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Comparing new Swedish concepts for production of second

generation biofuels – evaluating CO

2

emissions using a system

approach

Mimmi Flink

1

, Karin Pettersson

2

and Elisabeth Wetterlund

3

1

Department of Chemical Engineering and Technology, Royal Institute of Technology (KTH), 100 44 Stockholm, Sweden, flink@ket.kth.se

2

Department of Energy and Environment, Chalmers University of Technology, 412 96 Göteborg, Sweden, karin.pettersson@chalmers.se

3

Department of Management and Engineering, Linköping University, 581 83 Linköping, Sweden, elisabeth.wetterlund@liu.se

1. Introduction

Biomass based automotive fuels are needed both to meet today’s climate-change mitigation goals and to lower dependency on fossil oil. As there are several alternative biofuels, the need to make comparisons in a well-to-wheels (WTW) perspective is obvious. Since biomass is a limited resource, figures of merit con-cerning energy efficiency and climate impact are of great importance. The results from these types of com-parisons can for instance be used as a basis for decision-making for politicians. However, comcom-parisons are generally hard to make with adequate transparency, since many assumptions are needed for the calcula-tions, especially about future surrounding systems.

The aim of this study is to use a system approach to show how assumptions about systems surrounding the fuel production affect the calculations of climate impact for different biofuels. The focus is on second gen-eration biofuels and the three technologies represented by pilot plants in Sweden, i.e. black liquor gasifica-tion (BLG), solid biomass gasificagasifica-tion (BMG) and ligno cellulosic ethanol (EtOH). For comparison, co-produc-tion of electricity and heat in a BIGCC (Biomass Integrated Gasificaco-produc-tion Combined Cycle) is considered.

2. Difficulties when comparing future biofuels

When calculating figures of merit such as total energy efficiency and climate impact for future biofuels, a number of assumptions have to be made. Since second generation biofuel technologies are still under de-velopment there are uncertainties about both process efficiencies and vehicle powertrains. Visions for the biofuel production concepts developed in Sweden often include integration, especially heat integration, of the production plants with other industrial or district heating systems, which further complicates assumptions re-garding the production process. While this will not be an option at all potential production sites, it is never-theless an aspect that needs to be considered. Evaluation of energy efficiency and climate consequences necessitates assumptions about surrounding systems, e.g. electricity generation, heating and transportation systems. Depending on the assumptions for the development of these systems, different results are obtained when comparing future biofuels with each other and with other biomass applications, e.g. production of heat and electricity. Larson [1] states that the wide range of reported greenhouse gas (GHG) emissions results from LCA studies evaluating liquid biofuel systems is due in part to the wide range of plausible values for key input parameters, and that one of the most significant parameters is the allocation method used for by-product credits. There are a number of ways to handle by-by-product credits, e.g. allocation based on energy, weight, product market value etc. It is also possible to expand the system to include the by-product systems and give the biofuel a credit corresponding to the energy use and emissions that would have been caused by producing the commodities that can be replaced by by-products, by conventional routes.

One of the most widely spread WTW-studies was made by the EU JRC [2]. While being very detailed, with a large number of different fuels, both of fossil and renewable origin (including the technologies considered here), it is not completely consistent in its system view. In the study, the biofuel production processes are made electricity neutral by recalculation of electricity into biomass, using the nearest equivalent wood-to-electricity process. For production processes with a deficit of wood-to-electricity the calculated amount of biomass is added to the amount of biomass feedstock, and vice versa for processes with a surplus of electricity. In spite of the importance of comparability being accentuated in the study, different electricity production processes are considered for different biofuel routes. It should also be noted that for all other instances of electricity use in the study, EU mix 2010 is used. Another interesting aspect of the EU JRC study is that although CO2

capture and storage (CCS) is investigated for some routes, none of the routes considered are biofuel routes and it is never mentioned that CCS could be an option for those cases as well.

