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Department of Chemical Engineering, Massachusetts Institute of Technology, Cambridge, Massachusetts 02139
Correspondence: Address reprint requests to Bernhardt L. Trout, E-mail: trout{at}mit.edu.
| ABSTRACT |
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| INTRODUCTION |
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![]() | (1) |
![]() | (2) |
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![]() | (3) |
The presence of such an intermediate is implied by the first-order kinetics observed in accelerated aggregation studies (Kendrick et al., 1998
; Webb et al., 2001
), and in some cases this intermediate has been characterized (Cleland, 1991
).
The tendency of proteins to aggregate is an especially grave problem in biotechnology and the pharmaceutical industry where it is desired to synthesize, process, and store proteins at the highest possible concentrations and over long periods of time. Because proteins that are in the aggregated state generally do not have the same biological activity as proteins in the native state, can often be immunogenic, and may even have acute toxic effects in vivo, it is essential to develop strategies for preventing aggregation in these applications.
One such strategy is to add to protein solutions a compound that hinders aggregation. Molecules that have been shown to slow protein aggregation in different applications include urea, guanidinium chloride, amino acids (predominantly arginine and glycine), sugars, polyols, polymers (such as polyethylene glycol and cyclodextrins), surfactants, and antibodies. In most of these cases, the mechanisms by which the additives prevent aggregation are not known; therefore there is no potential to develop a rational methodology of additive selection, and additives are currently chosen by extensive, heuristic, experimental screening procedures.
In a few cases, however, qualitative mechanistic models have been developed to describe how a particular additive deters aggregation. Polyethylene glycol has been shown to inhibit the aggregation of carbonic anhydrase, interferon-
, tissue plasminogen activator, and deoxyribonuclease during refolding (Cleland, 1991
; Cleland et al., 1992
) by binding to the unfolded protein and folding intermediates through hydrophobic interactions (Fig. 2). This binding decreases the free energy of the unfolded protein and refolding transition state, increases the activation energy for aggregation, slows the rate of aggregation, and increases the final yield of active protein.
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from the native state in aqueous solution (Kendrick et al., 1998
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To affect the kinetics of protein association reactions selectively without affecting protein folding and solution phase structure, there must be a unique feature of the association transition state that can be exploited by a binding interaction with an additive. The emerging picture of protein association/dissociation transition states indicates that each protein in the encounter complex is still mostly solvated but near the orientation in the final complex (Selzer and Schreiber, 2001
; Schreiber, 2002
). Because the complex is still mostly solvated but the two protein molecules are in close proximity to one another, there is the potential for a "gap effect" to arise in a mixed solvent if the additive is significantly larger than the primary solvent (Fig. 4). This gap effect is analogous to osmotic stress (Rand, 1992
). In such a situation, the large additive will be excluded from solvating the gap between the protein molecules for steric reasons. This, in turn, results in an increase in the free energy of the protein-protein encounter complex.
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We expect that our study should have impact in protein processing and protein formulation (Wang, 1999
; Cleland et al., 1993
).
| THEORETICAL APPROACH |
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![]() | (4) |

µ
is the change in the activation free energy induced by the additive, kb is Boltzmann's constant, and T is the absolute temperature. Thus, to compute the relative rate constants, we must compute the shift in activation free energy for association and dissociation induced by the additives. Our approach to this is toThe details of each of these steps are described in the following sections.
Two-model association reactions
As two limiting models of proteins undergoing an association and dissociation reaction, we choose:
Å2 of area on a face. This area was selected to make the change in protein solvent-accessible area of reaction the same for the cases of the two spheres and two planes (the reaction coordinates are explained below). The thermodynamics properties of these plates are obtained by calculating the property per unit of surface area of a pair of infinite plates and then multiplying by the area above. Thus, edge effects are ignored.
These two geometries can be considered as extreme cases by which associating proteins approach one another. Because of the symmetry of these simple model proteins, the reaction coordinates, x, can be simply defined as the shortest distance between the planes and the distance between the centers of the spheres. We are then free to choose any representative free energy of the complex as a function of this reaction coordinate, µP, 0(x). For convenience, we set the reference states as the monomers (x
+
), define the dimer states to be 8 kcal/mol more stable than monomer states, and place a modest 2 kcal/mol free energy barrier for association between the two states. Arbitrarily, we select x = 20 Å as the dimer state for the spheres, and x = 1.5 Å as the dimer state for the planes. The resulting reaction coordinates can be modeled as
![]() | (5) |
![]() | (6) |
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![]() | (7) |
is the transfer free energy. The transfer free energy can be computed via the equation
![]() | (8) |
![]() | (9) |
XP, the preferential binding coefficient of additive to the protein in water, is defined as
![]() | (10) |
Following our earlier work in all-atom molecular dynamics simulations of preferential binding (Baynes and Trout, 2003
), we introduce the relation
![]() | (11) |
The above relation can be substituted into Eq. 9 to yield
![]() | (12) |
We now invoke three assumptions that allow significant simplification of the above equation:
where R is the gas constant. Since the ternary system in question here is dominated by the water and additive, this assumption effectively means that water-additive interactions are ideal. For aqueous solutions of many additives of interest, such as those of NaCl, glycerol, sucrose, and urea, the experimental activities of water-additive mixtures are within 10% of ideality at molalities up to 1 mol/kg (Scatchard et al., 1938
XP term.
mX).
