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* Department of Chemistry, The Scripps Research Institute, La Jolla, California; and
Department of Mathematics and Computer Science, Clarkson University, Potsdam, New York
Correspondence: Address reprint requests to Evan T. Powers, Dept. of Chemistry, The Scripps Research Institute, La Jolla, CA 92037. E-mail: epowers{at}scripps.edu.
| ABSTRACT |
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| INTRODUCTION |
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Nucleated polymerizations have several well-known features according to the classical model of Oosawa and Asakura (7
), including 1), a critical concentration, below which fibrils cannot form; 2), a lag phase before fibrils form, which can be eliminated by the addition of preformed fibrils (seeds); and 3), a strong dependence of the fibril formation rate on concentration, which increases with the size of the nucleus (7
9
). This concentration dependence can be expressed in terms of t50, the time at which a fibril formation reaction reaches 50% completion, as follows:
![]() | (1) |
| MATERIALS AND METHODS |
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| RESULTS |
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The rate equations for our nucleated polymerization model can be written using the information in Fig. 1 A. However, we have found it convenient to rescale the time and concentration variables as suggested by Goldstein and Stryer (9
):
![]() | (2) |
![]() | (3) |
![]() | (4) |
![]() | (5) |
![]() | (6) |
![]() | (7) |
![]() | (8) |
![]() | (9) |
= b/c = Ks/Kc;
is the rescaled equivalent of the supercritical concentration. Inspection of Eqs. 39 reveals that they cannot reach steady state, since df/d
and dm/d
are always >0. However, steady state can be most closely approached when x1 = 1 (i.e., [X1] = Kc), xi = 1/
i1, and, substituting these expressions into Eq. 8,
![]() | (10) |
, xtot, and n. Ferrone has warned, however, that rescaling can obscure whether a given value for a parameter is physically reasonable (8
105, xtot
106, and 3
n
9. These parameter ranges are justified in the Supplementary Material.
Limiting cases
We examine two limiting cases here. The first is that of a classical nucleated polymerization. The features of a classical nucleated polymerization (in particular, the high concentration dependence of the rate) are well known and have already been mentioned in the Introduction. We merely wish to add here that classical nucleated polymerizations require the following conditions to be met: 1), the monomer must quickly come to a preequilibrium with oligomers, so that the nucleation rate is dictated by the relative stabilities of the nucleus and monomer; 2), the oligomer concentrations must be low enough to be ignored relative to the monomer concentration (xi << xl, 2
i
n); and 3), the initial monomer concentration must be high enough for monomer dissociation from fibrils to be negligible throughout most of the fibril formation reaction. The first two conditions are met when xtot <<
and the third is met when 1 << xtot, so this limiting case obtains when 1 << xtot <<
. The rate equations (Eqs. 39) can be simplified for a classical nucleated polymerization and solved analytically (7
) (see Supplementary Material). We show the solutions for x1, f, and m here (since they will be used later):
![]() | (11) |
![]() | (12) |
![]() | (13) |
Equation 13 allows the constant in Eq. 1 to be expressed in terms of the parameters n and
. Monomer dissociation from fibrils is ignored in classical nucleated polymerizations (because of the third condition listed above), so m = xtot at completion and therefore m = 0.5xtot at
50. Inserting m = 0.5xtot into Eq. 13, solving for
50, inserting the solution into Eq. 1, and converting from t50 and [X]tot to
50 and xtot yields
![]() | (14) |
Equation 14 shows that the value of
50 for a classical nucleated polymerization can be determined at any value of xtot if n and
are known.
