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Article
Dissolution and Design Space for an oral pharmaceutical product in tablet form Kalliopi A Chatzizaharia, and Dimitrios T Hatziavramidis Ind. Eng. Chem. Res., Just Accepted Manuscript • DOI: 10.1021/ie5050567 • Publication Date (Web): 01 Jun 2015 Downloaded from http://pubs.acs.org on June 8, 2015
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Industrial & Engineering Chemistry Research
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Dissolution efficiency and Design Space for an oral
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pharmaceutical product in tablet form
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Kalliopi A. Chatzizaharia, Dimitrios T. Hatziavramidis*
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School of Chemical Engineering, National Technical University of Athens
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Heroon Polytechniou 9, Zografou 15771, Athens GR
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KEYWORDS Design Space, Mixture Design, generic oral tablet, dissolution similarity factor,
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Bayesian approach
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Abstract
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The primary drug quality requirements, safety, efficacy and reliability, for oral pharmaceutical
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products in tablet form, translate into bioavailability, and tablet weight and strength. The
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bioavailability of an oral drug, i.e., the amount of the drug that can reach the systemic
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circulation, depends on drug permeation rate through the epithelial membrane or on dissolution
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rate, in case of bioequivalence. Thus, the critical quality attributes affecting bioavailability can
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be the dissolution profile, tablet weight and tablet hardness, which are affected by process
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conditions and drug product composition, i.e., active pharmaceutical ingredients (APIs) and
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excipients and their mass fractions. A Mixture Design (DOE) experiment has been carried out
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for a generic oral drug, with input factors the mass fractions of three excipients and response
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variables the dissolution profile, tablet weight and hardness. While the last two response
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variables are single-point-value attributes, a dissolution profile is a multi-point-value attribute
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and is assessed using integral measures, e.g., similarity factor, from pair-wise, model-
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independent methods. The data from the Mixture Design experiment are used to develop a multi-
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regression and multi-response optimization model, which, in turn are used to determine the
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Design Space (DS) for the pharmaceutical product of interest.
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1. Introduction
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The majority of oral pharmaceutical products in tablet form are powder mixtures of Active
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Pharmaceutical Ingredients (API) and excipients. Excipients, in conjunction with process
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parameters, facilitate processing of the powder mixture and improve quality attributes of the
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tablet dosage. During the drug development stage, a multi-regression model relating Critical
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Quality Attributes (CQAs) to critical process and formulation parameters, where the latter
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consist of the mass fractions, particle size distribution, water content and other properties of
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excipients and APIs, are constructed and critical process and formulations parameters that
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optimize the quality attributes are determined 1. Under the Quality by Design (QbD) initiative, it
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is possible to use knowledge from development studies to create a Design Space (DS) within
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which changes in formulation and manufacturing processes promoting continuous improvement
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of process capability and product quality can be implemented without the need for further
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regulatory approval
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planning informative experiments. When the composition of the drug mixture (API + excipients)
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is under investigation to optimize drug quality attributes, a Mixture DOE is utilized. Advances in
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supporting software, automated synthesis instrumentation, and high-throughput analytical
2–4
. Design of Experiments (DOE) techniques are well-established tools for
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techniques have led to the broader adoption of the QbD approach in pharmaceutical discovery
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and chemical development laboratories 5.
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Bioavailability of a drug in a solid oral dosage form, i.e., the fraction of drug dose that reaches
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the systemic circulation, depends on the release of the drug substance from the drug product, the
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balance among its dissolution, elimination, metabolism and absorption rates, as well as its
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solubility in the gastrointestinal fluids and permeability across the epithelial membrane. The
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distinct nature of dissolution and solubility must be emphasized, the former being a quantity of
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kinetic and the latter of thermodynamic nature. As early as 1995 it has been recognized that drug
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dissolution and intestinal permeability are the primary factors in determining drug transfer to
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systemic circulation, and a biopharmaceutics classification system (BCS) was developed to
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identify classes of drugs for which an in vivo-bioequivalence and in vitro-dissolution (IVIVR)
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correlation exists. When such a correlation is strong, regulatory testing of in-vivo bioequivalence
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can be waived in favor of in vitro dissolution testing 6–9. Whenever a waiver can be granted and
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drug dissolution is tested, the drug under study is compared to a reference drug and both drugs
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are assumed to be bioequivalent if their dissolution profiles are similar. Both, the European
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Medicines Agency (EMEA) and the USA Food and Drug Administration (FDA) assure that any
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methods to prove similarity of dissolution profiles are accepted as long as they are justified 10–12.
