Synergies from Combined Pulp&Paper and Fuel Production
(2012) In Biomass & Bioenergy 40. p.174-180- Abstract
- Abstract in Undetermined
In this paper, the prospect of integrating a combined paper&pulp mill with fuel production via biomass gasification was investigated. In the study, three different types of gasifiers (circulating fluidised bed, entrained flow and indirect gasification) and three fuel processes (dimethyl ether, methanol and Fischer-Tropsch wax synthesis) were investigated using computer simulations. The paper reports differences from the stand-alone cases and the integrated cases, using the electricity equivalence efficiency as a measure.
Only 6 out of the 18 integrated cases studied displayed a positive result from integration and no obvious fuel selection that stand out as the most beneficial one, however the... (More) - Abstract in Undetermined
In this paper, the prospect of integrating a combined paper&pulp mill with fuel production via biomass gasification was investigated. In the study, three different types of gasifiers (circulating fluidised bed, entrained flow and indirect gasification) and three fuel processes (dimethyl ether, methanol and Fischer-Tropsch wax synthesis) were investigated using computer simulations. The paper reports differences from the stand-alone cases and the integrated cases, using the electricity equivalence efficiency as a measure.
Only 6 out of the 18 integrated cases studied displayed a positive result from integration and no obvious fuel selection that stand out as the most beneficial one, however the synthesis of dimethyl ether is, in combination with all gasifiers assessed a rather good choice, with an change in efficiency from integration ranging from −1% to 4%.
Dimethyl ether is not the best choice if the electrical equivalence is to be maximised however. In this case the combination of circulating fluidised bed gasification and methanol synthesis should be pursued. The production of Fischer-Tropsch wax should according to the chosen measure not be produced; however there is an added value in the production of a non-oxygenated fuel which has not been taken into account in this particular study.
All cases leads to a reduction of 0.4–0.9 kg CO2 per kg of dry biomass used in the process for fuel synthesis and the possibility to export bark is a more significant factor in this respect than which type of fuel is synthesised. (Less)
Please use this url to cite or link to this publication:
https://lup.lub.lu.se/record/2371590
- author
- Tunå, Per LU ; Hulteberg, Christian LU ; Hansson, Jens ; Andersson, Eva and Åsblad, Anders
- organization
- publishing date
- 2012
- type
- Contribution to journal
- publication status
- published
- subject
- keywords
- Fuel synthesis, Paper, Pulp, Gasification, Biomass, Integration
- in
- Biomass & Bioenergy
- volume
- 40
- pages
- 174 - 180
- publisher
- Elsevier
- external identifiers
-
- wos:000303291500020
- scopus:84859164905
- ISSN
- 1873-2909
- DOI
- 10.1016/j.biombioe.2012.02.020
- language
- English
- LU publication?
- yes
- id
- 465f7c12-be88-4a07-a3dd-f776598b3eee (old id 2371590)
- date added to LUP
- 2016-04-01 10:03:38
- date last changed
- 2023-11-09 11:02:31
@article{465f7c12-be88-4a07-a3dd-f776598b3eee, abstract = {{Abstract in Undetermined<br> In this paper, the prospect of integrating a combined paper&pulp mill with fuel production via biomass gasification was investigated. In the study, three different types of gasifiers (circulating fluidised bed, entrained flow and indirect gasification) and three fuel processes (dimethyl ether, methanol and Fischer-Tropsch wax synthesis) were investigated using computer simulations. The paper reports differences from the stand-alone cases and the integrated cases, using the electricity equivalence efficiency as a measure.<br> <br> Only 6 out of the 18 integrated cases studied displayed a positive result from integration and no obvious fuel selection that stand out as the most beneficial one, however the synthesis of dimethyl ether is, in combination with all gasifiers assessed a rather good choice, with an change in efficiency from integration ranging from −1% to 4%.<br> <br> Dimethyl ether is not the best choice if the electrical equivalence is to be maximised however. In this case the combination of circulating fluidised bed gasification and methanol synthesis should be pursued. The production of Fischer-Tropsch wax should according to the chosen measure not be produced; however there is an added value in the production of a non-oxygenated fuel which has not been taken into account in this particular study.<br> <br> All cases leads to a reduction of 0.4–0.9 kg CO2 per kg of dry biomass used in the process for fuel synthesis and the possibility to export bark is a more significant factor in this respect than which type of fuel is synthesised.}}, author = {{Tunå, Per and Hulteberg, Christian and Hansson, Jens and Andersson, Eva and Åsblad, Anders}}, issn = {{1873-2909}}, keywords = {{Fuel synthesis; Paper; Pulp; Gasification; Biomass; Integration}}, language = {{eng}}, pages = {{174--180}}, publisher = {{Elsevier}}, series = {{Biomass & Bioenergy}}, title = {{Synergies from Combined Pulp&Paper and Fuel Production}}, url = {{http://dx.doi.org/10.1016/j.biombioe.2012.02.020}}, doi = {{10.1016/j.biombioe.2012.02.020}}, volume = {{40}}, year = {{2012}}, }