Department of Chemical and Biological Engineering, Tufts
University, Medford, Massachusetts 02155
In this study, we have extended a mathematical model of
microvascular exchange in the renal medulla to elucidate the mechanisms by which plasma proteins are transported between vasa recta and the
interstitium. In contrast with other work, a distinction was made
between the paracellular pathway and the transcellular route (i.e.,
water channels) in descending vasa recta (DVR). Our model first
indicates that concentration polarization on the interstitial side of
vasa recta has a negligible effect on medullary function. Our results
also suggest that, whereas proteins are cleared from the interstitium
by convection, both diffusion and convection play a role in carrying
proteins to the interstitium. In those regions where transcapillary
oncotic pressure gradients favor volume influx through the paracellular
pathway in DVR, diffusion is the only means by which proteins can
penetrate the interstitium. Whether the source of interstitial protein
is DVR or ascending vasa recta depends on medullary depth, vasa recta
permeability to proteins, and vasa recta reflection coefficients to
small solutes and proteins. Finally, our model predicts significant
axial protein gradients in the renal medullary interstitium.
microcirculation; medullary interstitium; urine concentration; mathematical model
 |
INTRODUCTION |
SEVERAL STUDIES HAVE
SHOWN that albumin is present in the medullary interstitium in
significant concentrations (11, 12, 15). The mechanisms by
which this extravascular pool of albumin is generated and maintained
have long remained uncertain. Radiolabeled albumin injected in the
medullary interstitium is rapidly cleared (12), but it is
unclear how. Lymphatics are absent in the inner medulla and sparse in
the outer medulla, and the possibility of clearance of albumin by
drainage via prelymphatic channels is not supported by experimental
evidence (12).
The most likely mechanism is that of protein clearance by the
microcirculation itself. Pallone (14) suggested descending vasa recta (DVR) as the source of interstitial proteins and postulated that accumulation of albumin in the interstitium results from convective transport processes. Because the reflection coefficient of
DVR to albumin is higher than that of ascending vasa recta (AVR), it is
possible in principle to maintain steady fluxes of albumin from DVR
through the interstitium to AVR (12). Wang and Michel
(25) recently developed a model of microvascular exchange
of fluid, plasma proteins, and small solutes among DVR, AVR, and the
medullary interstitial fluid (ISF) to examine this hypothesis. Their
results suggest that convection may indeed be the main mechanism by
which plasma proteins are transported from DVR to AVR via the interstitium.
Their model, however, does not distinguish between two parallel
transport pathways in DVR that differ significantly. The first one
consists of aquaporin-1 (AQP1) water channels, which are present in DVR
only and are impermeable to all solutes; transcellular volume fluxes
across water channels cannot, therefore, carry albumin by solvent drag
into the ISF. The second route, the paracellular pathway, appears to
have a reflection coefficient to small solutes that is close to zero
(16) and to favor water transport from the ISF toward the
lumen in most parts of the medulla (4). In those
regions where the paracellular flux is directed toward the lumen, the
convective transport of albumin from DVR to the interstitium is not
possible, even though there is overall volume efflux from DVR. The
objective of this work was to reexamine the mechanisms of albumin
exchange with a model that accounts for the presence of two separate
transport pathways in DVR as well as for concentration polarization.
We first evaluated albumin concentration differences between the bulk
interstitium and the interstitial side of vasa recta walls (i.e.,
immediately adjacent to the capillaries) to calculate accurately the
driving forces for transcapillary transport. We then used conservation
equations in the interstitium to determine both interstitial protein
concentrations and the processes by which proteins are transported
across vasa recta (i.e., diffusion and/or convection from AVR to DVR or
vice versa). Because the latter mechanisms appear to vary according to
the values of vasa recta permeability to proteins and reflection
coefficient to small solutes and macromolecules, corresponding
parameter sensitivity studies are conducted.
