Abstrakt
The paper investigates the precipitation of salicylic acid from a highly supersaturated solution (βin = 46.3) in three reactor types: Koflo STM, STR, and STR+DT, operating in both silent and ultrasound-assisted (sonoprecipitation) modes. It examines process intensification in terms of conversion, supersaturation discharge, and yield by adjusting operating conditions, including turbulence distribution (via reactor type selection) and turbulence intensity induced either by mixing (εmix) or by a combination of mixing and ultrasound assistance. Across all systems, pure crystalline salicylic acid was obtained, as confirmed by FT-IR and XRD analyses. Results show that the distribution of unit power inputs and the residence time distribution (RTD) significantly influence both reaction and precipitation kinetics, regardless of ultrasound use. In the silent STM, increasing εmix improved conversion but reduced the mean residence time, negatively affecting yield due to incomplete supersaturation discharge. Conversely, in the silent STR, higher εmix impaired reaction kinetics, limiting conversion, but also reduced outlet supersaturation, promoting nucleation. The impact of ultrasound assistance was complex and not straightforward compared to silent systems, with final outcomes resulting from overlapping and often opposing effects. In US-assisted reactors, increasing εUS decreased induction time and led to both improved supersaturation discharge and higher yield.
| Język oryginału | angielski |
|---|---|
| Numer artykułu | 110847 |
| Czasopismo | Chemical Engineering and Processing - Process Intensification |
| Tom | 226 |
| Identyfikatory DOI | |
| Status publikacji | Opublikowano - sie 2026 |
Obszary tematyczne ASJC Scopus
- Chemia ogólna
- Ogólna inżynieria chemiczna
- Inżynieria energetyczna i technologia energetyczna
- Inżynieria przemysłowa i produkcyjna
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