Applying these approximations to Eq. 12 yields
![]() | (13) |
In the case of the additive, we wish to introduce a simple, physically based model for the additive-protein radial distribution function, gX. To do this, we relate gX to the potential of mean force between the additive and protein,
UXP
,
![]() | (14) |
We then choose the form of the potential of mean force as a standard intermolecular potential function. To select a suitable function, we fit the parameters of standard, physically based intermolecular potentials, such as Lennard-Jones, Kihara, and exponential-6 (Exp-6) to the radial distribution functions of water, urea, and glycerol obtained from all-atom molecular dynamics simulations (Baynes and Trout, 2003
). In each case, the intermolecular potential parameters were fit by nonlinear minimization (Marquardt method) of the squared residuals although constraining (Lagrange method) the radial distribution to give the same preferential binding coefficient (
XP, via Eq. 11) as the actual additive radial distribution function. Preferential binding coefficients were preserved in the fitting procedure because of their tight relationship (via Eq. 9) to the transfer free energy, the property we ultimately wish to model.
After obtaining the best fits with each potential function, it was observed that the Lennard-Jones potential did not adequately fit the data, and the Kihara potential did not fit the data well at physically meaningful parameter values. Therefore, the three-parameter Exp-6 potential was selected as a model of the additive-protein potential of mean force as
![]() | (15) |
In the above equation, r is the distance between the solvent molecule and protein, and rm,
, and
are the Exp-6 parameters, described below. Results of the fitting process are shown in Fig. 7 and Table 1. Note that the first peak in the radial distribution functions occurs at a value of r smaller than what might be expected. This is because in our case, r is defined as the distance from the center of mass of the solvent or additive to the van der Waals shell of the protein, not to the nucleus of the atoms at the protein surface. This also leads to a value of rm that may be smaller than expected.
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UXP
. However, we wished to constrain ourselves to standard potential functions whose parameters had some physical meaning. Fits are also shown for water because water-protein radial distribution function data was available; however, the full radial distribution function for water was used for all of the calculations in this work.
The Exp-6 potential combines an exponential repulsive term with an inverse sixth-power attractive term and has a single minimum at U(r = rm) =
. The last Exp-6 parameter,
, is related to the breadth of the minimum near r = rm, and reflects the rigidity and shape of the additive.
In extending the Exp-6 representation to neutral crowders and other additives for which no radial distribution functions are available, rm is used as a measure of additive size;
is held constant at 3.7, the mean of the observed values for water, glycerol, and urea; and
is set to yield a desired preferential binding coefficient between the additive and dissociated protein state. For a neutral crowder,
XP is set to 0 at x
(the dissociated state) by the constraint that such an additive should not affect the free energy of isolated protein molecules.
| RESULTS |
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was set according to the neutrality condition (
XP = 0 for the dissociated state, x
).
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XP, the gap effect on the transfer free energy increases proportionately with increasing additive size, rm. For the additive sizes illustrated, the effect on transfer free energy ranges from 0 to almost 6 kcal/mol. At the same additive size and change in surface area of reaction, the planes exhibit approximately double the gap effect of the spheres. This is because the lack of curvature of the planes necessitates that their gap effect is concentrated over a narrower region of the reaction coordinate. These transfer free energy effects can be superimposed onto a free energy diagram by simple addition (Eq. 7). The final free energy diagrams are shown in Fig. 9. In the case of the spherical model, the transition state in the original free energy surface (µP, 0(x)) is near the maxima in the transfer free energies, so the transfer free energy effects make significant changes to the activation free energy of the association and dissociation reactions in an additive solution at all values of rm. For the planar model, the location of the maximum in the transfer free energy depends on rm. Consequently, the transfer free energy maximum for the planar model does not always build on the existing free energy barrier in µP, 0(x). In fact at higher rm, the transition state for association and dissociation results completely from the gap effect. The original transition state is "drowned out."
