SUBCUTANEOUS RESERVOIR DEVICE AND METHOD OF MANUFACTURE
20180235900 ยท 2018-08-23
Inventors
- Stephanie Lynn Swarner (Cary, NC, US)
- Leah Johnson (Durham, NC, US)
- Robert F. Praino, Jr. (Westwood, MA, US)
- Phillip Gregory Durham (Broadway, NC, US)
- Mark E. Kleiman (Canton, MA, US)
- Ginger Denison Rothrock (Cary, NC, US)
- Ariane Van Der Straten Ponthoz (Kensington, CA, US)
Cpc classification
B29C43/56
PERFORMING OPERATIONS; TRANSPORTING
B29C66/8122
PERFORMING OPERATIONS; TRANSPORTING
B29K2067/046
PERFORMING OPERATIONS; TRANSPORTING
B29K2827/18
PERFORMING OPERATIONS; TRANSPORTING
B29K2067/00
PERFORMING OPERATIONS; TRANSPORTING
B29C66/8322
PERFORMING OPERATIONS; TRANSPORTING
B29C43/18
PERFORMING OPERATIONS; TRANSPORTING
B29K2067/046
PERFORMING OPERATIONS; TRANSPORTING
B29L2031/753
PERFORMING OPERATIONS; TRANSPORTING
B29C66/1122
PERFORMING OPERATIONS; TRANSPORTING
A61K47/34
HUMAN NECESSITIES
B29C66/8122
PERFORMING OPERATIONS; TRANSPORTING
B29C66/43
PERFORMING OPERATIONS; TRANSPORTING
B29C66/71
PERFORMING OPERATIONS; TRANSPORTING
B29C66/71
PERFORMING OPERATIONS; TRANSPORTING
A61K9/0024
HUMAN NECESSITIES
B29C66/8242
PERFORMING OPERATIONS; TRANSPORTING
B29K2067/00
PERFORMING OPERATIONS; TRANSPORTING
A61K31/685
HUMAN NECESSITIES
A61K9/0019
HUMAN NECESSITIES
B29C66/81431
PERFORMING OPERATIONS; TRANSPORTING
B29C66/731
PERFORMING OPERATIONS; TRANSPORTING
B29C66/949
PERFORMING OPERATIONS; TRANSPORTING
B29K2827/18
PERFORMING OPERATIONS; TRANSPORTING
B29C66/73921
PERFORMING OPERATIONS; TRANSPORTING
B29C65/10
PERFORMING OPERATIONS; TRANSPORTING
B29C66/919
PERFORMING OPERATIONS; TRANSPORTING
International classification
A61K9/70
HUMAN NECESSITIES
B29C43/56
PERFORMING OPERATIONS; TRANSPORTING
B29C65/00
PERFORMING OPERATIONS; TRANSPORTING
A61K9/00
HUMAN NECESSITIES
B29C43/18
PERFORMING OPERATIONS; TRANSPORTING
A61K47/34
HUMAN NECESSITIES
Abstract
The medical devices of the present disclosure are filled reservoirs such as a cylinder comprised of a polymer film which contains a reservoir of active agent, plus excipient, in some cases, for disease prevention, treatment, and/or contraception. The polymer film is permeable to the active agent after subcutaneous implantation of the device into a body. The cylinder is comprised by the lamination of one or two polymer films which are ultrasonically welded to contain the drug material. The use of an ultrasonic welding process enables sealing of the polymer films to create the closed cylinder. The medical device is useful for long term disease prevention, such as prevention of HIV infection.
Claims
1. A reservoir device comprising an active agent contained within a reservoir, the reservoir defined by one or more porous polymer membranes sealed with an ultrasonic weld, the porous membrane allowing for diffusion of the active agent through the pores of the membrane when positioned subcutaneously in a body of a subject.
2. The device of claim 1, wherein the porous polymer membrane comprises polycaprolactone (PCL), poly(lactic-co-glycolic acid) (PLGA), or polylactic acid (PLA).