Glossary
| Aim |
Cross-sectional area of inner medulla
|
| Aint |
Cross-sectional area of inner medullary interstitium
|
| AVR |
Ascending vasa recta
|
C , C |
Interstitial albumin concentration in bulk and at the vasa recta wall,
respectively
|
C , C ,
C |
Concentration of solute i in plasma, red blood cells, and
interstitium, respectively
|
Chb, C |
Molar and molal concentrations of hemoglobin in red blood cells,
respectively
|
| D |
Vessel diameter
|
| Di |
Diffusivity of solute i
|
| DVR |
Descending vasa recta
|
| f |
Fractional volume of distribution of urea in red blood cells
|
| fp |
Fraction of capillary surface occcupied by pores
|
| FVR |
Fraction of the inner medullary cross-sectional area occupied by vasa
recta
|
| Hi |
Hydrodynamic hindrance factor for diffusive transport of solute
i
|
| IM |
Inner medulla
|
| INT |
Interstitium
|
| ISF |
Interstitial fluid
|
| Ji |
Paracellular molar flux of solute i across capillaries
|
Jv, J |
Volume fluxes across capillaries and red blood cell membranes,
respectively
|
| Jvp, Jvt |
Paracellular and transcellular volume fluxes across capillaries,
respectively
|
Juc, J |
Carrier-mediated transcapillary molar flux of urea, and molar flux of
urea across red blood cell membranes
|
| l |
Capillary pore length
|
| L |
Length of renal medulla
|
| Lim |
Length of inner medulla
|
| Lp, Lt |
Hydraulic conductivities of paracellular and transcellular pathways,
respectively
|
| LR |
Hydraulic conductivity of red blood cell membrane
|
| N |
Number of vasa recta
|
| Nv |
AVR-to-DVR number ratio
|
| OM |
Outer medulla
|
| P, PI |
Hydraulic pressure in plasma and interstitium, respectively
|
| Pe |
Peclet number
|
| Pi |
Permeability of capillary wall to solute i
|
| Puc, Pur |
Permeability of urea transporter in capillary wall and red blood cell
membrane, respectively
|
| QB |
Blood flow rate
|
| QP |
Plasma flow rate
|
| QR |
Red blood cell flow rate
|
| r |
Radius
|
| rp |
Capillary pore radius
|
| ri |
Radius of solute i
|
| RBC |
Red blood cell
|
| v |
Fluid velocity in interstitium
|
| Xim |
Dimensionless inner medullary coordinate, based on length of inner
medulla
|
| W |
Half-width of slit pore
|
|
Solute distribution coefficient
|
|
Red blood cell-to-vessel surface area ratio
|
i |
Activity coefficient of solute i
|
i |
Oncotic pressure due to solute i
|
i |
Reflection coefficient of the paracellular pathway to solute
i
|
v, Na, u |
Generation rate of volume, sodium, and urea, respectively, per unit
area of interstitium
|
| a |
Albumin
|
| hb |
Hemoglobin
|
| Na |
Sodium
|
| pr |
Plasma protein
|
| ss |
Small solute (sodium and urea)
|
| u |
Urea
|
 |
METHODS |
Mathematical Model
The fundamental assumptions of our model of renal medullary
microvascular transport have been extensively described earlier (4-6). We consider only those vasa recta that are
destined for the inner medulla (IM), i.e., those that lie in the center
of the vascular bundles and do not perfuse the capillary plexus of the
outer medulla (OM). The deposition of NaCl, urea, and water into the IM
interstitium from the loops of Henle and the collecting ducts is
simulated with generation rates that undergo spatial variation within
the IM interstitium. In the vascular bundles, exchanges occur only
between vasa recta and the interstitium, so that generation rates are
taken to be zero. Plasma and red blood cells (RBC) are considered as
two separate compartments. Two transcellular pathways are present in
DVR only: AQP1 water channels and urea transporters.
Conservation and transport equations in vasa recta plasma.
If x is the axial coordinate along the corticomedullary
axis, changes in the plasma flow rate (QP) in DVR and AVR
at steady state are given by the following equation, based on mass
conservation
|
(1)
|
where Jv and
J
are the volume fluxes (per
unit membrane area) across the capillary wall and the RBC membrane,
respectively,
is the cell-to-vessel surface area ratio, N denotes the number of vessels and D their
diameter, and + and
apply to AVR and DVR, respectively.
Jv is the sum of two contributions, the
paracellular (Jvp) and transcellular
(Jvt) volume fluxes, which are given by
|
(2a)
|
|
(2b)
|
where Lp and Lt represent the hydraulic
conductivities of the paracellular and transcellular pathways,
respectively,
P is the transcapillary hydraulic pressure difference,

a and 
pr are the transcapillary
oncotic pressure differences due to albumin and all plasma proteins,
respectively, and
a is the reflection coefficient of the
paracellular pathway to albumin. The plasma and interstitial
concentrations of solute i are denoted by
C
and C
,
respectively;
i is the activity coefficient
of i, and
i is the reflection coefficient of the paracellular pathway to i. Note that
reflection coefficients are taken to be one for the solute-impermeable
transcellular pathway and that Jvt is zero
across AVR, where no AQP1 has been found. The oncotic pressures due to
albumin and all plasma protein are calculated as, respectively
|
(3)
|
where Ca and Cpr are the albumin and
total protein concentration, respectively, in grams per deciliter.