Our second limiting case is that of very high concentrations. Monomer dissociation from both fibrils and oligomers can be ignored when the protein concentration is high enough (xtot >>
) (9
). Thus, this limiting case corresponds to an irreversible polymerization. The rate equations for an irreversible polymerization can be solved analytically (see Supplementary Material), yielding
![]() | (15) |
![]() | (16) |
Goldstein and Stryer have also obtained Eq. 15 for the special case i = 1 (9
). Solutions for xi in terms of
could in principle be obtained by inverting Eq. 16, but this yields an exponential integral:
![]() | (17) |
Equation 17 can only be integrated numerically, but inspection reveals that
as s
1, which implies that the reaction is complete at s = 1. The concentration of the monomer at this point, the end of the reaction, is 0, whereas the concentrations of the other species are:
![]() | (18) |
Fig. 2 A is a plot of the weight fractions (ixi/xtot) of monomers to hexamers over the course of an irreversible polymerization. Fig. 2 B is a plot of weight fractions at the end of an irreversible polymerization against aggregate size. (Weight fractions are plotted instead of concentrations because they are independent of xtot; see Eqs. 15 and 18). Fig. 2 shows that species larger than hexamers are always negligible (weight fraction <0.01 for all
for i > 6) and that dimers, trimers, and (to a lesser extent) tetramers are the dominant species at the end of an irreversible polymerization. It should be noted that experimental fibril formation reactions can behave like irreversible polymerizations only while the monomer concentration is high. Eventually, when the monomer concentration is low enough and oligomer concentrations are high enough, monomer dissociation will no longer be negligible. The fibril formation reaction will then relax from the (oligomer-rich) state it is in when monomer dissociation can no longer be ignored to the near-steady-state point (where fibrils dominate). The effect of fibril formation reactions obeying the kinetics of irreversible polymerizations early in their time courses does not manifest itself in the distribution of products at the end of the reaction, but in the concentration dependence of the fibril formation rate. This point will be discussed further below.
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= 1000, and xtot varying from 100.25 to 106 in steps of 100.25. Fig. 3 A is a plot of the fraction completion, defined as the fibril mass concentration at a given time divided by the fibril mass concentration at the near-steady-state point (given by Eq. 10), against
(on a logarithmic scale) for selected values of xtot. Fig. 3 B is a log-log plot of the values of
50 from the numerical solutions versus xtot. Fig. 3 shows that the concentration dependence of fibril formation kinetics changes as the concentration increases, as has also been observed by Kodaka (39
). In the low-concentration regime, where xtot is much less than
(xtot
101.5), the time courses in Fig. 3 A are evenly spaced and the
50 vs. xtot log-log plot in Fig. 3 B is linear. In fact, these
50 values are very close (within 0.1 log10 unit) to the solid line in Fig. 3 B, which represents the
50 values expected for a classical nucleated polymerization (the solid line was plotted using Eq. 14). In the medium-concentration regime, where xtot is closer to, but still less than,
(101.5 < xtot
= 103), the fraction completion plots become increasingly closely spaced in Fig. 3 A and the
50 values deviate from the solid line in Fig. 3 B (although they still fall on the dashed curve, the origin of which is explained below). The curvature in the log-log plot of
50 vs. xtot shows that the fibril formation reaction does not meet the requirements of classical nucleated polymerizations in the medium-concentration regime. In the high-concentration regime, where xtot >
, the fraction completion plots in Fig. 3 A are almost identical, and
50 is nearly independent of xtot when xtot
105 in Fig. 3 B (
50 changes by <0.05 log units between xtot = 105 and 106). This behavior marks an even more serious departure from classical nucleated polymerization.
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= 102), the concentrations of oligomers are low (<2% of xtot), and xtot >> 1 throughout most of the reaction. This assertion is supported by the similarity between the numerical solutions of Eqs. 39 (solid curves) and the classical nucleated polymerization solutions (dashed curves) in Fig. 4 A. These solutions deviate only near the end of the conversion phase (and only because monomer dissociation from fibrils is not accounted for in classical nucleated polymerizations). In contrast, substantial amounts of oligomers form during the preequilibration phase in the medium-concentration regime (>15% of the total amount of protein when xtot = 100; see Fig. 4 B), where the total protein concentration is closer to the supercritical concentration. This degree of oligomer formation violates the second requirement of classical nucleated polymerizations. It causes the monomer concentration to be <xtot during the nucleation phase, which lowers the nucleus concentration, which in turn decreases the fibril nucleation rate and slows the fibril formation reaction. This point is illustrated by the deviation of the numerical solutions (solid curves) from the classical nucleated polymerization solutions (dashed curves) in Fig. 4 B, and by the deviation of
50 from the theoretical line at xtot = 100 in Fig. 3 B. This deviation increases as xtot approaches
.