3. The device of claim 1, wherein the porous polymer membrane comprises polycaprolactone (PCL) at a molecular weight ranging from 15,000-80,000 kDa.
4. The device of claim 1, wherein the porous polymer membrane has a membrane thickness ranging from 1-30 m or from 10-25 m.
5. The device of claim 1, wherein the active agent is one or a combination of a therapeutic, a preventative, or a contraceptive.
6. The device of claim 5, wherein the active agent comprises an antibody, a small molecule, a protein, or a peptide.
7. The device of claim 1, wherein a size of the pores of the porous polymer membrane ranges from 1-2 times the diameter of the active agent.
8. The device of claim 1, wherein the active agent comprises an antibody for the prevention of HIV infection.
9. (canceled)
10. The device of claim 1, further comprising an excipient contained within the reservoir.
11. (canceled)
12. The device of claim 1, wherein the porous polymer membrane is biodegradable.
13. The device of claim 1, wherein the reservoir has a cylindrical shape.
14. (canceled)
15. A method for manufacturing a reservoir device for delivery of an active agent to a subject, the method comprising: imparting a vacuum to a first porous membrane positioned on a mold defining at least one cavity, wherein the first porous membrane takes a shape of the cavity in the presence of the vacuum; depositing an active agent into a portion of the first porous membrane that is received in the cavity; positioning a second porous membrane carried on a release liner over the active agent and in contact with the first porous membrane; applying an ultrasonic force to a release liner positioned over the porous membrane(s) in an area surrounding the active agent to create a welded seal to contain the active agent within the cavity; and releasing the welded porous membranes from the mold and the release liner to provide a reservoir device(s), the porous membranes allowing for diffusion of the active agent through the pores of the membrane when the reservoir device is positioned subcutaneously in a body of a subject.
16. The method of claim 15, further comprising a distribution of apertures within the mold of the cavity to spread the vacuum over a broader surface area of the portion of the first porous membrane that is received in the cavity.
17. The method of claim 15, further comprising cutting the porous membranes to singulate the reservoir devices.
18. The method of claim 15, wherein one or both of the first and the second porous polymer membranes comprise polycaprolactone (PCL), poly(lactic-co-glycolic acid) (PLGA), or polylactic acid (PLA).
19. The method of claim 15, wherein the first and the second porous polymer membranes comprise polycaprolactone (PCL) at a molecular weight ranging from 15,000-80,000 kDa.
20. The method of claim 15, wherein the first and the second porous polymer membranes have a membrane thickness ranging from 1-30 m or from 10-25 m.
21. (canceled)
22. (canceled)
23. (canceled)
24. (canceled)
25. (canceled)
26. (canceled)
27. (canceled)
28. (canceled)
29. (canceled)
30. (canceled)
31. A method for sustained delivery of an active agent to a subject, the method comprising implanting the reservoir device of claim 1 subcutaneously in a body of a subject, wherein diffusion of the active agent through the pores of the membrane of the device provides sustained delivery of the active agent to the subject for one or a combination of prevention, treatment, or contraception.
32. The method of claim 31, wherein the prevention is prevention of infection with HIV.
33. (canceled)
34. (canceled)
35. The method of claim 31, wherein the reservoir device is biodegradable.
36. (canceled)
37. (canceled)
38. (canceled)
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0012] The foregoing aspects and other features of the disclosure are explained in the following description, taken in connection with the accompanying drawings, wherein:
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DETAILED DESCRIPTION OF THE DISCLOSURE
[0037] For the purposes of promoting an understanding of the principles of the present disclosure, reference will now be made to preferred embodiments and specific language will be used to describe the same. It will nevertheless be understood that no limitation of the scope of the disclosure is thereby intended, such alteration and further modifications of the disclosure as illustrated herein, being contemplated as would normally occur to one skilled in the art to which the disclosure relates.
[0038] Articles a and an are used herein to refer to one or to more than one (i.e. at least one) of the grammatical object of the article. By way of example, a reservoir device means at least one reservoir device and can include more than one reservoir device.
[0039] Unless otherwise defined, all technical terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this disclosure belongs.
