IMAC capture of recombinant protein from unclarified mammalian cell feed streams

Fusion‐tag affinity chromatography is a key technique in recombinant protein purification. Current methods for protein recovery from mammalian cells are hampered by the need for feed stream clarification. We have developed a method for direct capture using immobilized metal affinity chromatography (IMAC) of hexahistidine (His6) tagged proteins from unclarified mammalian cell feed streams. The process employs radial flow chromatography with 300–500 μm diameter agarose resin beads that allow free passage of cells but capture His‐tagged proteins from the feed stream; circumventing expensive and cumbersome centrifugation and/or filtration steps. The method is exemplified by Chinese Hamster Ovary (CHO) cell expression and subsequent recovery of recombinant His‐tagged carcinoembryonic antigen (CEA); a heavily glycosylated and clinically relevant protein. Despite operating at a high NaCl concentration necessary for IMAC binding, cells remained over 96% viable after passage through the column with host cell proteases and DNA detected at ～8 U/mL and 2 ng/μL in column flow‐through, respectively. Recovery of His‐tagged CEA from unclarified feed yielded 71% product recovery. This work provides a basis for direct primary capture of fully glycosylated recombinant proteins from unclarified mammalian cell feed streams. Biotechnol. Bioeng. 2016;113: 130–140. © 2015 Wiley Periodicals, Inc.     

Purification of <Emphasis Type="Italic">Bm</Emphasis>R1 Recombinant Protein

This paper describes a refinement in the purification step that facilitated the downstream recovery of high purity BmR1 recombinant protein, which is a protein used as a test reagent in the commercialized rapid tests for detection of lymphac filariasis i.e. Brugia Rapid^TM and panLF rapid^TM. Purification was performed by immobilized metal affinity chromatography (IMAC), followed by ion exchange chromatography (IEX). Results showed that a total of 10.27 mg of BmR1 was obtained when IMAC was performed using 20 mM of imidazole and 5 column volume of wash buffer containing 500 mM of NaCl. Purity of the target protein was enhanced when buffer at pH 5.8 was used during the IEX. Two proteins that recurrently appeared below the BmR1 recombinant protein were identified by mass-spectrometry analysis as the same protein, thus they were probably degradation products of BmR1. These strategies improve purity of the target protein to be used in applications such as production of aptamers and monoclonal antibodies.     

Protein purification via aqueous two-phase extraction (ATPE) and immobilized metal affinity chromatography. Effectiveness of salt addition to enhance selectivity and yield of GFPuv

This study illustrates the compatibility and complementary nature of aqueous two-phase extraction (ATPE) and immobilized metal affinity chromatography (IMAC) in a general recovery scheme. The purification of green fluorescent protein (GFPuv) from extracts of Eschericia coli was investigated using a combination of these two techniques. High molarity of sodium chloride was found effective in increasing selectivity, with the promotion of hydrophobic interaction the probable mechanism that drove the target protein to a particular phase in ATPE, as well as that which enhanced GFPuv adsorption in IMAC. Moreover, the similar salt condition allows the direct application of the GFPuv-containing phase to the IMAC column without additional adjustment step. A simple screen of conditions was therefore performed to generate a favorable two-step purification scheme for GFP leading to an overall high purity.     

Combining protein-based IMAC, peptide-based IMAC, and MudPIT for efficient phosphoproteomic analysis

Immobilized metal affinity chromatography (IMAC) is a common strategy used for the enrichment of phosphopeptides from digested protein mixtures. However, this strategy by itself is inefficient when analyzing complex protein mixtures. Here, we assess the effectiveness of using protein-based IMAC as a pre-enrichment step prior to peptide-based IMAC. Ultimately, we couple the two IMAC-based enrichments and MudPIT in a quantitative phosphoproteomic analysis of the epidermal growth factor pathway in mammalian cells identifying 4470 unique phosphopeptides containing 4729 phosphorylation sites.     

