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Am J Physiol Renal Physiol 281: F478-F492, 2001;
0363-6127/01 $5.00
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Vol. 281, Issue 3, F478-F492, September 2001

Transport of plasma proteins across vasa recta in the renal medulla

Wensheng Zhang and Aurélie Edwards

Department of Chemical and Biological Engineering, Tufts University, Medford, Massachusetts 02155


    ABSTRACT
TOP
ABSTRACT
INTRODUCTION
METHODS
RESULTS
DISCUSSION
APPENDIX
REFERENCES

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
TOP
ABSTRACT
INTRODUCTION
METHODS
RESULTS
DISCUSSION
APPENDIX
REFERENCES

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<UP><SUB>a</SUB><SUP>I</SUP></UP>, C<UP><SUB>a</SUB><SUP>w</SUP></UP>   Interstitial albumin concentration in bulk and at the vasa recta wall, respectively
C<UP><SUB><IT>i</IT></SUB><SUP>P</SUP></UP>, C<UP><SUB><IT>i</IT></SUB><SUP>R</SUP></UP>, C<UP><SUB><IT>i</IT></SUB><SUP>I</SUP></UP>   Concentration of solute i in plasma, red blood cells, and interstitium, respectively
Chb, C<UP><SUB>hb</SUB><SUP>m</SUP></UP>   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<UP><SUB>v</SUB><SUP>R</SUP></UP>   Volume fluxes across capillaries and red blood cell membranes, respectively
Jvp, Jvt   Paracellular and transcellular volume fluxes across capillaries, respectively
Juc, J<UP><SUB>u</SUB><SUP>R</SUP></UP>   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
 Phi    Solute distribution coefficient
 Gamma    Red blood cell-to-vessel surface area ratio
 gamma i   Activity coefficient of solute i
 Pi i   Oncotic pressure due to solute i
 sigma i   Reflection coefficient of the paracellular pathway to solute i
 psi v, psi Na, psi 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
TOP
ABSTRACT
INTRODUCTION
METHODS
RESULTS
DISCUSSION
APPENDIX
REFERENCES

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
<FR><NU>dQ<SUP>P</SUP></NU><DE>d<IT>x</IT></DE></FR><IT>=</IT>±(<IT>J</IT><SUB>v</SUB><IT>−&Ggr;J</IT><SUP>R</SUP><SUB>v</SUB>)<IT>&pgr;ND+</IT><FENCE><FR><NU>Q<SUP>P</SUP></NU><DE><IT>N</IT></DE></FR></FENCE> <FR><NU>d<IT>N</IT></NU><DE>d<IT>x</IT></DE></FR> (1)
where Jv and J<UP><SUB>v</SUB><SUP>R</SUP></UP> are the volume fluxes (per unit membrane area) across the capillary wall and the RBC membrane, respectively, Gamma  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
J<SUB>vp</SUB><IT>=</IT>L<SUB>p</SUB>[<IT>&Dgr;</IT>P<IT>−&sfgr;</IT><SUB>a</SUB><IT>&Dgr;&Pgr;</IT><SUB>a</SUB><IT>−&Dgr;</IT>(<IT>&Pgr;</IT><SUB>pr</SUB><IT>−&Pgr;</IT><SUB>a</SUB>) (2a)

<IT>−</IT>RT <LIM><OP>∑</OP><LL><IT>i</IT>=sodium, urea</LL></LIM><IT> &sfgr;<SUB>i</SUB>&ggr;<SUB>i</SUB></IT>(C<SUP>P</SUP><SUB><IT>i</IT></SUB><IT>−</IT>C<SUP>I</SUP><SUB><IT>i</IT></SUB>)]

J<SUB>vt</SUB><IT>=</IT>L<SUB>t</SUB>[<IT>&Dgr;</IT>P<IT>−&Dgr;&Pgr;</IT><SUB>a</SUB><IT>−&Dgr;</IT>(<IT>&Pgr;</IT><SUB>pr</SUB><IT>−&Pgr;</IT><SUB>a</SUB>) (2b)