Conservation of solutes to which RBCs are impermeable, such as
sodium, albumin, and other proteins, can be written as
|
(4)
|
where Ji is the (paracellular)
molar flux of solute i (per unit membrane area) from plasma
to interstitium. With the assumption of negligible loss of protein
other than albumin to the interstitium, the flux of nonalbumin protein
is taken to be zero. Conservation of urea, which is exchanged across
the RBC membrane, yields
|
(5)
|
where Ju and Juc
are the paracellular and carrier-mediated transcapillary molar fluxes
of urea, respectively, and J
is the molar
flux of urea across RBCs. The paracellular flux of solute i
(i = sodium, albumin, urea) across capillary walls can be written as (2)
|
(6)
|
where Pi is the permeability of the
vessel to solute i, and the Peclet number, Pe, is a measure
of the importance of convection relative to diffusion. The
carrier-mediated trancapillary and transmembrane fluxes of urea,
respectively, are given by
|
(7)
|
where Puc and Pur
are the permeabilities of the urea transporter in the capillary wall
and in the RBC membrane, respectively, and C
is the
RBC concentration of urea.
Conservation and transport equations in RBCs.
Conservation of mass in RBCs can be expressed as
|
(8)
|
where QR is the RBC flow rate. If we assume that
there is no hydraulic pressure difference across the RBC membrane,
J
is given by
|
(9)
|
where LR is the RBC membrane hydraulic conductivity,
pr and
hb are the oncotic pressures due
to plasma proteins and to hemoglobin in the cells, respectively, and
C
denotes the RBC concentration of solute
i. As described in Edwards and Pallone (5), the
oncotic pressure due to hemoglobin in RBCs is calculated as
|
(10)
|
where Chb and C
are the molar and
molal RBC concentrations of hemoglobin, respectively, and
= 0.75 mg/l is the partial specific volume of hemoglobin.
Conservation of hemoglobin and other nonurea solutes (e.g., potassium,
magnesium, and associated intracellular anions) in RBCs yields
|
(11)
|
The RBC concentration of urea can be obtained on the basis of
the conservation equation
|
(12)
|
where f is the fractional volume of distribution of urea within
RBCs, taken to be 0.86.
Conservation equations in interstitium.
As described in Edwards et al. (4), the deposition of
NaCl, urea, and water into the medullary interstitium from the loops of
Henle and collecting ducts is simulated with generation rates that
undergo spatial variation within the IM interstitium. The interstitial
hydraulic pressure (PI) and small solute concentrations
(C
and C
) are determined by
considering that, at any location along the corticomedullary axis, the
sum of the fluxes from DVR and AVR, weighted according to their
respective surface area, must be equal and opposite to the rate of
generation in the interstitium
|
(13a)
|
|
(13b)
|
|
(13c)
|
where Aint is the cross-sectional area of
the medullary interstitium (in cm2), and
v,
Na, and
u are the local generation rates
of volume, sodium, and urea, respectively, per unit area of
interstitium. The latter three terms are taken to be zero in the OM,
where in the vascular bundles the exchange of water, sodium, and urea
can occur only between vasa recta and interstitium.
The cross-sectional area of the IM interstitium is calculated on the
basis of that of the inner medulla,
Aim(6)
|
(14)
|
where Xim is the dimensionless IM axial
coordinate based on the length of the IM.
Concentration polarization: annular space model.
As water is reabsorbed from the interstitium into AVR, the accumulation
of albumin near the AVR wall on the interstitial side, a phenomenon
known as concentration polarization, reduces the transcapillary oncotic
pressure difference and therefore decreases the driving force for water
reabsorption. Conversely, during volume efflux from DVR, the
concentration of albumin on the interstitial side of the DVR wall will
be lower than that averaged radially over the interstitium; i.e.,
reverse polarization will occur, leading to a decreased rate of fluid
filtration. Polarization (or its reverse) is not expected to be
significant within vasa recta, due to the presence of RBCs, which
create a circulatory flow that homogenizes plasma concentrations
(3).
Transport of fluid and solutes in the interstitium is predominantly in
the radial direction (i.e., normal to the corticomedullary axis); not
only do the orientation and density of lipid-laden IM interstitial
cells appear to hinder axial diffusion (10), but the
length of the renal medulla is about a thousand times the distance
between adjacent vasa recta. In our analysis, interstitial transport in
the axial direction is therefore deemed negligible compared with radial
diffusion and radial convection.
