`
`BEFORE THE PATENT TRIAL AND APPEAL BOARD
`
`
`J KYLE BASS and ERICH SPANGENBERG,
`Petitioner
`
`
`
`v.
`
`
`
`FRESENIUS KABI USA, LLC
`Patent Owner
`
`
`Case No. IPR2016-00254
`U.S. Patent No. 8,476,010
`
`
`
`
`EXHIBIT 2036 - DECLARATION OF STANLEY S. DAVIS Ph.D.
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`
`
`
`
`Mail Stop “PATENT BOARD”
`Patent Trial and Appeal Board
`U.S. Patent and Trademark Office
`P.O. Box 1450
`Alexandria, VA 22313-1450
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`
`
`Fresenius Ex. 2036
`Bass et al. v. Fresenius Kabi USA, IPR2016-00254
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`
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`I, STANLEY DAVIS, Ph.D., hereby declare and state as follows:
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`
`1.
`
`I submit this expert declaration at the request of counsel for patentee
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`Fresenius Kabi USA, LLC (“Fresenius”) in the above-captioned matter. My
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`compensation pertaining to this matter is not dependent on the outcome of this
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`matter.
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`I.
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`QUALIFICATIONS AND EXPERIENCE
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`2.
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`I am an Emeritus Professor of Pharmacy at the University of
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`Nottingham, United Kingdom. For over forty years, I have been active in the field
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`of pharmaceutical science. I have taught courses, conducted research, written
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`papers, edited books, and consulted for industry on a wide-range of topics, to
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`include emulsion formulations and their use in drug delivery.
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`3.
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`I am the co-founder of three pharmaceutical companies and the
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`recipient of awards relating to my research. I have authored or co-authored over
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`750 scientific papers and have co-edited seven books relating to the pharmaceutical
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`sciences. I am also a named inventor on several patents in the pharmaceutical area.
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`4.
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`I continue to provide consulting services relating to the development
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`of pharmaceutical formulations and stay abreast of relevant scientific publications.
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`5.
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`I have consulted for various pharmaceutical companies all over the
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`world on matters relating to pharmaceutical formulation, pharmaceutical analysis,
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`processing, scale-up, material science, drug stability, controlled release, and other
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`formulation issues. These companies have included: Abbott, Pharmaceutical
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`Profiles, Hoechst, Alza, Synthelabo Pharma, Pierre Fabre, Jouveinal, Eli Lilly,
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`Glycoform, Aradigm, Gene Medicine, Leopold, ICI Pharmaceuticals (Zeneca),
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`Marion Merrell Dow, Fresenius, Baxter and Arakis. I was also a visiting scientist
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`at Allergan, Syntex and Alza in the United States.
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`6.
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`I graduated from the School of Pharmacy at the University of London
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`in 1964 with a Bachelor’s degree in Pharmacy. I continued my studies at the
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`University of London and received a Ph.D. in 1967 for studies on emulsion
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`systems. I was awarded a Doctor of Science degree (higher doctorate) in 1982 for
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`my subsequent research work.
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`7.
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`In 1967, I was appointed to the faculty of the University of London
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`and in 1968 I was awarded a one year Fulbright Scholarship to undertake
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`postdoctoral studies with Professor Takeru Higuchi at the University of Kansas in
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`the field of solution thermodynamics.
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`8.
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`In 1970, I moved to the University of Aston in Birmingham, UK, as
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`Senior Lecturer and Head of the Pharmaceutics section where I developed an
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`active research group in the field of drug delivery systems that included work on
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`emulsions and other colloidal systems.
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`9.
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` In 1975, I became Lord Trent Professor of Pharmacy at the
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`University of Nottingham. In this role, I ran a large research group specializing in
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`the study of novel drug delivery systems including disperse systems such as
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`emulsions, liposomes and microparticles for human and animal use.
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`10.
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`I have supervised over 100 Ph.D. candidates and 20 post-doctoral
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`fellows in different areas of pharmacy.
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`11.
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`In 2003, I became an Emeritus Professor of Pharmacy at the
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`University of Nottingham.
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`12.
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`I have served on numerous committees and panels including the
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`British and European Pharmacopoeias, the Medicines Commission (United
`
`Kingdom), and the Science & Engineering Research Council (United Kingdom).
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`13.
