open access publication

Article, 2024

An experimental, theoretical, and kinetic modeling study of gas-phase sulfation of KCl

Fuel, ISSN 0016-2361, Volume 363, 10.1016/j.fuel.2024.130974

Contributors

Chanpirak A. 0000-0002-8660-3819 [1] [2] Wu H. 0000-0003-0462-2491 [2] Marshall P. 0000-0002-8181-983X [3] Glarborg P. 0000-0002-6856-852X (Corresponding author) [2]

Affiliations

  1. [1] Naresuan University
  2. [NORA names: Thailand; Asia, South];
  3. [2] Technical University of Denmark
  4. [NORA names: DTU Technical University of Denmark; University; Denmark; Europe, EU; Nordic; OECD];
  5. [3] University of North Texas
  6. [NORA names: United States; America, North; OECD]

Abstract

The effect of a radical pool on KCl sulfation by SO is investigated through flow reactor experiments on KCl sulfation with and without the presence of CO. These experiments, together with results reported in literature, are interpreted in terms of an updated chemical kinetic model for sulfation. In the absence of combustibles, the rate limiting step in the sulfation of KCl is the oxidation of potassium sulfite to potassium sulfate through the reaction KHSO + O → KHSO + O (R17b). Based on chemical kinetic modeling of a range of sulfation experiments, the rate constant for the reverse, exothermic step KHSO + O is estimated to be k ∼ 2⋅10 cm mol s. Oxidation of combustibles such as CO facilitates establishment of a radical pool that strongly promotes sulfation. In this case, the sulfation rate is controlled by the oxidation of SO to SO, mostly through SO + O (+M) → SO (+M). An alternative sulfation pathway involving KSO as an intermediate is discarded, because the formation through either KO + SO or KSO + O involves significant barriers to reaction.

Keywords

Flow reactor, KCl sulfation, Kinetic modeling

Funders

  • Ørsted Bioenergy & Thermal Power A/S

Data Provider: Elsevier