To assess the effects of concentration polarization at a given depth in
the medulla, we used a one-dimensional, cylindrical model of
polarization in the radial direction, following the approach of Lee
(9). The objective was to estimate the albumin
concentration difference between the bulk interstitium and in the
interstitium immediately adjacent to the capillary membrane. With the
assumption that each vas rectum can be represented as a cylinder
embedded in a coaxial, conic interstitium, as shown in Fig.
1, conservation of albumin in the
annular space (i.e., in the interstitium) is written as
|
(15)
|
where Ja, Ca, and
Da are the flux, concentration, and diffusivity
of albumin in the interstitium, respectively, and v is the
fluid velocity. Conservation of water implies that
|
(16)
|
where rA is the radius of the inner
cylinder (i.e., of DVR or AVR) and vA is the
(known) velocity at that boundary. Equations 15 and 16 can be combined to yield
|
(17)
|
Given the bulk interstitial albumin concentration,
C
, the following boundary conditions have to be satisfied
|
(18a)
|
|
(18b)
|
where rB is the outer radius, and
Ja, the (specified) transcapillary flux of
albumin, is constant in the r-direction in the annular space
(see Eq. 15). The differential equation Eq. 17,
coupled with the boundary conditions (Eq. 18, a and
b), has an explicit solution
|
(19)
|
By substituting r = rA
into Eq. 19, the albumin concentration at the vasa recta
wall, C
, can be determined.

View larger version (10K):
[in this window]
[in a new window]
|
Fig. 1.
Idealized representation of vasa recta and interstitium,
used to evaluate the effects of concentration polarization at capillary
walls.
|
|
If diffusion is negligible across the capillary wall, the
transcapillary flux of albumin Ja is directly
proportional to the paracellular water flux (see Eq. 24
below in the limit when Pe
). In AVR where there are no
water channels, the paracellular water flux (per unit membrane area) is
equal to vA, so that
Ja = (1
a) · C
· vA
in that limit and the wall-to-bulk albumin concentration ratio is given
by
|
(20)
|
where
a is the reflection coefficient of vasa
recta to albumin. When water flows from the interstitium toward AVR,
Pea is negative, and the concentration ratio is >1. The
interstitial oncotic pressure at the AVR wall is, therefore, greater
than that which would be calculated based on the bulk interstitial
concentration. Polarization thus reduces the driving force for volume
flux toward AVR, thereby limiting fluid uptake.
In DVR, even when convection is highly dominant,
Ja is not directly proportional to
vA, because there is a transcellular component to the water flux and water channels are impermeable to albumin. Equation 19, with r = rA, cannot therefore be reduced to Eq. 20. It can be shown, however, that C
is less than C
when water flows out of DVR. The reduction in
the interstitial oncotic pressure then serves to limit volume efflux.
Interstitial space size calculations.
Because both the number of AVR and their diameters are greater than
those of DVR, the average distance between the bulk of the interstitium
and the capillary wall (i.e., rB
rA in the model described above) is different
for AVR and DVR. At every depth and for each type of vessel,
rB is approximated using the equation
|
(21)
|
Because we consider only those vasa recta that are destined for
the IM, the number of vasa recta in the OM remains constant. In the IM,
the number of DVR and AVR is given by (4)
|
(22)
|
where FVR, the fraction of the inner medullary
cross-sectional area occupied by vasa recta, and
Nv, the AVR-to-DVR number ratio, are taken to be
constant and equal to 0.3 and 2.25, respectively (26).
With those assumptions,
rB/rA varies between 1.3 at the OM-IM junction and 2.4 at the papillary tip for DVR and between 1.1 and 1.5 at the same boundaries for AVR. (Note that, even though rA is constant and Aint
decreases along the corticomedullary axis, the number N of
vessels decreases more rapidly, which is why the ratio
rB/rA increases.) In the
OM, we assume that rB/rA
remains constant and equal to its value at the OM-IM junction. In
addition, in those simulations of concentration polarization, the
diffusivity of albumin in the interstitium, Da, is
estimated to be ten times smaller than that in water (8).
Albumin interstitial concentration.
In our previous approaches (4, 6), the interstitial
concentration of albumin was taken to be fixed and constant along the
corticomedullary axis. The issue of albumin polarization having been
addressed, the transport of albumin may now be modeled more rigorously.
