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* Biozentrum of the University of Basel, Division of Biophysical Chemistry, Basel, Switzerland; and
Åbo Akademi University, Department of Biochemistry and Pharmacy, Turku, Finland
Correspondence: Address reprint requests to Heiko Heerklotz, E-mail: heiko.heerklotz{at}unibas.ch.
| ABSTRACT |
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| INTRODUCTION |
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An assay for studying functions of cho is based on the effects of removing cho from cells (or model membranes) by means of cyclodextrin (cyd). Cyd is a ring-shaped molecule consisting of glucose units (seven units for ß-cyd), which is well soluble in water but contains a hydrophobic cavity that binds (and thus solubilizes) small hydrophobic molecules including cho. Many biological studies have utilized this phenomenon on a semi-empirical basis for extracting cho from cells or (re-)supplying it to them (e.g., 13
,14
). The interpretation of such experiments is, however, complicated by the fact that cho has multiple biochemical and biophysical effects in cells and that cyd interacts also with other membrane constituents, including phospholipids.
Our study pursues two major goals. First, we establish an optimized model describing the partitioning of cho between a cyd solution and a membrane phase and show its importance for avoiding artifacts in cho extraction assays. Second, we are using cyd as a tool to investigate the key thermodynamic parameters of nonideal interactions between cho and phospholipid in the membrane.
Much insight in the membrane effects of cho has been gained from scanning calorimetry and other studies of the phase behavior of lipid-cho mixtures (7
,15
17
). A classical approach to the problem of cho-lipid affinities has been based on measuring the equilibrium distribution of cho between two fractions of vesicles with different lipid composition (18
). This technique may, however, suffer from problems due to slow kinetics of cho transfer and difficulties to separate the two vesicle fractions from each other. One sophisticated solution to this problem was described by Huster et al. (19
), who measured differences in cho-lipid affinities within the same membrane in terms of the NMR cross-relaxation rates between cho and different lipids. NMR served also to determine differential affinities of cho to different lipids expressed in terms of tie lines in ternary phase diagrams (20
). Other authors solved the problem of slow cho exchange kinetics between different lipid vesicles by cyd. Steck and co-workers (21
) used cyd-extraction kinetics to provide additional evidence for a fast transbilayer flip-flop of cho in the red cell membrane. Leventis and Silvius (22
) showed that small amounts of cyd act as a potent catalyst for cho exchange so that, for example, 1 mM cyd speeds up the intervesicle transfer of cho by a factor of
60. Hence, cho can become equilibrated between different glycerolipid vesicles within a few minutes. Given the almost exclusive catalytic role of cyd in this approach, interactions between cyd and cho need not be quantified (see also Silvius' general review (23
)). Niu and Litman (24
) pointed out that problems in separating the two fractions of vesicles can be avoided by studying the different vesicles in separate experiments. They used cyd not as a catalyst but as a means to solubilize substantial amounts of cho. Then, the partitioning of cho between vesicles and cyd (as a common reference state) was measured and quantified in terms of a mole-ratio partition coefficient. Assuming implicitly a 1:1 stoichiometry of cho-cyd complexes, they obtained, e.g., a partition coefficient of 6.7 for cho between cyd and POPC at 37°C. The partitioning of cho between two different lipid membranes is then derived as the ratio between the two lipid-cyd partition coefficients.
Here we establish similar assays measuring the partitioning of cho between cyd and lipid vesicles using isothermal titration calorimetry (ITC). The major advantage of this technique is that it yields the affinity of cho for a lipid species as well as the enthalpic and entropic contribution to the cho-lipid interactionshedding light on the generalized forces governing mixing or demixing in cho-lipid membranes. Furthermore, it is fast and straightforward and does not require the use of labeled compounds. Two protocols are introduced, analogously to the ITC uptake and release protocols for membrane-water partitioning of soluble compounds (25
). The cho-uptake protocol is based on a titration of lipid vesicles into a solution of cyd and cyd-cho complexes. After each injection, some cho is transferred into the membrane. For the cho-release protocol, mixed lipid-cho vesicles are injected into a cyd solution so that part of the membrane-bound cho is extracted by cyd. The data are evaluated in terms of four alternative models, comparing mole-ratio with mole-fraction partition coefficients and allowing for different stoichiometries of the cho·cyd complex. The study gives rise to a comprehensive thermodynamic understanding of the system and to rules to be considered upon application of cyd to membranes. The new protocols can now be applied to vesicles of other lipids.
| THEORY |
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is extremely small and cannot be determined experimentally is no problem, since it does not show up in the final equation relating membrane-bound and cyd-complexed cho with one another.
