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v
TABLE OF CONTENTS
8.0 OPTIMAL CANNULA DESIGN ........................................................................... 294
8.1 INVESTIGATION OF OBJECTIVE FUNCTIONS DETERMINED
THROUGH FLUID SIMULATION............................................................................... 295
8.1.1 Fluid Dynamic Simulation of a Cannula ................................................ 296
8.1.2 Principal Component Analysis of Objective Functions......................... 299
8.1.2.1 Methods ............................................................................................. 299
8.1.2.2 Results and Discussion ..................................................................... 307
8.1.2.3 Summary ........................................................................................... 312
8.2 SHAPE OPTIMIZATION OF A 2D CANNULA......................................... 312
8.2.1 Methods...................................................................................................... 312
8.2.2 Results and Discussion.............................................................................. 314
8.3 PLATELET MEDIATE THROMBOSIS IN CANNULAE ........................ 320
8.3.1 Cannula Optimization .............................................................................. 320
8.3.1.1 Methods ............................................................................................. 320
8.3.1.2 Results and Discussion ..................................................................... 322
8.3.1.3 Conclusions........................................................................................ 323
8.3.2 Quintessential Ventricular Cannula ....................................................... 324
vi
8.3.2.1 Methods ............................................................................................. 325
8.3.2.2 Results and Discussion ..................................................................... 326
8.4 BIBLIOGRAPHY............................................................................................ 330
vii
LIST OF TABLES
Table 8.1: Optimal parameters and objective function evaluations for the baseline geometry, the
four optimal values, and the anti-optimal values. ....................................................................... 370
viii
ERROR! NO TABLE OF FIGURES ENTRIES FOUND.LIST OF FIGURES
Figure 8.1: The cannulation and anatomical placement of the Streamline VAD. .......................348
Figure 8.2: The geometry of the 2D cannula model showing the control points of the Bezier-
curves and the full range of the walls. Points 1, 4, 5, and 8 were constrained to prevent motion.
Points 2 and 6 were allowed limited horizontal motion. Points 3 and 7 had limited vertical
motion. .........................................................................................................................................349
Figure 8.3: The coarse mesh used for the Cannula CFD study. ..................................................351
Figure 8.4: Mesh convergence diagram for velocity and pressure in the baseline geometry......351
Figure 8.5: The histogram of the element quality for the fine mesh used to simulate flow in the
cannula-CFD study. .....................................................................................................................352
Figure 8.6: Confluence can also be calculated by through observing the velocity and deviation
angles with a small windowed localized about the point of calculation......................................360
Figure 8.7: Comparison of the optimal results when using the mean velocity, a prescribed
velocity field, and the solution to the Stokes flow as predictors of confluence...........................365
Figure 8.8: Statement of the cannula shape optimization problem subject to the geometry in
Figure 8.1. f( apux vvr ,,, ) is the objective function, a is the vector of design parameters, and u and
p are the velocity and pressure predictions from the Navier-Stokes equations. ..........................367
Figure 8.9: Comparison of the final geometry of the four optimal cannula. ...............................370
ix
Figure 8.10: The results of the flow simulation for each of the optimal cannulae. The cannulae
are minimum shear (top left), minimum extension (top right), minimum confluence (bottom left),
and maximum Peclet number (bottom right).. All of the cannula showed a peak velocity at the
outlet of 144 cm/s.........................................................................................................................371
Figure 8.11: Fluid flow through the maximum extension cannula. The contraction results in a
high speed jet, which generates a recirculation region as the domain expands to the exit. .........372
Figure 8.12: The Pareto fronts comparing pairs of the four objective functions: Peclet Number,
Stress, Extension, and Confluence...............................................................................................373
Figure 8.13: Comparison of the MOO optimal cannula, the minimum active platelet cannula, and
the minimum Damkohler cannula................................................................................................377
Figure 8.14: The three traditional geometries for cannulation (Left to Right) the blunt tip, the
beveled tip, and the caged tip. Variations of the cannula tip includes the addition of side ports.379
Figure 8.15: The ventricular geometry used to compare the cannula tips. ..................................380
Figure 8.16: Results depicting the activation of platelets caused by the different cannula tips and
insertion depths. Dark red indicates complete activation of platelets (Color scales not equal)...381
Figure 8.17: Comparison of the flow deviation angle (top) and stagnation area (bottom) for the
cannula insertion study. The color scale for flow deviation in degrees is given in the top right.
Regions of stagnation, i.e. where the velocity less than 5% of the mean inlet velocity, are
indicated by dark red....................................................................................................................382
Figure 8.18: Normalized platelet activation, given by integrating the normalized platelet
concentration over the entire volume of the domain. The baseline value was determined by
integrating the initial activation level (0.05) over the domain.....................................................383
x
Figure 8.19: The formation of a ring thrombus around a standard cannula tip after a PediaFlow
implantation in a sheep. ...............................................................................................................384
xi
ERROR! NO TABLE OF FIGURES ENTRIES FOUND.PREFACE
[It is recommended that acknowledgments, nomenclature used, and similar items should be
included in the Preface.]
[The Preface is optional.]
294
8.0 OPTIMAL CANNULA DESIGN
Cannulae are conduits that connect
two separate regions for the purpose of
transporting a biofluid. Some
examples of cannula include
tracheotomy tubes for feeding
patients, the needles used in blood
donation, and fistula for renal dialysis.
This section focuses on the ventricular
cannula used to connect the apex of
the ventricle to an artificial blood
pump (See Figure 8.1). There are relatively few investigations into the fluid-dynamics of the
ventricular cannula, despite the adverse effects the cannula can have on flow into the blood
pump. It is well known that the flow through curved tubes results in Dean Vortices and the
skewing of the velocity toward the outer-wall of curved tubes. In the collective experience of our
research group, kinks in the cannula tubing and mal-placed insertion into the ventricle can have
deleterious effects on outcomes. The thrombus formed at on the bearing strut of the HMII shown
in Figure 1.2D was initiated by the suck-down of the ventricular wall, which partially obstructed
the flow path resulting in high shear stress and flow disturbances.
Figure 8.1: The cannulation and anatomical placement of the Streamline VAD.
295
8.1 INVESTIGATION OF OBJECTIVE FUNCTIONS DETERMINED
THROUGH FLUID SIMULATION
A multi-objective shape optimization of a cannula flow path was studied in detail in prior
work [1]. The work revolved around four flow parameters, namely Peclet number, shear stress,
extension rate and confluence, which are typically available from numerical fluid packages.
These objectives were calculated by taking
the volume integral of the squared value.