Enrichment of phosphopeptides using biphasic immobilized metal affinity-reversed phase microcolumns

Immobilized metal affinity chromatography (IMAC) based on Fe (3+) or Ga (3+) chelation is the most widely employed technique for the enrichment of phosphopeptides from biological samples prior to mass spectrometric analysis. An IMAC resin geared mainly toward phosphoprotein enrichment, Pro-Q Diamond, has been assessed for its utility in phosphopeptide isolation. Using both single phosphoprotein tryptic digests of beta-casein and ovalbumin and synthetic mixtures composed of tryptic digests of phosphorylated and nonphosphorylated protein standards, the selectivity and sensitivity of Pro-Q Diamond resin in an immobilized metal affinity-reversed phase microcolumn format were compared to an alternate titanium dioxide approach. The biphasic microcolumn method was found to be superior to metal oxide-based phosphopeptide capture in biological samples of increasing complexity. The lower limit of mass spectrometric detection for the immobilized metal affinity-reversed phase microcolumn approach was determined to be 10 pmol of beta-casein monophosphorylated peptide in 20 muL of a solution of human serum protein digest (from 200 mug total serum protein after digestion and desalting).     

Two-step metal affinity purification of double-tagged (NusA-His6) fusion proteins

The present purification protocol applies to target proteins that are fused to a double tag, such as NusA-His6, through a linker that includes a protease-recognition sequence. It involves two steps of immobilized metal ion affinity chromatography (IMAC). NusA stabilizes the passenger protein during translation, whereas the His-tag enables affinity purification of the fusion. The eluate resulting from the first IMAC is buffer-exchanged to remove the imidazole and to achieve optimal conditions for the enzymatic cleavage performed by a His-tagged recombinant protease. The digested sample is loaded directly for a second IMAC step and the target protein is selectively recovered in the flow-through. The resin binds residual non-digested fusion protein, double-tagged moiety, protease and any contaminant that bound the affinity resin and was eluted from the first IMAC. The purity of the target protein usually makes a further purification step unnecessary for most of the lab applications. It takes less than 5 hours to purify the protein from a 5 g pellet.     

Trypsin immobilization by direct adsorption on metal ion chelated macroporous chitosan-silica gel beads

Silica gel bead coated with macroporous chitosan layer (CTS-SiO₂) was prepared, and the metal immobilized affinity chromatographic (IMAC) adsorbents could be obtained by chelating Cu²⁺, Zn²⁺, Ni²⁺ ions, respectively on CTS-SiO₂, and trypsin could be adsorbed on the IMAC adsorbent through metal–protein interaction forces. Batch adsorption experiments show that adsorption capacity for trypsin on these IMAC adsorbent variated with change of pH. The maximal adsorption reached when the solution was in near neutral pH in all three IMAC adsorbents. Adsorption isothermal curve indicated that maximal adsorption capacity could be found in the Cu²⁺-CTS-SiO₂ with the value of 4980 ± 125 IU g⁻¹ of the adsorbent, while the maximal adsorption capacity for trypsin on Zn²⁺ and Ni²⁺ loaded adsorbent was 3762 ± 68 IU g⁻¹ and 2636 ± 53 IU g⁻¹, respectively. Trypsin immobilized on the IMAC beads could not be desorbed by water, buffer and salt solution if the pH was kept in the range of 5–10, and could be easily desorbed from the IMAC beads by acidic solution and metal chelating species such as EDTA and imidazole. The effect of chelated metal ions species on CTS-SiO₂ beads on the activity and stability of immobilized trypsin was also evaluated and discussed. Trypsin adsorbed on Zn-IMAC beads retained highest amount of activity, about 78% of total activity could be retained. Although the Cu-IMAC showed highest affinity for trypsin, only 25.4% of the calculated activity was found on the beads, while the activity recovery found on Ni-IMAC beads was about 37.1%. A remarkable difference on stability of trypsin immobilized on three kinds of metal ion chelated beads during storage period was also found. Activity of trypsin on Cu-IMAC decreased to 24% of its initial activity after 1-week storage at 4 °C, while about 80% activity was retained on both Ni-IMAC and Zn-IMAC beads. Trypsin immobilized on Zn-CTS-SiO₂ could effectively digest BSA revealed by HPLC peptide mapping.     

重组人Fab金属螯合层析法纯化条件的研究

在重组人Fab(rh Fab)表达载体的羧基端插入六个组氨酸, 使其对金属螯合层析介质产生特异性吸附, 可用金属螯合亲和层析法进行分离纯化. 采用自制金属(铜、锌金属离子)螯合层析介质, 以pH和咪唑两种洗脱方法,对rh Fab段的纯化效果进行了探讨. 结果显示: 铜离子螯合层析介质比锌离子螯合层析介质对rh Fab的亲和能力更强; pH洗脱方法的重复性优于咪唑法; 金属铜离子螯合层析法对rh Fab进行一步纯化可得到纯度大于95%的rh Fab产品.     