Membrane-water partitioning
There are many different definitions of membrane-water partition coefficients used in the literature. This is due to the fact that the application of Nernst's partitioning law (26
) for dilute solutions in two macroscopically separate phases (such as octanol/water) can only approximately be applied to substantial contents of additives in microheterogeneous systems such as vesicle suspensions.
The mole fraction partition coefficient,
between bilayer and water (b/w) is constant if the additive mixes ideally with the host lipid (27
),
![]() | (1) |
). The concentration of a dilute aqueous solution is generally
The phospholipid concentration is CL and all lipids are assumed to be in the bilayer.
Many amphiphilic compounds partitioning into membranes can be well described assuming a constant mole ratio partition coefficient,
(28
30
),
![]() | (2) |
corresponds to a characteristic nonideal mixing represented by a decreasing
:
![]() | (3) |
Stoichiometric binding of cho to cyd
For the binding process of cho to cyd, we may write
![]() | (4) |
The equilibrium constant Kcyd/w is given by the mass action law,
![]() | (5) |
stands for the concentration of cho bound to cyd which is equal to the concentration of cho·cydn complexes (assuming that each complex contains one cho molecule), n is the stoichiometry of the complex, and Ccyd is the total cyd concentration. The approximation in the last part of Eq. 5 applies to the case of negligible saturation of the cyd,
which is generally fulfilled in our experiments.
Membrane-cyd partitioning of cho
Relating either Eq. 1 or Eq. 2 with Eq. 5 eliminates
and yields the bilayer/cyd mole fraction partition coefficient,
![]() | (6) |
![]() | (7) |
Assuming n = 1, Eq. 7 becomes equivalent to the model used by Niu and Litman (24
). Substituting
we may solve Eqs. 6 and 7 for the membrane-bound cholesterol concentration,
![]() | (8) |
![]() | (9) |
| MATERIALS AND METHODS |
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100 nm in a Lipex extruder (Northern Lipids, Vancouver, Canada). Extrusion was performed at 50°C. Our results imply in agreement with the literature (31
ITC measurements
ITC experiments were performed on a VP ITC calorimeter from MicroCal (Northampton, MA) (34
,35
). The calorimeter performs a series of injections from a computer-controlled, 300-µL injection syringe into the calorimeter cell (1.4 mL). The temperature of the cell is kept constant by a power compensation feedback. Each injection leads to a peak of the power of the compensation heater, which is integrated to obtain the heat response of the system.
Both uptake and release assays are based on a titration of lipid vesicles (10 mM POPC) into a solution of cyd (2.510 mM). Cholesterol is either included in the titrant (release assay) or in the initial cell content (uptake assay). The cho/cyd ratio was always below 1:20 so that free cyd was in large excess and saturation with cho remained negligible. Mixing after each injection leads to an equilibration of cho between membranes and cyd which, in turn, gives rise to the heat signal.
All solutions were degassed before filling to avoid air bubbles. The typical sequence of injections was 1 x 1 µL, 3 x 5 µL, and
10 x 10 µL. The first injection is subject to larger errors, therefore its volume is chosen very small and its heat is not taken into account upon curve fitting. The three 5-µL injections are performed to increase the resolution in the beginning of the titration, where the heats are largest and vary strongly from one to another.
After each injection, the heat power of reaction was recorded for a sufficient time to ensure that the signal returns to the baseline level. Depending on the kinetics of cho exchange between membrane and cyd, waiting times ranged between 10 min (in particular at 50°C) and 1 h (25°C) giving rise to a total time of
214 h per titration.
The primary data analysis was performed using Origin for ITC (MicroCal) provided with the instrument. Integration of the power peaks after each injection (see Fig. 1, top) from a manually adjusted baseline yields the differential heat response of the system to the injection. These data are normalized with respect to the number of moles of lipid injected. The results of a blank run, i.e., titration of pure lipid into a cyd solution for both protocols, were subtracted from each data set of cho partitioning. The resulting corrected, normalized heats were exported into an Excel spreadsheet for curve fitting.
