Continuous Manufacturing: Excipients and Continuous Manufacturing

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 Continuous Manufacturing: Excipients and Continuous Manufacturing
Chris Moreton 
FinnBrit Consulting


Continuous manufacturing of pharmaceutical finished products is now a reality. At this time, pharmaceutical companies are using continuous processes to manufacture four drug products licensed in the US and Europe. They are all solid oral dosage forms (SODFs). One drug product was a conversion from a batch process; the other three used continuous methods from the outset. 

In principle, you can apply continuous manufacturing to most types of pharmaceutical dosage forms, but you have to make a product in sufficient volume to justify the investment. It isn’t surprising that most interest lies in SODFs, because they are the most common formulation types and are typically manufactured in large quantities. 

Continuous manufacturing is a logical extrapolation from the combination of process analytical technology (PAT) and quality-by-design (QbD) in pharmaceutical development and manufacturing. Certainly, it’s difficult to imagine achieving the successful development of a continuously manufactured tablet or capsule without the enhanced understanding required under QbD and the enhanced monitoring capabilities from the proper implementation of the necessary PATs. 

Continuous manufacturing imposes different constraints on available excipients compared to conventional batch manufacturing and requires a better understanding of why the excipients work and what is important for their functionality and performance. This article attempts to provide some indications of the types of understanding that may be important.

Batch versus continuous manufacturing 

The logical first step is to consider the differences between batch and continuous SODF manufacturing. For example, consider an immediate-release tablet formulation. (Similar considerations would apply to immediate- release powder-filled hard capsules.)

In batch manufacture of a tablet formulation, you process predetermined quantities of API and excipients together in a single unit operation, which you complete in its entirety before passing to the next unit operation. You have a predetermined batch size and theoretical yield. Some of your unit operations may be inherently continuous, such as sieving, milling, and tablet compression, but you typically carry out blending and wet-granulation on the entire batch at once. In continuous manufacturing at a quasi-steady state, all unit operations are occurring simultaneously. As you continuously feed the API and excipients into the equipment train, you produce tablets and remove them from it. 

Each type of processing has advantages and disadvantages. For example, if some catastrophic failure occurs in batch processing, you may lose the whole product batch, while in continuous manufacturing, a catastrophic failure may cause you to lose only part of the batch1. In truly continuous operations, operator intervention isn’t possible if you need to accommodate variations in component properties, such as end-point detection in wet granulation or dry blending. If the process requires an intervention, you must consider some form of hybrid approach, in which you run a particular unit operation in batch mode and then convert the process train back to continuous mode again. An even better option would be to engineer the variability out of the formulation and/or process. Another advantage of continuous manufacturing is that it allows for real-time release testing (RTRT), when combined with an appropriate set of PAT sensors and controls, which saves on costly post-process testing. Constraints on adoption of continuous manufacturing 

Again, in truly continuous manufacturing operations, the opportunity for operator intervention and/or processing to an end point is nonexistent unless you implement such controls using a hybrid approach, which isn’t optimal. Continuous manufacturing requires you to resolve other issues as well, including: 

  • Determining how to meter low-dose and veryfine materials, including highly potent APIs (HPAPIs) and excipients present at low levels in the formulation, such as lubricants, glidants, and possibly disintegrants.
  • Understanding the variability of the critical material attributes (CMAs) of the excipients and/or APIs and determining how this variability impacts the drug product’s critical quality attributes (CQAs). The CMAs may include some properties in the pharmacopeial monograph specification but will likely also include additional physical or chemical characteristics. As with any drug product development process, whether batch or continuous, you must also address other factors, such as bioavailability, manufacturability, and the chemical and physical stability of both the API and the dosage form, among others. Routinely manufacturing an acceptable finished drug product requires: 
  • Creating segregation resistance in the final blend, even for continuous direct-compression processes. This involves adequately dispersing the API throughout the blend to achieve both content uniformity and bioavailability—particularly for some poorly water-soluble APIs—and maintaining that dispersion until manufacture of the final unit dose (by forming an ordered mixture, for example, in which the blend components adhere to each other to form ordered units); 
  • Ensuring the flowability of the final powder blend into the tablet die or through the capsule dosing mechanism to achieve acceptable weight and content uniformity; and 
  • Ensuring the compactibility of the final blend for tableting or consolidation during encapsulation. 

Excipients and continuous manufacturing 

Excipients will play an important role in the transition to continuous pharma manufacturing, and the industry can facilitate that transition by encouraging progress in the following areas: 

  • Improved understanding of the excipients currently in use; 
  • Creation of new grades of existing excipients; 
  • Development of new co-processed excipients; and 
  • Development of new chemical excipients. 

Improved understanding of current excipients

Formulators should consider using excipient-characterization methods beyond the methods in the pharmacopeia monograph and the traditional functional-assessment methods, such as compaction of powder blends to assess lubricant performance. This may involve using analytical methods not traditionally associated with excipient characterization. 

For example, Delaney et al. used solid-state 13C-nuclear magnetic resonance (SS 13C-nmr) and other characterization methods to investigate magnesium stearate from different commercial sources and were able to show that at least three, and possibly four, types of magnesium stearate were commercially available2. The data also suggested that a batch-to-batch variability can exist in magnesium stearate from the same supplier.

Pharmaceutical manufacturers have long recognized that magnesium stearate is a problematic excipient. Can the variability found by Delaney et al. explain at least some of the performance variability seen with magnesium stearate? Applying other spectroscopic methods, such as near infra-red (NIR) and Raman spectroscopy, to excipients on a regular basis may further enhance our knowledge of their characteristics and variability. 