<IT>−</IT>RT <LIM><OP>∑</OP><LL><IT>i</IT>=sodium, urea</LL></LIM><IT> &ggr;</IT><SUB><IT>i</IT></SUB>(C<SUP>P</SUP><SUB><IT>i</IT></SUB><IT>−</IT>C<SUP>I</SUP><SUB><IT>i</IT></SUB>)]
where Lp and Lt represent the hydraulic conductivities of the paracellular and transcellular pathways, respectively, Delta P is the transcapillary hydraulic pressure difference, Delta Pi a and Delta Pi pr are the transcapillary oncotic pressure differences due to albumin and all plasma proteins, respectively, and sigma a is the reflection coefficient of the paracellular pathway to albumin. The plasma and interstitial concentrations of solute i are denoted by C<UP><SUB><IT>i</IT></SUB><SUP>P</SUP></UP> and C<UP><SUB><IT>i</IT></SUB><SUP>I</SUP></UP>, respectively; gamma i is the activity coefficient of i, and sigma 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
&Pgr;<SUB>a</SUB><IT>=</IT>2.8C<SUB>a</SUB><IT>+</IT>0.18C<SUP>2</SUP><SUB>a</SUB><IT>+</IT>0.012C<SUP>3</SUP><SUB>a</SUB>

&Pgr;<SUB>pr</SUB><IT>=</IT>2.1C<SUB>pr</SUB><IT>+</IT>0.16C<SUP>2</SUP><SUB>pr</SUB><IT>+</IT>0.009C<SUP>3</SUP><SUB>pr</SUB> (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
<FR><NU>d(Q<SUP>P</SUP>C<SUP><IT>P</IT></SUP><SUB><IT>i</IT></SUB>)</NU><DE>d<IT>x</IT></DE></FR><IT>=</IT>±<IT>J</IT><SUB><IT>i</IT></SUB><IT>&pgr;ND+</IT><FENCE><FR><NU>Q<SUP>P</SUP>C<SUP>P</SUP><SUB><IT>i</IT></SUB></NU><DE><IT>N</IT></DE></FR></FENCE> <FR><NU>d<IT>N</IT></NU><DE>d<IT>x</IT></DE></FR> (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
<FR><NU>d(Q<SUP>P</SUP>C<SUP>P</SUP><SUB>u</SUB>)</NU><DE>d<IT>x</IT></DE></FR><IT>=</IT>±(<IT>J</IT><SUB>u</SUB><IT>+J</IT><SUB>uc</SUB><IT>−&Ggr;J</IT><SUP>R</SUP><SUB>u</SUB>)<IT>&pgr;ND+</IT><FENCE><FR><NU>Q<SUP>P</SUP>C<SUP>P</SUP><SUB>u</SUB></NU><DE><IT>N</IT></DE></FR></FENCE> <FR><NU>d<IT>N</IT></NU><DE>d<IT>x</IT></DE></FR> (5)
where Ju and Juc are the paracellular and carrier-mediated transcapillary molar fluxes of urea, respectively, and J<UP><SUB>u</SUB><SUP>R</SUP></UP> 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)
J<SUB><IT>i</IT></SUB><IT>=J</IT><SUB>vp</SUB>(1<IT>−&sfgr;</IT><SUB><IT>i</IT></SUB>) <FENCE><FR><NU>C<SUP>P</SUP><SUB><IT>i</IT></SUB><IT>−</IT>C<SUP>I</SUP><SUB><IT>i</IT></SUB><IT> exp</IT>(−Pe)</NU><DE>1<IT>−exp</IT>(−Pe)</DE></FR></FENCE>

Pe<IT>=</IT><FR><NU><IT>J</IT><SUB>vp</SUB>(1<IT>−&sfgr;<SUB>i</SUB></IT>)</NU><DE><IT>P</IT><SUB><IT>i</IT></SUB></DE></FR> (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
J<SUB>uc</SUB><IT>=</IT><IT>P</IT><SUB>uc</SUB>(C<SUP>P</SUP><SUB>u</SUB><IT>−</IT>C<SUP>I</SUP><SUB>u</SUB>)

J<SUP>R</SUP><SUB>u</SUB><IT>=</IT><IT>P</IT><SUB>ur</SUB>(C<SUP>R</SUP><SUB>u</SUB><IT>−</IT>C<SUP>P</SUP><SUB>u</SUB>) (7)
where Puc and Pur are the permeabilities of the urea transporter in the capillary wall and in the RBC membrane, respectively, and C<UP><SUB>u</SUB><SUP>R</SUP></UP> is the RBC concentration of urea.