An interstitial mass conservation equation can be written to determine
the concentration of albumin in the interstitium. If there are no
interstitial sources or sinks of albumin (such as transcytosis,
proteolysis, or lymphatic drainage), the amount of albumin carried from
DVR and AVR should counterbalance
|
(23)
|
where Ja is the transcapillary flux of
albumin. Implicit in Eq. 23 is the assumption that axial
transport in the interstitium is negligible, as discussed earlier. The
albumin flux can be written as
|
(24)
|
where Pe, the Peclet number, is given by Eq. 6. Note
that Eq. 24 includes the interstitial concentration of
albumin immediately adjacent to the capillary wall,
C
, which is related to the bulk interstitial
concentration, C
, as described in Concentration
Polarization. At every depth along the corticomedullary axis, as
flow rates and concentrations in plasma are determined, Eq. 23, which relates albumin concentrations in vasa recta to
C
, is solved to determine interstitial albumin concentrations.
Parameter selection.
Parameter values for our model are given in Table
1. The hydraulic pressure P is assumed to
remain constant in AVR and IMDVR, with fixed values of 7.8 and 9.2 mmHg, respectively. In OMDVR, P is assumed to decrease linearly from 20 to 9.2 mmHg (5). The fraction of the filtered load
recovered by IM vasa recta for water, NaCl, and urea is taken as 1, 1, and 40%, respectively; the filtered load is calculated as described in
Edwards et al. (4), based on the values of
corticomedullary DVR concentrations and whole kidney glomerular
filtration rate (GFR) that are given in Table 1. In the baseline case,
the interstitial area-weighted generation rate of water decreases
linearly between the OM-IM junction and the papillary tip, whereas
those of sodium and urea increase linearly and exponentially,
respectively (4).
Permeability of vasa recta to albumin.
The permeability of AVR to albumin is <10
5 cm/s and is
therefore too low to be measured by present methods (14).
If we assume that the paracellular pathway consists of parallel pores
of uniform size, estimates of pore dimensions can be obtained using
pore theory and other available measurements, and the permeability of
vasa recta to albumin may be calculated using pore theory as well.
Calculations are made for both cylindrical and slit pores.
For cylindrical pores, the (osmotic) reflection coefficient in the
absence of electrical interactions between the solute and pore wall is
given by (2)
|
(25)
|
where rs and rp
are the radii of the solute and pore, respectively, and
is the
distribution coefficient, i.e., the ratio of the average intrapore
concentration to that in bulk solution at equilibrium. The reflection
coefficient of DVR to albumin (rs = 3.5 nm)
has been measured as 0.89 (23), yielding 4.6 nm as the
pore radius. In AVR, where the average value of
a is
~0.70 (12, 14), the pore radius is calculated to be 5.9 nm. Even if there are electrical interactions between the negatively
charged albumin and the endothelial glycocalyx, those values should
represent reasonable order-of-magnitude estimates of
rp.
For slit pores, the osmotic reflection coefficient can be written as
(2)
|
(26)
|
where W, the half-width of the slit, is calculated to
be 3.8 nm in DVR and 4.4 nm in AVR, following the procedure described immediately above.
The permeability Pi of the porous pathway to a
given solute i can be written as
|
(27)
|
where Di is the solute diffusivity in
dilute bulk solution, the coefficient Hi
expresses the hydrodynamic hindrance to diffusive solute transport,
fp is the fraction of capillary surface occupied by pores,
and l is the pore length. The permeability of the
paracellular pathway to urea (or sodium) being known, the permeability
to albumin can then be calculated as
|
(28)
|
where the subscripts a and u refer to albumin and urea
(rs = 0.28 nm), respectively. An expression
for Hi for uncharged solutes in cylindrical
pores is given by Bungay and Brenner (1) as a function of
= rs/rp
|
(29)
|
In slit pores, with
= rs/W, Hi can
be determined as (2)
|
(30)
|
The diffusivity of albumin in dilute bulk solution is calculated
using the Stokes-Einstein equation, yielding 9.3 × 10
7 cm2/s, and that of urea is estimated as
2.0 × 10
5 cm2/s on the basis of the
Wilke-Chang correlation for small solutes (20). In this
manner, the permeability to albumin of DVR and AVR is calculated to be
5.6 × 10
8 and 9.9 × 10
7 cm/s,
respectively, assuming that the pores are cylindrical and 1.3 × 10
6 and 5.4 × 10
6 cm/s, respectively,
in the case of slit pores. A range of parameter values for
Pa must therefore be explored.
