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PHARMACEUTICAL AEROSOLS – ENHANCING THE METERED DOSE INHALER


  Dr. John Green, Dr. Erik Gommeren – DuPont Central Research & Development
            Joseph Creazzo, Dr. Keith Palmer – DuPont Fluoroproducts


INTRODUCTION

        Pharmaceutical aerosols have been playing a crucial role in the health and
well being of millions of people throughout the world for many years. These products
include pressurized metered dose inhalers (MDIs), dry powder inhalers (DPIs),
nebulizers, sublinguals, skin sprays (coolants, anesthetics, etc.) and dental sprays.
The technology’s continual advancement, the ease of use, and the more desirable
pulmonary-rather-than-needle delivery for systemic drugs has increased the
attraction for the pharmaceutical aerosol in recent years.

        Since the mid 1950s, aerosol forms of pharmaceuticals have played an
important role in treating respiratory illnesses such as asthma and chronic obstructive
pulmonary disease (COPD), and MDIs and DPIs have become an important part of
that treatment. But administration of drugs by the pulmonary route is technically
challenging because oral deposition can be high, and variations in inhalation
technique can affect the quantity of drug delivered to the lungs. Therefore, there have
been considerable efforts to provide more efficient and reproducible aerosol systems
through improved drug delivery devices and through better formulations that disperse
more readily during inhalation.

        Traditionally most pharmaceutical aerosols have been propelled with
chlorofluorocarbons (CFCs), but current global regulations require pharmaceutical
aerosols to be reformulated to contain non-ozone-depleting propellants. In the
process of reformulation for this transition, there is the opportunity to improve today’s
pulmonary delivery technology and to create new systems to treat a wide array of
infirmities and afflictions.

         Alternatives to CFC propellants must satisfy many other criteria in addition to
environmental acceptability. Most importantly, they need to have acceptable toxicity
profiles given their use in the delivery of medicaments. For the sake of patient safety,
it is also important that they are nonflammable. Finally, their physical properties must
allow workable formulations within the available technology. The two current
alternatives to CFC propellants for pharmaceutical aerosols are hydrofluorocarbon
(HFC) 134a (also known as hydrofluoroalkane (HFA) 134a or 1,1,1,2-
tetrafluoroethane), and HFC-227ea (HFA-227ea or 1,1,1,2,3,3,3-
heptafluoropropane).

       While HFCs are more environmentally friendly compounds, eliminating
chlorine from these molecules has added a significant solvency challenge.



                                                                                       1
Addressing these reduced solvency characteristics has been a major element
of pharmaceutical reformulation programs for replacing CFCs and has amplified the
need for new technology.

       The lower solvency of the pharmaceutical HFC fluids, by comparison with their
CFC predecessors, is not easily overcome; it is an even tougher technical hill to climb
since the group of FDA acceptable solubility enhancing excipients is relatively small.
So, with the advent of HFC propellants, recent attention has turned more and more to
suspension MDIs.

        In a suspension MDI, the drug is relatively insoluble in the propellant and
hence drug particles are maintained as a slurry inside the can. While the drug
substance itself is usually more chemically stable in the solid-state than in the
dissolved-state, there are still quite complex dispersion and device related challenges
in formulating a stable microcrystalline suspension MDI. In particular, for suspension
MDIs, the interfacial chemistry of the suspended drug particles tends to be a
dominating factor. Surfactants are required to disperse the particles in their
biologically preferred aerodynamic size of 1–5 microns. In many instances, the
surfactants that are permissible for inhalation drug formulation are better suited to the
interfacial chemistry of CFC products, and there is a lengthy road to approval of new
surfactants. Hence, the formulator’s task is constrained to reformulations with the
standard CFC MDI surfactants, and therefore has had to look for assistance in other
technology. Some of this technology has come via new developments in aerosol
valves and can coatings to cope with the challenges of metering small precise
volumes of slurries, which are more prone to block the orifice of a metering valve and
lead to poor dose uniformity. This article discusses a research program that DuPont
began recently to assist pharmaceutical formulators with developing suspension
MDIs based on HFCs. The concept of this research has been to better understand
surfactant chemistry and combine that understanding with new processing
techniques that could help provide stable dispersions of asthma medicaments in
liquid HFC propellants.