On-column refolding of an insoluble histidine tag recombinant exopolyphosphatase from Trypanosoma brucei overexpressed in Escherichia coli

An exopolyphosphatase gene has been cloned by polymerase chain reaction (PCR) from Trypanosoma brucei and the corresponding protein overexpressed as a recombinant His-tag (histidine tag) exopolyphosphatase in E. coli in order to characterize its biochemical activity and to produce antibody to determine its localization. Because overexpression of this protein in bacteria resulted in the formation of inactive inclusion bodies, these structures were first solubilized in denaturant condition (6 M urea). Secondly, after a capture step using immobilized metal affinity chromatography (IMAC), a gradual refolding of the protein was performed on-column from 6 M to 0 M urea in the presence of 1% Triton X-100. Triton X-100 was used to abolish protein aggregation during the refolding step. The purified enzyme was active, demonstrating that at least part of the proteins was properly refolded.     

Production of polygalacturonase from <Emphasis Type="Italic">Coriolus versicolor</Emphasis> grown on tomato pomace and its chromatographic behaviour on immobilized metal chelates

Tomato pomace and pectin were used as the sole carbon sources for the production of polygalacturonase from a strain of Coriolus versicolor in submerged culture. The culture of C. versicolor grown on tomato pomace exhibited a peak of polygalacturonase activity (1,427 U/l) on the third day of culture with a specific activity of 14.5 U/mg protein. The production of polygalacturonase by C. versicolor grown on pectin as a sole carbon source increased with the time of cultivation, reaching a maximum activity of 3,207 U/l of fermentation broth with a specific activity of 248 U/mg protein. The levels of different isoenzymes of polygalacturonase produced during the culture growth were analysed by native PAGE. Differential chromatographic behaviour of lignocellulosic enzymes produced by C. versicolor (i.e. polygalacturonase, xylanase and laccase) was studied on immobilized metal chelates. The effect of ligand concentration, pH, the length of spacer arm and the nature of metal ion were studied for enzyme adsorption on immobilized metal affinity chromatography (IMAC). The adsorption of these lignocellulosic enzymes onto immobilized metal chelates was pH-dependent since an increase in protein adsorption was observed as the pH was increased from 6.0 to 8.0. The adsorption of polygalacturonase as well as other enzymes to immobilized metal chelates was due to coordination of histidine residues which are available at the protein surface since the presence of imidazole in the equilibration buffer abolished the adsorption of the enzyme to immobilized metal chelates. A one-step purification of polygalacturonase from C. versicolor was devised by using a column of Sepharose 6B-EPI 30-IDA-Cu(II) and purified enzyme exhibited a specific activity of about 150 U/mg protein, final recovery of enzyme activity of 100% and a purification factor of about 10. The use of short spacer arm and the presence of imidazole in equilibration buffer exhibited a higher selectivity for purification of polygalacturonase on this column with a high purification factor. The purified enzyme preparation was analysed by SDS-PAGE as well as by "in situ" detection of enzyme activity.     

Two-step method to isolate target recombinant protein from co-purified bacterial contaminant SlyD after immobilised metal affinity chromatography

As part of a study to purify the internal domain of HER2 (ICD) from recombinant expression, through metal immobilised affinity chromatography (IMAC), we encountered a contaminant, SlyD, a 29 kDa native E. coli protein. SlyD is a recurrent contaminant, with a histidine rich domain enabling binding to IMAC columns and thus co-elution with the target protein. Research has been carried out on this protein and its purification, however, no work mentions how to treat it as a true contaminant or describe procedures to isolate it from target proteins. In this report, we described a two-step chromatographic method for the purification of ICD, including IMAC as a capture step and size exclusion chromatography (SEC) as a polishing step. IMAC allowed us to purify ICD from bacterial crude with SlyD co-eluting. SEC then allowed us to resolve ICD from SlyD and achieve a purity greater than 95% for ICD. However, this method has been developed to accommodate any protein whose molecular weight is different enough from SlyD to be separated by SEC.     

