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Low temperature circulating fluidized bed gasification and co-gasification of municipal sewage sludge. Part 1: Process performance and gas product characterization.

作者信息

Thomsen Tobias Pape, Sárossy Zsuzsa, Gøbel Benny, Stoholm Peder, Ahrenfeldt Jesper, Frandsen Flemming Jappe, Henriksen Ulrik Birk

机构信息

Technical University of Denmark, Department of Chemical Engineering, DTU Risø Campus, Building 313, Frederiksborgvej 399, 4000 Roskilde, Denmark.

Technical University of Denmark, Department of Chemical Engineering, DTU Risø Campus, Building 313, Frederiksborgvej 399, 4000 Roskilde, Denmark.

出版信息

Waste Manag. 2017 Aug;66:123-133. doi: 10.1016/j.wasman.2017.04.028. Epub 2017 Apr 25.

Abstract

Results from five experimental campaigns with Low Temperature Circulating Fluidized Bed (LT-CFB) gasification of straw and/or municipal sewage sludge (MSS) from three different Danish municipal waste water treatment plants in pilot and demonstration scale are analyzed and compared. The gasification process is characterized with respect to process stability, process performance and gas product characteristics. All experimental campaigns were conducted at maximum temperatures below 750°C, with air equivalence ratios around 0.12 and with pure silica sand as start-up bed material. A total of 8600kg of MSS dry matter was gasified during 133h of operation. The average thermal loads during the five experiments were 62-100% of nominal capacity. The short term stability of all campaigns was excellent, but gasification of dry MSS lead to substantial accumulation of coarse and rigid, but un-sintered, ash particles in the system. Co-gasification of MSS with sufficient amounts of cereal straw was found to be an effective way to mitigate these issues as well as eliminate thermal MSS drying requirements. Characterization of gas products and process performance showed that even though gas composition varied substantially, hot gas efficiencies of around 90% could be achieved for all MSS fuel types.

摘要

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