INTEGRATING CHEMISTRY AND PROCESS

        Recognizing a need for better understanding of the dispersion chemistry, and
that HFC propellant technology alone would not provide a full solution to MDI
reformulation issues, the DuPont Dymel® propellants group sponsored a research
program with the DuPont Particle Science and Technology group. This research
program seeks to tackle HFC reformulation challenges from two aspects:
1. Characterizing the surface interaction between the formulation components, and
2. Introducing process benefits by integrating chemistry with new milling techniques
    to improve HFC dispersions of MDI medicaments.




                                                                                       2
The ultimate goals are:

      •   To use a fundamental understanding, rather than a trial-and-error,
          reformulation approach
      •   Integrate formulation and process development, and
      •   Accomplish HFC performance equivalent to CFC performance in MDIs

Research has proceeded in two phases. The first phase evaluates chemistry of
formulation components with various asthma medicaments. The second phase
advances optimized formulations to processing in a high-pressure media mill.


PHASE 1: FORMULATION CHEMISTRY

In phase 1, experiments were conducted to understand interactions of the basic MDI
formulation components:
• Drug active
• Surfactant
• Co-solvent
• Propellant

In doing so, each formulation component was characterized by certain physical
properties judged to be important to the surface interactions.

The MDI medicaments were characterized by:
• log POW (octanol-water partition coefficient)
• density
• particle size
• surface energy
• morphology

The propellants were characterized by:
• density
• dielectric constant

The surfactants were characterized by:
• head/tail structure
• molecular weight
• chemistry

The following tables summarize characterization properties for the formulation
components that were considered in the program.




                                                                                 3
TABLE 1
           PHYSICAL PROPERTIES FOR THE DRUG ACTIVES

                                                        Critical
                                                                       Particle
                                            Density     Surface
  Drug Active       Log POW      MW                                     Size
                                             (g/cc)     Tension
                                                                        (µm)
                                                        (mJ/m2)
  Budesonide          2.55       431         1.26         29             2.6
   Albuterol
                      0.11       239         1.14         29             15
 (Salbutamol)
Albuterol Sulfate     1.83       409         1.31         36             11
  Ipratoprium
                        -        412         1.37         41              6
    Bromide


                           TABLE 2
           PHYSICAL PROPERTIES FOR THE PROPELLANTS

                                              HFC 134a     HFC 227ea
            Boiling Point           °C          -26.1          -15.6
      Vapor Pressure @ 25°C        Bar           6.7           4.5
      Liquid Density @ 25°C        g/cc          1.2           1.4
        Dielectric Constant          -           9.5           4.1
          Dipole Moment             D            2.1           0.9


                         TABLE 3
     PHYSICO-CHEMICAL PROPERTIES FOR THE SURFACTANTS

          Head Group          Tail Group           Surfactant
            Acidic             Aliphatic           Aerosol OT
              EO              Fluorinated         Zonyl® FSO
              EO                 PPO            Pluronics® 25R4
             Basic            Fluorinated          Zonyl® UR
            Acidic                EO
             Basic               PPO            Propomeen T/12
             Basic               PPO              Armeen 12D
             Basic                EO            Ethomeen C/15
            Acidic            Fluorinated         Zonyl® FSD
              EO               Aliphatic          Neodol 25-7
              EO                  EO


                                                                                  4
Using these characteristic properties, a matrix of test formulations was
                               developed to evaluate different component combinations at different concentrations.
                               The test formulations were prepared in glass aerosol bottles and evaluated for the
                               optimum dispersion stability using two methods to allow rapid screening of a large
                               number of samples.

                                      The first method was a simple direct visual evaluation to qualitatively rate
                               dispersion stability against a set of yes-no criteria. Promising formulations were then
                               quantitatively evaluated using an internally developed method that measures light
                               transmittance through the dispersion versus time. Measuring light transmittance
                               versus time provides quantitative data that can be mathematically related to
                               dispersion stability. Figure 1 illustrates an example of the data collected.