[0040] The invention is a medical device and the associated process by which it can be produced for long acting delivery of an active agent such as an active pharmaceutical ingredient (API). The devices of the present disclosure address key drawbacks of existing technologies such as: (1) in the event of a drug-related serious adverse event, existing products and technologies cannot be removed; and (2) the first-order dissolution of nanosuspended drug in existing products and technologies results in a first-order pharmacokinetic (PK) profile with a gradual decrease, resulting in a potentially long tail extending beyond the effective duration of the dose in which suboptimal levels of drug continue to be delivered systemically. In contrast, the reservoir devices of the present invention provide zero-order drug release kinetics, resulting in a flat PK profile at a steady state. Upon depletion of drug from the implant, only a minimal tail can be expected according to the drug's half-life and supported by results described herein in the Examples. An example of one advantage of the disclosed devices is systemic administration, combined with long-term delivery, to significantly protect a wider variety of HIV exposure routes, including vaginal, rectal, and parenteral. This technology can be useful for a wide variety of therapeutics and preventatives, including small molecules and biologics.
[0041] The devices of the present invention also address the unmet need for a long-acting biodegradable implant for a contraceptive method. Although long-acting contraceptives are preferable for longer duration of protection and greater effectiveness, a quick return to fertility is believed to be important from an end-user perspective.
[0042] In one embodiment, the devices of the present invention are fabricated from the FDA-approved biodegradable polymer polycaprolactone (PCL) and provide a zero-order drug release profile to meet both of these needs. Finally, by combining both pregnancy and HIV prevention, the device offers women an empowering tool to protect themselves against multiple risks. Mulitpurpose Prevention Technologies (MPTs) that are simple, acceptable, and accessible hold great potential for significant impacts in public health. Women can receive dual protection discreetly, even if their stated intention is to address just one health need, because of pressures from their sociocultural context (e.g., HIV stigma) or relationships.
[0043] As shown in
[0044] Active agent 12 can be one or a combination of a therapeutic, a preventative, or a contraceptive. In some embodiments, active agent 12 comprises an antibody, a small molecule, a protein, and/or a peptide. For example, in some embodiments, the active agent comprises an antibody for the prevention of HIV infection. In some embodiments, the active agent comprises a nucleotide reverse transcriptase inhibitor (NRTI) for treatment of HIV infection. The nucleotide reverse transcriptase inhibitor can be Tenofovir Alafenamide Fumarate (TAF).
[0045] Porous membranes 16, 18 allow for diffusion of the active agent through the pores of the membranes when positioned subcutaneously in a body of a subject. In some embodiments, membranes 16, 18 comprise polycaprolactone (PCL), poly(lactic-co-glycolic acid)(PLGA), or polylactic acid (PLA). For example, membranes 16, 18 can comprise polycaprolactone (PCL) at a molecular weight ranging from 15,000 to 80,000 kDa. In some embodiments, membranes 16, 18 have a thickness ranging from 1-30 m or from 10-25 m. The pore size of the disclosed membranes can range from 1-2 times the diameter of active agent 12. In some embodiments, porous polymer membranes 16, 18 are biodegradable.
[0046] Device 10 can be designed for controlled release of a wide range of therapeutic and preventive active pharmaceutical ingredients (i.e., active agents). Unlike other sustained release technologies, membrane-controlled devices are functionally tunable to achieve zero-order release kinetics, attaining a flat drug release profile and a tight concentration range over several weeks to months. By engineering the porosity to average 1 to 2 times the molecular diameter of a target drug, release rates can be controlled throughout the device lifetime, and an isolated reservoir can provide the necessary therapeutic or preventative payload. This ability to load and protect the drug is critical for therapies that often undergo rapid degradation and clearance. The device design proposed herein will mitigate many of the challenges of sustained delivery. The general mechanism of the proposed device is shown in
[0047] Thus, the presently disclosed subject matter includes a method for sustained delivery of active agent 12 to a subject, comprising implanting the disclosed reservoir device subcutaneously in a body of a subject. Diffusion of the active agent through the pores of membranes 16 and/or 18 provide sustained delivery of the active agent to the subject for one or a combination of a prevention, treatment, or contraception. In some embodiments, the diffusion of the active agent through the pores of membranes 16, 18 is zero order kinetics at a steady state. In some embodiments, the sustained delivery is a period ranging from 2-3 months. In some embodiments, the prevention is the prevention of infection with HIV.