Numerical Methods
In the microcirculation, nine variables must be determined along
both DVR and AVR: plasma flow rate, RBC flow rate, albumin plasma
concentration, other protein plasma concentration, sodium plasma
concentration, urea plasma concentration, urea RBC concentration, hemoglobin RBC concentration, and the RBC concentration of other nonurea solutes. Equations 1, 4, 5, 8, 11, and 12
form the corresponding set of ordinary differential equations
(ODEs) that need to be integrated to determine the profiles of these
variables. The initial values in DVR at the corticomedullary junction
are specified (see Table 1). At the papillary tip, i.e., at the
entrance to AVR, DVR and AVR values have to match.
The set of ODEs expressing mass conservation in DVR and AVR is highly
coupled. At each point along the corticomedullary axis, evaluating
fluxes across DVR requires that values in the interstitium and in AVR
be known, and vice versa. However, the ODEs cannot be simply integrated
simultaneously along DVR and AVR, because boundary values for flow
rates and concentrations in AVR at the papillary tip are not known
until differential equations for DVR have been integrated along the
entire axis. Hence, we used the following approach.
An initial guess was made for the profiles in AVR of the nine variables
along the entire corticomedullary axis. The set of ODEs (Eqs. 1,
4, 5, 8, 11, and 12) was then numerically integrated along DVR; at each step along the corticomedullary axis, algebraic equations were solved to determine the interstitial hydraulic pressure
as well as sodium, urea, and albumin interstitial concentrations (Eqs. 13, a-c, and 23). Once papillary tip
values were obtained, the same set of differential equations was
numerically integrated back up along AVR, and AVR flow rates and
concentration values were updated. This process was iterated until the
normalized difference between the current and previous estimates of
each variable in AVR at any x was <10
5. Tests
demonstrating mass conservation are described in the
APPENDIX.
ODEs were integrated along vasa recta by use of Gear's method, which
is a self-adaptive, multistep, predictor-corrector method for stiff
ODEs. At each value of x, the system of three or four nonlinear algebraic equations (Eqs. 13, a-c, and
23) was solved using a modified Powell hybrid method. This
algorithm, which is a variation of Newton's method, uses finite
difference approximations to the Jacobian and avoids large step sizes
or increasing residuals (13). Simulations were performed
on an Alpha PC64 workstation. Convergence was typically achieved in
5 h.
When the effects of concentration polarization are assessed, the
incorporation of Eq. 19 into the simulations of medullary microvascular transport is complicated by the fact that
vA, and hence Pea and
Ja, are themselves functions of
C
through the interstitial oncotic pressure term in
the paracellular and transcellular volume fluxes (Eqs. 2 and 3). At each integration step along DVR and AVR, we
first calculated the volume fluxes on the basis of the bulk
interstitial concentration of albumin. The albumin interstitial
concentration immediately adjacent to the walls was then determined
using Eq. 19, and the volume fluxes were calculated anew on
the basis of this value. The latter two steps were iterated until
convergence was achieved.
 |
RESULTS |
We first examined the extent to which concentration polarization
in the medullary interstitium affects flow rates and concentration profiles in vasa recta; for simplicity, the bulk interstitial concentration of albumin was assumed to be constant and known in those
calculations. We then eliminated that hypothesis and used instead
conservation equations in the interstitium to determine protein
interstitial concentrations and the mechanisms by which proteins are
exchanged between vasa recta and the interstitium. In the absence of
measurements for certain capillary wall permeabilities and reflection
coefficients, parameter sensitivity studies were performed in which a
range of possible values was explored.
Albumin Concentration Polarization
The AVR-to-interstitium albumin concentration difference is a
major determinant of fluid reabsorption into the microcirculation. To
evaluate this driving force, the effects of concentration polarization must be taken into consideration, because polarization significantly reduces the oncotic pressure gradient across AVR walls. We had previously postulated that the accumulation of albumin on the interstitial side of the AVR wall is high enough to eliminate the
oncotic pressure difference due to albumin (4). The more rigorous approach to concentration polarization developed here allowed
us to test this hypothesis as well as to examine the effects of reverse
polarization at DVR walls. During volume efflux from DVR, interstitial
concentrations adjacent to the membrane are smaller than those in the
bulk, thereby increasing oncotic pressure gradients across DVR walls.