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`I am or have been a member of many learned pharmaceutical
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`societies, including the Royal Pharmaceutical Society, Royal Institute of
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`Chemistry, Society of Rheology, Society of Chemical Industry, American
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`Association of Pharmaceutical Scientists, Controlled Release Society and the
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`Society for Drug Research.
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`14.
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`I have served as an Editorial Board member for many journals dealing
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`with the pharmaceutical sciences as well as the materials sciences.
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`15.
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`I have received awards from various organizations to include the
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`Swedish Pharmaceutical Society, the Royal Pharmaceutical Society of Great
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`Britain, and in 2005 I received the Høest-Madsen Medal for lifetime achievement
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`in the pharmaceutical sciences from the International Pharmaceutical Federation
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`(FIP).
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`16.
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`In 2008, I was awarded an honorary Doctor of Science degree from
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`London University and in 2012 I was made a Fellow of University College
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`London.
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`17.
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`I have more than 40 years of experience in development of
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`commercial drug products in the pharmaceutical industry and academic research,
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`with specific focus on drug product formulation development. Specifically, I have
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`extensive personal research experience in the area of colloids and colloidal drug
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`product formulations, including emulsions and suspensions, and in particular, oil-
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`in-water emulsions containing propofol, including Diprivan®, and have authored
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`or co-authored many reviewed publications and made numerous presentations in
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`this area at scientific meetings. I have also authored or co-authored several
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`scientific publications and book chapters on physicochemical properties of
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`emulsions and emulsion stability, including propofol oil-in-water emulsions, large
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`particle contaminants in intravenous emulsions (e.g. Davis et al., Encyclopedia of
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`Emulsion Technology, Chapter 3, Applications). I am an author of the Han,
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`Washington and Davis reference describing the physical stability of commercially
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`marketed Diprivan® that is cited in Petitioner’s Expert Declaration (see Exh. 1002,
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`Feinberg Declaration at ¶16).
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`18. Attached hereto as Exhibit 2037 is a copy of my curriculum vitae
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`setting out in detail my qualifications and professional expertise, including a list of
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`publications which I have authored or co-authored.
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`19.
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`In forming my opinions expressed herein, I considered the materials
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`cited in this Declaration (attached hereto as Exhibit 2036). I have further relied on
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`my knowledge, education and training and my many years of experience in the
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`field of pharmaceutical sciences, as reflected in my qualifications and credentials
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`set forth above and in my curriculum vitae.
`
`20.
`
`I have reviewed U.S. Patent No. 8,476,010 (“the ’010 Patent”, Exh.
`
`1001). I have also reviewed the petition filed in this matter, the expert declaration
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`by Dr. Feinberg (the “Feinberg Declaration”, Exh. 1002) filed by the Petitioner in
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`support of the petition, and the references identified by the Petitioner. I have also
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`reviewed the Patent Owner Preliminary Response filed by the patentee in response
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`to the petition in this matter.
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`21. Based on my experience, I believe that a person of ordinary skill in
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`the field of the invention described in the ’010 patent prior to July of 2003 would
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`have been someone with substantial research or industry experience in
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`pharmaceutical drug product formulation, including experience in drug product
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`emulsions and their packaging, including chemical and physical characteristics of
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`oil-in-water emulsion systems such as propofol emulsions, and having at least a
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`master’s degree or doctorate in a related technical field, such as analytical, physical
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`or organic chemistry, pharmaceutics or related subject matter having equivalent
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`experience in such fields, or a bachelor’s degree in those related fields with at least
`
`three years of practical experience.
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`II. BACKGROUND OF THE PROPOFOL OIL-IN-WATER
`EMULSION (DIPRIVAN®)
`
`22. Propofol (2,6-Diisopropylphenol), has been a widely used intravenous
`
`anesthetic agent since its introduction in 1989. Oil-in-water emulsion systems had
`
`previously been described for the delivery of lipophilic drugs such as propofol.
`
`(For a review, see Exh. 2038, S.S. Davis et al., Lipid emulsions as drug delivery
`
`systems Ann. NY Acad. Sci., 507 (1987), pp. 75–88.) Because propofol is a
`
`hydrophobic, water-insoluble oil, it cannot be safely delivered in a simple aqueous
`
`solution (Exh.1001 at Col. 1:20-25.) In order to overcome propofol’s solubility
`
`limitation, pharmaceutical compositions containing propofol are typically
`
`formulated as oil-in-water emulsions in which the propofol is dissolved in an oil
`
`solvent, and then emulsified with a suitable emulsifying agent and water for
`
`injection (see, id. at Col. 2:20-47.)