[0048] For PrEP specifically, the biostability and required injection volumes of agents constrain delivery technologies. Recent evidence has been published indicating that long-term protection is feasible. However, the persistence is still generally characterized as first order, which requires administration of high dosing and the need for high burden infusion procedures. Device 10 is designed for subcutaneous implantation, which simplifies administration with lower-skilled staff, facilitating access in resource-limited settings. Moreover, this biodegradable product alleviates the need for an extra clinic visit to remove the implant after depletion. Importantly, as shown in
[0049] Long-term storage stability presents challenges, as biologics and some small molecule therapeutics inherently have limited stability in the aqueous state where they are subject to chemical and physical degradation, as well as aggregation. By contrast, when lyophilized, the shelf-life of antibodies can be extended, even with room temperature storage in many cases. The presently disclosed devices can utilize API in a dry lyophilized form, packaged within the device and subsequently resolubilized in vivo for release into the subcutaneous space. Alternatively, the API drug can exist as a slurry. Rehydration and release are controlled via the engineered membrane.
[0050] Because polymer properties and drug formulations (e.g., connectivity and pore size) affect the release rate of APIs through PCL films, proper design of architectures is crucial to achieve zero-order release kinetics. To this end, the present disclose provides methods to fabricate biocompatible thin PCL films of different properties, including differences in molecular weight, porosities, and films thickness, ultimately tuning release kinetics according to required duration.
[0051] Methods are provided herein in the EXAMPLES for manufacturing and evaluating devices comprising PCL thin films that meet mechanical properties required for device insertion and utilization (
[0052] The invention differs from prior devices as follows:
[0053] Device 10 is a flexible, permeable polymer film cylinder filled with active ingredient 12 (
[0054] In some embodiments, device 10 can be manufactured by folding porous membrane 16 over to define tubular cavity, depositing active agent 12 into the cavity, and applying an ultrasonic force to the porous membrane to create welded seal 20 that contains the active agent within the tubular reservoir 14. Porous membrane 16 allows for diffusion of active agent 12 through the pores of the membrane when device 10 is positioned subcutaneously in a body of a subject.
[0055] Alternatively, as shown in
[0056] In some embodiments, the disclosed method further comprises a distribution of apertures within mold 30 of the cavity 32 to spread vacuum 34 over a broader surface area of the portion of first porous membrane 16 that is received in cavity. In some embodiments, the method further comprises cutting membranes 16, 18 to singulate the reservoir devices.
[0057] One or both of first and second porous polymer membranes 16, 18 can comprise polycaprolactone (PCL), poly(lactic-co-glycolic acid) (PLGA), or polylactic acid (PLA). For example, in some embodiments, the first and the second porous polymer membranes comprise polycaprolactone (PCL) at a molecular weight ranging from 15,000-80,000 kDa. Membranes 16, 18 can have a thickness ranging from 1-30 m or from 10-25 m.
[0058] The use of other thermal processes to achieve fabrication of device 10 (contact heating via conduction only, heated convection air) are not sufficiently controllable and result in damage to the film and failure of the seal. This is due to the sharp melting temperature of PCL and lack of cohesive strength of the melted film.
[0059] One skilled in the art will readily appreciate that the present invention is well adapted to carry out the objects and obtain the ends and advantages mentioned, as well as those inherent therein. The present examples along with the methods described herein are presently representative of preferred embodiments, are exemplary, and are not intended as limitations on the scope of the invention. Changes therein and other uses will occur to those skilled in the art which are encompassed within the spirit of the invention as defined by the scope of the claims.
