Analysis of fouling and breakthrough of process related impurities during depth filtration using confocal microscopy

Titer improvement has driven process intensification in mAb manufacture. However, this has come with the drawback of high cell densities and associated process related impurities such as cell debris, host cell protein (HCP), and DNA. This affects the capacity of depth filters and can lead to carryover of impurities to protein A chromatography leading to early resin fouling. New depth filter materials provide the opportunity to remove more process related impurities at this early stage in the process. Hence, there is a need to understand the mechanism of impurity removal within these filters. In this work, the secondary depth filter Millistak+ X0HC (cellulose and diatomaceous earth) is compared with the X0SP (synthetic), by examining the breakthrough of DNA and HCP. Additionally, a novel method was developed to image the location of key impurities within the depth filter structure under a confocal microscope. Flux, tested at 75, 100, and 250 LMH was found to affect the maximal throughput based on the max pressure of 30 psi, but no significant changes were seen in the HCP and DNA breakthrough. However, a drop in cell culture viability, from 87% to 37%, lead to the DNA breakthrough at 10% decreasing from 81 to 55 L/m² for X0HC and from 105 to 47 L/m² for X0SP. The HCP breakthrough was not affected by cell culture viability or filter type. The X0SP filter has a 30%–50% higher max throughput depending on viability, which can be explained by the confocal imaging where the debris and DNA are distributed differently in the layers of the filter pods, with more of the second tighter layer being utilized in the X0SP.     

Mechanistic evaluation of virus clearance by depth filtration

Virus clearance by depth filtration has not been well‐understood mechanistically due to lack of quantitative data on filter charge characteristics and absence of systematic studies. It is generally believed that both electrostatic interactions and sized based mechanical entrapment contribute to virus clearance by depth filtration. In order to establish whether the effectiveness of virus clearance correlates with the charge characteristics of a given depth filter, a counter‐ion displacement technique was employed to determine the ionic capacity for several depth filters. Two depth filters (Millipore B1HC and X0HC) with significant differences in ionic capacities were selected and evaluated for their ability to eliminate viruses. The high ionic capacity X0HC filter showed complete porcine parvovirus (PPV) clearance (eliminating the spiked viruses to below the limit of detection) under low conductivity conditions (≤2.5 mS/cm), achieving a log₁₀ reduction factor (LRF) of > 4.8. On the other hand, the low ionic capacity B1HC filter achieved only ～2.1–3.0 LRF of PPV clearance under the same conditions. These results indicate that parvovirus clearance by these two depth filters are mainly achieved via electrostatic interactions between the filters and PPV. When much larger xenotropic murine leukemia virus (XMuLV) was used as the model virus, complete retrovirus clearance was obtained under all conditions evaluated for both depth filters, suggesting the involvement of mechanisms other than just electrostatic interactions in XMuLV clearance. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:431–437, 2015     

Control of antibody high and low molecular weight species by depth filtration-based cell culture harvesting

Depth filtration-based harvesting is widely used in mAb manufacturing to remove cell and process-related impurities. However, it has not been studied on control of product-related impurities, which are very critical for product quality. In this article, we studied the interactions of depth filter with high and low molecular weight species (HMWs and LMWs) for their direct removal from cell culture. The process parameters (filter, loading, temperature, and flux) were evaluated for adsorption of HMWs and LMWs by depth filters. The adsorption is significantly dependent on filter media and loading capacity and is mainly on the basis of hydrophobic interaction during harvesting. The HMW and LMW species were characterized as HMW1, HMW2, LMW1, and LMW2. The increasing binding from LMW2 to LMW1, HMW1, and HMW2 is correlated with their increasing hydrophobicity score. Adsorption using enriched HMW sample demonstrated similar total protein binding capacity (36–40 g/m²) between depth filters D0HC and X0HC. However, X0HC has stronger HMW binding than D0HC (71% vs 43% of bound protein), indicating more hydrophobic interaction in X0HC. HMW2 DBC on X0HC reached 12 g/m², similar to protein binding on hydrophobic interaction membrane adsorbers. Further study showed LMW can induce HMW formation. This study provides a critical understanding of HMW and LMW interaction with depth filters. The strategy of HMW and LMW control by depth filtration-based harvesting was implemented successfully in mAb manufacturing.     