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In a previous paper
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, the DS for an oral drug granulation was determined from data in the
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literature by three different methods; response surface, Bayesian approach and neural networks.
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The effectiveness of a particular method, measured by the composite desirability function,
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indicated the presence or not of completeness, structure and uncertainty in the data. In this paper,
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the DS of a generic oral drug for which dissolution is important was determined from data
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obtained with our involvement, assuming not uncertainty. The aim of pharmaceutical
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development is to design a product and a series of processes to manufacture the product and
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consistently deliver performance to ensure product efficacy, safety and quality. Knowledge
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gained from pharmaceutical development and manufacturing experience facilitate identification
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of critical quality attributes (CQA), critical material attributes (CMA), and critical process
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parameters (CPP) and support the establishment of relations and mechanistic product-process
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design models between the CQAs, as output variables, and CMAs and CPPs, as input variables
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and parameters. CMAs and CPPs are identified through an assessment of the impact their
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variation can have on CQAs. Product and process requirements, attributes performance
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specifications, along with multivariate models based on chemistry and engineering fundamentals,
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help to define the feasible region for the subsequently formulated optimization problem. Solution
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of the multi-objective optimization problem yields an optimal product design14,15.
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In the combined granulation-compression process of making the tablet dosage form, CQAs
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include, but are not limited, to granule size, powder and granule flowability, and tablet weight
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and its variation, crushing strength, friability, disintegration time and dissolution, while CMA
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and CPP can be type and amount of binders, disintegrants, diluents, lubricants, and inlet air
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temperature, atomizing air pressure and other process variables, respectively.
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The regulatory framework regarding the manufacture of pharmaceutical products ensures
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patient safety through the use of well-defined processes with specified parameter ranges
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governed by a control plan which is the responsibility of the pharmaceutical company.
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According to this framework any type of change in formulation or process conditions requires
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regulatory approval. Under the new Quality by Design (QbD) initiative, however, it is possible to
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use knowledge from development studies to create a Design Space (DS) within which changes in
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formulation and manufacturing processes promoting continuous improvement of process
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capability and product quality can be implemented without the need for further regulatory
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approval 16,17.
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According to ICH Q8, a Design Space is defined as “the multidimensional combination and
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interaction of input variables (e.g., material attributes) and process parameters that have been
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demonstrated to provide assurance of quality”. The Design Space is proposed by the applicant
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and is subject to regulatory assessment and approval. Once approved, it sets the boundaries
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within which changes in the input variables and process parameters can be made without further
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regulatory approval. Changes that result in input variable and process parameters values outside
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the Design Space initiate a regulatory post approval change process2. If the Design Space is
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intended to span multiple operational scales (lab, pilot plant, plant), normalized (coded) variables
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in the interval [-1, 1] may be used18.
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Our literature review has shown that determination of the DS in QbD of pharmaceutical
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products was done using various methods with little or no regard for the type of experimental
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data obtained to this end. In a previous work of ours13, a methodology accommodating for the
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type of experimental data obtained for the sake of determining the DS was presented for
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pharmaceutical tablet development. This methodology of DS determination is applied in the
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present work to a generic drug development in which the CQA of the product are tablet weight
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and hardness, and bioequivalence to the original drug and the CMA the mass fractions of the
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excipients.
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In the present work, as in other works19, 20, 21, 22, bioequivalence is reduced to a comparison of
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dissolution profiles of product (generic) and reference (original) drug at multiple time points. A
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short review of methods for dissolution profile comparison is given in the Materials and Methods
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section. To our knowledge, there is no literature on determination of DS when one of the CQAs
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is multi-point valued, as is the case with dissolution profiles. The present work proposes the
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evaluation of previously established integral measures, such as similarity and Dissolution Area
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Difference factors, at critical and final times, the former defined as the time that separates slow
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from rapid dissolution, the latter defined as the time for dissolution cessation, for an effective
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assessment of bioequivalence between product and reference drugs.
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2. Materials and Methods
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2.1 Materials- Experimental Data
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A Simplex Centroid mixture design experiment was conducted for a generic tablet
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formulation, with 2 main components x1 and x2 chosen from the list of main excipients and two
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replicates of the center point, using Minitab software. A third component, excipient x3, used in a
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small percentage of 2-5% w/w, is added to facilitate the design analysis and the ternary mixture
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plots (Table 1). The APIs were mixed with x1, x2, x3 and other excipients, compressed into
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tablets and then coated. In the following analysis, the three excipients were chosen so that their
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mass fractions sum up to unity in a mixture of 312 mg, in which the mass remains constant. The
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response variables for tablet design (CQAs) were tablet weight and hardness, and the dissolution
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profile.