The Peclet Number is an indication of
chemical trauma to blood as it measures
domain washing and clearance of chemical
agonist and active platelets that can
ultimately cause thrombosis. Shear stress is
related to direct mechanical trauma to
blood cells through destruction of the
membrane (hemolysis) or complex
signaling events (SIPA). Confluence is an
indicator of flow perturbations which
results in the transport of cells toward walls and increased residence times. Finally, extension
rate is related to direct mechanical destruction of cells through extensional stresses. The work in
Chapter 5 identified extension rate as an important indicator of blood damage beyond shear
stress. The work reported in Hund[1] was repeated here using a newer, and consequently faster,
version of Femlab and an expanded list of possible parameters.
(x,y)
(x,y) (x,y)
(x,y)(x,y)
(x,y)
(x,y) (x,y)(x,y)
(x,y) (x,y)
(x,y)(x,y)
(x,y)
(x,y) (x,y)
Figure 8.2: The geometry of the 2D cannula model showing the control points of the Bezier-curves and the full range of the walls. Points 1, 4, 5, and 8 were constrained to prevent motion. Points 2 and 6 were allowed limited horizontal motion. Points 3 and 7 had limited vertical motion.
296
8.1.1 Fluid Dynamic Simulation of a Cannula
The cannula design was selected to match the tapered cannula originally selected for use with the
Streamliner VAD. The inlet of the devices had a radius of 0.7 cm and an outlet radius of 0.55 cm
for a resulting area ratio Ao/Ai of 0.617. The cannula was designed to divert flow by a full ninety
degrees from heart to blood pump. The center of the inlet was 4.5 cm above the cannula outlet,
while the centroid of the outlet was 4.3 cm from the inlet, both measured perpendicularly. The
device was designed for a nominal flow rate of 6.0 lpm, although the effect of flow ranges was
also examined to determine off-peak performance.
The ninety degree cannula design was reduced to a 2D problem for four key reasons: 1)
they are much faster than 3D simulation, 2) are more accurate at a given element size 3) have
higher element quality, hence lower numerical error, and 4) have more robust meshing
techniques. Four design parameters were used to describe the shape of the 2D cannula (See
Figure 8.2), where at least 14 parameters were needed to describe the cross-section and
centerline for a 3D cannula. For the sequential quadratic programming (SQP) optimization
technique used here, a single increase in the number of parameters results in the need for
approximately ten times that number in function evaluations due to the finite difference
approximation used for the gradient calculations and line-search algorithms. Finally, the
numerical noise in the 3D simulations was much higher than those of the 2D simulation due to a
coarser mesh for equal degrees of freedom and lower element quality. The noise can result in the
optimizer becoming trapped within local noise minimum or a large gradient approximation
which would slow progress towards a minimum and possibly prohibit finding the global
optimum.
297
The geometry is shown in Figure 8.2.
The sides of the cannula were described by a 3rd
order Bezier curve with weights of 1. The first
and last control points of the curves were
constrained to be the inlet and outlet points for
the cannula. The middle points were constrained
so that the inlet and outlet walls would be
perpendicular to the inlet/outlet surfaces. This
reduced the freedom of motion of the internal
control points to a distance from the inlet or
outlet. An additional non-linear constraint was
placed on the inner wall points to prevent the
geometry from becoming inverted. The constraint prevented the inner wall points from extending
beyond a straight line drawn between the two
free moving outer wall points. Finally, the
free-control points were not allowed to over
lap, i.e. to reduce the line from 3rd order to 2nd
order. This geometry allowed for greater
freedom than previous work by He et. al.[2]
or Abraham et al. [3, 4] despite using less a
third of the design parameters, but showed
reasonable ability to predict channels similar
Figure 8.3: The coarse mesh used for the Cannula CFD study.
Figure 8.4: Mesh convergence diagram for velocity and pressure in the baseline geometry.
298
to those by Gersvirg-Hansen and Haber [5] who used over 2800 design parameters using
topology optimization.
The fluid was assumed to be laminar
with a Reynolds number of 2730 at the inlet,
which is less than the turbulent transition for
blood [6]. The inlet condition was set to be
parabolic with a mean velocity equal to the
average velocity (Q/Ai = 65.0 cm/s) through
the inlet of the Streamliner cannula. The outlet
which extended 3 cm beyond that shown in
Figure 8.2 was set to neutral with pressure set
to 0 at point 5. The walls of the cannula were set to the no-slip velocity conditions. Flow was
simulated using FEMLAB 3.1 using the Navier-Stokes equation, except for one test case using
the MKM viscosity and the generalized Navier-Stokes equations. The geometry was discretized
using a regular-rectangular mesh (See Figure 8.3) The average element quality for the fine mesh,
45 node across the inlet and outlet and 101 nodes along the walls, was 0.63 with a range of 0.53
to .75 (See Figure 8.5).
The accuracy of the simulations was tested using mesh convergence. The simulation did
not reach a grid independent state due to a lack of memory coupled to double digit accuracy of
the flow solver. The L2 norm (Equation 8.13) of velocity showed linear convergence at a rate of
3.5 to 4 which is approximately the theoretical value. The L2 norm of pressure also showed an
estimated convergence rate of 3.5 but was decreased to 2.3 as the mesh became finer. The L2
norm of the differences versus the average element size is shown in Figure 8.4.
Figure 8.5: The histogram of the element quality for the fine mesh used to simulate flow in the cannula-CFD study.
299
8.1.2 Principal Component Analysis of Objective Functions
Principal component analysis is a useful tool from reducing the order of a large subspace, in this
case number of possible objective functions. Although principal component analysis may select
possible objective functions outside of user-feedback, this was avoided because there are
additional mathematical identifiers and user preferences involved in choosing an objective
function. For example, Hund [7] also took into account 1) the first and second variations of
objective function which are directly related to the gradient and Hessian and indirectly to the
convergence of the optimization problem, 2) ease of implementation, and 3) computational time.
8.1.2.1 Methods
The control-points of the Bezier curves were varied parametrically to generate 952 distinct
geometries from a narrow pinch to a bulbous flow path. The range of geometries provided a rich
set of test cases with high and low values of each objective function. The correlation coefficient:
( )ji
jjiiij N
XXXXR
σσ)1()(
−
−−= ∑ , (8.1)
where i and j represent two objective function, X is the value of the objective function for each
design, N is the number of designs, and s is the estimated standard deviation for each objective
function, was calculated for each combination of objective functions. The eigenvalues were
calculated for the correlation matrix and ranked to determine the number of objective properly
selected objective functions were necessary to predict total information of the system.
