TY - JOUR
T1 - Cleaning in place of plate heat exchangers – Removal behavior of whey protein fouling
AU - Zhang, Yimin
AU - van den Berg, Frans W.J.
AU - Andersen, Mogens L.
AU - Parjikolaei, Behnaz Razi
AU - Bakalis, Serafim
N1 - Publisher Copyright:
© 2025 The Author(s)
PY - 2026
Y1 - 2026
N2 - Maintaining hygiene is critical in food manufacturing, and Cleaning-in-Place (CIP) is the standard method used. In this study we examine the CIP process to remove whey protein fouling in plate heat exchangers (PHEs). Fouling layers, representative for typical manufacturing processes, were generated through a controlled fouling process. The effects of temperature, velocity, pH, and amount of fouling on the cleaning process were assessed by measuring protein mass in the CIP effluent. Regardless of the cleaning conditions, removing the last 2 % of fouling mass takes up almost 50 % of the total cleaning time. To further investigate this slow second stage, the cleaning process was paused, and PHE channels were disassembled to quantify the residual fouling distribution on the plates. The cleaning solution (80 °C of 0.5 wt% NaOH at velocity 27.5 cm·s−1) formed preferential pathways through the PHE channel rather than following the plate's liquid-distribution pattern, thus limiting contact with the residual fouling layer. The subsequent fouling removal was primarily driven by NaOH diffusion. A cleaning mathematical model was developed and validated against experimental data, effectively estimating the cleaning process in two distinct PHE systems.
AB - Maintaining hygiene is critical in food manufacturing, and Cleaning-in-Place (CIP) is the standard method used. In this study we examine the CIP process to remove whey protein fouling in plate heat exchangers (PHEs). Fouling layers, representative for typical manufacturing processes, were generated through a controlled fouling process. The effects of temperature, velocity, pH, and amount of fouling on the cleaning process were assessed by measuring protein mass in the CIP effluent. Regardless of the cleaning conditions, removing the last 2 % of fouling mass takes up almost 50 % of the total cleaning time. To further investigate this slow second stage, the cleaning process was paused, and PHE channels were disassembled to quantify the residual fouling distribution on the plates. The cleaning solution (80 °C of 0.5 wt% NaOH at velocity 27.5 cm·s−1) formed preferential pathways through the PHE channel rather than following the plate's liquid-distribution pattern, thus limiting contact with the residual fouling layer. The subsequent fouling removal was primarily driven by NaOH diffusion. A cleaning mathematical model was developed and validated against experimental data, effectively estimating the cleaning process in two distinct PHE systems.
KW - Cleaning model
KW - Cleaning-in-place
KW - Plate heat exchanger
KW - Whey protein fouling
U2 - 10.1016/j.ces.2025.122395
DO - 10.1016/j.ces.2025.122395
M3 - Journal article
AN - SCOPUS:105012954343
SN - 0009-2509
VL - 320
JO - Chemical Engineering Science
JF - Chemical Engineering Science
M1 - 122395
ER -