user's manual for corhyd: an internal diffuser hydraulics model - IfH
user's manual for corhyd: an internal diffuser hydraulics model - IfH
user's manual for corhyd: an internal diffuser hydraulics model - IfH
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Glossary<br />
Table 1: Summary of parameters, Parameters are used with the following major indices: d = <strong>diffuser</strong><br />
pipeline section; p = port pipe; j = jet<br />
Parameter Dimension Definition<br />
ρ a kg/m³ average density of ambient water body<br />
ρ e kg/m³ average density of the effluent<br />
A m² pipe cross sectional area<br />
B m equivalent slot width B = A p /l<br />
C c - jet contraction coefficient<br />
D m <strong>internal</strong> pipe diameter<br />
E m energy head<br />
g’ m/s² reduced gravity, g’ = ∆ρ/ρg<br />
H m head above datum (additional indices: H t = total head at headworks; H d = design<br />
water level elevation of ambient water)<br />
i - numbering of port/riser configurations (counting from seaward end to shore,<br />
starting with 1)<br />
j - numbering of local losses in ports, risers or the <strong>diffuser</strong><br />
j 0 m³/s³ buoy<strong>an</strong>cy flux per <strong>diffuser</strong> length, j 0 =g’q 0<br />
k s m equivalent s<strong>an</strong>d roughness<br />
l m riser spacing<br />
L m length of the considered pipe section<br />
n - total number of local losses j in between one pipe section<br />
N - total number of port/riser locations i of <strong>diffuser</strong><br />
N d - total number of <strong>diffuser</strong> sections (includes feeder)<br />
N g - total number of port/riser groups<br />
N gp - number of risers per group<br />
N p - number of ports per riser<br />
p Pa = N/m² pressure, (additional indices: p l = pressure loss, p a = ambient water pressure)<br />
Q m³/s total flow through outfall system<br />
q m³/s individual discharge through a riser or port at position i<br />
q 0 m²/s mass flux per <strong>diffuser</strong> length , q 0 = V j B<br />
R m radius of bend<br />
Re - Reynolds number Re = VD/ν<br />
S c - plume centerline dilution<br />
SecNo - <strong>diffuser</strong> segment number where this group is located in<br />
t s time<br />
V m/s me<strong>an</strong> flow velocity<br />
x m horizontal coordinate of pipe segment centerline location<br />
y m horizontal coordinate of pipe segment centerline location<br />
z m position or elevation in the vertical<br />
α i - 1 / (number of ports at a riser at position i)<br />
β ° <strong>an</strong>gle of gradual exp<strong>an</strong>sion or contraction<br />
ζ - dimensionless loss coefficient <strong>for</strong> local losses<br />
λ - dimensionless friction coefficient<br />
ν m²/s kinematic viscosity<br />
Institut für Hydromech<strong>an</strong>ik, Universität Karlsruhe 3