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2.2 Methods for dissolution profile comparison
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Regulatory authorities for pharmaceutical products consider as acceptable any approach to
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establish similarity of dissolution profiles, through comparison of single and multiple time-point
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dissolution data for reference and test products, by utilizing statistical, model-dependent and
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model-independent methods. FDA and EMEA methodologies emphasize the need of providing
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justification for similarity of dissolution profiles 10,11 .
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In statistical models, the sources of variation of percent dissolved at each time level can be
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analyzed by univariate (ANOVA) and multivariate (MANOVA) analysis of variance 19. Model-
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dependent methods include zero and first order kinetics, Hixson–Crowell, Weibull, Higuchi,
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Baker–Lonsdale, Korsmeyer–Peppas and Hopfenberg models for the amount of drug released
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over time
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about dissolution data. Model-dependent methods utilize expressions for the quantity of released
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drug as a function of time and drug concentration, thus making the quantitative interpretation of
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dissolution data easier and becoming more useful in the formulation-development stage of a drug
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product.
20,21
. Statistical methods are more discriminative and provide detailed information
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Model-independent methods can be further differentiated as ratio and pair-wise tests. Ratio
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tests compare the dissolution profiles of two formulations at a particular time point, while pair-
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wise procedures provide a simple way to describe the comparison of the data but sensitive to the
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number of dissolution time points.
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The ratio tests are relations between parameters obtained from the release assay of the
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reference formulation and test products at the same time and include ratios of percent dissolved
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drug, area under the release curve or mean dissolution time. The pair-wise procedures of
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comparing dissolution profiles utilize measures like the difference factor (f1), similarity factor
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(f2) and Rescigno index (ξi). Like the ratio test, pair-wise procedures compare dissolution
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profiles of a pair of products and establish 90% confidence intervals 20,22,23.
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The similarity factor f2 is defined as:
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f2 =50* log 1+1/N ∑Ni=1x-x ti ri
2 -1/2
*100
(1)
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,where N is the number of time points, xti is the mean percent of drug dissolved for the test
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product and xri is the mean percent drug dissolved for the reference product.
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When two dissolution profiles are identical, i.e., the difference of averages in Eq.1 is 0%, f2 =
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100%. If the difference of averages is 10%, f2 ≈ 50% and the two profiles are considered
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adequately similar. Thus, any value of f2 between 50 and 100% indicates that the two dissolution
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profiles are similar. The value of f2, as expected, is sensitive to the number of time points and
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reliable dissolution profile comparison in terms of the similarity factor requires at least three to
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four more points. Only one time point is needed after 85% dissolution. For products which are
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rapidly dissolving, i.e., more than 85% of the drug is dissolved in less than 15 min, no
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dissolution profile comparison is necessary 10,11,22.
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Other parameters used to characterize the drug release profile are: time to release a determined
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percentage of the drug, sampling time and dissolution efficiency. The dissolution efficiency (DE)
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of a pharmaceutical product is the ratio of the area under the dissolution curve up to a testing
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time point to the area of the rectangle that describes 100% dissolution up to the same time point.
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It can be calculated by the equation:
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DE=100*
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, where d is the function of drug percent dissolved at time t 20.
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In order to compare dissolution profiles with a combination of the DE criteria and the pair-
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t d*dt"d100 *t 0
(2)
wise procedure, a Dissolution Area Difference (DAD) factor can be calculated as: t t d *dt" 0 dref *dt $ 0 exp
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DAD=$1-
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, where dexp is the dissolution function of drug under investigation at a particular time, dref the
(3)
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dissolution function of the reference drug dissolved during the same time, and the area
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calculated using the multiple segment trapezoidal rule
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t d*dt 0
is
. The division of the time integration
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interval into segments is necessitated by steep changes in the dissolution - time curves. A
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minimum value of the DAD factor implies best similarity of the compared dissolution profiles.
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2.3 Materials- Experimental Data
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For a generic oral drug considered in this publication, the dissolution rate is a critical quality
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attributes. The critical formulation attributes are the mass fractions of three excipients. The
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acceptable ranges of the latter are determined by multivariate models, such as Mixture Design
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analysis
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method of choice for data which are complete and lack a correlation structure. The Bayesian
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approach, on the other hand, takes into account the correlation structure of the data and the
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uncertainty in determining model parameters. The basis for the Bayesian approach is as follows.