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3. Method and assumptions

For the two gasification technologies considered in this study, only the case of DME production is consid-ered. To compare the efficiency of making motor fuels with other biomass use, a BIGCC case is included in the study. The four cases (BLG, BMG, EtOH and BIGCC) are used to exemplify how different assumptions about the surrounding system influence the results when evaluating total CO2 emissions consequences.

Since the main raw material is assumed to be forest residuals no other GHG emissions than CO2 are

con-sidered.

3.1. Method for evaluating CO2 emissions

The four cases are evaluated on the basis of net CO2 consequences, by assuming that the net flows of

energy and material entering or leaving the plant cause a change in the surrounding system. This method is similar to the system expansion by-product allocation method mentioned in the previous section and used by e.g. [2]. The difference from [2] is that here the system expansion method is used to evaluate the CO2

emis-sions of all flows, not only the by-product flows. For example, if the biofuel production plant has a surplus of electricity, this causes a decreased marginal electricity production. In case of an electricity deficit of the plant, marginal electricity production increases. To take future integration possibilities into account, waste heat is also considered, and is assumed to replace alternative district heating production.Since biomass is a limited resource, biomass used for biofuel production lessens the amount of biomass available for other applications in the system. This is acounted for by assuming a marginal biomass usage.

To assess net CO2 emissions, four energy market scenarios for 2020 developed by Axelsson et al. [3] are

used. The scenarios reflect different possible future energy market conditions and are based on assumptions on fossil fuel prices and policy instruments, such as CO2 emissions charge. For electricity production, the

marginal technology in each of the scenarios is assumed to be the technology with the lowest production cost. The marginal biomass usage is determined by the intersection of the demand and supply curves for biomass. No marginal transportation technology is included in the scenarios in [3]. Here, the proposed EU target for 2012 [4] for new cars is used as base value. To account for CO2 emissions related to other steps of

the WTW-chain, values from [2] for emissions from production and distribution of gasoline are added to the base value of 130 g CO2/km. For district heating the alternative production is assumed to be a modern

bio-mass boiler with a heat efficiency of 115 %LHV. This releases biomass for other uses, in this case the

mar-ginal biomass usage, as defined in the scenarios. Table 1 shows the CO2 emission values used.

Scenario 1 Scenario 2 Scenario 3 Scenario 4 Fossil fuel price level Low Low High High CO2 emission chargea Low High Low Highb

Electricity production NGCC Coal with CCS Coal Coal with CCS

[kg CO2/MWhel]c 374 136 723 136

Biomass use Co-firing with coal Co-firing with coal Co-firing with coal DME production [kg CO2/MWhbiomass]

c

329 329 329 159 Transportation EU target EU target EU target EU target

[g CO2/km] 150 150 150 150

District heating Biomass boiler Biomass boiler Biomass boiler Biomass boiler [kg CO2/MWhheat]

c

286 286 286 138

a Low level corresponds to a moderate ambition for reduction of CO

2 emissions, high level to high ambition. b

In Scenario 4 policy instruments promoting production of green transportation fuels are assumed. c

Well-to-gate from marginal use.

Table 1. CO2 emissions used for calculations of external effects.

3.2. Input data

Input data used for the calculations are presented in Table 2. For black liquor gasification with DME produc-tion data from [5] are used. The data are based on calculaproduc-tions where the recovery boiler, used for combus-tion of the black liquor, at a pulp mill using best available technology is replaced by a gasificacombus-tion plant coupled to a product gas conversion plant for production of DME. Table 2 shows the incremental biomass and electricity use compared to the pulp mill reference case. For biomass gasification, data from [6] are used for the DME case, while data from [7] are used for the BIGCC case. For the ethanol case, data from [7], [8] and [9] are used. The data are based on a process with enzymatic hydrolysis where lignin and other solid by-products are used in a CHP-plant. Biogas, another by-product from the ethanol production, is used in a gas engine, also producing heat and electricity. To account for CO2 emissions related to collection, chipping and

transportation of biomass, as well as to distribution and dispensing of the produced biofuel, values from [2] are used. The produced biofuels are assumed to be used in hybrid vehicles. Vehicle efficiency data, as given in Table 3, are taken from [2].

