Optimising coating process parameters and formulation concepts for functional taste-masking during continuous manufacturing

Published: 15-Jul-2022

This article describes work done to optimise the coating process parameters (spray rate, inlet air temperature, inlet airflow), formulation and functionality of a taste-masking coat for oral solid dosage forms during continuous production

Continuous manufacturing (CM) is a major trend in today’s pharmaceutical industry. Short development times and technological flexibility paired with cost-efficiency during development and production, as well as the creation of constantly high-quality dosage forms, are some of the main reasons for this initiative.1

One key element in CM is the integration of unit operations such as blending, granulation, tableting and film coating. In particular, the coating process needs to be optimised to allow for shorter process cycles without compromising on coating quality.

From a Quality by Design (QbD) perspective, coating functionality and uniformity are potential Critical Quality Attributes (CQAs). Consistently, these parameters require special attention, particularly with respect to polymers affecting drug release; any variation in coating uniformity might result in a deviation from the expected drug release pattern.2

One such example is the use of functional film coating polymers to mask the taste of oral solid dosage (OSD) forms. Taste-masking is typically employed to overcome the bitter or unpleasant flavour of an active pharmaceutical ingredient (API), leading to higher patient compliance and acceptability.

A methyl methacrylate (MMA) and diethylaminoethyl methacrylate (DEAEMA) copolymer (Kollicoat Smartseal) has been designed for such applications (Figure 1). The cationic polymer is insoluble in water at neutral or basic pH values to ensure effective taste-masking in the saliva. At pH values below 5.5 (such as in the patient’s stomach), it dissolves readily, allowing for immediate release of the active.3

Optimising coating process parameters and formulation concepts for functional taste-masking during continuous manufacturing

Figure 1: Structure of Kollicoat Smartseal, a methyl methacrylate (MMA) and diethylaminoethyl methacrylate (DEAEMA) copolymer

Materials and methods

Tablet cores used for the coating trials were composed of 74.0% Ludipress LCE (coprocessed lactose and povidone), 5.0% Kollidon CL-F (crospovidone, type B), 5.0% Kollidon VA 64 (copovidone), all from BASF, 15.5% caffeine anhydrous 0.2–0.5 (Siegfried) and 0.5% magnesium stearate (Baerlocher).

The taste-masking functionality was to be delivered by different grades of Kollicoat Smartseal: Kollicoat Smartseal 30 D is a low-viscosity aqueous dispersion of MMA and DEAEMA, whereas Kollicoat Smartseal 100 P represents a spray dried powder grade of the polymer.

Three different formulation strategies based on the same polymer were used: formulations containing Kollicoat Smartseal 30 D, Kollicoat Smartseal 100 P (spray dried powder grade, redispersed) and organic solutions of Kollicoat Smartseal 100 P were assessed using a GEA Coater (Figure 2).

Optimising coating process parameters and formulation concepts for functional taste-masking during continuous manufacturing

The slightly alkaline, milky white dispersion of Kollicoat Smartseal 30 D was directly formulated with additional excipients (Table I) and applied to the caffeine tablets. In contrast, the powder grade Kollicoat Smartseal 100 P had to be redispersed in water by adding an organic acid (succinic) before being used.

Figure 2: Design of the GEA Coater used in this study

All aqueous formulations required a plasticiser to reduce the minimum film forming temperature (MFFT) of the polymer (~57 °C) and to decrease the brittleness of the film formed.

When selecting a plasticiser, it’s important to consider that some (such as citric acid esters) are prone to hydrolysis in alkaline aqueous environments and may cause the formation of free acid, counteracting the functionality of the cationic polymer.4 In view of this and because of its wide acceptance in the pharmaceutical industry, tributyl O-acetylcitrate (ATBC) was selected for this study.

The lipophilic antioxidant, butylated hydroxytoluene (BHT), was used to stabilise the amino ester moiety of the polymer and thereby avoid any potential yellowing of the film coating with time. Further excipients such as antisticking agents (talc) or colourants (Ponceau 4R HC) were used as listed in Table I.

Organic solutions of Kollicoat Smartseal 100 P were prepared with an acetone-isopropanol mixture (1:1). As the film forming mechanism of a polymer dispersed in water and the film forming mechanism of dissolved polymer is fundamentally different, the need for a plasticiser and other additives had to be tested. Organic Kollicoat Smartseal solutions were tested with the respective formulations (F5–7).