                                        Figure 1 - Sample of Light Transmittance Data Set
                          25



                          20       B1
Transmittance (L) - lux




                          15



                          10



                          5

                                   B2                                B3          B4
                          0
                               0             10              20             30              40             50            60
                                                                    Time (t) - seconds




                                                                                                                     5
The light transmittance data (L) versus time (t) from agitation is fitted to an
equation (Equation 1), which can be used to design experiments that identify the
optimum combinations for stable dispersions.


                                      B2 − B1
          L = B1 +                                                ( Equation 1 )
                             1 + e B3 ∗(log t -log B4)
        Coefficients B1 through B4 describe parameters of the L versus t curve. B2
describes the fully dispersed state immediately after shaking and B1 describes the
final equilibrated state after a long period of time. B4 is the time for the L to reach
halfway between B1 and B2. And B3 is the slope of the L versus t curve at B4.

        Using this relationship, experiments can be designed to identify formulations
that exhibit optimum parameters for stable dispersions. In this way, a large number of
combinations can be evaluated for the optimum chemistry. Optimum formulations
identified in phase 1 are carried forward to phase 2, to evaluate impact of process.


PHASE 2: PROCESSING

        Slurry media milling is an important unit operation in various industries for fine
and ultra-fine grinding of materials, like minerals, paints, inks, pigments, food,
agricultural products and pharmaceuticals. In these mills, the feed material particles
are reduced in size between a large number of small grinding media that are usually
sand, plastic, glass, steel, or ceramic beads. Internal agitation, coupled with very
small grinding media and the liquid medium, produce sub-micron or nano-size
particles.

       The specific media milling processing developed for this research was
designed to operate at high pressures, allowing preparation of dispersions using the
propellant itself as the milling medium. This high-pressure media milling (HPMM)
process yields stable, fine particle dispersion of medicament in liquid HFC propellant.
The milling is performed with the entire MDI formulation so that surfactants and co-
solvents are available to the drug actives during the milling process. “In-situ” milling is
believed to increase dispersion stability because having the surfactant available
during milling results in improved deposition or adsorption onto the surface of the
medicament particles as they are milled.




                                                                                          6
Figure 2 - Schematic of the High Pressure Media Mill (HPMM)




                                Motor and
                                  drive



                                                        Circulation
        Flow Meter                                         and/or
                                                        premix tank


               Agitator

                                              Cooling
HFC
Feedstock
cylinder
                Grinding
                media
                                                             Pump     Collection
                                                 PG
                                                                      cylinder




                                                                              7
A second advantage for HPMM process using HFC propellant as the medium is that,
                              when milling is complete, it is the final formulation that is available. Conceptually, the
                              batch in the mill can be filtered and directly packaged to the MDI container, offering a
                              potential improvement in commercial processing productivity, cost and quality.

                                     The HPMM process produces medicament dispersions in liquefied HFC
                              propellant that are stable for long periods of time and that are easily re-suspended if
                              they do settle. Figure 3 shows the light transmittance data from a prototype
                              budesonide formulation optimized by the interaction studies and processed in the
                              HPMM. Note that the formulation shows some slight initial flocculation, but
                              equilibrates and remains stable for a long period of time. The photographs in Figures
                              4 and 5 show the prototype formulation with and without milling, demonstrating the
                              impact of the HPMM process. Figure 5 is a milled prototype budesonide formulation
                              undisturbed for about 2 weeks.


                                    Figure 3 - Data for Milled Prototype Budesonide Formulation
                          2
Transmittance (L) - lux




                          1




                          0
                              0             50             100             150             200            250              300
                                                                   Time (t) - seconds




                                                                                                                      8
Figure 4 – Unmilled Budesonide Prototype Formulation after 30 minutes




Figure 5 – Milled Budesonide Prototype Formulation Undisturbed for about 2
Weeks




                                                                             9
SUMMARY

        In recent years, much attention and research has been devoted to drug
delivery via the lungs, which enable tremendous mass transfer from the gas phase to
the blood stream. While oral dosage forms are typically preferred by patients, in
many cases they lack efficient bioavailability – especially for newly discovered drugs
that have very low solubility in water. Meanwhile, parenteral products (injectibles) are
least preferred by patients, yet they deliver the highest bioavailability. Aerosol
delivery of drugs via the lung can provide the benefits of both, without discomfort,
efficiently delivering drugs that might otherwise be metabolized before reaching the
intended treatment site. Research efforts, as those described above, continue to
provide opportunities for new patient-friendly treatments using the pressurized MDI
despite the additional challenges from non-medically related issues.