Results based on the present model of polarization were compared with
those obtained in two cases: 1) concentration polarization and its reverse are negligible (the "no-polarization" hypothesis); and 2) the accumulation of albumin on the interstitial side
of the AVR wall is so significant that albumin oncotic pressure
differences across that barrier vanish entirely (the
no-AVR-
a hypothesis). The bulk interstitial
concentration of albumin, C
, was kept fixed, either
at 3.4 g/dl, as measured by Pallone (15) or at 1 g/dl, as
reported by MacPhee and Michel (12). To maintain high
osmolalities at the papillary tip, we varied only the spatial distributions of the interstitial area-weighted generation rate of
urea. As described in the previous section, the set of differential equations (Eqs. 1, 4, 5, 8, 11, and 12) was
numerically integrated along vasa recta to obtain flow rates and
concentration profiles in plasma; at each step, the algebraic equations
(Eq. 13, a-c) had to be solved to yield interstitial
values. When polarization is accounted for, the albumin interstitial
concentration at the wall was related to that in the bulk through
Eq. 19. Results are shown in Table
2.
Reverse polarization at the DVR wall increases the transcapillary
albumin oncotic pressure difference, thereby reducing water efflux from
DVR; the rise in sodium and urea concentrations along the
corticomedullary axis is therefore less accentuated. Polarization at
the AVR wall has the same effect: a reduced 
a limits
water influx into AVR and, hence, efflux from DVR, since the
interstitial water balance must be maintained; sodium and urea
concentrations thus remain lower. Consequently, as shown in Table 2,
the osmolality at the papillary tip is always overestimated when
concentration polarization and its reverse are neglected and
systematically underpredicted if 
a across AVR walls
is omitted.
In the former case, however, the error remains small, <2%, and the
lower the C
, the smaller the error, because
differences between interstitial concentrations in the bulk and near
the capillary walls then have less of an effect on oncotic pressure
gradients (see Eqs. 2 and 3). If the assumption that 
a can be neglected across AVR walls is employed
rather than our present approach, the discrepancy can be as high as
15%, suggesting that the no-AVR-
a hypothesis, which
we used previously (4), is an overly simplifying assumption.
Given the uncertainty in model geometry and in parameter values such as
generation rates and albumin permeability, errors on the order of 2%
are not very significant. The annular space model developed here,
although based on an idealized representation of the medulla, therefore
suggests that the effects of concentration polarization in the renal
medulla can be neglected, as they will be in the remainder of this study.
Transport Mechanisms of Plasma Proteins Across Vasa Recta
Paracellular and transcellular volume fluxes.
AQP1 water channels in DVR are impermeable to all solutes
(18). Because small solutes such as sodium and urea are
more concentrated in the medullary interstitium than in DVR, osmotic
pressure gradients drive water from DVR toward the interstitium through
this transcellular pathway (i.e., Jvt > 0). The reflection coefficient to small solutes of the paracellular
pathway (
ss), however, is close or equal to zero
(16), so that osmotic pressure gradients have little to no
effect on Jvp. Transcapillary protein
concentration differences are therefore the dominant driving force
across that route, and water moves in the opposite direction through
the paracellular pathway, i.e., from the interstitium toward DVR
(Eq. 2, a and b).
Shown in Fig. 2 are the paracellular and
transcellular water fluxes across DVR and AVR when albumin interstitial
concentration is specified and with the assumption that
ss is zero. Generation rates are those of the baseline
case, parameter values are given in Table 1, and C
is
fixed at 3.4 g/dl, as measured by Pallone (15). As
illustrated in Fig. 2, the paracellular flux of water across DVR is
positive only near the corticomedullary junction; it is negative, i.e.,
directed toward the capillary lumen, throughout most of the medulla.
With a smaller interstitial albumin concentration, in the range of 1 g/dl as measured by MacPhee and Michel (12), albumin
concentration gradients across DVR walls are even larger, resulting in
more water influx through the paracellular route.

View larger version (15K):
[in this window]
[in a new window]
|
Fig. 2.
Transcapillary volume fluxes across descending (DVR) and
ascending vasa recta (AVR) based on the circumference of all vessels
(i.e., JvN D, as in
Eq. 1), as a function of position along the corticomedullary
axis, x. L represents the total length of the
medulla. The junction between the outer medulla (OM) and the inner
medulla (IM) corresponds to x/L = 0.24. The sharp bends
at this junction are due to anatomical changes and the sudden
reabsorption of water and solutes from the loops of Henle and the
collecting duct in the IM. The interstitial concentration of albumin is
fixed at 3.4 g/dl. The permeability to albumin of DVR
(P ) and AVR
(P ) is taken to be 1 × 10 7 and 1 × 10 6 cm/s, respectively,
and the reflection coefficient of the paracellular pathways to small
solutes ( ss) is zero. Because the paracellular flux of
volume across DVR is directed mostly toward the capillary lumen, it is
unlikely that albumin is carried to the interstitium only by solvent
drag from DVR.
|
|
Because there can be no transport of albumin across AQP1, solvent drag
is effective only across paracellular routes and will therefore carry
albumin away from the interstitium in most of the medulla and toward
both DVR and AVR. Hence, it is unlikely that convective transport can
solely explain the presence of protein in the medullary interstitium.