Creation of new grades of existing excipients

As discussed previously, continuous manufacturing puts additional constraints on excipients. It might not be possible to overcome these constraints using existing excipients and grades. Excipient suppliers may be able to develop new excipient grades to meet the needs of continuous or other advanced manufacturing methods, but only so much leeway exists within an excipient’s monograph definition and specification. Potential users may be reluctant to use excipients that exceed those bounds, since revising a pharmacopeia monograph takes time. Many companies prefer to use materials that comply with the monograph because the regulatory filing is more straightforward.

Development of new co-processed excipients

Co-processing has great potential to solve many problems related to continuous pharmaceutical manufacturing and/or other advanced manufacturing technologies. Co-processed excipients can provide functionalities and performance that non-co-processed excipients most likely won’t be able to achieve. Co-processing may also be a means to incorporate excipients at low levels without requiring an extra feeder and/or avoiding the problems associated with metering poorly flowing materials. 

For example, using the co-processed excipient silicified microcrystalline cellulose (SMCC) is a convenient way to add colloidal silicon dioxide to the continuous manufacturing train while simultaneously enhancing direct-compression carrying capacity or post-wet-granulation compactibility compared to adding the individual components separately. This concept of ease of addition of low-concentration excipients could possibly be extended to other materials, such as lubricants, surfactants, and disintegrants, and even to APIs. 

Other co-processed excipients are available that may find application in continuous manufacturing. Functionalities and/or performance characteristics for which co-processing may provide the solution could include improved blend-segregation resistance; improved compaction for both direct-compression and wet-granulation applications; and improved hot-melt processing.

A disadvantage of new co-processed excipients is that they don’t have pharmacopeia monographs and require a safety/toxicology assessment. However, if you can demonstrate that no new covalent compound forms, you can bridge this assessment back to the individual components. This is less desirable than being able to simply declare that the excipient is a compendial material, but it’s a lot more straightforward than introducing an entirely new chemical excipient (see the following section). The disadvantage of not having a pharmacopeia monograph may be more than offset by the enhanced functionality and performance compared to a new grade of an existing excipient. 

Pharmaceutical manufacturers have long recognized that magnesium stearate is a problematic excipient. Can the variability found by Delaney et al. explain at least some of the performance variability seen with magnesium stearate? Applying other spectroscopic methods, such as near infra-red (NIR) and Raman spectroscopy, to excipients on a regular basis may further enhance our knowledge of their characteristics and variability. Creation of new grades of existing excipients. As discussed previously, continuous manufacturing puts additional constraints on excipients. It might not be possible to overcome these constraints using existing excipients and grades. Excipient suppliers may be able to develop new excipient grades to meet the needs of continuous or other advanced manufacturing methods, but only so much leeway exists within an excipient’s monograph definition and specification. Potential users may be reluctant to use excipients that exceed those bounds, since revising a pharmacopeia monograph takes time. Many companies prefer to use materials that comply with the monograph because the regulatory filing is more straightforward.

Development of new chemical excipients

Finding entirely new chemical excipients is the least appealing option for developing excipients for continuous manufacturing. The uncertainty regarding a new chemical excipient’s ultimate regulatory acceptance makes pharmaceutical manufacturers very reluctant to risk a new potential blockbuster drug product on the new chemical excipient. Only five new chemical excipients that have entered the market in the last 30 years or so are currently being used in commercial pharmaceutical products. 

This trend is likely to continue for the foreseeable future. In the absence of an independent assessment by regulatory authorities, acceptance of a new chemical excipient requires an overwhelming technical need that can’t be met by existing excipients. Presently, this doesn’t seem likely for continuous manufacturing. 

Conclusions 

Formulators need to be aware that differences likely exist in the constraints on excipients between batch and continuous processing in the manufacture of finished drug products. It seems likely that conventional, single- component excipients and grades won’t be able to provide all the answers. Of the alternatives discussed, new co-processed excipients seem to have the most promise to solve some of the challenges of continuous manufacturing, such as metering low-dose components and improved blend-segregation resistance. 


References 

1. US Department of Health and Human Services, Food and Drug Administration, Center for Drug Evaluation and Research (CDER). Draft Guidance for Industry: “Quality Considerations for Continuous Manufacturing,” February 2019. 

2. Delaney et al. “Characterization of synthesized and commercial forms of magnesium stearate using differential scanning calorimetry, thermogravimetric analysis, powder x-ray diffraction and solid-state NMR spectroscopy.” J Pharm Sci. 2017; 106(1):338-347. 


Chris Moreton is partner and vice president of pharmaceutical sciences at FinnBrit Consulting, Waltham, MA (www.fin nbrit.com). Ink Viscosity and Cleaning Systems Available on All Models Printing Inspection Systems SAT’s, FAT’s, and IQ’s/OQ’s Machines are FDA and EU Compliant Over 138 Years Experience Manufactured in the USA Global Support & Service TABLET, CAPSULE, AND SOFTGEL PRINTING MACHINES Trusted by Hundreds of Companies in Over 40 Countries Worldwide IBM MACHINE Our high-speed printer’s mark your soft-gels, capsules, and tablets with pinpoint precision. With vision inspection to ensure accuracy, single tablet rejection, and out put rates of up to 500,000 units per hour, identifying your products has never been easier. Contact Us Today! 215-969-9190 info@rwhartnett.com k_


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