Immobilized metal affinity chromatography of monoclonal immunoglobulin M against mutant amidase from Pseudomonas aeruginosa

The chromatographic behavior of monoclonal antibodies (MAbs) of immunoglobulin (Ig) M class against mutant (T103I) amidase from Pseudomonas aeruginosa was investigated on immobilized metal chelates. The effect of ligand concentration, the length of spacer arm, and the nature of metal ion were investigated in immobilized metal affinity chromatography (IMAC). The MAbs against mutant amidase adsorbed to Cu(II), Ni(II), Zn(II), Co(II), and Ca(II)-iminodiacetic acid (IDA) agarose columns. The increase in ligand concentration (epichlorohydrin: 30-60 and 1,4-butanediol-diglycidyl ether: 16-36) resulted in higher adsorption to IgM into immobilized metal chelates. The length of spacer arm was found to affect protein adsorption, as longer spacer arm (i.e., 1,4-butanediol-diglycidyl ether) increased protein adsorption of immobilized metal chelates. The adsorption of IgM onto immobilized metal chelates was pH dependent because an increase in the binding of IgM was observed as the pH varied from 6.0 to 8.0. The adsorption of IgM to immobilized metal chelates was the result of coordination of histidine residues to metal chelates that are available in the third constant domain of heavy chain (CH3) of immunoglobulins, as the presence of imidazole (5 mM) in the equilibration buffer abolished the adsorption of IgM to the column. The combination of tailor-made stationary phases for IMAC and a correct design of the adsorption parameters permitted to devise a one-step purification procedure for IgM. Culture supernatants containing IgM against mutant amidase (T103I) were purified either by IMAC on EPI-60-IDA-Co (II) column or by gel filtration chromatography on Sephacryl S-300HR. The specific content of IgM and final recovery of antibody activity exhibited similar values for both purification schemes. The purified preparations of IgM obtained by both schemes were apparently homogeneous on native polyacrylamide gel electrophoresis with a Mr of 851,000 Da. The results presented in this work strongly suggest that one-step purification of IgM by IMAC is a cost-effective and processcompatible alternative to other types of chromatography.     

A new strategy for the on-column exopeptidase cleavage of poly-histidine tagged proteins

This paper describes a new strategy, which aims to make on-column poly-histidine tag removal more useful in the production of recombinant proteins by improving the yield and efficiency of on-column exopeptidase cleavage. This involves improvement of the on-column cleavage condition by using imidazole concentrations in the range of 100-500 mM in the cleavage buffer. At 300 mM imidazole, maximum on-column cleavage yield (in excess of 99%) was achieved in 3h of incubation. However, as a result of the increased imidazole concentration, this new strategy of on-column cleavage results in some residual uncleaved poly-histidine tagged proteins (~0.1%) and the production of cleaved dipeptides, both of which need to be further removed in a subsequent step. A method involving the recirculation of recovered proteins and peptides through the immobilized metal affinity chromatography (IMAC) column (same-column recirculation) was found to be superior to subtractive IMAC for the purpose of contaminant clearance. Recovery of the detagged target proteins was achieved using 10 column volumes of recovery buffer, which had the effect of diluting the imidazole concentration to a suitably low level for contaminant removal by same-column recirculation. This strategy was also applicable at a higher adsorbent loading of 10 mg protein/mL adsorbent with an optimal ratio of 200 mU of DAPase per mg of adsorbed tagged maltose binding protein (MBP), giving a cleavage yield of 99.1% in 3 h. Finally, on-column cleavage conditions including the effect of protease concentration and incubation time on the new strategy have been investigated and comparisons are made for different tag removal strategies.     

Purification and characterization of RGD tumor-homing peptide conjugated human tumor necrosis factor alpha over-expressed in Escherichia coli

A number of approaches have been investigated to enhance the selective toxicity of tumor necrosis factor alpha (TNFalpha) to permit its systemic use in cancer therapy. Because vascular targeting has been proven to be a valid strategy for improving the therapeutic index of TNFalpha, we prepared RGD-hTNF consisting of human TNF fused with the ACDCRGDCFCG peptide, a ligand of alpha(v)beta(3) and alpha(v)beta(5) integrins. Recombinant RGD-hTNF was produced in Escherichia coli as a polyhistidine fusion protein. Between polyhistidine tag and RGD-hTNF, a tobacco etch virus (TEV) protease cleavage site (ENLYFQG) was introduced to ensure the release of intact RGD-hTNF. The purification strategy consisted of the target protein capture step by immobilized metal affinity chromatography (IMAC), TEV protease cleavage of fusion protein, the subtractive depletion of removed His-tag by IMAC and the final gel filtration step. As a result, about 18 mg of intact RGD-hTNF was obtained from 1l of bacteria culture. The purified RGD-hTNF was characterized by SDS-PAGE, Western blot, mass spectroscopy and gel filtration. Since the RGD-hTNF molecule retained the cytotoxic activity of the TNF moiety and the integrin binding ability of the RGD moiety, the purification method provided material for assessing its anti-tumor activity in animal model.     