Effectiveness of host cell protein removal using depth filtration with a filter containing diatomaceous earth

The increased cell density and product titer in biomanufacturing have led to greater use of depth filtration as part of the initial clarification of cell culture fluid, either as a stand-alone unit operation or after centrifugation. Several recent studies have shown that depth filters can also reduce the concentration of smaller impurities like host cell proteins (HCP) and DNA, decreasing the burden on subsequent chromatographic operations. The objective of this study was to evaluate the HCP removal properties of the Pall PDH4 depth filter media, a model depth filter containing diatomaceous earth, cellulose fibers, and a binder. Experiments were performed with both cell culture fluid (CCF) and a series of model proteins with defined pI, molecular weight, and hydrophobicity chosen to match the range of typical HCP. The location of adsorbed (fluorescently labeled) proteins within the depth filters was determined using confocal scanning laser microscopy. Protein binding was greater for proteins that were positively charged and more hydrophobic, consistent with adsorption to the negatively charged diatomaceous earth. The lowest degree of binding was seen with proteins near their pI, which were poorly removed by this filter. These results provide new mechanistic insights into the factors governing the filter capacity and performance characteristics of depth filters containing diatomaceous earth that are widely used in the clarification of CCF.     

Depth filter material process interaction in the harvest of mammalian cells

Upstream advances have led to increased mAb titers above 5 g/L in 14-day fed-batch cultures. This is accompanied by higher cell densities and process-related impurities such as DNA and Host Cell Protein (HCP), which have caused challenges for downstream operations. Depth filtration remains a popular choice for harvesting CHO cell culture, and there is interest in utilizing these to remove process-related impurities at the harvest stage. Operation of the harvest stage has also been shown to affect the performance of the Protein A chromatography step. In addition, manufacturers are looking to move away from natural materials such as cellulose and Diatomaceous Earth (DE) for better filter consistency and security of supply. Therefore, there is an increased need for further understanding and knowledge of depth filtration. This study investigates the effect of depth filter material and loading on the Protein A resin lifetime with an industrially relevant high cell density feed material (40 million cells/ml). It focuses on the retention of process-related impurities such as DNA and HCP through breakthrough studies and a novel confocal microscopy method for imaging foulant in-situ. An increase in loading of the primary-synthetic filter by a third, led to earlier DNA breakthrough in the secondary filter, with DNA concentration at a throughput of 50 L/m² being more than double. Confocal imaging of the depth filters showed that the foulant was pushed forward into the filter structure with higher loading. The additional two layers in the primary-synthetic filter led to better pressure profiles in both primary and secondary filters but did not help to retain HCP or DNA. Reduced filtrate clarity, as measured by OD600, was 1.6 fold lower in the final filtrate where a synthetic filter train was used. This was also associated with precipitation in the Protein A column feed. Confocal imaging of resin after 100 cycles showed that DNA build-up around the outside of the bead was associated with synthetic filter trains, leading to potential mass transfer problems.     

Development of adsorptive hybrid filters to enable two-step purification of biologics

Recent progress in mammalian cell culture process has resulted in significantly increased product titers, but also a substantial increase in process- and product-related impurities. Due to the diverse physicochemical properties of these impurities, there is constant need for new technologies that offer higher productivity and improved economics without sacrificing the process robustness required to meet final drug substance specifications. Here, we examined the use of new synthetic adsorptive hybrid filters (AHF) modified with the high binding capacity of quaternary amine (Emphaze? AEX) and salt-tolerant biomimetic (Emphaze? ST-AEX) ligands for clearance of process-related impurities like host cell protein (HCP), residual DNA, and virus. The potential to remove soluble aggregates was also examined. Our aim was to develop a mechanistic understanding of the interactions governing adsorptive removal of impurities during filtration by evaluating the effect of various filter types, feed streams, and process conditions on impurity removal. The ionic capacity of these filters was measured and correlated with their ability to remove impurities for multiple molecules. The ionic capacity of AHF significantly exceeded that of traditional adsorptive depth filters (ADF) by 40% for the Emphaze? AEX and by 700% for the Emphaze? ST-AEX, providing substantially higher reduction of soluble anionic impurities, including DNA, HCPs and model virus. Nevertheless, we determined that ADF with filter aid provided additional hydrophobic functionality that resulted in removal of higher molecular weight species than AHF. Implementing AHF demonstrated improved process-related impurity removal and viral clearance after Protein A chromatography and enabled a two-step purification process. The consequences of enhanced process performance are far reaching because it allows the downstream polishing train to be restructured and simplified, and chromatographic purity standards to be met with a reduced number of chromatographic steps.     