Conservation and transport equations in RBCs. Conservation of mass in RBCs can be expressed as
<FR><NU>dQ<SUP>R</SUP></NU><DE>d<IT>x</IT></DE></FR><IT>=</IT>±<IT>J</IT><SUP>R</SUP><SUB>v</SUB><IT>&Ggr;&pgr;ND+</IT><FENCE><FR><NU>Q<SUP>R</SUP></NU><DE><IT>N</IT></DE></FR></FENCE> <FR><NU>d<IT>N</IT></NU><DE>d<IT>x</IT></DE></FR> (8)
where QR is the RBC flow rate. If we assume that there is no hydraulic pressure difference across the RBC membrane, J<UP><SUB>v</SUB><SUP>R</SUP></UP> is given by
J<SUP>R</SUP><SUB>v</SUB><IT>=</IT>L<SUB>R</SUB><FENCE><IT>&Pgr;</IT><SUB>pr</SUB><IT>−&Pgr;</IT><SUB>hb</SUB><IT>−</IT>RT <LIM><OP>∑</OP><LL><IT>i</IT>=sodium,</LL></LIM><SUB>  urea, nonurea solutes<SUB>in RBCs</SUB> </SUB><IT>&ggr;<SUB>i</SUB></IT>(C<SUP>R</SUP><SUB><IT>i</IT></SUB><IT>−</IT>C<SUP>P</SUP><SUB><IT>i</IT></SUB>)</FENCE> (9)
where LR is the RBC membrane hydraulic conductivity, Pi pr and Pi hb are the oncotic pressures due to plasma proteins and to hemoglobin in the cells, respectively, and C<UP><SUB><IT>i</IT></SUB><SUP>R</SUP></UP> 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
&Pgr;<SUB>hb</SUB><IT>=</IT>RT[C<SUP>m</SUP><SUB>hb</SUB><IT>+</IT>0.106(C<SUP>m</SUP><SUB>hb</SUB>)<SUP>2</SUP><IT>+</IT>0.020(C<SUP>m</SUP><SUB>hb</SUB>)<SUP>3</SUP>]

C<SUP>m</SUP><SUB>hb</SUB><IT>=</IT><FR><NU>C<SUB>hb</SUB></NU><DE>1<IT>−<A><AC>v</AC><AC>&cjs1171;</AC></A></IT>C<SUB>hb</SUB></DE></FR> (10)
where Chb and C<UP><SUB>hb</SUB><SUP>m</SUP></UP> are the molar and molal RBC concentrations of hemoglobin, respectively, and <A><AC>v</AC><AC>&cjs1171;</AC></A> = 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
<FR><NU>d(Q<SUP>R</SUP>C<SUP>R</SUP><SUB><IT>j</IT></SUB>)</NU><DE>d<IT>x</IT></DE></FR><IT>=</IT><FENCE><FR><NU>Q<SUP>R</SUP>C<SUP>R</SUP><SUB><IT>j</IT></SUB></NU><DE><IT>N</IT></DE></FR></FENCE> <FR><NU>d<IT>N</IT></NU><DE>d<IT>x</IT></DE></FR>

<IT>j</IT><IT>=</IT>hemoglobin, other nonurea solutes (11)
The RBC concentration of urea can be obtained on the basis of the conservation equation
<FR><NU>d(fQ<SUP>R</SUP>C<SUP>R</SUP><SUB>u</SUB>)</NU><DE>d<IT>x</IT></DE></FR><IT>=</IT>±<IT>J</IT><SUP>R</SUP><SUB>u</SUB><IT>&Ggr;&pgr;ND+</IT><FENCE><FR><NU>fQ<SUP>R</SUP>C<SUP>R</SUP><SUB>u</SUB></NU><DE><IT>N</IT></DE></FR></FENCE> <FR><NU>d<IT>N</IT></NU><DE>d<IT>x</IT></DE></FR> (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<UP><SUB>Na</SUB><SUP>I</SUP></UP> and C<UP><SUB>u</SUB><SUP>I</SUP></UP>) 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
[(J<SUB>vp</SUB>(<IT>x</IT>)<IT>+J</IT><SUB>vt</SUB>(<IT>x</IT>))<IT>N</IT>(<IT>x</IT>)<IT>&pgr;D</IT>]<SUB>DVR</SUB><IT>+</IT>[<IT>J</IT><SUB>vp</SUB>(<IT>x</IT>)<IT>N</IT>(<IT>x</IT>)<IT>&pgr;D</IT>]<SUB>AVR</SUB> (13a)