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50 values for fibril formation if xtot is replaced with the concentration of monomer that actually exists during the nucleation phase. The actual monomer concentration can be determined by noting that at preequilibrium
(see Supplementary Material) and the fibril mass concentration should be negligible (m
0). The conservation of mass (Eq. 8) then becomes
![]() | (19) |
The relevant root of Eq. 19 is
![]() | (20) |
Equation 20 is accurate to <5% for n
4 and xtot
. The error is >10% only when n = 3 and xtot > 0.97
. Note that x1
xtot at preequilibrium when xtot <<
. Replacing xtot in Eq. 14 with the expression on the right-hand side of Eq. 20 yields
![]() | (21) |
Equation 21 is plotted as the dashed curve in Fig. 3 B. This curve deviates from the numerically calculated
50 values by <0.15 log units between xtot = 100.25 and 103. The closeness of this fit justifies the assertion made above that the test case still behaves like a classical nucleated polymerization in the medium-concentration regime, except for the amount of oligomers formed. The dashed curve in Fig. 3 B, however, still deviates from the
50 values in the high-concentration regime.
As in the medium-concentration regime, a large amount of oligomeric protein quickly forms in the high-concentration regime (>97% of the total by
= 104 at xtot = 105). Furthermore, preequilibrium between monomer and oligomers is never attained, as illustrated by the lack of a plateau in the oligomer concentration in Fig. 4 C. These two observations indicate that neither the first nor the second requirement for a classical nucleated polymerization is met by fibril formation reactions in the high-concentration regime, and it is therefore unlikely that the classical nucleated polymerization framework will be useful in understanding their behavior. In contrast, the coincidence of the numerical solutions of the rate equations (solid curves) and the irreversible polymerization solutions (dashed curves) in Fig. 4 C shows that the irreversible polymerization model accurately predicts fibril formation kinetics until the monomer concentration becomes small enough that dissociation reactions are no longer negligible (
104). This similarity to an irreversible polymerization can be used to explain the near-independence of
50 and xtot in the high-concentration regime as follows.
Fibril formation reactions at high concentrations behave initially like irreversible polymerizations because association reactions dominate dissociation reactions (x1xi >>
xi for all i). However, the monomer concentration decreases as fibril formation proceeds, allowing monomer dissociation reactions to become more and more significant. Eventually the association and dissociation rates balance. This point is illustrated in the inset to Fig. 4 C, which shows that the monomer concentration reaches a gently sloping plateau at x1
1500, or 3
/2. It can be shown (see Supplementary Material) that the same happens at higher concentrations with the plateau always being close to 3
/2, no matter what xtot is. When x1 reaches its plateau, the concentrations of dimers, trimers, etc. are close to the concentrations expected at the end of an irreversible polymerization (see Supplementary Material). As a result, the concentrations of oligomers are directly proportional to xtot (see Eq. 18). Now, the time required for the fibril formation reaction to proceed from the point at which x1 has reached its plateau to completion depends on the magnitudes of the individual terms in the rate equations relative to the total amount of protein that has to be converted into fibrils. Almost all of the terms in Eqs. 37 have the form x1xi or
xi. Since x1 is independent of xtot once it reaches its plateau and xi is directly proportional to xtot for all i
2, these terms are directly proportional to xtot. In other words, the terms in the rate equations increase in direct proportion to the amount of protein that has to be converted into fibrils. Therefore, in the high-concentration regime, the time required to convert the protein into fibrils remains roughly constant as the protein concentration increases. In fact, it can be shown that
![]() | (22) |
50 at extremely high concentrations. Equation 22 is accurate to within a factor of
4, depending on n and
(see Supplementary Material). Note that the parameter n in Eq. 22 does not represent the size of the thermodynamic nucleus, since the monomer is the "nucleus" in the high-concentration regime. Instead, n represents the size of the structural nucleus, that is, the size of the species that would be the nucleus if the protein concentration were less than the supercritical concentration.
Our assumption that species grow only by monomer addition, which is crucial to the results described above, may not be physically realistic in the high-concentration regime. Because oligomers are abundant during fibril formation in the high-concentration regime (Fig. 4 C), there is no reason to expect that they will not associate with each other. If oligomer-oligomer association occurred, the fibril formation reaction would have the same kinetics as colloidal aggregation, as first described by von Smoluchowski (50
,51
). Fibril formation models in which oligomer-oligomer associations occur are beyond the scope of this work, but Kodaka has shown that, under these circumstances, the rate of fibril formation would be inversely proportional to the total protein concentration (39
).