The objective functions, 109 in total, were broken down into four categories, 1)
mechanical trauma due to shear, 2) mechanical trauma due to extensional flow, 3) chemical
clearance, and 4) flow deviation.
300
Stress is the most common indicator of blood trauma from viscometric studies, but for
more-complex flows stress is a tonsorial quantity. Therefore it is necessary to calculate a norm
that reduces the tensor to a scalar quantity. Four methods are used to such, the first being:
τττ :21
= (8.2)
which is the standard definition by the Society of Rheology [8]. The second is the maximum
principal shear stress calculated from Mohr’s circle, which for 2D flows can be calculated as:
( ) 22 2/ xyyyxxττττ +−= . (8.3)
The third norm is the von Mises stress or octahedral stress modified to be consistent with
viscometric flows:
( ) ( ) ( )( )231
232
2216
1 σσσσσστ −+−+−= , (8.4)
where σ1, σ2, and σ3 are the principal components of the stress tensor [9]. Finally, the Tresca
criterion is:
),,max( 313221 σσσσσστ −−−= . (8.5)
The infinity norm, which is calculated from the maximum absolute matrix element, was not used
in this study. The magnitude of the vorticity, or curl of the velocity vector:
)(ucurl r=ω , (8.6)
and viscous dissipation:
2γη &=VD , (8.7)
have been suggestion as relating to shear induced blood trauma [2, 10, 11]. In other flow
situations, the stress and strain are studied through the invariants of the gradient of velocity
tensor L, the symmetric portion of L, and the skew-symmetric portion of L. First:
301
uL v∇≡ (8.8)
It then follows that:
( )TuuD vv ∇+∇=21 (8.9)
and
[ ]TuuW vv ∇−∇=21 . (8.10)
The first invariant of a matrix is its trace, therefore the 1st invariant of L and D reduce to the
divergence of velocity which is zero for all incompressible fluids. The first invariant of any
skew-symmetric tensor is zero as well. The second invariant of a matrix is the trace of the square
of the matrix, hence:
)(:)( 2XtraceXXXII == . (8.11)
Finally, the third invariant is the determinant of the matrix, which in 2D is:
2)det()( xyyyxx XXXXXIII −== (8.12)
All of these quantities can be evaluated using the norms: 1) L2:
∫Ω
Ω= dxx 22
, (8.13)
the average norm:
Ω= 2
xx
a (8.14)
and the infinity norm:
Ω∨=∞
)max( xx . (8.15)
The most common method for evaluating shear-induced blood trauma is the power-law
model:
302
βατ tAD = . (8.16)
The power-law model was evaluated using several methods: 1) local estimation:
βατ ⎟
⎠⎞
⎜⎝⎛=UhAD , (8.17)
where h is the local element diameter and U is the average velocity over the element, 2) method
of Garon et al. describe by Equations 6.2 – 6.4, 3) full Eulerian simulation (Equations 6.6), and
4) the Lagrangian method. The local estimation was evaluated using the L2, average, and infinity
norms. Lagrangian damage was also calculated using the model of Yeleswarapu et al. from
Equation 582. Sharp has developed a threshold model for blood damage that takes the form:
500,106.0τrest
D = . (8.18)
It is also possible to study sub-lethal blood trauma through the strain energy of the RBC.
Three strain energy models have been used for the simulation of RBCs on a micro-scale: 1)
⎟⎟⎠
⎞⎜⎜⎝
⎛+
+−=1
116 2
1 λλτE , (8.19)
where E is the strain energy, and λ1 and λ2 are the planar deformation of the membrane, 2)
( )22 )1log(5.)12log(1
6+++−= λλλτE , (8.20)
and 3)
⎟⎠
⎞⎜⎝
⎛ +−+=8
)5(.41 2
2121
λλλλτ
CE . (8.21)
The planar strain was estimated using the elongational index fit to the data of Lee et al. [12],
having the form:
( ) )()exp(1 bmAEI +−−= ττ , (8.22)
303
where A, m, and b are the empirical constants 0.0397 dyn-1, 3.64e-4 dyn-1, and 0.508
respectively. Now, if it is assumed that the RBCs have a constant volume, given by the equation:
abcV π43
= , (8.23)
where V is volume, and a, b, c are the radii of the semi-axes. It has been shown for RBCs that the
semi-minor axes are almost equal, therefore:
2
43 acV π= . (8.24)
The elongational index, identical to the Taylor index, is defined as:
cacaEI
+−
≡ . (8.25)
If an aspect ratio is defined as:
caAR = , (8.26)
then the elongational index can be transformed into:
11
+−
=ARAREI , (8.27)
and the aspect ratio can be determined from:
EIEIAR
+−
=11 . (8.28)
Combining the aspect ratio and the volume, the semi-minor axis can be found from:
3
43
ARVc = . (8.29)
The strain approximation are defined as:
micronsa
8.51 =λ , (8.30)
304
and
micronsb
1.22 =λ . (8.31)
Two functions have been used to represent damage caused by pure extension of RBCs,
namely extension rate and acceleration. The magnitude of the acceleration is calculated from:
uuuuaaA vvvvrv ∇⋅∇=⋅= (8.32)
Extensional rate can be calculated in several ways. The simplest is:
sU∂∂
=ε& . (8.33)
Another approximation is to take the square root of the sum of the diagonal components of the
stress tensor squared. An improvement to this method is to rotate the stress tensor into the local
velocity frame and taking the square root of sum of the diagonal components squared. The final
method is to decompose the field into extensional and simple shear. The elongational index and
acceleration were evaluated through the L2, average, and infinity norms.
Flow deviation can be determined through two general methods, confluence and the
inversion of the wall shear stress. The confluence is the angle between the velocity vector of the
simulation and a reference vector:
)vfuf,vf-atan2(uf yxxy +=φ . (8.34)
The reference velocity can be prescribed [7], set to the mean-flow velocity[13-16], set to the
Stokes flow solution, or parallel to the nearest wall location. The Stokes solution can be obtained
for free by setting the initial velocity to the zero vector, thus the first iteration of the non-linear
solver is the Stokes solution. The confluence can also be calculated using windowing function,
namely local evaluations (See). The windowing function calculated confluence at a position x, y
305
through several methods. The first method uses the velocity at x, y as the reference velocity, and
then calculates the deviation as:
∫Ω
Ω= dyxuwyxw )),((),( φφ , (8.35)
where w was 1 within 0.1/π cm of x and y and zero outside or 1 throughout the entire domain.
