1988
DOI: 10.1080/08940630.1988.10466974
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Modeling of Dry Injection Flue Gas Desulfurization

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Cited by 9 publications
(7 citation statements)
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“…Muzio & Sonnichsen [8] reported 29% in‐duct SO 2 removal by nahcolite upstream of a filter baghouse and Davis & Keener [5] measured 87% by sodium bicarbonate. Garding & Svedberg [9,10] reported data on SO 2 removal in the ductwork upstream of a pilot‐scale dry sodium injection FGD system that used a filter baghouse particle collector. They concluded that much of the SO 2 removal occurred while the injected sodium bicarbonate particles were suspended in the gas stream.…”
Section: Introductionmentioning
confidence: 99%
“…Muzio & Sonnichsen [8] reported 29% in‐duct SO 2 removal by nahcolite upstream of a filter baghouse and Davis & Keener [5] measured 87% by sodium bicarbonate. Garding & Svedberg [9,10] reported data on SO 2 removal in the ductwork upstream of a pilot‐scale dry sodium injection FGD system that used a filter baghouse particle collector. They concluded that much of the SO 2 removal occurred while the injected sodium bicarbonate particles were suspended in the gas stream.…”
Section: Introductionmentioning
confidence: 99%
“…This compound may be formed along with Cr(OH) 3 . Molybdate was detected in all the passive films formed on the high Ni-Cr-Mo alloys.…”
Section: The Role Of Alloying Elements In the Passive Filmmentioning
confidence: 97%
“…This was achieved by enhancing the deportonation of Cr(OH) 3 alloys are formed in the cracks which decreases the size of the active sites available for chloride ion ingress.…”
mentioning
confidence: 98%
“…The developed study proposes a numerical model in a pseudostationary state for dimensioning and for characterizing the reactor for the SO 2(g) elimination with NaHCO 3(s). Previous works using NaHCO 3 as a SO 2 sorbent normally describe steady state operation without providing validated guidelines on the equipment design and its hydrodynamic stability during operation; as examples, see the work from previous colleagues. ,, The model proposed in this article, on the other hand, considers the sorbent particles’ properties, the progressive degradation of the sorbent-bed while exposed to the gas, and the variations in the gas properties correspondingly. In response, it estimates the gas profiles within the reactor as a function of the operation time and its length, predicting the replacement time for the bed.…”
Section: Introductionmentioning
confidence: 99%