Exploitation of the adsorptive properties of depth filters for host cell protein removal during monoclonal antibody purification

Depth filtration has been widely used during process scale clarification of cell culture supernatants for the removal of cells and cell debris. However, in addition to their filtration capabilities, depth filters also possess the ability to adsorb soluble species. This aspect of depth filtration has largely not been exploited in process scale separations and is usually ignored during cell culture harvest development. Here, we report on the ability of depth filters to adsorptively remove host cell protein contaminants from a recombinant monoclonal antibody process stream and characterize some of the underlying interactions behind the binding phenomenon. Following centrifugation, filtration through a depth filter prior to Protein A chromatographic capture was shown to significantly reduce the level of turbidity observed in the Protein A column eluate of the monoclonal antibody. The Protein A eluate turbidity was shown to be linked to host cell protein contaminant levels in the Protein A column load and not to the DNA content. Analogous to flowthrough chromatography in which residence time/bed height and column loading are key parameters, both the number of passes through the depth filter and the amount of centrifuge centrate loaded on the filter were seen to be important operational parameters governing the adsorptive removal of host cell protein contaminants. Adsorption of proteins to the depth filter was shown to be due to a combination of electrostatic and hydrophobic adsorptive interactions. These results demonstrate the ability to employ depth filtration as an integrative unit operation combining filtration for particulate removal with adsorptive binding for contaminant removal.     

A rapid filtration assay for cAMP

The receptor-binding assay for cAMP was improved by using polyethylenimine-treated glass filters. A polyethylenimine-treated glass filter has high protein binding capacity. This high capacity allows an increase in the amount of protein per assay tube and the use of a crude preparation, such as a beef heart extract, as specific binding protein instead of a purified protein, which has been used in the classical filtration assays involving cellulose ester filters. Since the time required for the separation of the protein-cAMP complex and the free nucleotide can be shortened by the use of polyethylenimine-treated filters, the dissociation of the bound ligand during the separation procedure, which is a serious problem with other modified assay methods involving charcoal adsorption, is minimized. Filtration through polyethylenimine-treated glass filters also gives low blanks and prevents the loss of protein or ligand due to breakage of the filters, which is often observed with fragile cellulose ester membranes. In consequence, this simple and rapid filtration assay allows more accurate and reproducible determinations.     

The interaction of pentosan polysulphate (SP54) with human neutrophil elastase and connective tissue matrix components

The binding of pentosan polysulphate (SP54) to human polymorphonuclear leucocyte elastase (PMNE) and some of its natural and synthetic substrates has been investigated. Using an ion exchange (DE52) assay system the binding of SP54 to PMNE was found to be 100 times stronger than to collagen or proteoglycan (PG). While the order for in vitro binding of the drug to purified substrates was found to be PG greater than gelatin greater than type I collagen, in vivo experiments indicated that SP54 was localized in tissues rich in collagen. Using gel-exclusion chromatography it was shown that these tissues also contained proteinaceous components other than PG and collagen which interacted with SP54. These results indicate that the potent inhibitor activity of SP54 against PMNE (50% inhibition at 1.7 X 10(-7)M) probably occurs by a specific interaction with the enzyme rather than by substrate binding inhibition, although the latter interaction may be important for localising the drug in these tissues.     

Minimized virus binding for tests of barrier materials.

Viruses are used to test the barrier properties of materials. Binding of virus particles during passage through holes in the material may yield misleading test results. The choices of challenge virus and suspending medium may be important for minimizing confounding effects that might arise from such binding. In this study, different surrogate viruses, as well as different support media, were evaluated to determine optimal test parameters. Two membranes with high-binding properties (nitrocellulose and cationic polysulfone) were used as filters to compare binding activities of different surrogate challenge viruses (MS2, phi X174, T7, PRD1, and phi 6) in different media. The media consisted of buffered saline with surfactants, serum, or culture broth as additives. In addition, elution rates of viruses that bound to the membranes were determined. The results suggest that viruses can bind by hydrophobic and electrostatic interactions, with phi X174 displaying the lowest level of binding by either process. The nonionic detergents Triton X-100 and Tween 80 (0.1%) equally minimized hydrophobic interactions. Neither anionic nor cationic surfactants were as effective at nontoxic levels. Serum was effective at reducing both hydrophobic and electrostatic binding, with 2% being sufficient for eliminating binding under our test conditions. Thus, phi X174 remains the best choice as a surrogate virus to test barrier materials, and Triton X-100 (0.1%) remains a good choice for reducing hydrophobic binding. In addition, binding of viruses by barrier materials is unlikely to prevent passage of blood-borne pathogens.     

