Effect of Baffle Clearance on Scale Deposition in an Agitated Vessel.


Journal

ACS omega
ISSN: 2470-1343
Titre abrégé: ACS Omega
Pays: United States
ID NLM: 101691658

Informations de publication

Date de publication:
21 Sep 2021
Historique:
received: 04 07 2021
entrez: 27 9 2021
pubmed: 28 9 2021
medline: 28 9 2021
Statut: epublish

Résumé

The material deposition in a mixing tank agitated by the MAXBLEND impeller in a turbulent state was quantified and compared between cases with and without baffle clearance. Magnesium hydroxide formed from the chemical reaction between calcium hydroxide and magnesium chloride was used as a model of scale formation. Flow velocity in the tank was investigated by employing computational fluid dynamics simulation and experimentally validated by an ultrasonic velocity profiler method. Results showed that the amount of scale decreased with the increase in the rotational speed of the impeller due to the erosion effect on the tank wall. In the case without baffle clearance, the smaller weight of the scale was deposited on the front of the baffle plate due to the flow impingement, which enhanced the removal of the scale deposition. However, the lower-velocity magnitude behind the baffles resulted in an enhancement in the formation of scale. Installation of baffle clearance caused a contraction flow in between the tank wall and baffles, and consequently, the higher flow velocity reduced the amount and thickness of the scale. Measurement of the torque showed that the baffle clearance did not affect the power consumption, so the installation of baffle clearance can be a promising approach to reduce scale deposition in terms of saving operational costs and increasing process efficiency and safety.

Identifiants

pubmed: 34568685
doi: 10.1021/acsomega.1c03503
pmc: PMC8459426
doi:

Types de publication

Journal Article

Langues

eng

Pagination

24070-24074

Informations de copyright

© 2021 The Authors. Published by American Chemical Society.

Déclaration de conflit d'intérêts

The authors declare no competing financial interest.

Auteurs

Eri Sato (E)

Department of Chemical Science and Engineering, Kobe University, 1-1 Rokkodai-cho, Nada-ku, Kobe-shi 657-8501, Hyogo, Japan.

Yusuke Ochi (Y)

Department of Chemical Science and Engineering, Kobe University, 1-1 Rokkodai-cho, Nada-ku, Kobe-shi 657-8501, Hyogo, Japan.

Hiroo Horiguchi (H)

Sumitomo Heavy Industries Process Equipment Co., Ltd, 1501 Imazaike, Saijo 799-1362, Ehime, Japan.

Katsuhide Takenaka (K)

Sumitomo Heavy Industries Process Equipment Co., Ltd, 1501 Imazaike, Saijo 799-1362, Ehime, Japan.

Jie Wu (J)

CSIRO Mineral Resources, Bayview Avenue, Clayton 3168, Australia.

Rajarathinam Parthasarathy (R)

Chemical Engineering, School of Engineering, RMIT University, City Campus, Melbourne 3001, Australia.

Yoshiyuki Komoda (Y)

Department of Chemical Science and Engineering, Kobe University, 1-1 Rokkodai-cho, Nada-ku, Kobe-shi 657-8501, Hyogo, Japan.

Naoto Ohmura (N)

Department of Chemical Science and Engineering, Kobe University, 1-1 Rokkodai-cho, Nada-ku, Kobe-shi 657-8501, Hyogo, Japan.

Classifications MeSH