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FE Modelling and Simulation of Gasand Fluid Supported Structures 163<br />

phg ρt<br />

<br />

<br />

<br />

K = − N<br />

2<br />

e η ξ<br />

T ( ∗ ng T + g ∗ n T )N dξdη<br />

+ 1<br />

⎛ ⎞ ⎞T ⎛<br />

<br />

<br />

<br />

ξ η<br />

N 0 W W<br />

phgpt ⎝ N,ξ ⎠ ⎝ W<br />

2<br />

e η ξ N,η<br />

ξT<br />

0 0<br />

W ηT<br />

⎞ ⎛ ⎞<br />

N<br />

⎠ ⎝ N,ξ ⎠<br />

0 0 N,η<br />

dξdη,<br />

a = <br />

<br />

<br />

e<br />

η<br />

(52)<br />

N<br />

ξ<br />

T ∗ nt dξdη, (53)<br />

b = <br />

<br />

<br />

phgαtNT ∗ nt dξdη, (54)<br />

e<br />

η<br />

ξ<br />

<br />

<br />

<br />

phg<br />

f =<br />

phgptNT ∗ nt dξdη, (55)<br />

e<br />

η<br />

ξ<br />

phg<br />

αt = K<br />

2V −<br />

cpt −x pt<br />

,<br />

vt<br />

(56)<br />

phg<br />

pt = c p − x p − h p. (57)<br />

The nodal displacement vector for one iteration step is then given by a linear<br />

combination of the three auxiliary solution vectors: d = d(d1, d2, d3). For<br />

further details and the combination with arc-length schemes, we refer to [9]<br />

and [5]. For the cases pneumatics, hydraulics and incompressible fluids with<br />

open surfaces only a rank-one update is found. For pneumatics and hydraulics<br />

the pressure terms due to gravity disappear with c p = x p =0, as well as<br />

the first term in phg K,asg is not existent then. Depending on the pressure<br />

equation for gas or fluid<br />

k<br />

h pt<br />

αt = κ<br />

vt<br />

or<br />

h αt = K<br />

V<br />

= const. (58)<br />

and only a constant pressure term remains phg pt = − h pt.<br />

For incompressible fluids phg K has the same structure as for compressible<br />

fluids, but the pressure is dependent on the current coordinate of the fluid<br />

only hg pt = x p = ρg(−xt). However, we have to note that incompressibility<br />

can only be considered for fluids with open surfaces. For compressible fluids<br />

with open surface the pressure term h p due to overpressure is not present.<br />

Thenthevolumechange due to the fluid weight is included in the c p-term.<br />

However, in this case we have to keep also track of the current height of the<br />

fluid level, which is discussed in a forthcoming paper.<br />

5 Numerical Examples<br />

5.1 Pneumatic Multi-Chamber Structure Under Torsional Loading<br />

A pneumatic multi-chamber structure see Fig. 1, two chambers with different<br />

initial internal pressure (left pl0 = 0.01 bar,right pr0 =1bar, with material

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