The second method is to calculate a local mean velocity:
∫
∫
Ω
Ω
Ω
Ω=
wd
duwyxuw
v
v ),( (8.36)
and consequently:
∫Ω
Ω= dyxuwyx ww )),((),( φφ . (8.37)
Finally, the windowed confluence can be calculated through:
( ) windowe within th)),((max),( yxuyxw φφ = . (8.38)
Another method for mathematically quantifying flow reversal is to calculate the wall stress
which reverses sign when flow reverses itself. The wall shear stress, as calculated in Femlab, is
positive in forward flow and negative for reverse flow. Thus the indicator can be calculated as:
∫Γ
Γ<=Γwall
dwallrev )0(τ . (8.39)
The final set of functions is used to predict clearance and flow stagnation. Flow
stagnation, i.e. low velocity, is indicated by either the magnitude of the velocity, the Peclet
Number, or the Damkohler number. In addition, stagnation time is indicated by long residence
times, which can be estimated from:
Uht =exp (8.40)
306
These four indicators were evaluated using the L2, average, and infinity norms. Stagnation can
also be quantified using the stagnation area which can be calculated through:
∫Ω
Ω<= dUUSA ref )( . (8.41)
Another factor in the build up of chemical agonists is the surface-to-volume ratio:
ΩΓ
=VS . (8.42)
Finally, stagnation velocities results in low-wall shear stresses.
Figure 8.6: Confluence can also be calculated by through observing the velocity and deviation angles with a small windowed localized about the point of calculation.
307
8.1.2.2 Results and Discussion
The PCA showed that four objective functions represent 93.1% of the information that can be
calculated from the full set of objective function, where seven objective functions are required to
predict over 99% of the information. The functions in the class of clearance were anti-correlated
(R ranging from -0.4 to -0.23) with functions representing extensional deformation. Since there
were no strong anti-correlations (<-0.8), multi-objective optimization can be effectively
employed to find a compromise between opposing functions. The average and L2 norm were
well correlated with each other (R > 0.92) and correlated to the infinity norm (R > 0.87). The
infinity norm is not ideal for optimization because it only reflects a single point in the flow,
hence may produce designs that are sub-optimal. The infinity norm may also produce a
discontinuous objective function if the variation of the parameter causes the maximum value to
jump from one spatial location to another. The L2 and averaging norm show similar behaviors,
yet may bias the results. Since the L2 norm ignores area, it could be biased toward designs with
small area, and conversely the average norm is biased toward designs with higher areas. The
underlying problem should be well understood before selecting particular norm to reduce area
artifacts.
The various methods for calculating shear stress, viscous dissipation, the second
invariants of L, W, and D, and vorticity were all highly correlated (R > 0.999), despite varying
mathematical forms. This agrees with the work of Garon et al. who showed that blood damage
prediction using power-law models were not greatly altered by choice of norm [17]. Of the
various norms for reducing the tensor to a scalar, the one in Equation 10.2, has the greatest utility
because it is directly calculated from the components of the stress tensor. The principal stress,
the modified octahedral stress or von Mises stress, and Tresca criterion all rely on principal stress
308
values which require the determination of the eigenvalues of the stress tensor for 3D flows. The
calculation must be done for every node and can quickly become costly. As expected, the
invariants of L, D, and W were also well correlated with the stresses. The 2nd invariant of D is
proportional to the stress norm given by Equation 10.2. Vorticity also correlates well with the
shear stress, despite the different mathematical forms. It is difficult to explain shear induced
blood damage through vorticity. For example, pure solid body rotation shows a vorticity of half
the rotational speed but in this case RBCs would not deform and consequently be exposed to
damage. One possible reason for the correlation is that near walls vorticity can be approximated
by:
tu
nu nt
∂∂
−∂∂
=ω , (8.43)
and stress as:
tu
nu nt
∂∂
+∂∂
=ητ , (8.44)
where ut is the velocity tangential to the wall, un is the velocity normal to the wall, t is the
coordinate along the wall, and n is the coordinate perpendicular to the wall. Two consequences
of no-slip conditions are that the normal velocity is small and does not change considerably
along the tangential direction; hence both vorticity and stress are dominated by the derivative of
the tangential velocity in the normal direction. Another contraindication for the use of vorticity is
that the curl of the velocity vector is not frame invariant. The norm of stress given in 10.2 and
viscous dissipation (Equation 10.7) have desirable mathematical qualities and can readily be
calculated from the flow information. Viscous dissipation has the further advantage that most
turbulent models provide the energy dissipation, where an acceptable surrogate for the turbulent
stress has not been found.
309
The shear stresses were weakly correlated (R > 0.78) to the various damage models
irregardless of method of calculation, the 3rd invariants of L, W, and D, the elongational index,
and the strain energy equations. For the damage models, the reduced correlation was caused by
the value of α resulting in the Giersiepen model having a correlation of 0.97 and the PSF had a
correlation of 0.8 when compared to the norm of stress squared. The Richardson model, also
involving stress squared had a correlation coefficient of 0.999. Garon et al. [17] showed that the
accumulation of damage was approximately equation to the integral of the source term
(Equations 5.2 and 5.3) which is almost identical to the L2 norm of the scalar stress. In
optimization, it can be shown that for a quantity that is greater than zero over for the entire
domain the optimal value is the same irregardless of the power. Hence, the minimization of
hemolysis or SIPA can be done by simply minimizing the stress using the L2 norm. It should
also be noted that computers use approximate solutions when dealing with non-integer powers,
hence there is a higher numerical error when using the Giersiepen or Antaki coefficients. The
method for calculating blood damage also affected the correlation with shear stress, with the
Lagrangian method having the lowest correlations (0.78) and the method of Garon having the
highest (>0.999). This, combined with the additional time required to calculate the path-lines,
indicates that the Eulerian method would be preferred in this case. The 3rd invariants were also
weakly correlated with shear stress, but there have been no studies to date that implicate the 3rd
invariant in blood damage. The elongational index and strain energy calculations enrich the
objective function space, but required numerous assumptions and approximations, and hence are
not as accurate as the calculation of shear stress or dissipation.
The class of functions for extension were well correlated (R>0.9) with the stress group.
Of the various methods for determining extension rate, Equation 10.33 was the most accurate
310
outside of flow decomposition. Pressure gradient was another likely surrogate from this class (R
> 0.999) of functions and is far simpler to calculate than extension rate. The elongation index
was not well correlated with the extension rate (Equation 10.33, R = 0.913), but it should be
understood that cell elongation or extension is not the same as flow extension rate. Experiments
in simple shear cases, such as Couette and Poiseuille flow, show cell elongation despite no fluid
extension. Conversely, Lee et al. [18] showed that the elongation index is greater in extensional
flow than in simple shear flow.
