2019
DOI: 10.1016/j.cherd.2018.12.029
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A modelling approach to kinetics study and novel monolith channel design for selective catalytic reduction (SCR) applications

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Cited by 14 publications
(8 citation statements)
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“…It is suggested that honeycomb monoliths with a wall thickness of 0.5–0.6 mm and a channel width of 3–4 mm are suitable for the case of low dust gas, while greater wall thickness (>1 mm) and larger channels (e.g., 7 mm) are applicable for the flue gas with high dust content . Shin et al . found that elongated hexagonal channels have higher NO conversion than the conventional square channels.…”
Section: Monolith Catalystsmentioning
confidence: 99%
“…It is suggested that honeycomb monoliths with a wall thickness of 0.5–0.6 mm and a channel width of 3–4 mm are suitable for the case of low dust gas, while greater wall thickness (>1 mm) and larger channels (e.g., 7 mm) are applicable for the flue gas with high dust content . Shin et al . found that elongated hexagonal channels have higher NO conversion than the conventional square channels.…”
Section: Monolith Catalystsmentioning
confidence: 99%
“…Activities and selectivities were measured on 1 cm mini monoliths as described before [17] by mass spectrometry using helium as a background gas. The piece five from the inlet was used in the ammonia oxidation experiments.…”
Section: Measurements Of Catalyst Activity and Selectivitymentioning
confidence: 99%
“…The model was able to predict the catalyst output during the European Transient Cycle (ECT cycle). A recent paper [17] presented a method to simulate the kinetics of the SCR reactions as well as many of the NH 3 oxidation ones to obtain novel and better monolith channel designs. The results are detailed showing, among others, the temperature profile in the catalyst bed when converting 1500 ppm NO with NH 3 in the SCR process.…”
Section: Introductionmentioning
confidence: 99%
“…Mathematical modelling plays an important role in developing a new catalytic technology or for improving the design of existing reactors. The performance of a monolithic reactor is a complex function of design parameters, operating conditions, and properties of both the catalyst and reaction mixture [27,[30][31][32][33]. The approach to design and analyse catalytic SCR reactor customarily adopted in the early literature was based on pseudo-homogeneous models accounting for axial concentration gradients [4,28,29,34].…”
Section: Introductionmentioning
confidence: 99%
“…Depending on the objectives, applications and computational limitations, these models can be classified as one-dimensional (1-D), two-dimensional (2-D) and three-dimensional models (3-D), or as washcoat (catalyst layer), single channel, or multichannel (full reactor). [22,27,28,[31][32][33][34][35].…”
Section: Introductionmentioning
confidence: 99%