`
`23. Patent Owner’s Diprivan® product is an oil-in-water emulsion
`
`formulation containing 1% (w/v) propofol contained in an emulsion of soybean oil
`
`(10% w/v), glycerol and purified egg lecithin and a tonicity adjusting agent
`
`(glycerol). (See, id. at Col. 2:33-39.) The soybean oil, egg lecithin and glycerol
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`components in the Diprivan® oil-in-water propofol emulsion are present in the
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`same proportion as in a parenteral nutrition oil-in water emulsion known as
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`Intralipid®. (Farinotti, Exh. 1007 at 453-454.)
`
`24. The ’010 patent states that the described propofol emulsions can be
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`manufactured using terminal sterilization by autoclaving. (Exh. 1001 at Col. 7:31-
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`34.) Filtration of Diprivan® emulsion is impractical. Instead, the manufacturing
`
`steps for marketed Diprivan® included terminal heat sterilization by autoclaving
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`after filling into its storage container. (Exh. 1014 at Cols. 7-8.)
`
`25. Unlike a simple homogeneous single phase containing drug
`
`compounds dissolved in aqueous solutions, emulsions are a non-homogeneous,
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`three-component mixture of oil, water, and a surfactant. The components are
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`distributed in a multi-phase system consisting of at least two immiscible liquids.
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`One liquid (known as the internal or discontinuous phase) is dispersed in the form
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`of small droplets surrounded by a surfactant (also known as an emulsifying agent)
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`throughout the other (known as the external or continuous phase). (See, e.g.,
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`Merck Manuals, “Routes of Administration of Dosage Forms”, Exh. 2001.)
`
`26. Where oils are dispersed as particles or microdroplets in water or an
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`aqueous solution, the resulting system is called an oil-in-water emulsion. Unlike
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`homogeneous aqueous solutions, emulsions are, by nature, physically unstable.
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`Although emulsifying agents such as lecithin are included to increase their physical
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`stability, emulsions droplets nonetheless tend to coalesce into larger droplets or
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`emulsions can separate into two distinct phases when subjected to physical stresses
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`such as agitation, temperature or pH changes. (See, e.g., Exh. 1009.)
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`27. As an oil-in-water emulsion stabilized and dispersed by an
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`emulsifying agent, lecithin, Diprivan® would be expected to have a greater
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`propensity for removing silicone oil from a siliconized container closure, as
`
`compared to aqueous drug formulations without an emulsifier. To maintain
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`stability of the Diprivan® emulsion, the soybean oil, which holds the bulk of the
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`propofol active ingredient, is kept dispersed in the aqueous phase as extremely
`
`small oil droplets (mean droplet size 0.10- 0.30 µM) by the lecithin emulsifying
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`agent. (See e.g., Exh. 2026 at 862-863; Exh 1009 at 208.) Lecithin contains both a
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`polar hydrophilic group, and a lipophilic group whereby the oil-miscible
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`hydrophobic end interacts with the soybean oil, and the hydrophilic end interacts
`
`with the aqueous phase. The lecithin molecules, therefore, bridge the interface
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`between the propofol-containing oil droplets and the aqueous phase. (See Exh.
`
`2026 at 864 and Figure 4.) An electrical charge on the polar hydrophilic end of the
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`lecithin molecules causes the oil droplets to repel each other, thereby reducing the
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`tendency for the oil droplets to coalesce into larger droplets and thus to maintain
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`the physical stability of the emulsion. (Id.) Since Diprivan® contains an excess of
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`lecithin to ensure complete emulsification of the soybean oil droplets, the excess
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`lecithin that is not associated with oil droplets could interact with and emulsify
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`silicone oil when Diprivan® contacts rubber closures siliconized with silicone
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`oil. The potential for hydrogenated lecithin emulsifier to emulsify silicone oil was
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`already known in the prior art. (See Exhs. 2039, Bae et al. (2000) at Abstract, 526,
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`527 (Figures 7 and 8) and 2058.) Further, the manufacturing process for
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`Diprivan® utilizes a high shear mixing device to ensure that the emulsified
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`propofol-containing soybean oil is dispersed as extremely small droplets in the
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`aqueous phase of the emulsion. (See Exh. 1001 at Col. 7:31-34.) Because any
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`silicone oil emulsified from siliconized rubber closures is not subjected to any
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`mechanical homogenization process, it may form larger droplets relative to the
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`droplets in Diprivan®.