<IT>+A</IT><SUB>int</SUB>(<IT>x</IT>)<IT>&PSgr;<SUB>v</SUB></IT>(<IT>x</IT>)<IT>=</IT>0

[J<SUB>Na</SUB>(<IT>x</IT>)<IT>N</IT>(<IT>x</IT>)<IT>&pgr;D</IT>]<SUB>DVR</SUB><IT>+</IT>[<IT>J</IT><SUB>Na</SUB>(<IT>x</IT>)<IT>N</IT>(<IT>x</IT>)<IT>&pgr;D</IT>]<SUB>AVR</SUB> (13b)

<IT>+A<SUB>int</SUB></IT>(<IT>x</IT>)<IT>&PSgr;</IT><SUB>Na</SUB>(<IT>x</IT>)<IT>=</IT>0

[(J<SUB>u</SUB>(<IT>x</IT>)<IT>+J</IT><SUB>uc</SUB>(<IT>x</IT>))<IT>N</IT>(<IT>x</IT>)<IT>&pgr;D</IT>]<SUB>DVR</SUB><IT>+</IT>[<IT>J</IT><SUB>u</SUB>(<IT>x</IT>)<IT>N</IT>(<IT>x</IT>)<IT>&pgr;D</IT>]<SUB>AVR</SUB> (13c)

<IT>+A<SUB>int</SUB></IT>(<IT>x</IT>)<IT>&PSgr;</IT><SUB>u</SUB>(<IT>x</IT>)<IT>=</IT>0
where Aint is the cross-sectional area of the medullary interstitium (in cm2), and psi v, psi Na, and psi 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)
A<SUB>int</SUB><IT>=</IT>(0.25<IT>X</IT><SUB>im</SUB><IT>+</IT>0.05)<IT>A</IT><SUB>im</SUB>

A<SUB>im</SUB><IT>=</IT>0.175<IT>−</IT>0.3883<IT>X</IT><SUB>im</SUB><IT>+</IT>0.2606<IT>X</IT><SUP>2</SUP><SUB>im</SUB><IT>−</IT>0.04193<IT>X</IT><SUP>3</SUP><SUB>im</SUB> (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
<FR><NU>1</NU><DE>r</DE></FR><FR><NU>∂</NU><DE>∂r</DE></FR>(rJ<SUB>a</SUB>)<IT>=</IT><FR><NU>1</NU><DE><IT>r</IT></DE></FR><FR><NU><IT>∂</IT></NU><DE><IT>∂r</IT></DE></FR> <FENCE><IT>r</IT><FENCE><IT>v</IT>C<SUB>a</SUB><IT>−</IT><FR><NU><IT>D</IT><SUB>a</SUB></NU><DE><IT>r</IT></DE></FR><FR><NU><IT>∂</IT></NU><DE><IT>∂r</IT></DE></FR> (<IT>r</IT>C<SUB>a</SUB>)</FENCE></FENCE><IT>=</IT>0 (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
rv=constant<IT>=r</IT><SUB>A</SUB><IT>v</IT><SUB>A</SUB> (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
<FR><NU>∂<SUP>2</SUP>C<SUB>a</SUB></NU><DE><IT>∂r</IT><SUP>2</SUP></DE></FR><IT>+</IT><FR><NU>1</NU><DE><IT>r</IT></DE></FR> <FENCE>1<IT>−</IT><FR><NU><IT>r</IT><SUB>A</SUB><IT>v</IT><SUB>A</SUB></NU><DE><IT>D</IT><SUB>a</SUB></DE></FR></FENCE> <FR><NU><IT>∂</IT>C<SUB>a</SUB></NU><DE><IT>∂r</IT></DE></FR><IT>=</IT>0 (17)
Given the bulk interstitial albumin concentration, C<UP><SUB>a</SUB><SUP>I</SUP></UP>, the following boundary conditions have to be satisfied
at<IT> r=r</IT><SUB>B</SUB><IT>, </IT>C<SUB>a</SUB><IT>=</IT>C<SUP>I</SUP><SUB>a</SUB> (18a)

at<IT> r=r</IT><SUB>A</SUB><IT>, v</IT>C<SUB>a</SUB><IT>−D</IT><SUB>a</SUB> <FR><NU><IT>∂</IT>C<SUB>a</SUB></NU><DE><IT>∂r</IT></DE></FR><IT>=J</IT><SUB>a</SUB> (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
C<SUB>a</SUB>(<IT>r</IT>)<IT>=</IT>(C<SUP>I</SUP><SUB>a</SUB><IT>−J</IT><SUB>a</SUB><IT>/v</IT><SUB>A</SUB>)<FENCE><FR><NU><IT>r</IT></NU><DE><IT>r</IT><SUB>B</SUB></DE></FR></FENCE><SUP>Pe<SUB>a</SUB></SUP><IT>+J</IT><SUB>a</SUB><IT>/v</IT><SUB>A</SUB>