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Fuel [MJ/km] DME in diesel hybrid 1.4 Ethanol in gaso-line hybrida 1.6 a

Mean value of PISI and DISI hybrid.

4. Results

The results are illustrated in Figure 1 as net CO2 emissions reduction per TJ of biomass used, compared to a

reference system as defined in the scenarios. As can be seen, the results differ greatly between the scenar-ios. These differences reflect the influence on the results of assumptions about the surrounding system.

-40 -20 0 20 40 60 80 100 120

Scenario 1 Scenario 2 Scenario 3 Scenario 4

CO 2 -r e d u c tio n [t on nes C O2 /T J bi o m as s ] BLG: DME BMG: DME EtOH BIGCC

Figure 1. Net CO2 emissions reduction [tonnes CO2/TJ biomass] for the BLG, BMG, EtOH and BIGCC cases, assuming the four

differ-ent energy market scenarios for 2020 described in Table 1.

When assuming a high CO2 emissions charge, as in scenarios 2 and 4, all three studied technologies show

higher, or less negative, CO2 reduction compared to electricity and heat production by the BIGCC-concept.

In scenario 4, policy instruments promoting production of green transportation fuels are assumed and thereby marginal biomass usage changes from co-firing with coal, to DME production. In this scenario all three studied biofuel technologies achieve positive CO2 reduction. In scenario 3, with a low CO2 emissions

charge, the marginal electricity production is a coal-fired power plant (without CCS) which means that the BIGCC concept is highly favoured compared to the biofuel technologies. It should be noted that it is also possible to produce electricity and heat in a combined cycle from the BLG concept.

5. Discussion and conclusions

The results show that when varying the assumptions on surrounding systems, e.g. electricity- and transpor-tation systems as well as marginal usage of biomass, very different values regarding the potential to reduce CO2 emissions using biofuels are obtained, both when comparing different technologies and when

compar-ing biofuels to BIGCC CHP. This shows the importance of becompar-ing aware of the assumptions used in different WTW-studies regarding the surrounding systems and how they affect relative figures-of-merit for different technologies. It also shows the importance of a sensitivity analysis where the assumptions on surrounding systems are varied. Since energy market parameters are not independent of each other, but rather strongly connected, a good way to make a sensitivity analysis is to use different scenarios reflecting different possible future energy market conditions.

By using a system-oriented approach when evaluating potential for CO2 emissions reduction, the fact that

biomass is a limited resource for which there is competition from a number of different applications, is re-flected. The importance of taking this fact into consideration is stressed by presenting the potential to reduce CO2 emissions per unit of biomass. Another way to make allowance for the scarcity of biomass would be to Table 2. Input data for the studied plant configurations. Negative values indicate import to plant.

Table 3. Specific energy consump-tion for the studied biofuels in hybrid

vehicles (2010+ configurations). BLG BMG EtOH BIGCC Biomass [MW] -157 -229 -222 -114 Biofuel [MW] 275 131 58 – Electricity [MW] -101 -13 46 50 District heat [MW] –a 13 88 52 Conditioning and distribution emissionsc [kg CO2/ MWhfuel/el] 6.8 16 31 16 a

The excess heat from the BLG plant is used internally at the pulp mill. b

Emissions associated with collection, chipping and transportation of forest residuals to plant, as well as with distribution and dispensing of the biofuel.

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calculate CO2 emissions reduction per land area, but since the feed in this study is assumed to be forest

re-siduals, this would be a less suitable method. This consideration of the limited amount of biomass available is the reason for the relatively low (or negative) potential to reduce CO2 emissions using biofuels shown in

this study, compared to other similar studies, since here the biomass used for the studied technologies less-ens the amount of biomass available for other applications, thereby increasing the emissions for those appli-cations.

