Parameter
|
Greek Symbol
|
Units
|
Explanation of parameters
|
|
alpha |
a |
[-] |
Factor that describes the ratio of kLa
in the media as compared to the kLa in water/air under identical
conditions of power and gas flow rate. |
|
beta |
b |
[-] |
Factor that describes the ratio of dissolved oxygen
saturation in deactivated media as compared to that of water/air under
identical conditions of temperature and pressure. In a fermentation, the
microorganisms must be disabled for this determination. |
|
Shaft Deflection near bottom |
d SHAFT.BOT |
mm |
Deflection in the shaft near the bottom of the reactor,
tank, vessel, or fermenter. |
|
Shaft deflection near top |
d SHAFT.TOP |
mm |
Deflection in the shaft near the top of the reactor, tank,
vessel, or fermenter. |
|
Tank deflection at side |
d TANK.SIDE |
mm |
Deflection in the side wall of the reactor, tank, vessel,
or fermenter. This is a sign that the tank wobbles. |
|
Baffle thickness |
D BAF |
mm |
Thickness of the baffles. |
|
Blade thickness(i) |
D i,BLADES |
mm |
Thickness of the the blades of the i-impeller. |
|
Top head thickness |
D TOP |
mm |
Thickness of the top dish. Often found on data describing
the ASME pressure testing of the tank. |
|
Longitude relative to front |
F BAF |
deg |
Position of the first baffle from the front in CCW-direction.
If the baffles are not placed symmetrically around the tank, list their
positions separately. |
|
Longitude relative to front |
F COIL |
deg |
Position of first coil or bundle from the front. List them
if not symmetrical. Irrelevant for helical coils. |
|
Longitude relative to front |
F SP |
deg |
Position of the sparge pipe relative to the front in
degrees. |
|
Avg Shear Rate |
g·i,AVG |
1/s |
Average impeller shear rate for the i-impeller. |
|
Max Shear Rate |
g· i,MAX |
1/s |
Maximum impeller shear rate for the i-impeller. |
|
Newtonian Viscosity |
h |
cPs or mPas |
Although most fluids and slurries exhibit non-Newtonian
flow characteristics, this is a characteristic viscosity that a company
has used to date to describe the viscosity of their fluids. |
|
Viscosity factor |
h F |
|
Factor that reduces the kLa
as viscosity increases. It is
a constant for viscosity < 25. |
|
Rotational direction |
j |
|
Rotational direction of the shaft, either clockwise (CW)
or counter clockwise (CCW) as seen from the top-down. |
|
kLa Impeller Factor |
k F |
|
Ratio that describes how well an impeller system is, based
on kLa as compared to a standard single impeller system at the same P/V
and Qg. All single impeller systems have the same kLa at the same P/V and
Qg. |
|
Theta |
q |
|
Constant that describes the deviation of kLa
based on
different temperatures. The standard temperature is 20oC. Most reported
Theta-values vary between 1.016 and 1.047. |
|
Henzler's ThetaMix(95%) |
q 1i,MIX,HENZLER |
[-] |
Henzler’s ThetaMix number (95%) for a single mixer in a
standard tank for the i-impeller. |
|
Henzler's Mult-Imp ThetaMix(95%) |
q Mi,MIX,HENZLER |
[-] |
Modified Henzler’s ThetaMix number (95%) for multiple
impellers in a tank for the i-impeller for the i-impeller. |
|
Recirculation Time |
q RECIRC,i |
s |
Recirculation Time. Time for the average packet of fluid
to return to the place it started from for the i-impeller. |
|
Unaerated Density |
r |
kg/m3 |
Density of the media without any gas pockets. This should
be the density at the operating temperature. |
|
Density of unaerated water at temperature |
r H2O |
kg/m3 |
Density of water at the operating temperature. |
|
Average gassed density of the media |
r LIQ,G |
kg/m3 |
Density of media at the operating temperature taking the
entire gassed volume into account. |
|
Total MixTime(95%) for all impellers |
t MIX,95 |
s |
Mixing time based on 95% degree of blending. |
|
95% Blend Time for bottom impeller |
t MIX,B,95 |
s |
Mixing time based on 95% degree of blending for just the
bottom impeller (or single impeller). |
|
95.0% Blend Time for bottom impeller |
t MIX,B,x |
s |
Mixing time based on the degree of blending, x,
for just the bottom impeller (or single impeller). |
|
Total MixTime(95.0%) for all impellers |
t MIX,x |
s |
Total mixing time based on the degree of blending, x,
and the eAVG. |
|
Degree of mixing (blending) desired |
x |
% |
Point at which the reactor, tank, vessel, or fermenter is
considered mixed. 100% would take indefinitely long by definition. Typical
values are 90%, 95% or 99% mixed. |