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If f(x|θ) is the conditional probability distribution and p(θ) the probability of the parameter θ
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from prior times, the posterior probability p*(θ|x) is:
25–29
, Bayesian method and Neural Networks
13
. The Mixture Design analysis is the
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p* θ|x= py|θpθ⁄py = py|θpθ"
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, where p*(y|θ) is the likelihood for fixed (observed) data y 3,30.
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Both, the Mixture Design Analysis and the Bayesian approach, were used to determine the DS
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of the generic oral drug of interest. In determining the values of input variables in a multi-
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response problem that result in optimal product, a popular strategy is to reduce the
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dimensionality of the problem, by using a single aggregate measure, often defined as a
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desirability function 31,32. The most popular form of a desirability function is:
θ
py|θpθdθ
(4)
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. / µi µimin 0 , ymin ≤ŷµi ≤Τµi µi Τµi -yµi , , β ŷ -ymin
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α
dµi = / ŷµi -yµi 0 , Τ ≤ŷ ≤ ymax µi µi µi - Τµi -ymax µi , , 0, ŷ ymax µi µi + µi µi max
(5)
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, where ŷµi, ymin , ymax , Tµi denote the estimated mean response, minimum and maximum µi µi
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desired limits and target for ŷµi, respectively, and α, β are input parameters that determine the
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shape of the reliability function. The aggregate measure, D, called composite desirability, is the
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geometric mean of p individual desirabilities, dµi:
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D=dµ1 dµ2 …dµp
1/p
(6).
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3. Results
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In order to compare the different dissolution profiles of the experimental runs with the
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reference tablet profile (Fig. 1), the methods proposed are the dissolution similarity factor f2
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(Eq.1) and the Dissolution Area Difference (DAD) (Eq. 3).
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Figure 1 shows that time point t = 15 min marks the boundary between two areas of
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dissolution, one of rapid and one of slow change. Dissolution of the reference drug follows a first
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order kinetics equation and is simulated with Matlab software as
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dt=a+b*ek*t
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, where d is the drug percent dissolved at time t, a = 91.05, b = -91.29, k = -0.57 and the
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(7)
goodness of fit is R2 = 0.987.
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In evaluating the integral of DAD according to the trapezoidal rule, the time point t =15 min
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which marks the boundary between the two rapidly and slowly changing dissolution areas, is
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selected as the last point in the first trapezoidal segment. The results are shown in Table 2. The
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calculated similarity factors f2_15 and f2_60 for times of 15 and 60 min, respectively, are presented
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in Table 3.
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The response variables selected for the dissolution profile evaluation in the following DOE
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analysis are f2_15 and f2_60. The data range and specifications are presented in Table 4, where
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weight and hardness limits are calculated as ±2.5% of the target value, and the ideal case of
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100% is selected as the target value for the similarity factor. It should be noted that in Eq. 8, the
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mass fractions x1, x2 and x3 are expressed in mixture proportions, a fact that enables the scale-up
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to pilot and production levels.
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Regression generates the following models:
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weight = 314.293*x1 +309.056*x2 +315.642*x3 -2.811*x1 *x2
(8a)
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hardness = 17*x1 +10.73*x2 +359.87*x3 +588.22*x1 *x2
(8b)
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f2_15 = -296.78*x1 -195.01*x2 +753.42*x3 +1076.85*x1 *x2
(8c)
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f2_60 = -208.94*x1 -110.04*x2 +646.15*x3 +755.41*x1 *x2
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The optimization plot for the response variables and desirability is given in Figure 2. An
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optimum exists for x1 = 38.66 mg (0.4444 coded), x2 = 38.66 mg (0.4444 coded) and x3 = 9.67
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mg (0.1111 coded).
(8d)
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In addition to graphical representation of the overlapping common region of successful
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operating ranges (Fig. 3), the Design Space can be supplemented by a tabular form, where the
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boundaries (l: lower specification limit-LSL and u: upper specification limit-USL, Table 5) and
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the composite desirability (Eq. 6, Table 6) are determined by Mixture Design Analysis and
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Bayesian method. In Figure 3, the white area represents the “external” DS, while the purple area
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is the DS limited by the restriction of the x3 amount, ranging from 2 to 5%. The effectiveness of
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the various methods, in determining the DS, as measured by the composite desirability, is shown
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in Table 6.