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Vi changes each concentration by
![]() | (10) |
0) and the displacement of
Vi of cell content (average concentration (Ci + Ci1)/2) out of the completely filled cell. Eq. 10 is based on the assumption that overflown material is no longer in contact with the cell content as recommended by the manufacturer. Solving Eq. 10 for Ci yields
![]() | (11) |
Based on arbitrarily chosen initial values for K (either KR or KX), the table also calculates the corresponding concentration of membrane-bound cho after the ith injection,
(Eqs. 8 or 9), and the corresponding mole fraction of cho in the membrane, Xb(i). The difference between
after and before a given injection,
results from several effects:
![]() | (12) |
is the source of the measured heat.
The absolute heat measured after the ith injection, qi, is linearly related to the mole number of transferred cho, which is obtained from
by multiplication with the cell volume, Vcell, and the molar enthalpy of transfer,
H:
![]() | (13) |
H and
are generally defined for the membrane uptake of cho from cyd. The fact that the sign of the heat, qi, is different for cho release is considered by
becoming negative. Since qi should correspond to experimental data after subtraction of a blank that covers most heats of dilution and other unwanted heat effects, the remaining dilution heat qdil should be very small. However, tests have shown that the precision of the fit parameters is improved by allowing for a small constant qdil to account for imperfections of the blank or of the model (36
Eq. 13 could be used for fitting data, but we prefer using heats that are normalized with respect to the mole number of injected lipid, Qi, yielding (Vcell cancels out)
![]() | (14) |
H, and Qdil by the Excel solver tool to the experimental data. | RESULTS |
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) are obtained after subtraction of those measured in a blank run, injecting cho-free 10 mM POPC into 5 mM cyd. These blank heats presented as the symbol "x" are small and almost constant. Larger, more variable blanks are obtained for experiments utilizing 7.5 mM and in particular 10 mM cyd. Fig. 1 B shows raw data of an uptake experiment injecting 10 mM POPC vesicles into a mixture of 5 mM cyd and 90 µM cho. The injected lipid vesicles take up part of the cho from cho·cydn complexes. As the reverse transfer of the cho release, the accompanying heats must of course be exothermic. The blank is the same as for the release.
The fit curves in Fig. 1 are obtained by a global fit of both uptake and release data using Eq. 14 and correspond to KX = (37 ± 7) mM, n = 2 (set),
H = (16 ± 2) kJ/mol, and small constant heats of dilution Qdil(uptake) = 0.2 kJ/mol and Qdil(release) = 0.16 kJ/mol. The uncertainties are estimated maximum errors. The fit is good, showing that the data are consistent and that the system reaches equilibrium after each injection. Comparing data of many experiments, the data of independent uptake, independent release, and global fits agree often within experimental error. In some cases, there seems to be a trend of independent uptake fits to overestimate K and yield a
H that is somewhat less exothermic than obtained by global and release fits. Separate fits of the two curves in Fig. 1 yield, for example, KX = 41 mM (release) and 49 mM (uptake), and
H = 16 kJ/mol (release) and 11 kJ/mol (uptake).
A global evaluation of the same data based on Eq. 8 and n set to 1 yields similarly good fit curves with KR = 7,
H = 17 kJ/mol, qdil(uptake) = 0.2 kJ/mol, and qdil(release) = 0.5 kJ/mol. The value of KR agrees with the literature (6.7, as published by Niu and Litman (24
)) and
H is in line with the result of the model described above. The data could also be fitted by the models based on KX, n = 1 and on KR, n = 2 (results not shown). The selection of the best model requires a variety of data sets measured under different conditions (see below).
Using KX determined by the fit one can calculate the membrane composition in the calorimeter cell during the titration (Fig. 1 D). In the beginning of the release assay, the membrane-bound cho (Xb = 0.21 in the syringe) is almost fully extracted, but at the end, the injections cause only a reduction to Xb
0.15. Therefore the heat of titration decreases in the course of the titration. In the beginning of the uptake assay, all cho is already in the cell but there is very little POPC yet so that Xb is maximum,
0.2. In the course of the titration, the membrane-bound cho distributes over more vesicles and Xb decreases.
The effect of the cyclodextrin concentration
Cholesterol uptake experiments injecting POPC vesicles into cyd-cho solutions were performed at varying cyd concentrations. Technical constraints limit the applicable cyd concentration in our assays to the range from 2.5 mM through 10 mM. The lower limit is determined by the sensitivity of the calorimeter, because the cho/cyd ratio was always kept below 1:20 (mol/mol) and at least 3050 µM cho are required to obtain a sufficient signal/noise ratio.