EXAMPLES
Example 1
45 Day, In-Vitro Release of TAF from a TFPD
[0060] In one example, PCL films were fabricated by a solution casting method. 80 kDa PCL was dissolved at 7.0% wt in toluene and cast onto a glass substrate using a 25 mil slot to achieve a dry film thickness of 25 m. Thickness was measured with a micrometer. The Tenofovir Alafenamide Fumarate (TAF), a nucleotide reverse transcriptase inhibitor (NRTI), formulation was prepared by combining TAF and PEG.sub.600 at a 2:1 mass ratio and hand stirred until combined with a stainless-steel spatula. PCL films were then formed into tubes of the appropriate diameter and long welds were formed along the length of the tube using an impulse heat sealer. Formulated TAF was loaded into the tube by hand using a plastic funnel and plastic rod to within 1 mg of the target mass and recorded. Drug was subsequently packed tightly into the tube with the plastic rod and seals were made using the impulse sealer at the target device length. After characterization devices were packaged into amber glass vials, labeled serially and shipped to Steris Isomedix Services for terminal sterilization by gamma irradiation at a standard dose of 25 kGy (Gamma Engineering Run service was used which does not include sterility validation).
[0061] For the in-vitro studies, TFPD implants were submerged in 30 mL of phosphate buffered saline (1X PBS, pH=7.2) in conical centrifuge tubes and kept in a 37 C. shaking incubator at 120 rpm. At a frequency of approximately 48-72 hours samples of buffer were quantified for TAF mass and devices transferred to new buffer solution. Quantification of TAF was performed by ultraviolet-visible absorbance at 260 nm, measured using a spectrophotometer for a 200 L sample volume in a 96-well quartz microplate. UV absorbance at 260 nm was correlated to TAF concentration in 1X PBS buffer for a range of concentrations between 0.003-0.250 mg/mL. For samples above the absorbance maximum of the instrument, samples were diluted by a factor of 10 and measured again (1000 L sample diluted in 900 L of 1PBS).
[0062] Results show the linear release of TAF (in-vitro) from the TFPDs over time (
Example 2
30 Day, In-Vivo Release of TAF from a TFPD
[0063] For the in-vivo studies, twenty-one female New Zealand White rabbits were subcutaneously implanted with TFPD containing the TAF (or control devices) for 30 days of drug release. In an effort to investigate release tailing at the end of the device lifetime (i.e., drug depletion at Day 30), half of the animals continued for an additional 15 days and were euthanized on Day 45. Three dose groups were used: high dose (HD) targeted at 1.5 mg/day, medium dose (MD) targeted at 0.8 mg/day, and low dose (LD) targeted at 0.15 mg/day.
[0064] Blood samples for plasma TAF, TFV and PBMC TFV-DP were collected at predetermined intervals up to 45 days. After blood collection by cardiac puncture under pentobarbital sodium anesthesia, the animals were euthanized via an overdose of intravenous pentobarbital sodium. Blood for drug content were collected into tubes containing K.sub.3 EDTA and then centrifuged to obtain plasma before freezing, and stored at 80 C. Target tissues (vagina, cervix, rectal) and tissues surrounding the implant were placed in cryovials, snapped frozen in liquid nitrogen before freezing and stored at 80 C. Tissues (near implantation) for histopathology were collected into tubes containing formalin phosphate for 48 hours, transferred to another tube containing cold phosphate buffered saline before refrigeration and stored at 4 C. Tissues (near implantation) for inflammatory markers were placed in cryovials, snapped frozen in liquid nitrogen before freezing and stored at 80 C.