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4. Discussion
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For the dissolution evaluation, the results of DAD in Table 2 and of the similarity factors f2_15
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and f2_60 for times of 15 and 60 min in Table 3, both agree that run 2 seems to exhibit the best
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similarity to the original dissolution profile. Additionally, the optimum component amounts
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presented in Figure 2 are close to the optimum experimental conditions suggested by the f2 and
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DAD factors in run 2 of the mixture experiment.
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Finally, in Table 5, the effectiveness of the three methods is evaluated. The Mixture Design
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Analysis has a higher composite desirability than the Bayesian method, but the difference is not
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decisive to preclude the use of the latter when data uncertainty is considered. It should be noted
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that the values of composite desirability are limited by the setting of f2 target value at the
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maximum 100%, which is a rather ideal condition. Both methods perform very satisfactory even
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under this condition.
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5. Conclusions
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An earlier developed methodology of DS determination from experimental data, with and
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without uncertainty, obtained for this purpose, was applied to a generic oral drug with CQAs
258
tablet weight and hardness and bioequivalence of product (generic) and reference (original) drug,
259
and CMAs the mass fractions of the excipients. A Mixture Design of experiments was carried
260
out and analyzed to enable development of a multi-regression model with factors the CMAs and
261
responses the CQAs.
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Bioequivalence, which involves comparison of dissolution profiles of product and reference
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drugs on multiple time points, was assessed by evaluating two integral measures, similarity and
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DAD factors, at two times, the critical time, which marks the boundary between rapid and slow
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dissolution, and the final time at which dissolution ceases.
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As in an earlier work of ours, the DS was determined by response optimization and
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overlapping responses. Multi-response optimization leads to a DS with boundaries in the
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neighborhood of optimal conditions, while the method of overlapping responses leads to a DS
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with boundaries corresponding to global lower and upper specification limits of the response
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variables. The optimal component amounts calculated by these methods are the closest to the
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optimal experimental conditions suggested by evaluation of the similarity and DAD factors, a
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fact that validates the multivariate analysis performed and the adequacy of dissolution criteria
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selected.
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The effectiveness of the methods used for determination of the DS for the generic oral drug of
275
interest is measured by composite desirability, which is higher for multi-response method.
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However, if data uncertainty is to be accounted for, the Bayesian method shows a better
277
performance. Finally, it should be noted that the resulting optimal amounts should be replicated
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at laboratory and pilot scales in order to validate scale-up.
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AUTHOR INFORMATION
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Corresponding Author
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* Tel.: +30-210-7723125. Fax: +30-210-7723163. E-mail:
[email protected] 283 284
ACKNOWLEDGMENT
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The authors acknowledge the financial support to Ms. Kalliopi Chatzizacharia, PhD Candidate
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in Chemical Engineering, in the form of a scholarship from the National Technical University of
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Athens.
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ABBREVIATIONS
289
API Active Pharmaceutical Ingredient; DOE Design of Experiments; DS Design Space; CQA
290
Critical Quality Attributes ; QbD Quality by Design; CMA Critical Material Attributes; CPP
291
Critical Process Parameters; BCS Biopharmaceutics Classification System; EMEA European
292
Medicines Agency; FDA USA Food and Drug Administration; ANOVA Analysis of Variance;
293
DAD Dissolution Area Difference; LSL lower specification limit; USL upper specification limit
294
REFERENCES
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(1)
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Dekker Inc, 1999.
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(2)
ICH (European Medicines Agency). Q8 (R2) Pharmaceutical Development; 2009; Vol. 8.
298
(3)
Hayashi, Y.; Kikuchi, S.; Onuki, Y.; Takayama, K. Reliability Evaluation of Nonlinear
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Design Space in Pharmaceutical Product Development. J. Pharm. Sci. 2012, 101, 2.
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100 90
% drug dissolved
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reference drug
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run2
60
run4
50
run5
40 30
run1
20
run6
10
run3
0 0
10
20
30
40
50
60
t (min) Figure 1. Experimental dissolution profiles graph
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Figure 2. Mixture Design Optim mization plot
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Figure 3. Design Spaace for the Mixture Desiign experimeent
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API x1, Excipient 1 x2, Excipient 2 x3, Excipients 3,…,n
Tablets CMAs x1, x2, x3
Design Space
Specification CQAs Space Weight Hardness Dissolution: f2_15 , f2_60
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