Optional Photographs




                                                                                     10

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Metered dose

  • 1. PHARMACEUTICAL AEROSOLS – ENHANCING THE METERED DOSE INHALER Dr. John Green, Dr. Erik Gommeren – DuPont Central Research & Development Joseph Creazzo, Dr. Keith Palmer – DuPont Fluoroproducts INTRODUCTION Pharmaceutical aerosols have been playing a crucial role in the health and well being of millions of people throughout the world for many years. These products include pressurized metered dose inhalers (MDIs), dry powder inhalers (DPIs), nebulizers, sublinguals, skin sprays (coolants, anesthetics, etc.) and dental sprays. The technology’s continual advancement, the ease of use, and the more desirable pulmonary-rather-than-needle delivery for systemic drugs has increased the attraction for the pharmaceutical aerosol in recent years. Since the mid 1950s, aerosol forms of pharmaceuticals have played an important role in treating respiratory illnesses such as asthma and chronic obstructive pulmonary disease (COPD), and MDIs and DPIs have become an important part of that treatment. But administration of drugs by the pulmonary route is technically challenging because oral deposition can be high, and variations in inhalation technique can affect the quantity of drug delivered to the lungs. Therefore, there have been considerable efforts to provide more efficient and reproducible aerosol systems through improved drug delivery devices and through better formulations that disperse more readily during inhalation. Traditionally most pharmaceutical aerosols have been propelled with chlorofluorocarbons (CFCs), but current global regulations require pharmaceutical aerosols to be reformulated to contain non-ozone-depleting propellants. In the process of reformulation for this transition, there is the opportunity to improve today’s pulmonary delivery technology and to create new systems to treat a wide array of infirmities and afflictions. Alternatives to CFC propellants must satisfy many other criteria in addition to environmental acceptability. Most importantly, they need to have acceptable toxicity profiles given their use in the delivery of medicaments. For the sake of patient safety, it is also important that they are nonflammable. Finally, their physical properties must allow workable formulations within the available technology. The two current alternatives to CFC propellants for pharmaceutical aerosols are hydrofluorocarbon (HFC) 134a (also known as hydrofluoroalkane (HFA) 134a or 1,1,1,2- tetrafluoroethane), and HFC-227ea (HFA-227ea or 1,1,1,2,3,3,3- heptafluoropropane). While HFCs are more environmentally friendly compounds, eliminating chlorine from these molecules has added a significant solvency challenge. 1
  • 2. Addressing these reduced solvency characteristics has been a major element of pharmaceutical reformulation programs for replacing CFCs and has amplified the need for new technology. The lower solvency of the pharmaceutical HFC fluids, by comparison with their CFC predecessors, is not easily overcome; it is an even tougher technical hill to climb since the group of FDA acceptable solubility enhancing excipients is relatively small. So, with the advent of HFC propellants, recent attention has turned more and more to suspension MDIs. In a suspension MDI, the drug is relatively insoluble in the propellant and hence drug particles are maintained as a slurry inside the can. While the drug substance itself is usually more chemically stable in the solid-state than in the dissolved-state, there are still quite complex dispersion and device related challenges in formulating a stable microcrystalline suspension MDI. In particular, for suspension MDIs, the interfacial chemistry of the suspended drug particles tends to be a dominating factor. Surfactants are required to disperse the particles in their biologically preferred aerodynamic size of 1–5 microns. In many instances, the surfactants that are permissible for inhalation drug formulation are better suited to the interfacial chemistry of CFC products, and there is a lengthy road to approval of new surfactants. Hence, the formulator’s task is constrained to reformulations with the standard CFC MDI surfactants, and therefore has had to look for assistance in other technology. Some of this technology has come via new developments in aerosol