Interactions of the high-mobility-group-like Ceratitis capitata C1 proteins with DNA

We have studied the interactions of the high-mobility-group-like proteins (C1a1, C1a2 and C1b) from the fruit fly Ceratitis capitata with DNA. Nitrocellulose filter binding assays, thermal denaturation studies and spectrofluorimetry of the complexes revealed the existence of specific and nonspecific interactions. Thermal denaturation curves showed that the three proteins stabilized the DNA, thus suggesting a preferential binding to double-stranded DNA. The calculation of the thermodynamic parameters of the interactions showed that the nonspecific bindings were characterized by low association constants (Ka) with values ranging from 2.7 X 10(4) M-1 to 2.0 X 10(6) M-1. Also, the cooperativity of these interactions was relatively high (cooperativity factor, w, values ranging over 20-35), and the number of nucleotides involved was low (1-3 base pairs). On the other hand, the existence of specific interactions between C1 proteins and DNA was suggested by two facts: the retention of C. capitata [3H]DNA in nitrocellulose filters was only a low percentage of total input DNA and there was a marked size dependence of the binding (25% retention of a 40-kb DNA and only 3% retention with a DNA of 1 kb). The specific bindings had higher Ka values than the nonspecific ones, and they also were cooperative. Some differences were observed between C1b and the C1a proteins about the way they interact with C. capitata DNA.     

Utility of Polycation-Treated Filters for the Assay of Receptors for VIP

Abstract

This study examined the utility of four polycationic agents for treating glass fibre filters used in the receptor binding assay for vasoactive intestinal peptide (VIP). Polyethylenimine (PEI), polybrene, protamine and methylated bovine serum albumin proved satisfactory in terms of low filter binding of free radioligand and retention of membrane-bound radioligand. Their performance was superior or comparable to untreated Millipore EGWP cellulose acetate filters which we had previously utilized but which are no longer manufactured. The results with polycations indicate the importance of ionic interactions between filter, biological membranes and radioligand in determining the performance of a filtration assay for radioligand-receptor binding. At a practical level, PEI has the disadvantage of potential toxicity. The satisfactory performance of the other polycations indicates that they provide safer alternatives to PEI for filtration assay of the VIP receptor and possibly receptors for other basic ligands.     

Characterisation of a generic monoclonal antibody harvesting system for adsorption of DNA by depth filters and various membranes

The physical parameters governing adsorption of DNA by various positively charged depth filters and membranes have been assessed. Buffers that reduced or neutralised the depth filter or membrane charge, and those that impeded hydrophobic interactions were shown to affect their operational capacity, demonstrating that DNA was adsorbed by a combination of electrostatic and hydrophobic interactions. The adsorption profile of DNA by a Sartobind Q anion exchange membrane showed immediate breakthrough, irrespective of challenge DNA concentration or flow rate, and in this case adsorption was by electrostatic interactions only. The production-scale removal of DNA from harvest broths containing therapeutic protein by partitioning of cells and debris from protein in sequential centrifugation and filtration steps, and the concentration of DNA in process supernatant were assessed. Centrifugation reduced the quantity of DNA in the process material from 79.8 g ml^-1 to 9.3 g ml^-1 whereas the concentration of DNA in the supernatant of pre- and post-filtration samples had only marginally reduced DNA content: from 6.3 to 6.0 g ml^-1 respectively. DNA was concentrated to 27.3 g ml^-1 along with monoclonal antibody in the ultrafiltration step. Similar effects were observed in the harvest step for a second antibody.     