The maximum applicable cyd concentration of
10 mM is determined by the requirement to keep factors other than cholesterol transfer negligible. Blank experiments titrating POPC into cyd solutions excluding cho showed small, almost constant heats at cyd concentrations of up to 5 mM but increasing, variable signals at higher cyd concentrations. These blank heats were always subtracted from the experimental data of cholesterol uptake and release experiments, but at >10 mM cyd they were no longer small compared to the experimental signal, thus adding substantial experimental error. The origin of these heat effects at Ccyd > 10 mM probably relate to the binding of PC to cyd (24
,37
), possible minute impurities of the cyd, heats of dilution of the cyd solution by the injection, and others.
The dilution of cyd in the cell by the injection could be avoided (only in the uptake protocol) by including cyd in the syringe. However, a test titrating a POPC dispersion including 7.5 mM cyd into 7.5 mM cyd showed similar heats like the usual blank, injecting cyd-free POPC into 7.5 mM cyd. Test experiments titrating POPC/cyd into cyd/cho yielded consistent but somewhat less reproducible results for K and
H, possibly due to vesicle changes caused by long-term incubation with cyd. We therefore decided to use cyd-free titrants.
Apart from these technical limits for the cyd concentration, the interaction parameters determined by the fit procedure should not depend on the experimental cyd concentration if the model is correct. Both panels of Fig. 2 show the same results of release experiments injecting vesicles including 21 mol % of cho into cyd solutions of 2.5, 5, 7.5, and 10 mM at 50°C. The upper panel shows curves of a good global fit of all data sets based on a stoichiometry of n = 2, KX = 32 mM,
H = 5.0 kJ/mol and individual, small Qdil values ranging from 0.1 to 0.01 kJ/mol. Global fits as shown in Fig. 2 allow also for an additional, free fit of the stoichiometry, yielding values of n = 2.0 ± 0.2 for several data sets. The bottom panel illustrates the best fit that is possible with n set to 1; there is no doubt that the assumption of exclusive cho·cyd (1:1) complexes is inconsistent with these data. Analogous measurements at Xb = 0.1 and 0.3 yield the same result (not shown).
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H are a function of Xb. This appears to be in conflict with our model, which is based on constant values of K and
H. However, previous membrane partitioning studies of surfactants and peptides have shown that ITC data are usually not very sensitive to composition-dependent variations of K or
H (36
H constant) to a nonideal system yields rather good fits with parameters corresponding to an effective membrane composition, Xb, in the beginning of the titration. For example, the shape of the curves in Fig. 1 C is mainly determined by injections inducing changes in Xb from
0.2 to
0 (release) or vice versa (uptake) (Fig. 1 D). The results of both experiments correspond, thus, to an effective Xb of
0.2. It should be noted that a global fit of uptake and release data with substantially different effective Xb would be less consistent.
The fact that Xb changes only moderately during an experiment and the results can be approximately associated with one effective Xb makes the data rather insensitive to composition-dependent phenomena and makes it virtually impossible to derive information regarding nonideal effects from a single run. Imagine, for example, a formation of POPC2·cho complexes of relatively high affinity. Most cho molecules up to Xb
0.33 (and practically all up to Xb = 0.2) would form such complexes so that
H and KX in the experiments shown in Fig. 1 would be constant and provide no clue of complex formation.
Instead of refining the model for evaluating single ITC curves, we have to compare the results of different experiments with different effective Xb if we want to shed light on nonideal, composition-dependent phenomena. We have therefore performed series of uptake and release experiments at varying cho concentrations and evaluated the data using the ideal model. For release experiments, it is straightforward to assign the effective Xb to the known cho content in the titrant. For uptake experiments, we calculated Xb (CL
0) as an estimate (upper limit) of the effective Xb using the KX value obtained by the fit. For global fits of uptake and release data, we chose data sets with a similar effective Xb. A plot of the results as a function of the effective membrane composition is shown in Fig. 3.
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0.3, the composition-dependent variation of the data is smaller than the estimated maximum errors of ±20% for KX and ±2 kJ/mol for
H, indicating that deviations from ideal mixing are relatively small. For higher cho contents, nonideal mixing effects become significant at least for KX (increasing with Xb) and
H (25°C) (becoming less exothermic with increasing Xb).