Concentration dependence of fibril formation rates for 3
n
9 and 102
105
Fig. 5 is composed of log-log plots of
50 against xtot for several values of n and
. Each plot contains
50 values calculated from the numerical solutions to the rate equations for a range of total protein concentrations (xtot
106), for four values of
(
= 102, 103, 104, and 105) at a given value of n (n = 3, 6, or 9). The behavior observed in the test case described above is evident in the plots in Fig. 5. The
50 values (solid circles) are close to the values expected for a classical nucleated polymerization in the low-concentration regime (xtot <<
; solid lines). They deviate from classical behavior in the medium-concentration regime (xtot <
), but still are close to the values expected for a nucleated polymerization after correction for oligomer formation (dashed curves). Finally, the
50 values deviate from both of these approximations in the high-concentration regime (xtot >
), becoming nearly constant at very high concentrations. It is noteworthy that the fastest fibril formation reactions occur when both
and xtot are very large (compare the
50 values at xtot = 106 for the cases in which
= 102 and 105 for any nucleus size). This finding is, perhaps, counterintuitive, because high values of
should result in low nucleus concentrations and slow fibril formation rates. However, fast fibril formation reactions require not only high nucleus concentrations, but also high monomer concentrations (because the rate of fibril nucleation is the product of the concentrations of these two species, and the rate of fibril elongation is proportional to the monomer concentration). As shown in the preceding section, the monomer concentration quickly reaches a plateau value close to 3
/2 in the high-concentration regime. Larger values of
therefore lead to higher monomer concentrations and faster fibril formation.
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| DISCUSSION |
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50 vs. xtot. These plots start as straight lines in the low-concentration regime (protein concentration << supercritical concentration), as expected from the classical picture of nucleated polymerizations. The plots become curved in the medium-concentration regime (protein concentration < supercritical concentration), and eventually become flat lines in the high-concentration regime (protein concentration > supercritical concentration). These findings should be borne in mind when interpreting experimental data from fibril formation reactions; the mechanism shown in Fig. 1 A should not be dismissed only because log-log plots of experimental t50 values versus total protein concentration are found to be curved. In fact, as discussed below, useful information can be extracted from such data.
Connection to experiment
Log-log plots of
50 vs. xtot should be accurately described by Eq. 14 when 1 << xtot <<
and by Eq. 21 when xtot is closer to, but still less than,
. Relationships like those in Eqs. 14 and 21 can be established for the experimentally relevant unrescaled quantities, t50, [X]tot, and Ks:
![]() | (23) |
![]() | (24) |
Good fits of Eqs. 23 and 24 to experimental t50 data that yield physically reasonable estimates of n and Ks are evidence that a fibril formation reaction is a nucleated polymerization, but independent tests are always desirable. Examination of the time course of a fibril formation reaction can provide such a test. Ferrone has shown that the early portion of nucleated polymerization time courses (the first 1020%) are well described by the expression
![]() | (25) |
The effect of variable nucleus sizes
The findings described in the previous sections are most relevant to fibril formation reactions in which the nucleus size is constant, but they also have some relevance to fibril formation reactions in which the nucleus size depends on concentration. As we have argued above, in constant-nucleus-size-models, oligomers become more stable as the concentration increases, which causes log-log plots of
50 vs. xtot to be curved. In variable-nucleus-size models, the nucleus size will change in addition to oligomers becoming more stable as the concentration increases. The curvature in log-log plots of
50 vs. xtot for variable-nucleus-size models therefore should be even more pronounced than it is for constant-nucleus-size models. At very high concentrations, the nucleus ceases to be the highest energy species on the fibril formation pathway in both types of models. Fibril formation reactions will initially behave like irreversible polymerizations when the concentration is well above the supercritical concentration, and t50 values will be independent of the total protein concentration, no matter what type of model is used for nucleation.
| CONCLUSIONS |
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| SUPPLEMENTARY MATERIAL |
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| ACKNOWLEDGEMENTS |
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Submitted on September 1, 2005; accepted for publication March 21, 2006.
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