The scope of this research is to obtain a film coating on stainless steel surfaces in order to reduce the interaction between the metal surface and the precipitates, so to mitigate fouling in heat exchangers. Perfuoropolyethers were used to obtain nano-range fluorinated layers in order to make hydrophobic the stainless steel surfaces. A pilot plant with two identical heat exchangers was built to investigate the ability of the hydrophobic coating of preventing fouling. The heat exchangers, installed in parallel, operated at the same temperature and pressure conditions, i.e. laminar flow regime and inlet flow temperatures of 291–293 K for cold streams and 313–333 K for hot streams. We compared the heat transfer performance of the two heat exchangers. After a five months operation the decrease in the heat transferred was 56% for the coated heat exchanger and 62% for the uncoated heat exchanger. Moreover, the increase of heat transfer resistance due to scale on the uncoated heat exchanger, with respect to the coated one, was three times higher.

Perfluoropolyethers coatings design for fouling reduction on heat transfer stainless steel surfaces / V. Oldani, C.L. Bianchi, S. Biella, C. Pirola, G. Cattaneo. - In: HEAT TRANSFER ENGINEERING. - ISSN 0145-7632. - 37:2(2015), pp. 210-219. [10.1080/01457632.2015.1044417]

Perfluoropolyethers coatings design for fouling reduction on heat transfer stainless steel surfaces

V. Oldani
Primo
;
C.L. Bianchi
Secondo
;
C. Pirola
Penultimo
;
2015

Abstract

The scope of this research is to obtain a film coating on stainless steel surfaces in order to reduce the interaction between the metal surface and the precipitates, so to mitigate fouling in heat exchangers. Perfuoropolyethers were used to obtain nano-range fluorinated layers in order to make hydrophobic the stainless steel surfaces. A pilot plant with two identical heat exchangers was built to investigate the ability of the hydrophobic coating of preventing fouling. The heat exchangers, installed in parallel, operated at the same temperature and pressure conditions, i.e. laminar flow regime and inlet flow temperatures of 291–293 K for cold streams and 313–333 K for hot streams. We compared the heat transfer performance of the two heat exchangers. After a five months operation the decrease in the heat transferred was 56% for the coated heat exchanger and 62% for the uncoated heat exchanger. Moreover, the increase of heat transfer resistance due to scale on the uncoated heat exchanger, with respect to the coated one, was three times higher.
Settore ING-IND/25 - Impianti Chimici
Settore CHIM/04 - Chimica Industriale
2015
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/2434/277969
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