Temperature dependency
Results obtained at different temperatures are included in Fig. 3.
Fig. 4 shows the corresponding thermodynamic potentials of transfer of cho from cho·cyd2 complexes into POPC-cho vesicles as a function of temperature. The enthalpy changes,
H, were measured directly in the calorimeter; the points displayed in Fig. 4 refer to small cho contents in the membrane (Xb = 0.10.2). The changes in the standard Gibbs free energy,
G0, were calculated from KX according to
![]() | (15) |
G0 would be larger by
7 RT. A linear regression of
H(T) yields a positive heat capacity change of
CP = (0.8 ± 0.1) kJ/(mol K) and a temperature of vanishing
H of 56°C. Above 56°C, the transfer of cho into the membrane becomes endothermic. The
G0 data could, in the frame of the experimental uncertainty, be well described by a temperature-independent value of
G0 = (9.1 ± 0.2) kJ/mol (at least, within 3750°C). From these fit lines, the entropic contribution to
G0, T
S0, was calculated according to
![]() | (16) |
H =
H0. Fig. 4 also includes enthalpic nonideality parameters which are discussed in Nonideal Mixing of POPC and Cho, in the next section.
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| DISCUSSION |
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H:
![]() | (17) |
Hcyd
b,id, corresponds to the transfer of cho from cyd complexes into a hypothetical ideally mixed membrane; it is by definition independent of the membrane composition Xb. The second,
Hnonid(Xb) arises from specific, nonideal interactions between cho and POPC within the bilayer. Generally,
Hnonid = 0 for pure phases which would allow for a direct measurement of
Hcyd
b,id =
H(Xb
1). However, since pure cho forms no fluid bilayers, we have to compute
Hnonid using a model describing the composition-dependence of
H at lower Xb. The limited Xb-range and precision of the data do, unfortunately, not warrant a complex model. We have chosen a statistical model (see next section for a discussion of other possible concepts) with one or two nonideality parameters, yielding for the enthalpy (38
![]() | (18) |
![]() | (19) |
and
denote nonideality parameters of the enthalpy and of the free energy of mixing, respectively. For
and vanishing higher order terms,
i(i > 0) = 0, these equations correspond to the model of regular solutions, describing nonideality in terms of pairwise interactions. For lipid bilayers, we have to consider
since the entropy is not governed by the arrangement of the molecules alone (which is assumed to be random), but includes major contributions from intramolecular degrees of freedom. Higher order terms in
account for nonpairwise, multibody interactions of cooperative units of i + 2 molecules. It should be noted that such multibody interactions are equivalent to stoichiometric complexes of i + 2 molecules (i.e., lipid·cho2, and lipid2·cho in our case) provided the association constant of the complex is weak. Fitting Eqs. 18 and 19 to the data (curves in Fig. 3) allows us to approximately split the enthalpy and KX value of transfer to nonideal membranes into contributions from transfer into hypothetical, ideally mixed membranes (see The effect of acyl chain order on heat capacity, below) and from nonideal mixing of POPC and cho (see below).
Nonideal mixing of POPC and cho
The hypothesis that biological membranes contain lipid rafts, functional domains that are formed by a spontaneous demixing of different lipids in the presence of cholesterol, has led to an enormous interest in the nonideal mixing behavior of cho with phospholipids. In the case of ideal mixing of cho and POPC, the partition coefficients KX and enthalpies of uptake,
H, should be independent of the membrane composition, Xb. Nonideal systems may either show a tendency 1), to demix into different domains if cho-rich environments are favorable; 2), to arrange into superlattices if cho-rich environments are unfavorable; or 3), to form stoichiometric complexes.
Radhakrishnan and McConnell (40
) have found that saturated lipids can form stoichiometric complexes with cho, whereas unsaturated lipids do not. Indeed, our data show no evidence for the formation of high-affinity, cholesterol-rich complexes which should give rise to a drop in KX at a stoichiometric composition Xb
0.5 (41
,42
). Superlattice formation should also give rise to rather sudden drops of KX at specific Xb (43
,44
), which are not observed here. A real phase separation into coexisting liquid-ordered and liquid-disordered phases as reported by de Almeida et al. (45
) should be represented by jumps of
H at the boundaries but constant
H in between. This general behavior was explained in detail for the example of membrane-micelle coexistence (39
,46
) and would apply (qualitatively) analogously to an liquid-ordered/liquid-disordered coexistence. The value KX(Xb) should increase within the coexistence range, since cho affinity would be higher in the liquid-ordered, than in the liquid-disordered, phase. Again, we do not find evidence for such behavior.
