| Literature DB >> 32104308 |
Lan Zhang1, Shirui Mao1.
Abstract
Quality by Test was the only way to guarantee quality of drug products before FDA launched current Good Manufacturing Practice. To clearly understand the manufacture processes, FDA generalized Quality by Design (QbD) in the field of pharmacy, which is based on the thorough understanding of how materials and process parameters affect the quality profile of final products. The application of QbD in drug formulation and process design is based on a good understanding of the sources of variability and the manufacture process. In this paper, the basic knowledge of QbD, the elements of QbD, steps and tools for QbD implementation in pharmaceutics field, including risk assessment, design of experiment, and process analytical technology (PAT), are introduced briefly. Moreover, the concrete applications of QbD in various pharmaceutical related unit operations are summarized and presented.Entities:
Keywords: Critical quality attributes (CQA); Design of experiment (DoE); Near infrared (NIR) spectroscopy; Process analytical technology (PAT); Quality by design (QbD); Risk assessment
Year: 2016 PMID: 32104308 PMCID: PMC7032183 DOI: 10.1016/j.ajps.2016.07.006
Source DB: PubMed Journal: Asian J Pharm Sci ISSN: 1818-0876 Impact factor: 6.598
Fig. 1Comparison between QbT (a) and QbD (b). (QbT: quality by test; QbD: quality by design; QTPP: quality target product profile; CQA: critical quality attributes; CMA: critical material attributes; CPP: critical process parameters; DoE: design of experiments).
Representative applications of Quality by Design in pharmaceutical unit operations and dosage forms.
| Pharmaceutical unit operations | Dosage form | Model drug | Design of experiment (DoE) | Critical material attributes (CMA) | Critical process parameters (CPP) | Critical quality attributes (CQA) |
|---|---|---|---|---|---|---|
| Fluid bed granulation | Tablets | Not mentioned | Fractional factorial design (screening) | Viscosity, temperature and concentration of the binder aqueous dispersion | Inlet air temperature, binder spray rate and air flow rate | Particle size distribution (PSD), bulk and tapped densities, flowability and angle of repose |
| Roller compaction | Tablets | Not mentioned | Fractional factorial statistical design | API composition, API excipient ratio | API flow rate, lubricant flow rate, pre-compression pressure | Tablet weight, tablet dissolution, hardness, ribbon density |
| Film coating | Coated tablets | Placebo tablets | Central composite – face centered – response surface design | Solid percent of the coating dispersion | Inlet air temperature, air flow rate, solid level, coating pan speed, spray rate | Appearance (coating defects, gloss, and color uniformity), disintegration time (dissolution of the film coating) |
| Spray drying | Solid nano-crystalline dry powders | Indomethacin | Full factorial design | NA | Inlet temperature, flow rate, aspiration rate | Particle size, moisture content, percent yield, crystallinity |
| Hot-melt extrusion (HME) | Solid lipid nanoparticles (SLN) | Fenofibrate (FBT) | Plackett–Burman (PB) screening design | Lipid concentration, surfactant concentration | Screw speed, barrel temperature, zone of liquid addition | Particle size, polydispersibility index, zeta potential, entrapment efficiency |
| Homogenization | Nanoparticles | Paclitaxel | Box–Behnken design | Surfactant concentration in aqueous phase (%) | Homogenization rate | Average particle size, zeta potential, encapsulation efficiency |
| Solid lipid nanoparticle (SLN) | Rivastigmine | Factorial design | Drug: lipid ratio, surfactant concentration | Homogenization time | Size, PDI, entrapment efficiency | |
| O/W emulsification–solvent evaporation | Nanoparticles | Cyclosporine A (CyA) | Plackett–Burman (PB) design | Type of solvent organic to aqueous phase ratio, drug concentration, polymer concentration, surfactant concentration, O/W ratio | Stirring rate | Encapsulation efficiency, particle size, zeta potential, burst release and dissolution efficiency |
| Physical mixture, solvent evaporation | Controlled-release tablets | Felodipine | Box–Behnken design | Amount of polymer HPMC | Preparation technique | Maximum solubility after 30 min, equilibrium solubility after 24 h, dissolution efficiency |
| Homogenate membrane method | Orodispersible films | Theophylline | Central composite design | Percentage of HPMC, percentage of glycerol | Drying temperature | Tensile strength, elongation at break, Young's modulus, disintegration time |
NA, not available.
Fig. 2Ishikawa diagram for preparation of extruded particles [12]
Representatives of some monitoring tools used in pharmaceutical processes (2011–2015).
| Processes | Monitoring tool | Attributes measured | Major outcome |
|---|---|---|---|
| Co-precipitation process | Lasentec particle vision microscopy system PVM819 | Nucleation and crystal growth | Obtain direct information about the morphology and size of the co-precipitates |
| Mammalian cell culture process | Raman spectroscopy | Glycoprotein product yield | Selecting which small scale batches are progressed to large-scale manufacture, improving process efficiency significantly |
| Chinese hamster ovary (CHO) cell fed-batch process | Fluorescence excitation–emission matrix (EEM) spectroscopy | Key fluorophores (e.g. tyrosine, tryptophan, and the glycoprotein product) | Quantitative predictive analysis of recombinant glycoprotein production |
| Fluid bed granulation | Microwave resonance technology (MRT) | Determine moisture, temperature and density of the granules | Predict information about the final granule size |
| Pan coating process | New real-time monitoring tool (PyroButtons) | Record and data in real-time | Move with the tablets providing information on the thermodynamic conditions (microenvironment) |
| Continuous direct compaction tablet manufacturing process | Near infrared (NIR) spectroscopy | Powder blend bulk density | The NIR spectra are sent to a real time prediction engine that utilizes the NIR calibration models for blend density and drug concentration and a real time prediction tool (OLUPX) to generate the signals for the control variables in real time |
Representative applications of near infrared spectroscopy (NIR) in representative unit operations.
| Unit operations | Parameters | Description |
|---|---|---|
| Crystallization | Polymorphism and particle size of the indomethacin powder | In-line |
| Determine API and residual solvent contents | On-line | |
| Co-precipitation | Turbidity monitoring, and in situ crystal size monitoring | On-line |
| Freeze-drying | Moisture content analysis | In-line |
| Hot-melt extrusion | Screw speed and drug loading | In-line |
| Powder mixing | Monitor blending uniformity | In-line |
| Compression | Content uniformity | On-line |
| Continuous granulation process | Show the variation in solid state (transform anhydrous theophylline to theophylline monohydrate) | In-line |
| Fluidized bed granulation | Determine the moisture content, size distribution, and bulk density | In-line |
| Fluid-bed coating | Film thickness on pharmaceutical pellets | In-line |