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1. Introduction - Firenze University Press

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4 the CO2 emissions effect for BLGMF is further improved due to the occurrence of CCS on<br />

the margin in the power sector. If CCS is available, BLGCC gives almost as large CO2<br />

emission reductions as RBU:CCS, however, due to a higher capital intensity it always shows<br />

a poorer economic performance.<br />

5.5. Comparison with results for unchanged production capacity<br />

Here, the results of this paper are compared with the results from a previous study of the same<br />

mill where the production capacity remained unchanged (presented in [18]). Comparing the<br />

results from this paper with those previous results it becomes clear that the BLG cases,<br />

BLGMF and BLGCC (both with and without CCS), benefit from economy of scale. Thus,<br />

they have a better economic performance when increasing the production capacity than when<br />

the production capacity remains unchanged. For the BLGMF case, this means that if the<br />

production capacity is increased, BLGMF becomes more profitable than Lignin:Oil for some<br />

of the scenarios where lignin prices as oil were more profitable in case of unchanged<br />

production. For the RBU:Electricity and RBU:CCS cases, the production capacity increase<br />

affects the economic performance in a negative way. This is due to the fact that an additional<br />

investment in an upgrading of the recovery boiler has to be made. Thus, a production capacity<br />

increase benefits lignin extraction and BLG since these technologies unload the existing<br />

recovery boiler and thereby an investment in an upgrade of the recovery boiler can be<br />

avoided.<br />

6. Conclusions<br />

This paper compares different technologies for utilisation of a potential steam surplus and<br />

debottlenecking the recovery boiler of a typical Scandinavian kraft pulp mill assuming a pulp<br />

production increase of 25%. The technologies are compared with respect to annual net profit<br />

and global CO2 emissions for four different energy market scenarios using two time frames,<br />

2020 (where CCS is not available, neither for the mill nor in the surrounding power system)<br />

and 2030. Based on the results and discussion the following main conclusions can be drawn:<br />

For all energy market scenarios, both year 2020 and 2030, BLGMF and lignin<br />

extraction where the lignin is priced as oil have a better economic performance than<br />

upgrading the recovery boiler (and existing steam turbines).<br />

The BLGMF case generally has the best economic performance, but is contrary to<br />

lignin extraction very sensitive to changes of several parameters, especially the level<br />

of support for biofuels and the investment cost.<br />

Extraction of lignin that can be priced as oil has a very good economic performance<br />

and it is not highly influenced by any of the parameters studied outside the scenarios<br />

and can therefore be said to be a fairly robust investment. The CO2 emissions<br />

reduction from lignin extraction is also fairly stable between the scenarios.<br />

For the year 2020, where there are assumed to be no possibilities for CCS, BLGCC<br />

generally gives the highest CO2reduction potential. For the year 2030, where there is<br />

assumed to be an established infrastructure for CCS, upgrading the recovery boiler and<br />

investing in CCS coupled to the boiler flue gases render the highest CO2 reduction<br />

potential, followed by BLGCC and BLGMF, where CCS also can be included.<br />

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