As has been shown, CO2 emissions reduction depends strongly on assumptions about the surrounding

sys-tems. Therefore it is of course important to be consistent and use the same assumptions for all technologies compared in a study. This is however not always the case. As has been exemplified, studies can be incon-sistent in the system view, e.g. by using different technologies in order to make the biofuel production processes electricity neutral, where the power production technologies used do not necessarily reflect a re-alistic surrounding system. One important factor that has not been considered here, that could improve the results for the biofuels studied, is CCS. In the gasification processes as well as in the ethanol process, con-siderable amounts of CO2 could be separated rather easily, thereby increasing the CO2 reduction potential

significantly. It should be noted that there are of course other aspects besides climate impact to consider, within or outside a life cycle analysis, when comparing biofuels; e.g. other environmental aspects, the need for changes in infrastructure and of course economics.

In this study DME from BLG shows the highest CO2 emission reduction potential in all scenarios except

scenario 3. A big advantage with BLG is that excess process heat can be used at the pulp mill. The absolute potential for biofuels via BLG is however limited, since there is only a very limited amount of black liquor. Even in Sweden, a country with one of the largest pulp and paper industries in the world compared to popu-lation, biofuels based on BLG could only cover about 30 % of the need for transportation fuels. Hence, there is a need to continue the development of other technologies as well. For the BMG and ethanol processes there is no direct user of the excess process heat, as in the case of BLG. It is therefore of great importance to investigate possibilities of integration, e.g. with a district heating system or with another industrial process, in order to increase the total energy efficiency. However, since the amounts of low grade heat from the processes can be considerable, it will probably be hard to find large enough heat demand. When integrating with other industries, the complexity of the comparisons increases.

A final conclusion is that a system approach, such as the one described in this study, should be used when analysing the CO2 effectiveness of applications using the limited biomass resources. This is particularly

im-portant when evaluating technologies that are expected to use a substantial amount of the available biomass in the future, as in the case for the technologies evaluated in this study.

6. References

[1] Larson, E. D., 2006. A review of life-cycle analysis studies on liquid biofuel systems for the transport sector. Energy for Sustainable Development, Volume X, No. 2, June 2006.

[2] JRC/EUCAR/CONCAWE. 2007. Well-to-wheels analysis of future automotive fuels and powertrains in the European context, version 2c. Available for download on http://ies.jrc.cec.eu.int/wtw.html

[3] Axelsson, E., Harvey, S., Berntsson, T., 2007. A tool for creating energy market scenarios for evaluation of investments in energy intensive industry. Proceedings of ECOS, Padova, Italy, June 25-28, 2007. [4] Communication from the Commission to the Council and the European Parliament – Results of the

re-view of the Community Strategy to reduce CO2 emissions from passenger cars and light-commercial

ve-hicles, COM(2007) 19. Available for download on

http://eur-lex.europa.eu/LexUriServ/site/en/com/2007/com2007_0019en01.pdf

[5] Ekbom, T., Berglin, N. och Lögdberg, S., 2005. Black Liquor Gasification with Motor Fuel Production – BLGMF II, Stockholm.

[6] Boding, H., Ahlvik, P., Brandberg, Å. & Ekbom, T. 2003. BioMeeT II – Stakeholders for biomass based methanol/DME/power/heat energy combine. Final report. Ecotraffic AB, Nykomb Synergetics AB.

[7] Bärring, M., Gustafsson, J-O., Nilsson, P-A., Ohlsson, H. & Olsson, F., 2000. Electric power from new plants, 2000. (El från nya anläggningar, 2000, in Swedish) Elforsk report no 2000:01. Elforsk, Stockholm. [8] Lindstedt, J., 2007. Personal communication 2007-09-18.

[9] Wärtsilä, 2007. Combined heat and power. Available for download on

http://www.wartsila.com/,en,solutions,applicationdetail,application,001EECC8-F376-4672-8565-9764D8354459,39A96BFD-0563-48A7-92C0-841E847D83C4,,8003.htm

Acknowledgement – The work has been carried out under the auspices of the Energy Systems Programme,

References

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