) as a Regional Analyst. CS (Socio economist) and NL (Ecologist) are both Professors at Lakehead University with multi-disciplinary forestry-ecology-economics and statistics background. MS is a Forest Growth and productivity research scientist in Ontario Forest Research Institute of MNRF.
The authors declare that they have no competing interests.
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