主催: 日本エネルギー学会, 石炭科学部会, コークス工学研究部会, 重質油部会
共催: 日本学術振興会 石炭・炭素資源利用技術第148委員会, 化学工学会 エネルギー部会
会議名: 第56回石炭科学会議
回次: 56
開催地: ウィンクあいち
開催日: 2019/10/29 - 2019/10/30
p. 6-7
In slagging gasifiers, the ash flow down the gasifier walls and dra ine the gasifier as a molten slag . The b ehavior of the molten slag depend e on coal type . Coals choosed for slagging gasifiers should thus have an ash fusion temperature below the operating temperature of the gasifier ; thus evaluation of t he ash fusion temperature is important to operate stable the gasifier The estimation of the ash fusion temperature was performed by using Factsage 7.2 that is the thermodynamic equilibrium calculation software. And more the ash viscosity was estimated by Modified Urbain Model or Viscosity Module o f Factsage 7.2 . The equilibrium ash fusion temperatures w ere cal c ulated con s ider ing the equilibrium gas composition for 4 coals. The estimated ash fusion temepratures were different from JIS measurement results. Viscosity Module was good agreement with the ash viscosity measurement results u sing high temperature furnace.