Confluence and negative wall shear stress were well correlated (> .98). The various
methods for calculating confluence were highly correlated (>0.999). Figure 8.7 shows the
optimal cannula using each method to prescribe the desired flow field. The easiest method to
implement mathematically is that which prescribes desired velocity field. This method is
practical when the flow field is simple, such as the cannula used here, but may not be practical
for more complex flow situations such as ventricular assist device and dialysis machines. Also,
the optimal solution may be biased toward the prescribed flow field as shown in Figure 8.7. The
Figure 8.7: Comparison of the optimal results when using the mean velocity, a prescribed velocity field, and the solution to the Stokes flow as predictors of confluence.
311
use of the Stokes solution can be applied to any flow domain, but may require an additional
simulation, particularly when using CFD software, such as ADINA, CFX, or FLUENT, that use
the SIMPLE solver and alternate between pressure and velocity solves. For more general solver,
the Stokes solution can be obtained for “free” by setting the initial condition for velocity to zero,
thus obtaining the Stokes solution on the first iteration of the non-linear solver. However, the
non-linear solver may not converge from this initial condition, particularly in highly non-linear
flow situations. The mean velocity is readily obtained during post processing, but may
unnecessarily bias the flow as seen in Figure 8.7. Three optimal solutions were obtained for flow
deviation each avoiding recirculation. However, the optimal result was drastically different when
the reference velocity is the mean velocity in the domain as compared to the other two methods.
The window functions were correlated with the confluence methods (>0.72) but required
considerable computational time, 35.1 minutes or 7.44 times the clock time for the simulation.
When the using the window to determine the local mean had a higher correlation than the
windowed function that did all calculations locally (0.999 vs. 0.72). The difference in
performance of these functions can be attributed to the fact that the second set (R < 0.8) only
picked up the boundary between the recirculating and forward flow region. The windowed
functions produced the same optimal cannula as that using the mean velocity.
The clearance variables were also strongly correlated with each other (R= 0.999). The
magnitude of velocity and Peclet number are directly related, particularly when using a constant
diffusivity. The Damkohler Number gave the best physical representation of chemically induced
blood trauma, but required an additional simulation to estimate the reaction rate for platelet
activation. The residence time is another physically tangible estimator that is difficult to
calculate. The method described in 10.40 depends on the size of the mesh and works best when
312
the mesh is topologically consistent. Another method, required and additional simulation of the
convection-diffusion equation (Equation 4.10) with S = 1, could produce results that are mesh
independent but would require an additional simulation. Stagnation area is determined from an
arbitrary threshold value which is undesirable. It also penalized the near wall layer where the
velocity is low due to the wall.
8.1.2.3 Summary
Various objective functions were analyzed within a four class framework, stress,
extension, recirculation, and clearance. It was determined that the best indicator of stress is either
the norm of the stress tensor (Equation 10.2) or viscous dissipation (Equation 10.7). The best
indicator of extension rate was found to be the pressure gradient. The best indicator of flow
deviation is confluence as indicated by the Stokes flow. The best indicator of clearance is either
the magnitude of velocity or Peclet number.
8.2 SHAPE OPTIMIZATION OF A 2D CANNULA
8.2.1 Methods
The statement of the optimization problem is in Figure 8.8. The optimal design was determine
using the SQP method built into the fmincon function available through the MATLAB
optimization toolbox. This method, a gradient based approach, was chosen over gradient-free
methods (GFM) such as genetic algorithms or ant-hill models for several reasons. The GFM
methods require a large number of iterations compared to the expected number for a gradient
313
outlet andinlet thelar toperpendicu are wallscannula that thesoyrepectivel xand ,y , x,y todconstraine are xand ,y , x,y and
geometry VAD theand sconstraint anatomicalby fixed are y and , x,y , x,y , x,y , xwhere
solution a toEquations Stokes-Navier theof econvergenc :2geometry inverted none i.e. geometry, valida :1
:of tsrequiremennolinear with
:by boundEquations StokesNavier
:subject to],,,[:respect towith
),,,(min
85417632
88554411
7632
highlow aaa
yxyxaapuxf
vvv
v
vvr
≤≤−
=
Figure 8.8: Statement of the cannula shape optimization problem subject to the geometry in Figure 8.1. f( apux vvr ,,, ) is the objective function, a is the vector of design parameters, and u and p are the velocity and pressure predictions from the Navier-Stokes equations.
based method. Secondly, all of the shape
parameters are continuous and would
have to be discretized for the GFM. The
derivatives were calculated using the
finite difference approach while the
Hessian was approximated using the
BFGS method proposed independently
by Broyden [19], Fletcher [20], Goldfarb
[21], and Shanno [22] to guarantee that
it remained positive definite and led to
the minimum. The finite difference method was used to calculate the derivatives as other
methods, such as the adjoined method, require information on the variation of the mesh with
respect to the design variables. The BFGS method was used to update the Hessian matrix
because it only requires the gradient approximations and will remain positive definite if the
initial guess, here the identity matrix, is positive definite. A positive definite Hessian guarantees
that the optimization routine will converge to a solution and is indicative of a rapid solution. The
line search algorithm used a quadratic/cubic approximation to determine the step size. The
optimal point was validated from 5 different design starting points to ensure convergence to the
global optimum and not a local optima. This was also compared to the study of the optimal field
done in Hund [1]. The objective functions were normalized using the method suggested by Koski
[23, 24] to remove the effect of variance and magnitude for multi-objective optimization. In
essence they were normalized so that the optimal point was 0 and the worst case scenario became
314
1. The Pareto optimal front was calculated for various pairs of objective functions by determine
the optimal values for the objective:
jiijobj FaFF )1( −+= α , (8.45)
and varying the parameter alpha from 0 to 1. The clock-time of the Pareto calculation was
decreased by starting the optimization run using the initial condition of the previous alpha value.
The unbiased MOO function was simply the sum of the four transformed objectives:
)( extensionshearConfluencePecletMOO FFFFF +++= β , (8.46)
where the penalty coefficient β was set to 0.1. The unbiased approach gives use a design that
minimizes the total percent deviation of all objectives from their optimal point. This method
allows for a single optimal design to be determined without direct intervention of an engineer;
however the Pareto front can provide greater information that the engineer can use to determine
the best design choice.