Influence of Salts on Virus Adsorption to Microporous Filters

We investigated the direct and indirect effects of mono-, di-, and trivalent salts (NaCl, MgCl₂, and AlCl₃) on the adsorption of several viruses (MS2, PRD-1, X174, and poliovirus 1) to microporous filters at different pH values. The filters studied included Millipore HA (nitrocellulose), Filterite (fiberglass), Whatman (cellulose), and 1MDS (charged-modified fiber) filters. Each of these filters except the Whatman cellulose filters has been used in virus removal and recovery procedures. The direct effects of added salts were considered to be the effects associated with the presence of the soluble salts. The indirect effects of the added salts were considered to be (i) changes in the pH values of solutions and (ii) the formation of insoluble precipitates that could adsorb viruses and be removed by filtration. When direct effects alone were considered, the salts used in this study promoted virus adsorption, interfered with virus adsorption, or had little or no effect on virus adsorption, depending on the filter, the virus, and the salt. Although we were able to confirm previous reports that the addition of aluminum chloride to water enhances virus adsorption to microporous filters, we found that the enhanced adsorption was associated with indirect effects rather than direct effects. The increase in viral adsorption observed when aluminum chloride was added to water was related to the decrease in the pH of the water. Similar results could be obtained by adding HCl. The increased adsorption of viruses in water at pH 7 following addition of aluminum chloride was probably due to flocculation of aluminum, since removal of flocs by filtration greatly reduced the enhancement observed. The only direct effect of aluminum chloride on virus adsorption that we observed was interference with adsorption to microporous filters. Under conditions under which hydrophobic interactions were minimal, aluminum chloride interfered with virus adsorption to Millipore, Filterite, and 1MDS filters. In most cases, less than 10% of the viruses adsorbed to filters in the presence of a multivalent salt and a compound that interfered with hydrophobic interactions (0.1% Tween 80 or 4 M urea).     

Study of binding protein-ligand interaction by ammonium sulfate-assisted adsorption on cellulose esters filters

A technique for the study of neutral carbohydrate binding protein-ligand interaction is described in this report. It is based on filtration on cellulose esters filters of a mixture of the binding protein and the radioactive ligand, following a treatment of this mixture with ammonium sulfate; the technique is described for the galactose binding protein and for the maltose binding protein of Escherichia coli. For the galactose binding protein, an ammonium sulfate concentration far below that required for precipitation of the protein is sufficient to promote an almost complete retention of the protein on the filters. Furthermore, the addition of ammonium sulfate does not modify the amount of preexisting binding protein-ligand complex, and, in much less than one second, leads to a conformation of the protein-ligand complex which does not allow further ligand binding or dissociation. Hence, the technique is not only very useful for the detection of binding proteins in crude extracts and during purification procedures, it is also of value in the determination of the kinetic parameters of protein-ligand interactions.     

Scale‐down models to optimize a filter train for the downstream purification of recombinant pharmaceutical proteins produced in tobacco leaves

The extraction of biopharmaceutical proteins from intact leaves involves the release of abundant particulate contaminants that must be removed economically from the process stream before chromatography, for example, using disposable filters that comply with good manufacturing practice. We therefore scaled down an existing 200‐kg process for the purification of two target proteins from tobacco leaves (the monoclonal antibody 2G12 and the fluorescent protein DsRed, as monitored by surface plasmon resonance spectroscopy and fluorescence imaging, respectively) and screened different materials on the 2‐kg scale to reduce the number of depth filtration steps from three to one. We assessed filter cost and capacity, filtrate turbidity, and protein recovery when the filter materials were challenged with extracts from different tobacco varieties and related species grown in soil or rockwool. PDF4 was consistently the most suitable depth filter because it was the least expensive, it did not interact significantly with the target proteins, and it had the greatest overall capacity. The filter capacity was generally reduced when plants were grown in rockwool, but this substrate has a low bioburden, thus improving process safety. Our data concerning the clarification of plant extracts will help in the design of more cost‐effective downstream processes and accelerate their development.     

Electrostatic analysis of bacterial expansins

Expansins are a family of proteins with plant cell wall remodeling‐activity, which bind cell wall components through hydrophobic and electrostatic interactions. A shallow area on the surface of the protein serves as the polysaccharide binding site (PBS) and it is composed of conserved residues. However, electric charge differences on the opposite face of the PBS produce basic, neutral, or acidic proteins. An analysis of forty‐four bacterial expansins, homologues of BsEXLX1, revealed two main groups defined by: (a) the presence or absence of disulfide bonds; and (b) by the proteins isoelectric point (pI). We determined the location of the residues responsible for the pI on the structure of representative expansins. Our results suggest that the electric charge at the opposite site of the PBS may help in substrate differentiation among expansins from different species; in addition, electrostatic polarization between the front and the back of the molecule could affect expansin activity on cellulose. Proteins 2015; 83:215–223. © 2014 Wiley Periodicals, Inc.     