Immobilized metal affinity chromatography of monoclonal immunoglobulin M against mutant amidase from Pseudomonas aeruginosa

The chromatographic behavior of monoclonal antibodies (MAbs) of immunoglobulin (Ig) M class against mutant (T103I) amidase from Pseudomonas aeruginosa was investigated on immobilized metal chelates. The effect of ligand concentration, the length of spacer arm, and the nature of metal ion were investigated in immobilized metal affinity chromatography (IMAC). The MAbs against mutant amidase adsorbed to Cu(II), Ni(II), Zn(II), Co(II), and Ca(II)-iminodiacetic acid (IDA) agarose columns. The increase in ligand concentration (epichlorohydrin: 30–60 and 1,4-butanediol-diglycidyl ether: 16–36) resulted in higher adsorption to IgM into immobilized metal chelates. The length of spacer arm was found to affect protein adsorption, as longer spacer arm (i.e., 1,4-butanediol-diglycidyl ether) increased protein adsorption of immobilized metal chelates. The adsorption of IgM onto immobilized metal chelates was pH dependent because an increase in the binding of IgM was observed as the pH varied from 6.0 to 8.0. The adsorption of IgM to immobilized metal chelates was the result of coordination of histidine residues to metal chelates that are available in the third constant domain of heavy chain (CH3) of immunoglobulins, as the presence of imidazole (5 mM) in the equilibration buffer abolished the adsorption of IgM to the column. The combination of tailor-made stationary phases for IMAC and a correct design of the adsorption parameters permitted to devise a one-step purification procedure for IgM. Culture supernatants containing IgM against mutant amidase (T103I) were purified either by IMAC on EPI-60-IDA-Co (II) column or by gel filtration chromatography on Sephacryl S-300HR. The specific content of IgM and final recovery of antibody activity exhibited similar values for both purification schemes. The purified preparations of IgM obtained by both schemes were apparently homogeneous on native polyacrylamide gel electrophoresis with a M _r of 851,000 Da. The results presented in this work strongly suggest that one-step purification of IgM by IMAC is a cost-effective and process-compatible alternative to other types of chromatography.     

Buffer exchange using size exclusion chromatography, countercurrent dialysis, and tangential flow filtration: Models, development, and industrial application

There are three major methods for buffer exchange of proteins at industrial scale: size exclusion chromatography (SEC), tangential flow filtration (TFF), and countercurrent dialysis (CCD). In order to determine the optimal technology for a given process, a study was done to compare these technologies on a technological and economic basis. This comparison required that new mathematical models be developed which enable the common features of each unit operation to be directly compared. The new concept of a diavolume equivalent for SEC, defined as the inverse of the fractional loading, was also introduced to aid in this comparison. Variables that were examined for each unit operation included range of buffer exchange, dilution of protein solution, yield, buffer requirements, total operating time, throughput, plant space, capital, raw materials, and labor costs. It was found that TFF and CCD have a greater range of buffer exchange than SEC. TFF also provides the advantage that concentration of the protein can readily be accomplished in the same step. For processes of equal batch size and yield, TFF and CCD also provide a two- to five- fold improvement in each of the remaining variables. The major economic advantage in using TFF and CCD over SEC is the decreased plant size required for manufacturing and thus the longer term use of existing facilities. Situations where SEC (or CCD) would be favored over TFF are when protein denaturation occurs in TFF but does not occur in SEC. (c) 1995 John Wiley & Sons, Inc.     

