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P. Pallav, PhD IntroductionOn this page we start with a theoretical set up where an upper and a lower molar move
closer.
The space between the molars is filled with a pseudo plastic material (the food). The molars are cylindrical and on this page the occlusal surfaces are still absolutely flat. In the next pages we will gradually add more complexity to the occlusal surfaces and wearing restorations. Minimum Height Because the fluid resists the compression, pressure is needed. If the height would decrease all the way
down to zero, the pressure
in our set up would even
rise asymptotically (Equation 3 below). However, when you observe a real life wax bite, you will see that there is still a
small volume of wax left between the molars at centric occlusion. Therefore we
will take it that the vertical closing motion of our set up stops when the
volume is equal to the volume of the wax of the wax bite between the molars. Of
course the diameters of the molars must be similar too.
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Key parameters of the theoretical set up at or shortly before the end of a chewing motion. R is the radius of the molars, Vv is the vertical closing velocity at which the lower molar moves closer to the upper molar. Because of this, the distance between the surfaces represented by h (height) decreases and the fluid (food) flows out sideways at an average velocity, vav, which varies with the distance from the center r where it is zero. |
The flow rate (Q), the volume per unit time escaping at the circumference, is generated by the vertical speed (Vv) of the occlusal area (p·R2):
| Q = Vv · p·R2, Equation 1, |
At the circumference, the average velocity (vav,R) of the food is calculated as the flow rate (Q) divided by the cross-sectional area (width x height) of the parallel gap at the circumference. Of course the width of the gap is equal to the perimeter (2pR) of the set up.
| vav,R = Vv · |
p·R2
h·2p·R |
= Vv · | R
2h |
, Equation 2, |
The same is true at any distance (r) from the center
| vav,r = Vv · | r
2·h |
, Equation 2a, |
With the Equations in the pages Erosion, Shearing Action, and Velocity in Fluids, several things can be derived.
The average pressure on the surfaces and in the fluid (Pav), required to maintain the closing velocity (Vv)
| Pav = 2µ· | ((1/b + 2)·Vv)b·R(b + 1)
(b + 3)·h(2b + 1) |
, Equation 3 |
See Shearing Action for a description of µ and b. Because we assume pseudo plastic flow of the food (b = ½), Equation 3 simplifies to
| Pav = | 8µ·Vv½·R1½
7·h2 |
, Equation 3a |
Note that Equations 3 and 3a are limited to plane and parallel occlusal surfaces.