Optimising coating process parameters and formulation concepts for functional taste-masking during continuous manufacturing

All seven formulations were applied with a solid matter content (SMC) of 20%. Additionally, the aqueous formulations F2 and F3 were coated with an SMC of 30%. Three kilograms of uncoated tablets were fed into the fully perforated coating wheel of the GEA Coater.

Several spray rates (45–120 g/min) were applied at inlet air temperatures ranging from 45–70 °C and inlet air volumes between 200 and 250 m3/h. Samples of the caffeine tablets were taken at 1, 2, 3, 4, 5, 6, 7 and 8 mg/cm2 coating levels.

The aqueous coating formulations (F1, F2 and F3) contained 0.4% Ponceau 4R HC 70% E124, which was used as a visual tracer to determine the amount of coating applied per tablet. This colourant has a high specific absorption rate in the UV/VIS spectra at 509 nm, whereas the other components in the formulation didn’t interfere with the determination of the colourant.

Samples (n=5) of these tablets were dissolved individually in 200 mL of 0.08 N HCl solution. As the polymer is not soluble in water, but dissolves readily in acid media (pH 5.5 or lower), an 0.08 N HCl solution was chosen for sample preparation.

These samples were passed through a 0.45 µm syringe filter (PVDF or PTFE) and then measured in an Agilent 8453 UV/VIS spectrometer equipped with a 1 cm cuvette. Ponceau 4R HC signals (wavelength 509 nm) could be directly linked to the amount of coating applied.

Owing to its insolubility in acetone/isopropanol, Ponceau 4R HC could not be incorporated as a tracer into the solvent-based formulations (F5 and F7). The amount of applied coating on these tablets was determined by atomic absorption spectrometry (AAS) (ICP-OES Agilent 5100 SVDV) instead.

In addition to the quantification of the coating level on the tablets (content uniformity), the homogeneity of the applied coat (uniformity of thickness) was evaluated. This was done by the visual inspection of scanning electron microscopy (SEM) micrographs.

A standard USP Dissolution Apparatus 2 (Paddle) from ERWEKA, equipped with continuous online UV measuring (Agilent 8453), was used for the dissolution testing. As taste-masking functionality targets the saliva of the oral cavity, phosphate buffer (pH 6.8) was used as the dissolution medium (700 mL ±1%, 37°C ±0.5 K, n=3).

The criterion for a functional coat was that no drug release (±1%) was detected for a period of >30 minutes. HCl buffer (pH 1.1) was used to test the immediate release character of the taste-masked tablets (700 mL ±1%, 37°C ±0.5 K, n=3).

Results

Using just a single spray nozzle, process cycles of less than 10 minutes were achieved to coat the 3 kg batch at up to levels of 8 mg/cm2. Considering the high spray rates possible with the GEA Coater, even small sampling time variations led to applied coating level deviations.

Still, comparing the applied amount of polymer per tablet within one batch, standard deviations of ±0.1–0.4 mg/cm2 were deemed to be acceptable (n=5). Generally, higher coating levels showed lower relative standard deviations.

At the maximum tested weight gain of 8 mg/cm2, a relative standard deviation of 2–7% was found among all tested formulations. Reducing the spray rate had no effect on coating uniformity, neither did increasing the inlet air volume. A temperature of 70 °C is recommended, especially at coating levels of less than 3 mg/cm2.

The coating uniformity of single tablets is shown in Figure 3. Similar film thicknesses were found on top of the curvature and around the edges, even at low coating levels.

Optimising coating process parameters and formulation concepts for functional taste-masking during continuous manufacturing

Figure 3: Cross-section of tablets with a Kollicoat Smartseal 30 D coat (F2) of 3 mg/cm², applied using a GEA Coater

Of note, an aqueous Kollicoat Smartseal 30 D based formulation (F2) required a coating level of approximately 4 mg/cm2 to ensure full taste-masking functionality for more than 30 minutes (Figure 4).

In contrast, a redispersed Kollicoat Smartseal 100 P formulation (F3) required a distinctly higher coating level to meet the same criterion. Organic solutions of Kollicoat Smartseal 100 P provided taste masking functionality even below 3 mg/cm2, outperforming both the other formulation concepts.