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`28. Emulsions are metastable systems, which means that they are
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`thermodynamically unstable. After a period of time, the emulsion eventually
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`separates into two phases: a water plus surfactant phase and an oil phase,
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`depending strongly on the preparation method, the surfactant, and oil properties.
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`The separation process involves coalescence of the droplets which grow as a
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`function of time, which can vary significantly depending on the specific emulsion
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`system. (See Exh. 2026.)
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`29. Oil-in-water emulsions intended for intravenous use should have an
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`extremely small droplet size and remain highly stable, since large droplets
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`administered intravenously can lodge in blood vessels potentially leading to life-
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`threatening side effects. Particles greater than 5 μM are generally considered
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`unsafe in parenteral emulsions. (See Exh. 1009 at 208.)
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`30. The physical stability of the oil-in-water emulsion drug formulations,
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`such as Diprivan®, must be evaluated in terms of droplet particle size and
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`distribution, impurity and foreign particle contaminant levels, and the degradation
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`or loss of propofol potency. This can be done after the emulsion drug product is
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`subjected to accelerated stability tests and real-time shelf-life evaluation over the
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`proposed shelf-life, and to obtain data to confirm that the formulation is safe and
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`effective for administration to patients.
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`31.
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`In order to be a safe and effective drug formulation, parenteral
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`emulsions must, therefore, be formulated with adequate physical stability to
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`prevent an increase in droplet size during the shelf-life storage of the
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`pharmaceutical emulsion products. (Id.) In addition to the physical stability
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`requirement for emulsions (not susceptible to coalescence or separation), it is
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`important to maintain the stability of the active ingredient and/or excipients in the
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`emulsion (stability to degradation and/or loss due to adsorption or absorption to the
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`storage container components). (See Exh. 2051 at 168.)
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`32. The average particle size of the emulsion droplets in propofol oil-in-
`
`water emulsions is much less than 1 micron. The average particle size diameter of
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`emulsion droplets for Diprivan® have been reported to be 150-200 nm (0.15 – 0.2
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`M). (Exh. 1009 at 208.) It was known that both emulsion destabilization and
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`loss of propofol due to adsorption-diffusion are risks associated with Diprivan®.
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`(Exh. 1007 at Abstract.)
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`33. Although testing methods to determine emulsion physical stability for
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`emulsion drug formulations were known in the art, these were distinct and different
`
`from tests used to determine the stability of the drug active ingredient over the
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`proposed shelf-life of the product. The Han reference, which I co-authored,
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`reported a method of assessing physical stability used for Diprivan® “shaking,
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`freeze-thaw cycling and thermal cycling, physical agitation.” (Exh. 1009 at 213.)
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`The Han “shake testing” used a wrist-action shaker operating at 300 strokes/min. at
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`room temperature for 2, 4, 6, 8, 10, 12 and 16 hours, after which the particulate
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`size and particle distribution in the emulsion were analyzed with a variety of
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`particle size measurement techniques. (Id. at 215-17.) The Han shaking test was
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`designed to evaluate emulsion physical stability, and was not used nor intended for
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`use in determining the content of the active ingredient in the emulsion. Han’s
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`shaking test is unlike the closure compatibility testing described in the ’010 Patent.
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`Notably, the Han shaking test did not combine an HPLC chemical analysis with
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`the mechanical shake test for evaluating the loss of propofol active ingredient after
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`mechanical agitation.
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`III. BACKGROUND OF THE ‘010 PATENT INVENTION
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`34. The ’010 patent to Desai, et. al. issued on July 2, 2013 from U.S.