valves and can coatings to cope with the challenges of metering small precise volumes of slurries, which are more prone to block the orifice of a metering valve and lead to poor dose uniformity. This article discusses a research program that DuPont began recently to assist pharmaceutical formulators with developing suspension MDIs based on HFCs. The concept of this research has been to better understand surfactant chemistry and combine that understanding with new processing techniques that could help provide stable dispersions of asthma medicaments in liquid HFC propellants. INTEGRATING CHEMISTRY AND PROCESS Recognizing a need for better understanding of the dispersion chemistry, and that HFC propellant technology alone would not provide a full solution to MDI reformulation issues, the DuPont Dymel® propellants group sponsored a research program with the DuPont Particle Science and Technology group. This research program seeks to tackle HFC reformulation challenges from two aspects: 1. Characterizing the surface interaction between the formulation components, and 2. Introducing process benefits by integrating chemistry with new milling techniques to improve HFC dispersions of MDI medicaments. 2
  • 3. The ultimate goals are: • To use a fundamental understanding, rather than a trial-and-error, reformulation approach • Integrate formulation and process development, and • Accomplish HFC performance equivalent to CFC performance in MDIs Research has proceeded in two phases. The first phase evaluates chemistry of formulation components with various asthma medicaments. The second phase advances optimized formulations to processing in a high-pressure media mill. PHASE 1: FORMULATION CHEMISTRY In phase 1, experiments were conducted to understand interactions of the basic MDI formulation components: • Drug active • Surfactant • Co-solvent • Propellant In doing so, each formulation component was characterized by certain physical properties judged to be important to the surface interactions. The MDI medicaments were characterized by: • log POW (octanol-water partition coefficient) • density • particle size • surface energy • morphology The propellants were characterized by: • density • dielectric constant The surfactants were characterized by: • head/tail structure • molecular weight • chemistry The following tables summarize characterization properties for the formulation components that were considered in the program. 3
  • 4. TABLE 1 PHYSICAL PROPERTIES FOR THE DRUG ACTIVES Critical Particle Density Surface Drug Active Log POW MW Size (g/cc) Tension (µm) (mJ/m2) Budesonide 2.55 431 1.26 29 2.6 Albuterol 0.11 239 1.14 29 15 (Salbutamol) Albuterol Sulfate 1.83 409 1.31 36 11 Ipratoprium - 412 1.37 41 6 Bromide TABLE 2 PHYSICAL PROPERTIES FOR THE PROPELLANTS HFC 134a HFC 227ea Boiling Point °C -26.1 -15.6 Vapor Pressure @ 25°C Bar 6.7 4.5 Liquid Density @ 25°C g/cc 1.2 1.4 Dielectric Constant - 9.5 4.1 Dipole Moment D 2.1 0.9 TABLE 3 PHYSICO-CHEMICAL PROPERTIES FOR THE SURFACTANTS Head Group Tail Group Surfactant Acidic Aliphatic Aerosol OT EO Fluorinated Zonyl® FSO EO PPO Pluronics® 25R4 Basic Fluorinated Zonyl® UR Acidic EO Basic PPO Propomeen T/12 Basic PPO Armeen 12D Basic EO Ethomeen C/15 Acidic Fluorinated Zonyl® FSD EO Aliphatic Neodol 25-7 EO EO 4
  • 5. Using these characteristic properties, a matrix of test formulations was developed to evaluate different component combinations at different concentrations. The test formulations were prepared in glass aerosol bottles and evaluated for the optimum dispersion stability using two methods to allow rapid screening of a large number of samples. The first method was a simple direct visual evaluation to qualitatively rate dispersion stability against a set of yes-no criteria. Promising formulations were then quantitatively evaluated using an internally developed method that measures light transmittance through the dispersion versus time. Measuring light transmittance versus time provides quantitative data that can be mathematically related to dispersion stability. Figure 1 illustrates an example of the data collected. Figure 1 - Sample of Light Transmittance Data Set 25 20 B1 Transmittance (L) - lux 15 10 5 B2 B3 B4 0 0 10 20 30 40 50 60 Time (t) - seconds 5