[0065]
Example 3
15 Day, In-Vivo Release of TAF from a TFPD
[0066] In vivo implant studies: To assess the in vivo behavior of the implantable devices for PrEP, preliminary studies were conducted in female Sprague-Dawley rats (N=35) over 14 days. Devices fabricated using poly(caprolactone) (PCL) and containing a TAF/PEG.sub.300 formulation were subcutaneously implanted into the dorsal of the neck of the rats via standard microsurgical techniques. By tuning the device surface area, devices were designed for two different release profiles: high TAF dose (1.1 mg/d) or middle TAF dose (0.45 mg/d) (
Example 4
Characterization of PCL Films
[0067] PCL films can be tuned to meet the requisite biodegradation properties (i.e., optimize the time between depletion of API and film biodegradation). For example, 80 kDa MW PCL films exhibit an extended rate of biodegradation, typically on the order of >24 months. Table 1 shows a variety of new PCL film formulations considered. The PCL blended formulations must be tuned for two properties: adequate rates of biodegradation in relation to API release and mechanical robustness. The balance between these two factors proves critical for these thin films. For example, although PCL films comprising 10 kDa demonstrate faster biodegradation than 80 kDa films, the 10 kDa films failed to remain mechanically intact after casting and crumbled upon handling.
TABLE-US-00001 TABLE 1 PCL film formulations. Fragmentation Dissolution Mass Ratio Average M.sub.N Months until Months until 10 kDa 45 kDa 80 kDa (kDa) M.sub.N = 13 kDa* M.sub.N = 5 kDa* A 1 80 20 30 B 1 1 57.6 16 27 C 1 45.0 14 24 D 1 8 45.0 14 24 E 1 1 17.8 3 14 F 2 1 14.1 1 11 G 3 1 12.8 10
[0068] A 17.8 kDa average M.sub.N blend (Formulation E in Table 1 above) performed well in release evaluation with both caffeine and TAF. A 90 day evaluation was completed using 2:1 TAF:PEG.sub.600 in 80 kDa (standard) and 17.8 kDa (blend, formulation E above) PCL devices to (1) demonstrate 90 day sustained release and (2) evaluate any effects biodegradation may have on release. Of the six devices made, three (80k_1, 80 k_2, and 17k_1) demonstrated non-linear release indicative of fabrication defects and their data are not presented. The remaining three devices which performed as designed (80k_3, 17 k_2 and 17k_3) are presented in
Example 5
Excipients for TAF
[0069] Excipients on the FDA GRAS list of acceptable compounds were evaluated for TAF stability and short-duration TAF release. Devices containing TAF in combination with selected GRAS excipients were evaluated in prototype devices 60 days, presented in
TABLE-US-00002 TABLE 2 Summary of screened excipient stability and TAF release data TAF Chromatographic Release Solubility.sup.1 Purity.sup.1 Rate.sup.2,3 Excipient (mg/mL) (%) (mg/day) Kolliphor EL 15.3 98.78 1.71 0.39 (PEG-35 castor oil) Tocopherol 10.1 ND 3.56 1.25 (Vitamin E) Soybean oil 0.105 ND 0.44 0.15 Cottonseed oil 0.207 ND 0.50 0.02 Sesame oil 0.095 ND 0.52 0.2 Castor Oil 6.7 99.83 1.40 0.02 PEG 600 5.4 95.95 1.87 0.26 TAF std. 99.88 ND = None Detected .sup.1Excess TAF dissolved in excipient at 37 C., quantified by HPLC .sup.2Slope of cumulative release through 15 days normalized to 314 mm.sup.2 .sup.325 m 80 kDa PCL film
Example 6
Manufacturing of Medical Devices
[0070] Specific information regarding ultrasonic welding for medical device manufacture:
[0071] Qualification tests were performed with the set up diagrams provided in
[0072] An example of the fabricated reservoir device structure is represented in
[0073] The structure was created in accordance with the following procedure.
[0074] Coating Solution Preparation:
[0075] The PCL film layer was produced using a 16% by weight solution of SIGMA ALRDRICH Polycaprolactone (average MW 45,000) dissolved in toluene. The solution is prepared by weighing the appropriate amounts of material into a sealable glass container and allowing the polymer to dissolve over the course of several days at room temperature. The mix is initially agitated with a vortex unit; however, the polymer forms gels which do not mix easily. In addition to toluene, acetone and other solvents may be used. If these solvents are used, it is necessary to carry out the dissolution process at a slightly elevated temperature (30 C). The expected concentration range allowable for roll-to-roll production of the film is 5% to 20% by weight. Other polymer molecular weights can be viable (eg. PCL 15,000-80,000) and other polyester films, or copolymers with PCL can be used (e.g. PLGA, PLA).