Our data show the thermodynamic behavior as discussed for cho-induced chain ordering in a largely randomly mixed membrane. Fitting KX(Xb) excluding higher order terms (all
i = 0 for i > 0) is, within experimental error, compatible with the data but systematic deviations remain (solid lines in Fig. 3). These fits suggest pairwise interactions that are somewhat unfavorable by
at all temperatures investigated. This means that each molecule in a mixture containing 30% cho has, on average, an increased free energy of
1 kJ/mol as a result of unfavorable POPC-cho interactions (excess free energy; see Heerklotz et al. (39
)). Hence, the cost of nonideal mixing is less than, but on the same order of magnitude as, the gain due to the entropy of ideal mixing,
At room temperature, the nonideal interaction is highly exothermic
suggesting that the unfavorable Gibbs free energy is dominated by a large loss in intramolecular entropy. The nonideal interaction causes a strong increase in heat capacity by
(see open square in Fig. 4). The precision and particularly the limited composition range of the data in Fig. 3 do not strictly justify a fit with more adjustable parameters but we have, nevertheless, repeated the fits allowing also for
and
respectively (dotted lines in Fig. 3). These fits yield substantial values for
(4 and 13 kJ/mol at 25 and 50°C, respectively), suggesting slightly unfavorable POPC2·cho units but two- to threefold more unfavorable POPC·cho2 units.
The nonideal behavior observed here (unfavorable but exothermic) has been described to accompany the chain-ordering, membrane condensing effect of cho, since tighter packing and increased order cost entropy but improve enthalpically favorable interactions and conformations. The cooperative, multibody character of this interaction is also illustrated by the umbrella model (31
). This suggests that cholesterol intercalates between lipids without occupying much space in the headgroup region, so that it is screened from water by the headgroups like under an umbrella. The thermodynamic pattern (unfavorable but exothermic) has also been described for the transfer of cho from gel to fluid bilayers, which is also accompanied by chain ordering (47
).
The effect of acyl chain order on heat capacity
A surprising result is the positive heat capacity change. A generally accepted rule relates a positive
CP to either an increase in water-exposed hydrophobic surface area or to a dehydration of polar groups (48
). The intercalation of cho between lipids should, however, reduce the exposure of hydrophobic groups to water (umbrella) and allow for a better hydration of the surrounding lipid headgroups (since the polar group of cho needs very little space). This paradox suggests the hypothesis that the ordering of the lipid chains itself causes a strong increase in heat capacity. This is surprising, taking into account that lipid melting, which is accompanied by a dramatic change in chain order, has virtually no
CP (15
,49
). However, melting is a complex process including many phenomena which are different from gradual changes in order in a fluid membrane. This hypothesis also provides an explanation for the negative
(50
) and anomalously negative values of
CP observed for the membrane uptake of membrane-disordering compounds such as detergents (50
,51
) and alcohols (52
), which could not be explained in terms of the hydrophobic effect alone.
The transfer of cho from cyd into hypothetical, ideally mixed membranes
The fit parameter
Hcyd
b,id excludes specific cho-POPC interactions and allows us to interpret the dissociation of the cho·cyd2 complex and the transfer of cho to a state corresponding to a hypothetic ideally mixed membrane. The standard free energy gain of
(12 ± 1) kJ/mol is essentially of enthalpic nature (
Hcyd
b,id
(11 ± 2) kJ/mol) at 25°C. The entropy change (T
S0 = (1 ± 3) kJ/mol) and the heat capacity change d[
Hcyd
b,id]/dT = (0.1 ± 0.1) kJ/(mol K) are negligible. This means that the transfer of cho between cyd and the membrane is neither promoted nor opposed by the hydrophobic effect. One has, however, to keep in mind that the hydrophobic surface of cyd is fully exposed to water in the absence of cho whereas the membrane anneals after removal of cho and does not expose a free hydrophobic binding site to water. Hence, the screening of cho from water must be better in the membrane to compensate for the accessible hydrophobic surface of free cyd.
The cho·cyd2 complex
The binding of cho to cyd is governed by the hydrophobic effect as discussed in the previous section. That means that cho covers most of the hydrophobic surface area of cyd and vice versa, thus avoiding its exposure to water. Given the molecular dimensions, two stacked cyd molecules seem to be required to largely screen a cho molecule from water, taking into account that a cho molecule is
18 Å long, whereas the cavity of cyd is only
8 Å long.