  • 6. The light transmittance data (L) versus time (t) from agitation is fitted to an equation (Equation 1), which can be used to design experiments that identify the optimum combinations for stable dispersions. B2 − B1 L = B1 + ( Equation 1 ) 1 + e B3 ∗(log t -log B4) Coefficients B1 through B4 describe parameters of the L versus t curve. B2 describes the fully dispersed state immediately after shaking and B1 describes the final equilibrated state after a long period of time. B4 is the time for the L to reach halfway between B1 and B2. And B3 is the slope of the L versus t curve at B4. Using this relationship, experiments can be designed to identify formulations that exhibit optimum parameters for stable dispersions. In this way, a large number of combinations can be evaluated for the optimum chemistry. Optimum formulations identified in phase 1 are carried forward to phase 2, to evaluate impact of process. PHASE 2: PROCESSING Slurry media milling is an important unit operation in various industries for fine and ultra-fine grinding of materials, like minerals, paints, inks, pigments, food, agricultural products and pharmaceuticals. In these mills, the feed material particles are reduced in size between a large number of small grinding media that are usually sand, plastic, glass, steel, or ceramic beads. Internal agitation, coupled with very small grinding media and the liquid medium, produce sub-micron or nano-size particles. The specific media milling processing developed for this research was designed to operate at high pressures, allowing preparation of dispersions using the propellant itself as the milling medium. This high-pressure media milling (HPMM) process yields stable, fine particle dispersion of medicament in liquid HFC propellant. The milling is performed with the entire MDI formulation so that surfactants and co- solvents are available to the drug actives during the milling process. “In-situ” milling is believed to increase dispersion stability because having the surfactant available during milling results in improved deposition or adsorption onto the surface of the medicament particles as they are milled. 6
  • 7. Figure 2 - Schematic of the High Pressure Media Mill (HPMM) Motor and drive Circulation Flow Meter and/or premix tank Agitator Cooling HFC Feedstock cylinder Grinding media Pump Collection PG cylinder 7
  • 8. A second advantage for HPMM process using HFC propellant as the medium is that, when milling is complete, it is the final formulation that is available. Conceptually, the batch in the mill can be filtered and directly packaged to the MDI container, offering a potential improvement in commercial processing productivity, cost and quality. The HPMM process produces medicament dispersions in liquefied HFC propellant that are stable for long periods of time and that are easily re-suspended if they do settle. Figure 3 shows the light transmittance data from a prototype budesonide formulation optimized by the interaction studies and processed in the HPMM. Note that the formulation shows some slight initial flocculation, but equilibrates and remains stable for a long period of time. The photographs in Figures 4 and 5 show the prototype formulation with and without milling, demonstrating the impact of the HPMM process. Figure 5 is a milled prototype budesonide formulation undisturbed for about 2 weeks. Figure 3 - Data for Milled Prototype Budesonide Formulation 2 Transmittance (L) - lux 1 0 0 50 100 150 200 250 300 Time (t) - seconds 8
  • 9. Figure 4 – Unmilled Budesonide Prototype Formulation after 30 minutes Figure 5 – Milled Budesonide Prototype Formulation Undisturbed for about 2 Weeks 9
  • 10. SUMMARY In recent years, much attention and research has been devoted to drug delivery via the lungs, which enable tremendous mass transfer from the gas phase to the blood stream. While oral dosage forms are typically preferred by patients, in many cases they lack efficient bioavailability – especially for newly discovered drugs that have very low solubility in water. Meanwhile, parenteral products (injectibles) are least preferred by patients, yet they deliver the highest bioavailability. Aerosol delivery of drugs via the lung can provide the benefits of both, without discomfort, efficiently delivering drugs that might otherwise be metabolized before reaching the intended treatment site. Research efforts, as those described above, continue to provide opportunities for new patient-friendly treatments using the pressurized MDI despite the additional challenges from non-medically related issues. Optional Photographs 10