`
`Appl. No. 10/616,709, which was filed on July 10, 2003. I understand that claims
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`1, 13-15, 17, 18 20, and 24-28 have been challenged in this matter (the “challenged
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`claims”) and alleged to be unpatentable as obvious. Claim 1 states:
`
`1. A sterile pharmaceutical composition of propofol in a
`container, comprising:
`a container which includes a closure and a composition
`in the container, and
`the composition in the container comprising from 0.5%
`to 10% by weight propofol and from about 0 to about
`10% by weight solvent for propofol,
`
`where when the composition in the container sealed
`with the closure is agitated at a frequency of 300-400
`cycles/minute for 16 hours at room temperature, the
`composition maintains a propofol concentration (w/v)
`measured by HPLC that is at least 93% of the starting
`concentration (w/v) of the propofol;
`
`where the closure is selected from the group consisting of
`siliconized bromobutyl rubber, metal, and siliconized
`chlorobutyl rubber.
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`35. Claims 17 and 18, which depend from claim 1, require that the closure
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`consist of closure that is inert to propofol. Claim 19, which depends from claim 18
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`requires that the closure include siliconized bromobutyl rubber that is inert to
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`propofol.
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`36.
`
`I understand that the claims of the patent define the scope of the
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`exclusionary rights the patentee is entitled to. Claim 1 is directed to a sterile
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`propofol formulation stored in a container having a siliconized bromobutyl rubber,
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`metal, and siliconized chlorobutyl rubber closure that retains at least 93% weight
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`by volume of the initial propofol concentration in the formulation after being
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`subjected to the specified accelerated stability test.
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`37. The accelerated stability test required by claim 1 requires the propofol
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`emulsion to maintain at least 93% of the initial concentration in the container as
`
`determined by HPLC after being subjected to agitation or ‘shaking’ at the specified
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`frequency and time at room temperature. The patent specification describes the
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`accelerated stability test as a “method for testing compatibility of propofol
`
`emulsions”, and states that the test was used for accelerated testing of propofol
`
`emulsions on propofol emulsion degradation or potency. (Exh. 1001 at Col. 23:17-
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`37.) The specification further states that an HPLC assay of the propofol samples
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`before and after the accelerated testing determined if there was any loss in the
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`potency or concentration of propofol in the formulations, and that the testing
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`method allowed the rapid testing of closure compatibility with different propofol
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`formulations as well as emulsion stability.” (Id.) The specification further states
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`“the degradation or loss in potency of propofol potency should be such that the
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`propofol composition meets regulatory safety and efficacy standards. As a result,
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`impurity levels, such as silicone oil, levels of degradation products and potency
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`loss are within acceptable regulatory limits.” (Id. at 4:47-58.)
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`38.
`
`I agree with the construction of “siliconized” adopted by the Board.
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`The specification of the ’010 patent states that “[in] general the preferred closures
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`are made with inert, non-reactive materials with little to no leachables. Preferred
`
`closures also include those that are coated or treated with inert materials such as
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`siliconized polymer…” and that “[b]y way of example and not in limitation of the
`
`present invention, rubber closures that are suitable in the present invention include
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`silicones, siliconized bromobutyl rubber…and siliconized chlorobutyl rubber.”
`
`(Id. at Col. 9:40 - Col. 10:3.) For example, the Glossary entry in Smith et al. (Exh.
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`1004) states that the term “silicone” commonly refers to silicone fluid, which, in
`
`turn, is commonly used to describe a liquid silicone, including silicone oil. (See
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`Exh. 1004 at S12.) The Smith reference also describes “silicone polymer” (i.e.
`
`polysiloxane) as a general term describing a silicon containing polymer whose
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`silicon atoms are separated by oxygen atoms (contain si-O-Si bonds). (Id.) A
`
`person of ordinary skill in the art (POSA), based on the descriptions in the art,
`
`including Smith, would have known and understood that the term “siliconized” in
`
`the claims refers to a closure that is surface-treated, coated or manufactured with
`
`silicone or one or more siloxane polymers.
`
`39.
`
`I agree with the construction of “inert to propofol” adopted by the
`
`Board. The patent specification defines “inert to propofol” to mean that the
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`closure itself is non-reactive to propofol such that it does “not cause significant
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`degradation or loss of potency of the propofol formulation.” (Exh. 1001 at Col. 4:
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`47-51 and Col. 8: 39-43.) A POSA would therefore, have understood the term
`
`“inert to propofol” to mean “does not interact or react with propofol to cause a loss
`
`in the potency or concentration of propofol.”1
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`40. The ’010 patent inventors discovered that changes in propofol
`
`concentrations after agitation with a mechanical shaker (previously used to test
`
`only emulsion stability) correlated with the change in propofol concentration after
`
`real-time shelf stability testing as determined by HPLC analysis. The ’010 patent
`
`inventors concluded that when coupled with HPLC analysis for the active
`
`ingredient, “the shaker test, for which results could be obtained within 24 hours,
`
`was a suitable surrogate for accelerated testing in conventional shelf-stability
`
`chambers”, which took two months to complete. (Exh. 1001 at Col. 27:45-49.)