Transport of albumin and other plasma proteins.
To understand the mechanisms by which albumin appears in the medullary
interstitium, albumin concentration in the ISF was then calculated on
the basis of interstitial mass conservation (Eq. 23) instead
of being specified. The permeability of DVR and AVR to albumin was
initially taken as 1 × 10
7 and 1 × 10
6 cm/s, respectively; we assumed that
ss = 0, and all other parameters were set to their
baseline value (Table 1). The resulting concentration profile is shown
in Fig.
3A.
Transcapillary fluxes of water and albumin are shown in Fig. 3,
B and C, respectively, and Pe values for albumin
are given in Fig. 3D. A positive flux of albumin across DVR
(or AVR) walls indicates that albumin is carried from DVR (or AVR) into
the interstitium, and vice versa. In addition, the greater the absolute
value of Pe, the greater the importance of convection relative to
diffusion.

View larger version (14K):
[in this window]
[in a new window]
|
Fig. 3.
The interstitial concentration of albumin
(C ) is calculated on the basis of an interstitial
balance (Eq. 23), assuming that other plasma protein cannot
be exchanged across vasa recta. The permeability to albumin of DVR and
AVR is taken to be 1 × 10 7 and 1 × 10 6 cm/s, respectively, and ss = 0. Other parameters are those of the baseline case. A: albumin
concentration in DVR, AVR, and interstitium, divided by its initial
value in DVR at the corticomedullary junction. B:
transcapillary volume fluxes across vasa recta, based on the
circumference of all vessels. Note that, in the OM vascular bundles,
the sum of the fluxes is zero. C: transcapillary albumin
fluxes across vasa recta, based on the circumference of all vessels.
Because of mass conservation, the fluxes balance each other.
D: albumin Peclet number (Pe). After the sign change in the
DVR paracellular volume flux near the corticomedullary junction,
albumin enters the interstitium by diffusing out of AVR and is then
carried by convection into DVR.
|
|
Near the corticomedullary junction, water is drawn out of the lumen
through both pathways in DVR; in that region, albumin is carried mainly
by convection out of DVR and into AVR, and the concentration of albumin
increases simultaneously in interstitium and DVR. Below that upper
region, the DVR paracellular flux of water is reversed, and diffusion
out of AVR and convection into DVR account for the presence of albumin
in the interstitium. Indeed, even though there is volume influx into
AVR, the Pe for AVR is small, and diffusion of albumin down its
concentration gradient (i.e., from AVR toward the interstitium)
dominates; solvent drag then carries albumin into DVR, as Fig.
3D suggests.
Before the OM-IM junction, as water reabsorption into AVR decreases,
there is less and less solvent drag into AVR to oppose diffusion out of
AVR, and C
thus rises (right before the boundary,
there is actually some water efflux from AVR, so that both solvent drag
and diffusion carry albumin from AVR into the interstitium). After
the OM-IM junction, conversely, the increase in water influx into AVR
(due to volume generation rate in the interstitium) leads to a decrease
in C
. Toward the papillary tip, water fluxes are much
reduced as the generation rate for water decreases to zero, and
C
increases rapidly again. The volume average
interstitial concentration of albumin is 1.21 g/dl in the entire
medulla and 0.94 g/dl in the IM only.
We have until now assumed that there is negligible efflux of protein
other than albumin from plasma (4, 6), but other investigators (25) do not distinguish between albumin and
other proteins. If vasa recta are also permeable to other plasma
proteins, the interstitial concentration of protein
(C
) is likely to be higher on average. To examine
this hypothesis, we assumed, in the absence of data, that the transport
properties characterizing all plasma proteins (i.e., reflection
coefficient, permeability) were equal to those of albumin, and the
interstitial mass balance for albumin (Eq. 23) was taken to
apply to all proteins. All other parameter values were identical to
those used in the previous simulation. We also confirmed that
concentration polarization is negligible when all plasma proteins, not
just albumin, can be transported to the interstitium.
Results are shown in Fig. 4 (case
A). Variations in C
along the corticomedullary
axis are similar to those in C
when albumin is taken
to be the only plasma protein that can be exchanged across vasa recta,
and the mechanisms by which all proteins are transported to and from the interstitium are also as described above. That is, except near the
corticomedullary junction, proteins diffuse out of AVR and are carried
by solvent drag into DVR. As expected, the volume average interstitial
concentration of protein