Oxygen-Blown Gasification of Pulp Mill Bark Residues for Synthetic Fuel Production

Synthetic fuel production via gasification of residual biomass streams from the pulp and paper industry can be an opportunity for the mills to enable improved resource utilization and at the same time reduce the production of excess heat. This paper summarizes initial oxygen-blown gasification exper...

Full description

Bibliographic Details
Main Authors: Fredrik Weiland, Sandra Lundström, Yngve Ögren
Format: Article
Language:English
Published: MDPI AG 2021-01-01
Series:Processes
Subjects:
Online Access:https://www.mdpi.com/2227-9717/9/1/163
id doaj-5a946b749030456598e3430a345f88a3
record_format Article
spelling doaj-5a946b749030456598e3430a345f88a32021-01-16T00:06:16ZengMDPI AGProcesses2227-97172021-01-01916316310.3390/pr9010163Oxygen-Blown Gasification of Pulp Mill Bark Residues for Synthetic Fuel ProductionFredrik Weiland0Sandra Lundström1Yngve Ögren2RISE Energy Technology Center AB, Box 726, S-941 28 Piteå, SwedenRISE Energy Technology Center AB, Box 726, S-941 28 Piteå, SwedenRISE Energy Technology Center AB, Box 726, S-941 28 Piteå, SwedenSynthetic fuel production via gasification of residual biomass streams from the pulp and paper industry can be an opportunity for the mills to enable improved resource utilization and at the same time reduce the production of excess heat. This paper summarizes initial oxygen-blown gasification experiments with two bark residues from a European pulp and paper mill, i.e., a softwood bark and a hardwood bark. The gasification process was characterized by measuring syngas yields and process efficiency to find optimum operating conditions. In addition, impurities in the syngas and ash behavior were characterized. Maximum yields of CO and H<sub>2</sub> were obtained from softwood bark and amounted to approximately 29 and 15 mol/kg fuel, respectively. Optimum cold gas efficiency was achieved at an oxygen stoichiometric ratio of <i>λ</i> = 0.40 and was approximately 76% and 70% for softwood bark and hardwood bark, respectively. Increased <i>λ</i> had a reducing effect on pollutants in the syngas, e.g., higher hydrocarbons, NH<sub>3</sub>, HCl, and soot. The situation for sulfur species was more complex. Evaluation of the bark ashes indicated that slag formation could start already from 800 °C. Furthermore, a non-intrusive laser diagnostics technique gave rapid feedback on the millisecond scale. Measured syngas temperature and water content were in good agreement with the applied reference methods.https://www.mdpi.com/2227-9717/9/1/163gasificationoxygen blownsyngasbark residuespulp millonline TDLAS process measurement
collection DOAJ
language English
format Article
sources DOAJ
author Fredrik Weiland
Sandra Lundström
Yngve Ögren
spellingShingle Fredrik Weiland
Sandra Lundström
Yngve Ögren
Oxygen-Blown Gasification of Pulp Mill Bark Residues for Synthetic Fuel Production
Processes
gasification
oxygen blown
syngas
bark residues
pulp mill
online TDLAS process measurement
author_facet Fredrik Weiland
Sandra Lundström
Yngve Ögren
author_sort Fredrik Weiland
title Oxygen-Blown Gasification of Pulp Mill Bark Residues for Synthetic Fuel Production
title_short Oxygen-Blown Gasification of Pulp Mill Bark Residues for Synthetic Fuel Production
title_full Oxygen-Blown Gasification of Pulp Mill Bark Residues for Synthetic Fuel Production
title_fullStr Oxygen-Blown Gasification of Pulp Mill Bark Residues for Synthetic Fuel Production
title_full_unstemmed Oxygen-Blown Gasification of Pulp Mill Bark Residues for Synthetic Fuel Production
title_sort oxygen-blown gasification of pulp mill bark residues for synthetic fuel production
publisher MDPI AG
series Processes
issn 2227-9717
publishDate 2021-01-01
description Synthetic fuel production via gasification of residual biomass streams from the pulp and paper industry can be an opportunity for the mills to enable improved resource utilization and at the same time reduce the production of excess heat. This paper summarizes initial oxygen-blown gasification experiments with two bark residues from a European pulp and paper mill, i.e., a softwood bark and a hardwood bark. The gasification process was characterized by measuring syngas yields and process efficiency to find optimum operating conditions. In addition, impurities in the syngas and ash behavior were characterized. Maximum yields of CO and H<sub>2</sub> were obtained from softwood bark and amounted to approximately 29 and 15 mol/kg fuel, respectively. Optimum cold gas efficiency was achieved at an oxygen stoichiometric ratio of <i>λ</i> = 0.40 and was approximately 76% and 70% for softwood bark and hardwood bark, respectively. Increased <i>λ</i> had a reducing effect on pollutants in the syngas, e.g., higher hydrocarbons, NH<sub>3</sub>, HCl, and soot. The situation for sulfur species was more complex. Evaluation of the bark ashes indicated that slag formation could start already from 800 °C. Furthermore, a non-intrusive laser diagnostics technique gave rapid feedback on the millisecond scale. Measured syngas temperature and water content were in good agreement with the applied reference methods.
topic gasification
oxygen blown
syngas
bark residues
pulp mill
online TDLAS process measurement
url https://www.mdpi.com/2227-9717/9/1/163
work_keys_str_mv AT fredrikweiland oxygenblowngasificationofpulpmillbarkresiduesforsyntheticfuelproduction
AT sandralundstrom oxygenblowngasificationofpulpmillbarkresiduesforsyntheticfuelproduction
AT yngveogren oxygenblowngasificationofpulpmillbarkresiduesforsyntheticfuelproduction
_version_ 1724336040622161920