Lesson 2 - Wort Separation Principles
This lesson deals with the principles of wort separation. Before wort separation, we have completed mash conversion. We will now need to separate the liquid wort from insoluble material. This is mainly the husks from the malt, known as spent grain. We will review the reasons why filtered wort must be clear, and how this affects wort quality. We will examine how the all-important grain filter bed is formed differently, by each of the three most common mash separation devices. These devices are: the lauter tun, the mash filter and the mash tun. We will investigate a typical wort collection profile, which ends with the removal of the spent grain.
Darcy’s Law describes filtration flow rate. We will assess both the variables involved, and what influences them. We will finally use Darcy’s Law to predict the relative flow rates of the three mash separation devices.
Combining the Darcy’s Law Variables
Let’s use the values we derived earlier in the lesson, and use Darcy’s Law to predict the flow rates of our wort separation devices:
For the mash tun
|
Factor |
k m² |
A m² |
DP bar |
DP mPa |
µ mPa.s |
L m |
|
Mash tun |
9.72 x 10-11 |
20 |
0.1 |
1 x 107 |
1.85 |
1
|
Inputting our figures into Darcy's equation and calculating gives us:
For the lauter tun
|
Factor |
k m² |
A m² |
DP bar |
DP mPa |
µ mPa.s |
L m |
|
Lauter tun |
3.084 x 10-11 |
50 |
0.1 |
1 x 107 |
1.25 |
0.5
|
Inputting our figures into the equation and calculating gives us:
And finally for the mash filter:
|
Factor |
k m² |
A m² |
DP bar |
DP mPa |
µ mPa.s |
L m |
|
Mash filter |
3.525 x 10-13 |
330 |
0.3 |
3 x 107 |
1.65 |
0.05 |
Inputting our figures into the equation and calculating gives us:
To convert flow rate from m3/s to hL/hr, we multiply by 3,600 (seconds into hours) and multiply by 10 (m3 into hL). The table below shows the figures for each device along with their comparative flow rates.
Table: Comparison of flow rates for the different wort separation devices
|
Factor |
k m² |
A m² |
DP bar |
DP mPa |
µ mPa.s |
L m |
Q m³/s |
Q hL/h |
Comparative Q
|
|
Mash tun |
9.72 x 10-11 |
20 |
0.1 |
1 x 107 |
1.85 |
1
|
0.0105 |
378 |
1 |
|
Lauter tun |
3.084 x 10-11 |
50 |
0.1 |
1 x 107 |
1.25 |
0.5
|
0.0247 |
889.2 |
2.3 |
|
Mash filter |
3.525 x 10-13 |
330 |
0.3 |
3 x 107 |
1.65 |
0.05 |
0.0423 |
1,522.9 |
4 |
The mash tun is predicted to be the slowest. It does benefit from the highest bed permeability, but counteracting this, it has the highest bed loading (the deepest bed and lowest cross-sectional area).
The lauter tun is predicted to run over twice as fast as the mash tun. Its bed permeability is lower and would give a lower flow. However, this is more than compensated for by its bed loading being 2.5 times lower (shallower bed and larger cross-sectional area). The flow achieved may be higher than our prediction, as the lauter tun has a set of knives which can be used to cut the bed and increase the bed permeability.
The mash filter is predicted to run four times faster than the mash tun. Its bed loading is fifteen times lower but the benefit of this is reduced by a very low bed permeability, resulting from the fine comminution provided by the hammer mill.