TY - JOUR
T1 - Purification of a Fc-Fusion Protein with [Bathophenathroline:metal] Complexes
AU - Withanage, Thisara Jayawickrama
AU - Alcalay, Ron
AU - Krichevsky, Olga
AU - Wachtel, Ellen
AU - Mazor, Ohad
AU - Patchornik, Guy
PY - 2025/1/31
Y1 - 2025/1/31
N2 - In this study, we assess an alternative Fc-fusion protein purification method that does not rely on chromatographic media or ligands. Recombinant human acetylcholinesterase, fused to the Fc domain of human IgG1 (henceforth, AChE-Fc), was purified with precipitated aromatic complexes composed of the bathophenanthroline (henceforth, batho) chelator with either Zn
2+ or Cu
2+ ions (i.e., [(batho)
3:Zn
2+] or [(batho)
2:Cu
2+]) in the presence of polyethylene glycol 6000 (PEG-6000). In a three-step purification process conducted at pH 7, AChE-Fc was captured by the aromatic complexes (Step 1); unbound or weakly bound protein impurities were removed with 20 mM NaCl (Step 2); and AChE-Fc was then extracted at pH 7 (Step 3) using 100 mM Na citrate buffer in 250 mM NaCl. Purified AChE-Fc was not aggregated (as determined by dynamic light scattering (DLS) and Native PAGE). However, full enzymatic activity was only preserved with the [(batho)
3:Zn
2+] complex. Interaction between AChE-Fc and [(batho)
3:Zn
2+] led to ~83-88% overall protein yield. Thirty-fold process upscaling by volume required only proportional increase in the amounts of [(batho)
3:Zn
2+] and PEG-6000. Efficient (95-97%) chelator recycling was achieved by recrystallization. Chelator leaching into purified AchE-Fc was estimated to be ~0.3% relative to the total amount used. Taken together, this novel procedure has the potential to provide an economical and practical avenue for the industrial purification of Fc-fusion proteins.
AB - In this study, we assess an alternative Fc-fusion protein purification method that does not rely on chromatographic media or ligands. Recombinant human acetylcholinesterase, fused to the Fc domain of human IgG1 (henceforth, AChE-Fc), was purified with precipitated aromatic complexes composed of the bathophenanthroline (henceforth, batho) chelator with either Zn
2+ or Cu
2+ ions (i.e., [(batho)
3:Zn
2+] or [(batho)
2:Cu
2+]) in the presence of polyethylene glycol 6000 (PEG-6000). In a three-step purification process conducted at pH 7, AChE-Fc was captured by the aromatic complexes (Step 1); unbound or weakly bound protein impurities were removed with 20 mM NaCl (Step 2); and AChE-Fc was then extracted at pH 7 (Step 3) using 100 mM Na citrate buffer in 250 mM NaCl. Purified AChE-Fc was not aggregated (as determined by dynamic light scattering (DLS) and Native PAGE). However, full enzymatic activity was only preserved with the [(batho)
3:Zn
2+] complex. Interaction between AChE-Fc and [(batho)
3:Zn
2+] led to ~83-88% overall protein yield. Thirty-fold process upscaling by volume required only proportional increase in the amounts of [(batho)
3:Zn
2+] and PEG-6000. Efficient (95-97%) chelator recycling was achieved by recrystallization. Chelator leaching into purified AchE-Fc was estimated to be ~0.3% relative to the total amount used. Taken together, this novel procedure has the potential to provide an economical and practical avenue for the industrial purification of Fc-fusion proteins.
KW - acetylcholinesterase
KW - bathophenanthroline:Zn complexes
KW - Fc-fusion proteins
KW - non-chromatographic purification
U2 - 10.3390/antib14010011
DO - 10.3390/antib14010011
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C2 - 39982226
SN - 2073-4468
VL - 14
JO - Antibodies
JF - Antibodies
IS - 1
M1 - 11
ER -