8.2.2 Results and Discussion
The choice of objective was found to drastically affect the optimal design. Figure 8.9 shows an
over-lay view of the four optimal geometries. Table 8.1 quantifies the optimal parameters and
evaluates the various objective functions in each of the optimal cannulae. The minimum shear
stress (optimal) and Peclet number cannula (non-optimal) and the maximum confluence cannula
(non-optimal) were identical. None of the optimal, meaning highest quality, cannulae were the
same. The design improvement was evaluated through the use of an optimality index (OI),
computed as the percent difference from the baseline (one of the initial conditions for the
optimization algorithm):
315
%100base
baseopt
ObjObjObj
OI−
= . (10.47)
The optimal stress cannula showed reduced the shear stress 81.1% over the baseline value, and
also improved in extension rate of 48.0%. Confluence and Peclet number deteriorated by 941%
and 11.0% respectively. The optimal extension cannula reduced the extension rate by 48.4% and
the shear stress by 46.2%, with an increase in confluence of 700% and a decrease in clearance of
10.5%. The optimal confluence cannula improved confluence, shear stress, and extension rate by
99.8%, 29.2%, and 16.7% respectively, while decreasing clearance by 7.67%. The optimal
clearance cannula (Peclet number) improved the clearance, stress, and extension by 0.162%,
3.33%, and 13.7% respectively, but worsened confluence by 47.2%. The objective function for
the worst-case stress cannula was 1,500 times that of the optimal design. The objective function
for the maximum extension rate cannula was 2,860 times the optimal value. The cannula
exhibiting the highest recirculation had a
confluence of 5,030 times the optimal
cannula. Finally, the optimal clearance
cannula was only 12.8% higher than the
anti-optimal cannula.
Figure 8.9: Comparison of the final geometry of the four optimal cannula.
316
The optimal confluence was the only cannula that did not exhibit recirculation. (See
Figure 8.10). The optimal stress and extension cannulae presented large recirculating regions on
the inner wall and a smaller recirculation region on the outer wall. The optimal clearance cannula
resulted in a small recirculation region on the outer wall.
Optimization
was able to improve
each design when
compared to the initial
design. The greatest
improvement was seen
in confluence where the
optimal results were
0.2% of the baseline
value. The design was
least sensitive to Peclet
number with an overall
Figure 8.10: The results of the flow simulation for each of the optimal cannulae. The cannulae are minimum shear (top left), minimum extension (top right), minimum confluence (bottom left), and maximum Peclet number (bottom right).. All of the cannula showed a peak velocity at the outlet of 144 cm/s.
Table 8.1: Optimal parameters and objective function evaluations for the baseline geometry, the four optimal values, and the anti-optimal values.
Objective X1 Y1 X2 Y2 Stress Extension Confluence Pe #(cm) (cm) (cm) (cm) (dyn2/cm2) (cm2/s2) (cm2deg2) (cm2)
Baseline 3 3 4 4 1231 84,100 9,170 99,000
Stress 0.275 0.35 4.03 4.15 233 43,700 95,500 88,300Extension 1.7 0.35 4.03 4.15 662 43,400 73,300 88,600Confluence 2.35 1.76 2.43 3.54 871 70,100 19 91,400Peclet Number 2.91 3.03 4.03 4.15 1190 72,600 13,500 99,600
Max Shear 3.6 3.6 2.2 2.25 3.50E+05 4.21E+07 26,700 97,700Max Extension 1.75 1.76 0.7 0.55 57,000 1.24E+08 16,200 97,300Max Confluence 0.275 0.383 4.03 4.15 233 43,700 95,500 88,300Min Peclet 0.275 0.383 4.03 4.15 233 43,700 95,500 88,300
Optimal Parameters Function Evaluation
317
variability of 1.12%, where the other three objectives offered improvements of three orders of
magnitude. Clearance was a weak indicator of recirculation, as shown in Figure 8.11 where a
sufficient recirculation area counteracts the high velocity jet. However, clearance is not as
effective of an indicator of recirculation as confluence.
One might be inclined to select the optimal confluence cannula as the best design since it
successfully reduced recirculation, shear, and extension rate with minimum impact on the
clearance when compared to the base-line model. However, this is dependent on the choice of
initial design and may vary depending on that choice. Therefore, biocompatibility has numerous
facets and lends itself to multi-objective optimization (MOO). MOO optimization offers tools to
assist the designer in determining the best overall design. Figure 8.12 shows six Pareto fronts
showing the trade-offs between the various objective functions. All of the fronts are either
strongly linear or concave up, indicating that a compromise can be reached irregardless of the
chosen objective functions. The Pareto fronts also indicate that the stress and extension rate more
susceptible to trade-offs, meaning Peclet
number and confluence can be improved
by a large amount, without a large increase
in stress or extension.
Another approach to multi objective
optimization is to weight each objective
function and thus obtaining a single
optimal design. Two methods were used
here: 1) an unbiased optimization and 2) a
biased optimization. The unbiased
Figure 8.11: Fluid flow through the maximum extension cannula. The contraction results in a high speed jet, which generates a recirculation region as the domain expands to the exit.
318
Figure 8.12: The Pareto fronts comparing pairs of the four objective functions: Peclet Number, Stress, Extension, and Confluence.
319
optimization treats all weights as one and therefore minimizes the percent error. Since
mechanical blood trauma is low in a cannula, shear stress and extension rate, are weighted
(b=0.1) as a penalty function. The optimal results for the multi-objective cannula are shown in
Figure 8.13. There may be considerable error in the simulation when the domain contracts to a
small cross-sectional area, as seen in Figure 8.11. The fluid is rapidly accelerated as the area
decreases, hence increasing the flow velocity by a factor of 7.55 over the mean inlet velocity.
The Reynolds number increases to 4,400 indicative of a transition to a turbulent jet. The effect of
this error on an individual simulation is large, but since the optimal results remain within the
non-turbulent regime, this error can be neglected.
It should also be acknowledged that the 2D simulation misses several key flow features
observed in thee-dimensional flow through curved tubes. Several of these features, including
Dean vortices and a skewing of the velocity profile, require the full 3D geometry in order to
predict. The cannula evaluation here is primarily aimed and better understanding the
performance of various objective function and not at producing a functional device for real world
applications; therefore these effects are of secondary concern.
There are no guarantees that the optimal results are a global optimal although the initial
geometry was varied several times for each objective function. Future work should involve
global optimization routines such as genetic algorithms, pattern search, and simulated annealing.
