| | Target variables | Notes | Ref. |
| Trial-and-error without mathematical model | CQAs, CPPs, CMAs | Optimization of freezing process | [13, 31, 32, 33] | Optimization of primary drying process | [12] | Optimization of secondary drying process | [34] |
| Use of mathematical model | CMAs (Tb, Rp, and so on) and CPPs (Ts, Pc, the drying time, and so on) | A partial differential equation (PDE) | [31, 34–44] | A model predictive control (MPC) | [29, 42, 45, 46] | A computational fluid dynamics (CFD) | [15, 47, 48] | Kv-based modeling | [49] |
| Designs space | Pc-dm/dt plane (Figure 4) | Control of primary drying process | [13, 17, 18, 50–52] | Control of freezing process | [53] |
| Scale-up | Kv, Pc | Vial-position dependency of Kv | [12, 54] | A use of empty vials at the edge of the shelf | [17] | Equivalent resistance model under the dust-free condition using HEPA-filtered airflow (without empty vials) | [55] |
| Process analytical technology (PAT) | Kv, Rp, Tb, and Pc, dm/dt | In-line optimization | [56–67] |
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