ities, property-estimation methods, dispersion modelling, and correction to the k-¢ model. Considerable differences were found in fuelvapour distribution when using different models, The LIF measurements and the numerical simulations were compared in terms of the fuel-vapour distribution. The simula
The ash chemistry in fluidised bed gasification of biomass fuels. Part II: Ash behaviour prediction versus bench scale agglomeration tests
✍ Scribed by M Zevenhoven-Onderwater; R Backman; B.-J Skrifvars; M Hupa; T Liliendahl; C Rosén; K Sjöström; K Engvall; A Hallgren
- Publisher
- Elsevier Science
- Year
- 2001
- Tongue
- English
- Weight
- 518 KB
- Volume
- 80
- Category
- Article
- ISSN
- 0016-2361
No coin nor oath required. For personal study only.
✦ Synopsis
This paper is part II in a series of two. Ash behaviour modelling of the gasi®cation of four biomass fuels is compared with pilot-scale experiments carried out in a pressurised ¯uidised bed gasi®er at the Royal Institute of Technology (KTH) and an atmospheric test rig of Termiska Processer AB (TPS). Experiments were provocative with respect to agglomeration of the bed material. Thus, in the experiments, the agglomeration was allowed to happen without any corrective changes in the operation.
Small-scale experiments showed clear de¯uidisation in ®ve cases. Some degree of bed disturbance or agglomeration occurred in seven out of 13 cases. In nine of these cases, agglomerates were also found in the samples analysed with SEM/EDX analyses.
In six out of 13 cases, the thermodynamic multi-phase multi-component equilibrium calculations were in agreement with SEM/EDX analysis, i.e. predicted formation of agglomerates. In two cases, no or small amounts of agglomerates were predicted, nor were these found with SEM/EDX analysis. In two cases out of 13, the modelling predicted some degree of agglomeration while no agglomerates could be detected with SEM/EDX analysis. However, in these cases, agglomerates were found in the pilot-scale experiments.
Thus it is shown that the thermodynamic multi-phase multi-component equilibrium calculations are a useful prediction tool for the formation of agglomerates in (pressurised) ¯uidised bed gasi®cation of biomass fuels thereby enhancing the understanding of the chemistry involved.
📜 SIMILAR VOLUMES
This paper is part I in a series of two describing the modelling of the ash-chemistry of seven biomass fuels under reducing, pressurised conditions in ¯uidised bed gasi®cation by means of thermodynamic multi-phase multi-component equilibrium (TPCE) calculations. The fuels considered were Salix, a Sc
ities, property-estimation methods, dispersion modelling, and correction to the k-¢ model. Considerable differences were found in fuelvapour distribution when using different models, The LIF measurements and the numerical simulations were compared in terms of the fuel-vapour distribution. The simula