H2S REMOVAL FROM COAL-GAS AT ELEVATED-TEMPERATURE AND PRESSURE IN FLUIDIZED-BED WITH ZINC TITANATE SORBENTS .2. SORBENT DURABILITY

Citation
W. Mojtahedi et J. Abbasian, H2S REMOVAL FROM COAL-GAS AT ELEVATED-TEMPERATURE AND PRESSURE IN FLUIDIZED-BED WITH ZINC TITANATE SORBENTS .2. SORBENT DURABILITY, Energy & fuels, 9(5), 1995, pp. 782-787
Citations number
13
Categorie Soggetti
Engineering, Chemical","Energy & Fuels
Journal title
ISSN journal
08870624
Volume
9
Issue
5
Year of publication
1995
Pages
782 - 787
Database
ISI
SICI code
0887-0624(1995)9:5<782:HRFCAE>2.0.ZU;2-0
Abstract
High-temperature high-pressure sulfur removal is considered as one of the key steps of the hot gas cleanup train of an IGCC process. Coal-de rived gasifier gas contains sulfur gases (mainly H2S) which are conver ted to SO2 when the gas is combusted in the gas turbine, Cyclic sulfid ation/regeneration tests were carried out in a pressurized fluidized b ed reactor to remove H2S from a simulated coal gas to below 100 ppmv, using regenerable zinc titanate sorbents, The results, which were repo rted in part 1 of this paper, showed that the sorbent reactivity deter iorates in the cyclic process, In part 2, physical, chemical, and stru ctural changes which the sorbents undergo in the cyclic tests are repo rted and discussed. The results of analyses conducted with ''fresh'' a nd ''used'' sorbents indicate that the loss of reactivity and sorbent deterioration is probably due to zinc migration to the surface of the sorbent particle during high-temperature high-pressure cyclic process.