Optimising coating process parameters and formulation concepts for functional taste-masking during continuous manufacturing

Figure 4: Amount of drug released after 30 minutes in phosphate buffer (pH 6.8), depending on formulation concept and coating level: Kollicoat Smartseal 30 D (F2), redispersed aqueous Kollicoat Smartseal 100 P (F3) and an organic Kollicoat Smartseal formulation (F5) (mean value [n=3])

All aqueous formulations were sprayed with 20% and 30% solid matter content (SMC), enabling a comparison of the two formulation approaches at different SMCs. Any difference in functionality between 20% and 30% SMC was negligible for each aqueous formulation. Consistently, the process could be further optimised by selecting higher SMCs to deliver full taste-masking functionality in a shorter cycle.

Discussion

The application of Kollicoat Smartseal based-formulations to tablet cores in a GEA Coater led to a uniform coating layer, independent of the tested parameter or formulation. This was proven for the applied amount of polymer per tablet within a batch, as well as for the coating layer around the individual tablet (SEM).

Any differences between the actual and the target coating level can be attributed to (expected) spray loss and the sampling procedure.

Authors: Ivan Bogaerts, Leslie Van Eeckhout, Frederik Detobel and corresponding GEA author, Troels Pedersen; Thorsten Agnese, Florian Bang and corresponding BASF author, Nils Rottmann

As the spray rate had no impact on the intra-batch uniformity of the applied coating, higher spray rates could be applied to optimise the process time. As a higher inlet air volume didn’t allow for faster spray rates, an inlet air volume of 200 m3/h is recommended for the trials done in this study. Less air consumption contributes to energy and cost savings, and reduces the process’s environmental impact.

All the tested formulations delivered full taste-masking functionality as per the predefined criterion of >30 minutes coating stability in phosphate buffer (pH 6.8). However, differences in performance of the three formulation concepts were seen, particularly regarding the amount of coating required.

Organic formulations showed the best performance and may be the preferred option for moisture-sensitive APIs. Aqueous formulations based on the Kollicoat Smartseal 30 D dispersion showed better taste-masking capacities compared with the redispersed Kollicoat Smartseal 100 P at lower coating levels.

This was not unexpected as Kollicoat Smartseal 100 P needs to be partially neutralised to be redispersed. The succinic acid used to do this increased both the hydrophilicity and solubility of the cationic polymer slightly because of salt formation.

Conclusion

Short coating cycles, achieved without compromising coating quality, are a prerequisite in CM. Testing a series of taste-masking formulations in a GEA Coater led to robust processes that delivered high levels of coating uniformity and functionality. Neither altered spray rates nor variations in inlet air quantity affected the coating uniformity within the ranges tested.

To guarantee the best performance of the functional coating, a sufficiently high temperature was required. Varying the SMC had no influence on taste-masking functionality; an SMC of 30% ensures economic processing.

Organic solutions of Kollicoat Smartseal 100 P showed the best taste-masking performance at a coating level of less than 3 mg/cm2. As such, organic coating formulations are recommended if a minimum coating level is desired that doesn’t compromise the taste-masking performance.

If organic coating is not an option (owing to safety or equipment constraints), aqueous dispersions of Kollicoat Smartseal 30 D provide an appropriate alternative (at a slightly higher coating level). Partially neutralised, redispersed Kollicoat Smartseal 100 P needs a markedly higher coating level to deliver the same taste-masking performance (compared with a dispersion or organic solution).

Depending on the rate of release in saliva and on the amount of applied coating, aqueous formulations of the powder grade may still be viable.

References

  1. www.pharmaceuticalprocessingworld.com/the-benefits-of-continuous-manufacturing/.
  2. T. Agnese, et al., “Developing a Photometric Method to Determine the Amount of Film-Coating Material Applied Onto Individual Tablet Cores,” poster presented at the 3rd PharmSciFair (13–17 June 2011, Prague, Czech Republic).
  3. K. Kolter, et al., “Physicochemical Characteristics of a New Aqueous Polymer,” AAPS Annual Meeting and Exposition (14–18 November 2010, New Orleans, LA, US).
  4. F. Bang, et al., “Evaluating the Different Characteristics of Plasticisers Used in Cationic Polymer-Based Film-Coating Applications,” 3rd Conference on Innovation in Drug Delivery (22–25 September 2013, Pisa, Italy).

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