Production,IMAC purification,and molecular modeling of N-carbamoyl-D-amino acid amidohydrolase C-terminally fused with a six-his peptide

A six-His peptide was genetically engineered to the C-terminus of Agrobacterium radiobacter N-carbamoyl-D-amino acid amidohydrolase monomer to facilitate the protein purification with immobilized metal affinity chromatography (IMAC). The fusion enzyme, named as DCaseH, was overexpressed in Escherichia coli and one-step IMAC-purified. The production study showed that DCaseH was optimally produced at 15 degrees C for 25 h by the induction of 0.05 mM IPTG. Both Co(2+)-chelated TANOL gels and Ni(2+)-chelated nitriloacetic acid agarose gels efficiently purified DCaseH, with the former yielding purer enzyme than the latter. Highly pure DCaseH was obtained in the former purification with the addition of 5 mM imidazole in the washing buffer, and the specific enzyme activity was increased more than 11-fold. Denaturing IMAC purification successfully purified DCaseH from inclusion bodies that were mostly composed of the overexpressed DCaseH, while the attempt to refold the purified enzyme by either dialysis or solid-state refolding was not achieved. The purified native enzyme was optimally active at pH 6.5 and 50 degrees C, and the presence of 10% glycerol increased the activity. The molecular modeling of dimeric DCaseH indicated that the six-His tags were freely exposed to the protein surface, resulting in the selective and effective IMAC purification of DCaseH.     

Use of Streamline chelating for capture and purification of poly-His-tagged recombinant proteins

Expression of recombinant proteins with poly-histidine tags enables their convenient capture and purification using immobilized metal affinity chromatography (IMAC). The 6×His-tagged protein binds to a chelating resin charged with metal ions such as Ni²⁺, Cu²⁺ or Zn²⁺, and can therefore be separated from proteins which have lower, or no, affinity for the resin. Two recombinant proteins, a malaria transmission-blocking vaccine candidate secreted extracellularly by S. cerevisiae and a modified diphtheria toxin produced intracellularly by E. coli, were expressed with 6×His tags and could therefore be purified using IMAC. In an effort to further simplify the initial capture of these proteins, an expanded bed adsorption technique using a chelating resin (Streamline Chelating) was introduced. It was possible to capture the intracellular diphtheria protein from E. coli directly after cell lysis, without prior centrifugation or filtration. The extracellular malaria vaccine candidate was also directly captured from a high cell density yeast culture. Detailed information on the experimental work performed, and the capture processes developed, is provided.     

High-throughput protein purification and quality assessment for crystallization

The ultimate goal of structural biology is to understand the structural basis of proteins in cellular processes. In structural biology, the most critical issue is the availability of high-quality samples. "Structural biology-grade" proteins must be generated in the quantity and quality suitable for structure determination using X-ray crystallography or nuclear magnetic resonance (NMR) spectroscopy. The purification procedures must reproducibly yield homogeneous proteins or their derivatives containing marker atom(s) in milligram quantities. The choice of protein purification and handling procedures plays a critical role in obtaining high-quality protein samples. With structural genomics emphasizing a genome-based approach in understanding protein structure and function, a number of unique structures covering most of the protein folding space have been determined and new technologies with high efficiency have been developed. At the Midwest Center for Structural Genomics (MCSG), we have developed semi-automated protocols for high-throughput parallel protein expression and purification. A protein, expressed as a fusion with a cleavable affinity tag, is purified in two consecutive immobilized metal affinity chromatography (IMAC) steps: (i) the first step is an IMAC coupled with buffer-exchange, or size exclusion chromatography (IMAC-I), followed by the cleavage of the affinity tag using the highly specific Tobacco Etch Virus (TEV) protease; the second step is IMAC and buffer exchange (IMAC-II) to remove the cleaved tag and tagged TEV protease. These protocols have been implemented on multidimensional chromatography workstations and, as we have shown, many proteins can be successfully produced in large-scale. All methods and protocols used for purification, some developed by MCSG, others adopted and integrated into the MCSG purification pipeline and more recently the Center for Structural Genomics of Infectious Diseases (CSGID) purification pipeline, are discussed in this chapter.     

Purification of carboxypeptidase B by metal chelation affinity chromatography.

Norwegian lobster carboxypeptidase B (CPB) was purified in one step using immobilized metal chelate affinity chromatography (IMAC). The separation is based on the property that CPB has a high affinity for metal ions such as Cu2+. The CPB was purified from an hepatopancreas extract containing several endo- and exo-proteolytic activities. Its homogeneity was demonstrated by SDS-electrophoresis and isoelectric focusing in immobilized pH gradients. The implication of hydrophobic interaction between this enzyme and the IDA-Cu2+ gel is postulated.