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XP, as shown in Figs. 10 and 11. Increasing
XP can also be seen to decelerate association and accelerate dissociation. This is a well-known result consistent with the fact that denaturants are used to slow protein association reactions. The magnitude of this change depends on whether the free surface area of the transition state is more similar to that of the monomer or to that of the dimer. If the transition state is similar to the dimer, as in the case of the planar proteins, there is a strong effect on ka and almost no effect on kd. For the spherical protein geometry, the transition state is closer to the monomer, and the effect of
XP is larger on kd than on ka.
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XP decreases both the association and dissociation rates, consistent with the gap effect hypothesis. An approximately two-orders-of-magnitude drop in the association rate constant can be seen over the range of additive sizes shown (28 Å). In the case of two associating planes, this effect does not appear at moderate additive sizes (2.5 < rm < 5.5 Å) because, although the maximum in transfer free energy keeps increasing, it moves away from the original transition state on the reaction coordinate.
Designing additives for the control of aggregation
It may be possible to exploit the gap effect in designing solvent additives for the prevention of protein aggregation. Prevalent additives that work via a pure free surface effect, such as guanidinium and urea, have apparent radii (rm) of
23 Å. These have the disadvantage, however, that they can also enhance the unfolding or partial unfolding of proteins because of their positive preferential binding coefficients. The results of the preceding section suggest that if the size of these additives could be increased to
8 Å although maintaining their preferential binding coefficient with isolated protein molecules, the gap effect can potentially contribute another 12 order-of-magnitude depression in the association rate.
As the size of an additive is increased, its preferential binding coefficient will tend to decrease as the third power of radius. This is because increasing additive size increases the excluded volume of additive and protein, which decreases the preferential binding coefficient. To compensate for this excluded volume difference and return
XP to its original value, an additional additive-protein attraction must be introduced into the molecule.
If it is not possible to increase the additive-protein attraction in some way as size is increased, the additive will have a large, negative preferential binding coefficient, and a gap effect will not appear. A gap effect arises for neutral crowders because there is a region of solvent that is inaccessible to the additive around encounter complexes but not around isolated protein molecules. In the case of an "excluded crowder" with a large, negative preferential binding coefficient, the volume of exclusion is actually larger in the dissociated state than in the encounter complex or associated state. Thus, in stark contrast to neutral crowders, excluded crowders like sugars, polyols, and large, hydrophilic polymers favor association (Linder and Ralston, 1995
; Kosk-Kosicka et al., 1995
; Nichol et al., 1981
).
| CONCLUSIONS |
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Our analysis of the model supports the hypothesis that a "gap effect," analogous to osmotic stress, will occur in association reactions when large solution additives with sufficient protein affinity are present. This gap effect affects the free energy of protein-protein encounter complexes, such as the association transition state, and has only a small effect on the end states. Thus, we have demonstrated how it is possible for an additive to exert a purely kinetic effect on protein association/dissociation. We call additives which have these properties "neutral crowders": they are neutral in that they do not significantly shift the free energy of isolated protein molecules, but they decrease the rate of protein association and dissociation by being excluded from the interprotein gap in protein-protein encounter complexes for steric reasons.
For an optimal effect, the maximum in the transfer free energy induced by the gap effect must be near the original association free energy barrier. When this is not the case, the gap effect will be strongest when the original barrier is small (<12 kcal/mol) or nonexistent, such as in diffusion-controlled reactions.
As the size of a neutral crowder is increased, the gap effect becomes proportionately larger, but maintaining neutrality is difficult as size increases. At a constant protein-additive interaction energy, increasing additive size would decrease the protein-additive preferential binding coefficient as the third power of additive size due to an excluded volume effect. Thus, to make a large neutral crowder, additive-protein interactions must become significantly more attractive as size is increased. If this cannot be achieved, the gap effect will diminish and ultimately disappear.
Today, the best known additives for suppressing protein association reactions are small denaturants such as urea and guanidinium chloride. Our gap effect model predicts that if a significantly larger additive, perhaps 45-times the size of these small additives, can be developed, and it were a "neutral crowder," it would depress association rates by a factor of 1001000-times more than guanidinium or urea at the same molar concentration.
| APPENDIX: RELATION TO VIRIAL COEFFICIENTS |
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![]() | (16) |
UiP
is the potential of mean force between a solvent component i (additive or water) and the protein. In terms of the radial distribution functions, this is
![]() | (17) |
The preceding equation can then be substituted into the integrand of Eq. 13 for the water and additive to yield
![]() | (18) |
![]() | (19) |
Thus, the additive protein and water protein second virial coefficients are related to the radial distribution functions (Eq. 17) and to the transfer free energy (Eq. 19).
| ACKNOWLEDGEMENTS |
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The authors thank the National Institutes of Health Biotechnology Training Program, the Singapore-Massachusetts Institute of Technology Alliance, and the National University of Singapore for funding.
Submitted on March 8, 2004; accepted for publication June 15, 2004.
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