`
`Further, the inventors also surprisingly found that siliconized bromobutyl rubber
`
`closures maintained the concentration of propofol in the emulsion and the stability
`
`of the emulsion after subjecting it to accelerated stability testing, and that these
`
`advantages persisted over a wide range of soybean oil concentrations.
`
`41. The change in the level of the propofol active ingredient in the
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`propofol oil-in-water emulsions (i.e. drug loss) after the ’010 patent inventors
`
`subjecting it to the “shaker test,” in my opinion, was most likely caused by the
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`1 I understand that the Parties have agreed to the construction of the term
`“siliconized.”
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`partitioning of propofol, a highly hydrophobic compound, by the bromobutyl
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`rubber stopper, whereby propofol is adsorbed on the surface of the stopper, and
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`may subsequently be absorbed into the stopper material. While the siliconization
`
`of bromobutyl rubber stoppers were traditionally used in container-filling
`
`processes as a lubricant to prevent stoppers from sticking to one another in drug
`
`product fill lines, siliconization of bromobutyl rubber stoppers was not typically
`
`used to reduce drug loss in a formulation. In my opinion, a POSA, therefore,
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`would not have siliconized bromobutyl rubber stoppers to combat the issue of
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`propofol loss in propofol oil-in-water emulsions due to surface adsorption onto or
`
`absorption into the stopper material.
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`IV. PARENTERAL DRUG PRODUCT PARTICLE
`CONTAMINATION FROM SILICONIZED VIAL CLOSURES
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`42. Problems associated with siliconization of container closures were
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`well known and documented in the art long before July 2003. The Smith
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`reference2 (Exh. 1004), which published in 1988, states that although hydrophobic
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`silicone lubricants such as silicone oil (polydimethoxysilane (PDMS)) were used
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`generally in pharmaceutical packaging closures - because they were not generally
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`expected to mix with homogeneous aqueous drug solutions - “[h]eavy application
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`of PDMS to rubber closures …could result in the formation of silicone oil globules
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`2 The Smith reference was cited by Petitioner’s expert. (Exh. 1002, Feinberg Decl.
`at, e.g. ¶10.)
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`17
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`suspended in the formulation”, and that “[e]ven low application levels could result
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`in suspended particles due to vial agitation…” (Exh. 1004 at S11.)
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`43. By July of 2003, it was already well known in the art that silicone oil
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`or other lubricants used in closures for storage containers introduced undesired
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`large particle contaminants (e.g. particle size >10 M) into pharmaceutical drug
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`products that raised potential concerns with respect to regulatory requirements for
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`permissible levels of such large particle contaminants in injectable parenterals.
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`44. U.S Patent 5,163,919 (Exh. 2024) stated that a water-based medical
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`preparation after contact with the silicone oil treated elastomeric seal contained a
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`relatively large quantity of silicone oil droplets in emulsified state. (Exh. 2024,
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`Col. 2:42-29.) The ’919 patent disclosed that high particle contamination from
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`rubber closures covered with a silicone layer (50,000 particles per mL of
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`contacting fluid with particle size ≥ 2M) was observed compared to non-
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`siliconized rubber seal (2000 particles per mL with particle size ≥ 2M) after
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`contacting the rubber seals under steam sterilization conditions of 121oC for 30
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`minutes. (Id. at Col. 5:37-54, Cols. 8-9.) The ’919 patent disclosed an alternative
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`surface treatment for rubber closures with halogen or elementary halogen such as
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`fluorine resulted in significantly lower particle contaminants (500 particles with
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`particle size ≥ 2M) and similar friction coefficient as silicone oil treatment and
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`easy processing in packaging equipment. (Id.)
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`18
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`45. U.S. Patent 4,973,504 (Exh. 2040) stated that although the use of
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`silicone oil improved the lubricity of rubber closures, it created additional
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`problems of increased particle counts in various drug solutions during inspection.
