Influence of process parameters on the performance of an oxygen blown entrained flow biomass gasifier. (1st August 2015)

• Record Type: Journal Article
• Authors: Weiland, Fredrik; Wiinikka, Henrik; Hedman, Henry; Wennebro, Jonas; Pettersson, Esbjörn; Gebart, Rikard
• Is Part Of: Fuel. Volume 153(2015)
• Page Start: 510
• Page End: 519
• Publication Date: 2015-08-01
• Subjects: Gasification -- Oxygen blown -- Entrained flow reactor -- Biomass -- Wood -- Cold gas efficiency; Fuel -- Periodicals; Coal -- Periodicals; Coal; Fuel; Periodicals; 662.6
• DOI: 10.1016/j.fuel.2015.03.041
• Languages: English
• ISSNs: 0016-2361

Abstract

Highlights: A temperature >1400 °C is required to reduce the syngas CH4 content <1 mol%. The maximum cold gas efficiency based on all combustible constituents was 75% in the experiments. The corresponding cold gas efficiency based only on the CO and H2 concentrations was 70%. The syngas H2 /CO ratio was within the range 0.45–0.61 in the experiments. Abstract: Pressurized, O2 blown, entrained flow gasification of pulverized forest residues followed by methanol production is an interesting option for synthetic fuels that has been particularly investigated in the Nordic countries. In order to optimize gasification plant efficiency, it is important to understand the influence of different operating conditions. In this work, a pressurized O2 blown and entrained flow biomass gasification pilot plant was used to study the effect of four important process variables; (i) the O2 stoichiometric ratio ( λ ), (ii) the load of the gasifier, (iii) the gasifier pressure, and (iv) the fuel particle size. Commercially available stem wood fuels were used and the process was characterized with respect to the resulting process temperature, the syngas yield, the fuel conversion and the gasification process efficiency. It was found that CH4 constituted a significant fraction of the syngas heating value at process temperatures below 1400 °C. If the syngas is intended for catalytic upgrading to a synthetic motor fuel where CO and H2 are the only important syngas species, the process should be optimized aiming for a process temperature slightly above 1400 °C in order to reduce the energetic losses to CH4 and C6 H6 . This resulted in a cold gas efficiency (based only on CO and H2 ) of 70%. The H2 /CO ratio was experimentally determined within the range 0.45–0.61. Thus, the syngas requires shifting in order to increase the syngas composition of H2 prior to fuel synthesis.