It should also be acknowledged that this work only examined two methods for performing
multi-objective optimization and is far from complete in this analysis. Marler and Arora [25], in
their review on MOO, include two additional methods for normalizing the individual objective
functions and additional methods for optimization. The method used here falls into the class of
weighted sums with a priori statement of preference. Other methods that involve a priori
320
statement of preference include the lexicographical method with a ranked preference, the
weighted Tchebycheff method, exponential weighted sums which improve the calculation of
Pareto front, and product weighting. There are also methods for determining preference a
posteriori or without stating preference.
8.3 PLATELET MEDIATE THROMBOSIS IN CANNULAE
Despite the uncertainty in surface reactivities and RBC-induced migration, the platelet mediated
thrombosis model provides more information toward defining a biocompatible device than fluid
dynamic parameters alone. For example, the platelet activation model can elegantly combine
SIPA with chemically induced activation. In section 8.2, these two factors were taken into
account through minimizing shear stress and maximizing Peclet number, but can be uniquely
determined through kpa. Furthermore, platelet activation occurs based on a threshold which
indicates that shear stresses does not necessarily be minimized but only reduced to a level
sufficiently below that which could cause activation. In order to investigate the effectiveness of
the platelet model in predicting biocompatibility, the model was incorporated into the design of
both the 2D cannula presented in sections 8.1 and 8.2.
8.3.1 Cannula Optimization
8.3.1.1 Methods
The cannula simulation, described in detail in section 8.1.2.1 and 8.2.1, was augmented
with the platelet mediated thrombosis model described in Chapter 4. Since the reaction rates, krs,
321
kas, and kaa have yet to be calibrated to materials used in cannula the effects of platelet
deposition was neglected. The reactive wall conditions were replaced by zero flux conditions.
Since the scale of the model is much higher than the scales at which RBC induced margination is
significant, hematocrit was assumed to be uniform through-out the domain. Furthermore, platelet
activation was assumed to have reached steady-state since ventricular cannulae are long-term
devices. Several objective functions were used for the optimization of the cannula: 1) the
effluence of active platelets:
∫Γ
Γ⋅= dAPunF ][ˆ v , (8.48)
2) the rate of activation:
∫Ω
Ω= dkF pa , (8.49)
3) the area of activation:
( )∫Ω
Ω≥= dkpaF 1 , (8.50)
4) the production of TAT:
∫Γ
Γ= dPTF ][ , (8.51)
5) the accumulation of agonists:
∫ ∑Ω
Ω⎟⎟⎠
⎞⎜⎜⎝
⎛= d
AgonistAgonistF
N *, (8.52)
6) active platelets:
∫Ω
Ω= dAPF 2][ , (8.53)
and 7) Damkohler number:
322
MOO OptimalMinimum APMinimum Damkohler Number
MOO OptimalMinimum APMinimum Damkohler Number
Figure 8.13: Comparison of the MOO optimal cannula, the minimum active platelet cannula, and the minimum Damkohler cannula.
Ω⋅++
= ∫Ω
dRuu
kRF
inrbcb
pain
22
2
)( vvκκ. (8.54)
To further investigate the relationship between the functions estimated by the model and the
parameters obtained through fluid flow simulations, a design-space study similar to 8.1 was
performed. Since the thrombus model requires more computational time (a factor of 15.2) than
the a simple fluid simulation, only 117 different geometries were analyzed. The results model
results including SIPA were correlated with shear stress, confluence, Peclet number, and
stagnation area.
8.3.1.2 Results and Discussion
Figure 8.13 shows the optimal
cannulae for active platelets and
Damkohler number. The other objective
functions led to cannulae similar to that
for active platelets and were close to the
optimal confluence and MOO objective
cannula. This is an encouraging result
since platelet mediated thrombosis model
adds significant computation coast and
complexity due to eight highly-nonlinear,
coupled equations in addition to the fluid simulation. The Damkohler cannula was unique in its
shape resulting in a decisive pinch compared to that of any other objective function. This is most
likely due to the balance between the reaction rate in the numerator and the transport in the
denominator. The high transport or clearance, results in an increase in the RBC enhanced
323
diffusivity and the convective transport. The width of the flow path of the cannula is decreased
until the effect of shear-induced activation becomes significant.
The study of the design space showed several functions that were well correlated (r > .8).
The confluence, Peclet Number, and Stagnation were correlated to the platelet activation
functions represented by Equations 10.48-53. The correlations to the Damkohler number (8.54)
were between 0.6 to 0.75. These functions were also weakly anti-correlated to SIPA (-0.4 < r < -
0.3). However, shear stress was highly-correlated to SIPA (r = 0.97).
8.3.1.3 Conclusions
Despite the apparent need for two objective function (SIPA and one from Equation
10.48-53), the activation threshold included either directly (functions involving kpa) or indirectly
(functions involving active platelets or thrombin) and gives a more accurate picture of
thrombogenicity and biocompatibility. However, the multi-objective approach may be more
desirable as it avoids the high computation cost associated with platelet mediated model.
Furthermore, the functions directly using the activation term are non-differentiable using the
discontinuous model, meaning they can predict infinite or large gradients under the right
conditions. Even the continuous version, although being smooth, can result in a large gradient at
the point were activation occurs. The discontinuous and continuous activation rate also lack
curvature below the activation threshold leading to an infinite number of “optimal solutions”.
Other functions, such as the Damkohler number and power-law models, do not produce positive
definite Hessian matrices. A positive definite Hessian guarantees rapid convergence to the
optimal point, but if the Hessian is not positive definite convergence depends on how close the
initial guess is to the optimal point.
324
8.3.2 Quintessential Ventricular Cannula
Despite a nearly-nonstop effort to improve the performance and biocompatibility of
Ventricular Assist devices, very little effort has been placed on the cannula connection. One
revolutionary device, known as the Quintessential Ventricular Cannula (QVC), promises to
reduce the thrombogenicity of the ventricular connection. The QVC has a novel flanged tip that
fits flush against the ventricular wall as opposed to projecting into the ventricular cavity as done
with caged type, beveled, and blunt cannula. Figure 8.1shows the various cannula tips that have
had historical use. This study seeks to examine the flow improvements and biocompatibility of
the blunt tipped cannula and the QVC.
Figure 8.14: The three traditional geometries for cannulation (Left to Right) the blunt tip, the beveled tip, and the caged tip. Variations of the cannula tip includes the addition of side ports.