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`(Exh. 2040 at Col. 2:6-27.) The ’504 patent also stated that the FDA evaluated
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`pharmaceutical manufacturing processes by counting the total number of particles
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`present in the drug product, regardless of the source or nature of the particles. (Id.)
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`The ’504 patent further stated:
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`“Silicone oil in small amounts is normally not an
`undesirable contaminant in medicine but its use still adds to the
`count of particles and, therefore, detracts from the overall
`acceptance of its use in processing equipment”;
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`“[E]ven though the amount of silicone oil is minimal,
`being only that amount necessary to prevent the individual
`stoppers from sticking to one another, silicone oil is not able to
`adequately lower the coefficient of friction of rubber stoppers
`for use in high speed capping equipment so as to give uniform
`faster movement, particularly with centrifugal feeding
`systems”; and
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`“[R]ubber stoppers which have been treated by the use of
`silicone oil are not any more effective in surviving chemical
`tests concerning the compatibility with and contamination of
`material contained in the vials.”
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`(Id.)
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`46. The ’504 patent disclosed a non-silicone alternative coating for rubber
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`stoppers containing polyparaxylylene, and demonstrated that that polyparaxylylene
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`coated stoppers produced significantly reduced particle contamination levels
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`19
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`compared to siliconized rubber stoppers. (Exh. 2040, Col. 5:4-24, Col. 8:56 - Col.
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`9:2.) The ’504 patent further disclosed that after remaining in contact with an
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`aqueous solution for 30 minutes, both untreated rubber stoppers and those treated
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`with the polyparaxylylene coating produced less than 300 particles per stopper
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`having a particle size of ≥ 5M, whereas siliconized rubber stoppers produced
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`more than 10,000 particles of that size per stopper. (Exh. 2040, Col 9:3-23.) The
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`’504 patent also disclosed that paraxylylene coated stoppers exhibited lower
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`coefficient of friction than siliconized rubber closures thereby allowing silicone oil
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`to be eliminated in processing, and that paraxylylene polymer coated rubber could
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`be manufactured from conventional rubber material and formed into rubber
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`stoppers. (Exh. 2040 Col. 5:6-8, 20-21.)
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`47. A 1992 reference by Mannermaa et al. (Exh. 2041) disclosed that
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`siliconized rubber stoppers produced significantly higher number of particulate
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`contaminants in aqueous solution after being subjected to autoclave heat
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`sterilization compared to non-siliconized stoppers. (See Exh. 2041, Abstract.)
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`Specifically, Mannermaa reported that siliconized rubber stoppers produced as
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`much as a 600% increase of particles between 5M and 32M (~1200 to 4500
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`particles per mL of aqueous solution) after being sterilized by autoclaving at 121oC
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`for 15 minutes compared to corresponding stoppers that were not autoclaved (~200
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`to 900 particles per mL). (Exh. 2041, comparing stoppers 1-3 and 5-7 with
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`20
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`stoppers 8-10 and 12-14, respectively, in Figure 3 at 75.) Mammeraa further
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`reported that non-siliconized rubber stoppers produced a significantly lower
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`number of 5M and 32M particles(~ 500 particles) after sterilization by autoclave
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`. (Id.) Siliconized stoppers thus produced between about 120% to 900% more
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`particles compared to the non-siliconized stopper. (See id.) Mannermaa also
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`disclosed that the number of particles released from siliconized rubber stoppers
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`after sterilization by autoclaving varied considerably between different stoppers
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`(i.e. by manufacturer) and even between different batches of the same stopper.
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`(See, id. at Abstract.)
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`48. Significantly, Mannermaa disclosed that the only non-siliconized
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`stopper evaluated in their study “performed better” (i.e. produced lower particle
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`count) compared to all other siliconized stoppers tested. (Exh. 2041 at 74-76,
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`Figures 2 and 3.) Mannermaa concluded that absence of surface siliconization may
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`have contributed to the superior performance of the non-siliconized rubber stopper,
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`and that the increased number of large particle contaminants from the siliconized
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`stoppers “might indicate that silicone oil droplets shed from the stoppers have a
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`significant effect on the number of particles generated by stoppers during
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`sterilization.” (Exh. 2041 at 77.)
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`49. A 1992 reference by Cape