“…For the actual continuous processing, the switching times of the PCC process were controlled based on the dynamic UV control method developed by Cytiva (Bangtsson & Lacki, 2012) using column inlet UV absorbance and the column outlet UV absorbance of the first column in a connected set‐up to calculate the column breakthrough. However, we found that the proposed method with ΔUV as a controlling signal is error prone if the inlet feed concentration is not constant, which is a result of the integrated process; therefore, loading to approximately 70% breakthrough was controlled with a new approach developed by our group (Gerstweiler et al, 2022). A cycle of the PCC process consists of the following phases: Loading at a flowrate between 0.4 and 0.8 ml min −1 til breakthrough level triggered; Post loading wash of 2 CV at 1 ml min −1 ; Washing with 5 CV at 1 ml min −1 with equilibration buffer containing no DTT (lysis buffer pH 8.9 containing 0.35 M NaCl); Elution with 20 CV of elution buffer (40 mM di sodium hydrogen phosphate (SA026, ChemSupply), 1 M NaCl, 5% w w −1 glycerol, 1 mM EDTA) at 1 ml min −1 ; Cleaning with 1 M sodium hydroxide (SA178, ChemSupply) for 15 CV at 1 ml min −1 ; Washing with water for 5 CV at 1 ml min −1 , and; Re‐equilibration for with equilibration buffer for 5 CV at 1 ml min −1 .…”