325
Cannula Insertion Point(Normal Outflow, p=0)
Ventricular Wall(No-slip and insulation)Li
ne o
f Sym
met
ry(v
=0, z
ero
flux,
du/
dn=0
) VentricularRadius
Cannula Insertion Point(Normal Outflow, p=0)
Ventricular Wall(No-slip and insulation)Li
ne o
f Sym
met
ry(v
=0, z
ero
flux,
du/
dn=0
) VentricularRadius
Figure 8.15: The ventricular geometry used to compare the cannula tips.
8.3.2.1 Methods
The insertion of a blunt tipped
cannula and the QVC can readily be
represented by a 2D flow domain or an
axisymmetric domain. 2D domains allow
for denser meshes and better element
quality resulting in greater accuracy of
the numerical method. Secondly, the
reduction into 2D results in fewer
degrees of freedom and a reduction of
non-linear equations by one. Only the
lower portion of the ventricle was
simulated. (See Figure 8.15) The diameter of the heart was assumed to be 8 cm representing a
dilated heart which also indicated that the flow was laminar. Furthermore, blood was assumed to
be Newtonian with a density of 1.05 g/cm3 and viscosity of 3.5cP. The depth of the heart was
approximately 3.5 cm, assuming that the significant dilation occurs in the radial direction. The
flow rate was set to 6 lpm, effectively modeling a completely non-function ventricle. Due to the
complexity of simulating fluid-structure interactions, particularly for such a flaccid material firm
as a failed ventricle, the outer walls were considered immobile. The blunt tip cannula was
simulated at insertion depths of 0.5 cm and 1cm to show the effect of insertion depth on the flow
and thrombogenicity. Furthermore, the effect of insertion angle was simulated over a range of
zero to ten degrees. The QVC was design to fit flush against the ventricle wall thus resisting the
problem of over-insertion and preliminary studies proved that the QVC was not as sensitive to
326
insertion angle as blunt tipped cannulae [26], therefore the effect of insertion angle was not
studied. Thrombogenicity was determined through evaluation of the fluid dynamic parameters of
confluence and stagnation area and by simulation of the platelet activation as described in section
8.3.1.1. A finally measurement was a simulated dye-washout study in which an initially uniform
concentration (set to 1 U/cm3 for convenience) was allowed to wash out of the domain for 5
second indicating regions of poor washing.
8.3.2.2 Results and Discussion
Figure 8.16 shows the steady-state platelet activation caused by the three different insertions.
The 100% activation, indicated by red, is pronounced in the regions between the cannula and the
ventricular wall of both blunt cannula. The deeper the insertion depth, the greater the area of
platelet activation becomes and subsequent thrombogenicity was is increased. When the cannula
is only slightly inserted (the far right case) shows that some of the fluid impinges into the region
below the lip of the cannula. The QVC only shows a small amount of platelet activation near
Blunt Tip QVC Blunt TipBlunt Tip QVC Blunt Tip
Figure 8.16: Results depicting the activation of platelets caused by the different cannula tips and insertion depths. Dark red indicates complete activation of platelets (Color scales not equal)
327
φφ
Figure 8.17: Comparison of the flow deviation angle (top) and stagnation area (bottom) for the cannula insertion study. The color scale for flow deviation in degrees is given in the top right. Regions of stagnation, i.e. where the velocity less than 5% of the mean inlet velocity, are indicated by dark red.
where the flange contacts the ventricle wall. The thrombogenicity of this region can be reduced
by tapering the flange down as the distance from the insertion point increases. The effluence of
active platelets, when compared to the influx, showed a 375% increase, 40% increase, and 215%
increase for the deeply inserted blunt tip cannula, the QVC, and the well placed blunt tip
cannula.
328
0.070.060.050.040.030.020.010.0
0o 5o 10o
Nor
mal
ized
Act
ivat
ion
Baseline
Figure 8.18: Normalized platelet activation, given by integrating the normalized platelet concentration over the entire volume of the domain. The baseline value was determined by integrating the initial activation level (0.05) over the domain.
Figure 8.17 shows the confluence or flow deviation angle (top) and the stagnation area
(bottom). Both of these fluid dynamic parameters and the dye washout experiment indicate the
same regions of concern as the platelet activation model, namely the region between the cannula
tip and the ventricular wall and the end of the QVC flange. However, these region reveal an
additional recirculation region within the entrance of the cannula. This region did not show
activation, but shows recirculation and stagnation. A single numerical value quantifying the flow
deviation angle was evaluated using the L2 norm. The flow deviation index was 14,500, 2,640,
and 5,910 for the three cannula tips respectively. This index implies that the well placed cannula
is only twice as thrombogenic as the QVC, where the improperly placed blunt tip cannula was
5.5 times as thrombogenic as the QVC. After 1 second of flow, the forward flow regions were
entirely evacuated of dye leaving only the region between the cannula and the ventricular wall
for the blunt tipped cannulae with dye. The dye persists in that region even after the five second
simulation time. The dye was almost completely washed from the QVC after one second. Slight
amount of dye, less than 15%, remained near the regions of concern and on the inside of the
cannula. The total amount of dye remain in the
ventricles was 1.59 U, 0.0351 U, and 0.119 U
for the respective cannula.
Figure 8.18 shows the effect of insertion
angle on platelet activation with the blunt tipped
cannula. The platelet activation was lowest (I =
0.0482) at the ten degree deviation and peaked
at two degrees (0.0622) before decreasing to
0.0600 at zero degrees. An initial assessment
329
Figure 8.19: The formation of a ring thrombus around a standard cannula tip after a PediaFlow implantation in a sheep.
would imply that the cannula should be inserted at an angle and near the wall. However, the
cannula entrance located near the wall results in a higher risk of suck down [26]. Furthermore,
assessing the insertion angle inside the heart is difficult to do during actual surgery.
Irregardless of the method used to
evaluate the thrombogenicity of the
cannula tip, the QVC outperformed the
blunt tipped cannula. It was also shown
that the depth of insertion is a critical issue
when placing the cannula within a patient,
as over-insertion considerably increases
the thrombogenicity at the insertion point.
The danger is further augment due to the
trauma caused to the surrounding tissue
and blood as the cannula is inserted. The
QVC shows a reduction in predicted
thrombogenicity when compared to the
blunt tipped cannula. Figure xxx shows a ring of thrombus forming around a caged tip cannula
used during a PediaFlow animal study. The thrombus can pre-activate platelets or sensitize them
to shear activation before entering the ventricular assist device. Furthermore, the thrombus can
detach and releasing emboli into the arterial blood flow. Conversely, the QVC showed superior
performance irregardless of the selection criterion. These results are further corroborated by
experimental studies of Bachman, where micro-beads were shown to accumulate around the
blunt tip but not around the QVC [26].
330
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