We are often asked about the production capacity of our extrusion and spheronization systems. To provide this information there needs to be an understanding of the process parameters that will be used and that have been determined at the development stage. With that information, the advice that we give can be both meaningful and useful in the planning stages.
If you have proven your concept at the laboratory stage, then you will have established your process parameters so you could talk to Caleva about help with scale up. If you need to explore the development and formulation of your product then we can help with equipment to enable you to do that, such as the Caleva Multi Lab, design for R&D Success.
Production spheronizers have nominal bowl diameters of, 380 mm, 500 mm and 700 mm and these, respectively have a production capacity guide of 50 kg per hour, 100 kg per hour and 150 kg per hour. As a capacity guideline, these figures are simple, logical, and easy to remember. In addition, these do bear some resemblance to reality, but this is with a lot of assumptions. These assumptions are reasonable but not correct in all situations.
It is important to consider these assumptions so that the manufacturer can establish and understand the potential outcomes.
The spheronization process consists of four separate steps: mixing or granulation, extrusion, spheronization and drying (and possibly coating).
It is the spheronization step that normally (not always) determines the rate of production because it is the slowest process
If this is understood, then in normal circumstances the production rate described for the whole process is the rate at which material can be taken out of the spheronizer.
Spheronizers with different diameter bowls have different maximum load capacities. Estimates are shown below but these will, to some extent depend upon the density of the material that is being spheronized. Clearly, the amount of product being added to a single spheronizer run will be an important factor in determining the kilos per hour productivity.
Spheronizer 380 - generally up to about 4 kg
Spheronizer 500 - generally up to about 7 or 8 kg
Spheronizer 700 - generally up to about 12 or 15 kg
The second major factor will be the time that the material remains in the spheronizer bowl (the residence time)
P = The productivity in kilos per hour
L = The load in kilos that is put into the spheronizer
T1 = The time in minutes taken to load the machine
T2 = The time in minutes of the spheronization process
T3 = The time in minutes taken to discharge the machine
P = L x 60/(T1+T2+T3) = 8 x 60/5 = 8 x 12 = 96 Kg /Hr.
We would take our result as about 100 kg per hour. This would be a reasonable guide and is product and process dependent.