Pe<SUB>a</SUB><IT>=</IT><FR><NU><IT>r</IT><SUB>A</SUB><IT>v</IT><SUB>A</SUB></NU><DE><IT>D</IT><SUB>a</SUB></DE></FR> (19)
By substituting r = rA into Eq. 19, the albumin concentration at the vasa recta wall, C<UP><SUB>a</SUB><SUP>w</SUP></UP>, can be determined.


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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 right-arrow infinity ). In AVR where there are no water channels, the paracellular water flux (per unit membrane area) is equal to vA, so that Ja = (1 - sigma a) · C<UP><SUB>a</SUB><SUP>w</SUP></UP> · vA in that limit and the wall-to-bulk albumin concentration ratio is given by
<FR><NU>C<SUP>w</SUP><SUB>a</SUB></NU><DE>C<SUP>I</SUP><SUB>a</SUB></DE></FR><IT>=</IT><FR><NU>1</NU><DE>1<IT>+&sfgr;</IT><SUB>a</SUB><FENCE><FENCE><FR><NU><IT>r</IT><SUB>B</SUB></NU><DE><IT>r</IT><SUB>A</SUB></DE></FR></FENCE><SUP>Pe<SUB>a</SUB></SUP><IT>−</IT>1</FENCE></DE></FR> (20)
where sigma 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<UP><SUB>a</SUB><SUP>w</SUP></UP> is less than C<UP><SUB>a</SUB><SUP>I</SUP></UP> 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
N&pgr;r<SUP>2</SUP><SUB>B</SUB><IT>=N&pgr;r</IT><SUP>2</SUP><SUB>A</SUB><IT>+A</IT><SUB>int</SUB> (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)
N<SUB>DVR</SUB>(<IT>x</IT>)<IT>=</IT><FR><NU>F<SUB>VR</SUB><IT>A</IT><SUB>im</SUB>(<IT>x</IT>)</NU><DE>(<IT>D</IT><SUP>2</SUP><SUB>DVR</SUB><IT>+N</IT><SUB>v</SUB><IT>D</IT><SUP>2</SUP><SUB>AVR</SUB>)<IT>&pgr;/</IT>4</DE></FR>

N<SUB>AVR</SUB>(<IT>x</IT>)<IT>=N</IT><SUB>v</SUB><IT>N</IT><SUB>DVR</SUB>(<IT>x</IT>) (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
(J<SUB>a</SUB><IT>N&pgr;D</IT>)<SUB>DVR</SUB><IT>+</IT>(<IT>J</IT><SUB>a</SUB><IT>N&pgr;D</IT>)<SUB>AVR</SUB><IT>=</IT>0 (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
J<SUB>a</SUB><IT>=J</IT><SUB>vp</SUB>(1<IT>−&sfgr;</IT><SUB>a</SUB>)<FENCE><FR><NU>C<SUP>P</SUP><SUB>a</SUB><IT>−</IT>C<SUP>w</SUP><SUB>a</SUB><IT> exp</IT>(−Pe)</NU><DE>1<IT>−exp</IT>(−Pe)</DE></FR></FENCE> (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<UP><SUB>a</SUB><SUP>w</SUP></UP>, which is related to the bulk interstitial concentration, C<UP><SUB>a</SUB><SUP>I</SUP></UP>, 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<UP><SUB>a</SUB><SUP>w</SUP></UP>, 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).