Effects of pH and high ionic strength on the adsorption and activity of native and mutated cellobiohydrolase I from Trichoderma reesei

Cellobiohydrolase I (CBHI) is the major cellulase of Trichoderma reesei. The enzyme contains a discrete cellulose-binding domain (CBD), which increases its binding and activity on crystalline cellulose. We studied cellulase-cellulose interactions using site-directed mutagenesis on the basis of the three-dimensional structure of the CBD of CBHI. Three mutant proteins which have earlier been produced in Saccharomyces cerevisiae were expressed in the native host organism. The data presented here support the hypothesis that a conserved tyrosine (Y492) located on the flat and more hydrophilic surface of the CBD is essential for the functionality. The data also suggest that the more hydrophobic surface is not directly involved in the CBD function. The pH dependence of the adsorption revealed that electrostatic repulsion between the bound proteins may also control the adsorption. The binding of CBHI to cellulose was significantly affected by high ionic strength suggesting that the interaction with cellulose includes a hydrophobic effect. High ionic strength increased the activity of the isolated core and of mutant proteins on crystalline cellulose, indicating that once productively bound, the enzymes are capable of solubilizing cellulose even with a mutagenized or with no CBD. © 1995 Wiley-Liss, Inc.     

The Effect of Hydraulic Loading Rate and Influent Source on the Binding Capacity of Phosphorus Filters

Sorption by active filter media can be a convenient option for phosphorus (P) removal and recovery from wastewater for on-site treatment systems. There is a need for a robust laboratory method for the investigation of filter materials to enable a reliable estimation of their longevity. The objectives of this study were to (1) investigate and (2) quantify the effect of hydraulic loading rate and influent source (secondary wastewater and synthetic phosphate solution) on P binding capacity determined in laboratory column tests and (3) to study how much time is needed for the P to react with the filter material (reaction time). To study the effects of these factors, a 2² factorial experiment with 11 filter columns was performed. The reaction time was studied in a batch experiment. Both factors significantly (α = 0.05) affected the P binding capacity negatively, but the interaction of the two factors was not significant. Increasing the loading rate from 100 to 1200 L m⁻² d⁻¹ decreased P binding capacity from 1.152 to 0.070 g kg⁻¹ for wastewater filters and from 1.382 to 0.300 g kg⁻¹ for phosphate solution filters. At a loading rate of 100 L m⁻² d⁻¹, the average P binding capacity of wastewater filters was 1.152 g kg⁻¹ as opposed to 1.382 g kg⁻¹ for phosphate solution filters. Therefore, influent source or hydraulic loading rate should be carefully controlled in the laboratory. When phosphate solution and wastewater were used, the reaction times for the filters to remove P were determined to be 5 and 15 minutes, respectively, suggesting that a short residence time is required. However, breakthrough in this study occurred unexpectedly quickly, implying that more time is needed for the P that has reacted to be physically retained in the filter.     

Adsorption of glycinin and β-conglycinin on silica and cellulose: surface interactions as a function of denaturation, pH, and electrolytes

Soybean proteins have found uses in different nonfood applications due to their interesting properties. We report on the kinetics and extent of adsorption on silica and cellulose surfaces of glycinin and β-conglycinin, the main proteins present in soy. Quartz crystal microgravimetry (QCM) experiments indicate that soy protein adsorption is strongly affected by changes in the physicochemical environment. The affinity of glycinin and the mass adsorbed on silica and cellulose increases (by ca. 13 and 89%, respectively) with solution ionic strength (as it increases from 0 to 100 mM NaCl) due to screening of electrostatic interactions. In contrast, β-conglycinin adsorbs on the same substrates to a lower extent and the addition of electrolyte reduces adsorption (by 25 and 57%, respectively). The addition of 10 mM 2-mercaptoethanol, a denaturing agent, reduces the adsorption of both proteins with a significant effect for glycinin. This observation is explained by the cleavage of disulfide bonds which allows unfolding of the molecules and promotes dissociation into subunits that favors more compact adsorbed layer structures. In addition, adsorption of glycinin onto cellulose decreases with lowering the pH from neutral to pH 3 due to dissociation of the macromolecules, resulting in flatter adsorbed layers. The respective adsorption isotherms fit a Langmuir model and QCM shifts in energy dissipation and frequency reveal multiple-step kinetic processes indicative of changes in adlayer structure.