[0076] Coating Process:
[0077] Film samples are produced in a bench top coating system using a fixed gap set up and a smooth stainless steel rod. The gap is set to 10 mils to produce a liquid film 10 mils (250 microns). To carry out the coating, a disposable pipette is used to dispense fluid onto a silicone release film (carrier web), (Flexmark 200 Poly Sc-6 Liner). The dispensed liquid is drawn across the carrier web to create a uniform liquid layer. The coated liquid is dried with a hand held convection dryer set at 300 F and positioned 10 inches above the liquid. The coated liquid is dried until the layer has a uniform hazy appearance. Additional drying results in melting of the PCL layer which is seen by the layer becoming clear (indicating that the polymer temperature is >58 C. Removal of the heat gun after melting results in the film returning to having a hazy appearance. The hazy appearance occurs initially when the coated layer temperature reaches 30 C (measured with IR Thermometer).
[0078] Other coating processes expected to be usable include slot die, cascade, gravure, reverse roll in a r2r fabrication line. The drying process on such a coating line could include a drying zone, as well as a post-dry baking zone which melts the PCL and allows reduction of the residual solvent level in the finally dried PCL. Such a temperature condition could be held to approximately 60 C to limit deformation of the carrier web.
[0079] The carrier web can be a variety of release films having a range for the thickness. The preferred thickness is 2 mils to limit the waste after carrier web use. Films, thinner than 2 mils (eg. 1 mil commercially available films), have mechanical properties which are more susceptible to wrinkling in a process, and may be more sensitive to shrinkage.
[0080] Final dried film thickness can be adjusted by solids concentration in the coating fluid and by the wet thickness coated. This range can be adjusted from 1 micron up to 30 microns. The preferred thickness is 20 microns. 10 microns is probably a lower limit for use in the device fabrication process described below. A film thickness greater than 20 microns may limit the efficacy of the drug release properties.
[0081] The above coating process could also be carried out with the carrier web being in a sheet format, rather than r2r. In this case, gravure and reverse roll application processes would not be used.
[0082] Measurement:
[0083] Film thickness is measured using a Mitutoyo snap gauge No. 28049-10.
[0084] Device Fabrication:
[0085] A layout of the device fabrication is shown in
[0086] The dried PCL film is removed from the carrier web and place across the cavity shaping die in
[0087] The ultrasonic welding process utilizes the Branson model 941AE/947DA ultrasonic welding system and custom fixtures for forming the cylindrical cavity, filling the cavity, and final sealing as shown in
[0088] To fabricate a device, [0089] The first PCL layer is removed from the release liner substrate and is placed manually onto the bottom mold. The vacuum pump is turned on. Application of vacuum forces the PCL layer to form a recess by taking the shape of the slot in the mold under the vacuum. [0090] A syringe is used to fill the recess with the gel (glycerin) (
[0095] Repeating the drawing shown in
[0096] Important aspects of the process: [0097] Ultrasonic welding in a precise location of the perimeter of the cylindrical shape [0098] Controlled vacuum to form the PCL cylinder in the cavity without damaging the PCL film [0099] A distribution of vacuum holes inside the cavity to spread the vacuum source over a broader surface area [0100] A flat surface (land area) around the cavity to allow the film to be tensioned uniformly across the cavity, allowing film shaping into the cavity via vacuum [0101] Teflon (or other not stick coatings) on the cavity and flat land area to prevent the PCL from sticking to these surfaces [0102] Drug carrier (matrix) can be a liquid, gel, paste, powder, or other form. The technique and tools used to fill the cavity with the material will be dependent on the form of the filler.
[0103] Any patents or publications mentioned in this specification are indicative of the levels of those skilled in the art to which the invention pertains. These patents and publications are herein incorporated by reference to the same extent as if each individual publication was specifically and individually indicated to be incorporated by reference.