                              
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Table 1.   Parameter values*

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)
&sfgr;=(1−&PHgr;)<SUP>2</SUP>

&PHgr;=(1−r<SUB>s</SUB><IT>/r</IT><SUB>p</SUB>)<SUP>2</SUP> (25)
where rs and rp are the radii of the solute and pore, respectively, and Phi  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 sigma 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)
&sfgr;=1−<FR><NU>3</NU><DE>2</DE></FR>&PHgr;+½&PHgr;<SUP>3</SUP>

&PHgr;=1−r<SUB>s</SUB><IT>/W</IT> (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
P<SUB>i</SUB><IT>=</IT><FR><NU><IT>H</IT><SUB><IT>i</IT></SUB>D<SUB><IT>i</IT></SUB>f<SUB>p</SUB></NU><DE><IT>l</IT></DE></FR> (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
P<SUB>a</SUB><IT>=P</IT><SUB>u</SUB><FENCE><FR><NU><IT>H</IT><SUB>a</SUB></NU><DE><IT>H</IT><SUB>u</SUB></DE></FR></FENCE><FENCE><FR><NU>D<SUB>a</SUB></NU><DE>D<SUB>u</SUB></DE></FR></FENCE> (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 lambda  = rs/rp
H<SUB>i</SUB><IT>=</IT><FR><NU>6<IT>&pgr;</IT>(1<IT>−&lgr;</IT>)<SUP>2</SUP></NU><DE><IT>K</IT><SUB>t</SUB></DE></FR>

K<SUB>t</SUB><IT>=</IT><FR><NU>9</NU><DE>4</DE></FR><IT> &pgr;</IT><SUP>2</SUP><RAD><RCD>2</RCD></RAD>(1<IT>−&lgr;</IT>)<SUP><IT>−</IT><FR><NU>5</NU><DE>2</DE></FR></SUP><FENCE>1<IT>−</IT><FR><NU>73</NU><DE>60</DE></FR> (1<IT>−&lgr;</IT>)<IT>+</IT><FR><NU>77,293</NU><DE>50,400</DE></FR> (1<IT>−&lgr;</IT>)<SUP>2</SUP></FENCE><IT>−</IT>22.5083<IT>−</IT>5.6117<IT>&lgr;</IT><SUP>1</SUP><IT>−</IT>0.3363<IT>&lgr;</IT><SUP>2</SUP> (29)

<IT>−</IT>1.216<IT>&lgr;</IT><SUP>3</SUP><IT>+</IT>1.647<IT>&lgr;</IT><SUP>4</SUP>
In slit pores, with lambda  = rs/W, Hi can be determined as (2)
<IT>H<SUB>i</SUB></IT><IT>=</IT>(1<IT>−&lgr;</IT>)[1<IT>−</IT>1.004<IT>&lgr;+</IT>0.418<IT>&lgr;</IT><SUP>3</SUP><IT>+</IT>0.21<IT>&lgr;</IT><SUP>4</SUP><IT>−</IT>0.169<IT>&lgr;</IT><SUP>5</SUP>] (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<UP><SUB>a</SUB><SUP>w</SUP></UP> 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
TOP
ABSTRACT
INTRODUCTION
METHODS
RESULTS
DISCUSSION
APPENDIX
REFERENCES

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-Delta Pi a hypothesis). The bulk interstitial concentration of albumin, C<UP><SUB>a</SUB><SUP>I</SUP></UP>, 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.

                              
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Table 2.   Effect of concentration polarization on osmolality at the papillary tip

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 Delta Pi 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 Delta Pi a across AVR walls is omitted.

In the former case, however, the error remains small, <2%, and the lower the C<UP><SUB>a</SUB><SUP>I</SUP></UP>, 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 Delta Pi 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-Delta Pi 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 (sigma 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 sigma ss is zero. Generation rates are those of the baseline case, parameter values are given in Table 1, and C<UP><SUB>a</SUB><SUP>I</SUP></UP> 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.


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Fig. 2.   Transcapillary volume fluxes across descending (DVR) and ascending vasa recta (AVR) based on the circumference of all vessels (i.e., JvNpi 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<UP><SUB>pr</SUB><SUP>D</SUP></UP>) and AVR (P<UP><SUB>pr</SUB><SUP>A</SUP></UP>) 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 (sigma 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 sigma 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.


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Fig. 3.   The interstitial concentration of albumin (C<UP><SUB>a</SUB><SUP>I</SUP></UP>) 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 sigma 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<UP><SUB>a</SUB><SUP>I</SUP></UP> 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<UP><SUB>a</SUB><SUP>I</SUP></UP>. Toward the papillary tip, water fluxes are much reduced as the generation rate for water decreases to zero, and C<UP><SUB>a</SUB><SUP>I</SUP></UP> 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<UP><SUB>pr</SUB><SUP>I</SUP></UP>) 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<UP><SUB>pr</SUB><SUP>I</SUP></UP> along the corticomedullary axis are similar to those in C<UP><SUB>a</SUB><SUP>I</SUP></UP> 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