The section on the effect of the cyclodextrin concentration has indeed provided strong evidence that the cho-cyd interaction can be described much better in terms of the formation of a cho-cyd2 than cho·cyd complex. The comparison of these two most simple cases does, of course, not exclude more complex behavior such as sequential binding leading to a coexistence of cho·cyd, cho·cyd2, and maybe even cho·cyd3 complexes, but cho·cyd2 seems at least to be the dominating species.
The idea that more than one cyd molecule binds one cho is further supported by our observation that a stock solution of 100 mM cyd, 10 mM cho is stable, but dilution to 10 mM cyd, 1 mM cho leads to precipitation. This is very likely due to the formation of aggregates of free cho which are formed when the free cho concentration,
supersedes the solubility limit. The mass action law (Eq. 5) yields (replacing
:
![]() | (20) |
or leaves it unchanged (if Kcyd/w · Ccyd >> 1). An increase in
upon dilution, as suggested by the precipitation, implies a higher stoichiometry, n > 1.
Pointing out that a model based on KX and n = 2 is clearly superior, we note that the conclusions drawn by Niu and Litman (24
) working with KR and n = 1 are not questioned. They have related cho affinities for different lipids to each other that were measured at identical cyd and cho concentrations. Errors appear only if one used their K-values for calculating the cyd-membrane distribution at a different cyd concentration.
The application of cyd to the selective extraction of cho from membranes
Extraction of cho from cell and model membranes by cyd has become a widely used approach to study the function of cho. Our results imply that the cyd concentration used for this purpose must be carefully chosen. Our model parameters (K, n) allow calculating the fraction of cho that remains membrane-bound,
at a given cyd concentration. We calculated curves showing this fraction assuming membranes of 1 and 0.1 mM POPC + cho (30 mol % cho) as shown in Fig. 5.
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in the same range of cyd concentrations on the basis of the results of Anderson et al. (37
![]() | (21) |
Let us, at first, consider a sample of 0.3 mM cho, 0.7 mM POPC (top panel of Fig. 5). At a cyd concentration of 1 mM, the removal of molecules from the membrane is negligible as discussed already by Leventis and Silvius (22
). A cyd concentration of 5 mM extracts 40%, and one of 10 mM removes
75% of the cho from the membrane, without binding significant amounts of phospholipid. The range where
90% of cho but
10% of POPC are extracted (cross-hatched in Fig. 5, top) is quite narrow,
1824 mM cyd. At 40 mM cyd, most of the membrane is destroyed by cyd.
Our calculations suggest two strategies for broadening the applicable range in cyd concentrations in which a substantial extraction of cho is reached without removal of lipid. These are dilution of the membrane system and lower extraction temperature. For example, a 10-fold dilution and extraction at 25°C increases the cross-hatched range to 618 mM cyd (Fig. 5, bottom).
Fig. 5 cannot, of course, specify an optimum cyd concentration window that would be applicable to all membrane systems. For example, preliminary data suggest that sphingomyelin seems to be more susceptible to extraction by cyd but to attenuate the extraction of cho. Hence, the available window of cyd concentrations for selective removal of cho would become even narrower. The discussion of Fig. 5 illustrates, at least, the problem of optimizing the cyd concentration, and provides typical concentrations and optimization strategies that may also be worth trying when biological membranes are concerned.
Another technically important problem is how much time is needed for cho extraction from or cho loading into membranes. We could show that both cho extraction from membranes and cho loading into membranes (of POPC) equilibrate largely within <1 h at 25°C and within a few minutes at 50°C. The observation that the same state is reached by both uptake and release is a strict criterion for equilibration, confirming the suggestion from Niu and Litman (24
), who found that no further uptake is detectable after
1 h.
| CONCLUSIONS |
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CP. Hence, heat capacities of additive partitioning into membranes may deviate markedly from the otherwise well-established rule relating
CP to changes in water-exposed surface area. | ACKNOWLEDGEMENTS |
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Financial support from the Swiss National Science Foundation (grant No. 31-67216.01) and from Prof. Joachim Seelig (Biozentrum Basel) is gratefully acknowledged.
Submitted on March 3, 2005; accepted for publication May 19, 2005.
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