Process for the continuous manufacture of a polyisobutylene based transdermal patch
The present invention is directed to a process for manufacturing a transdermal delivery device comprising a backing layer, a release liner, and an adhesive layer between the backing layer and release liner. More specifically, the invention is directed to a process of preparing an adhesive layer, wherein the adhesive layer is comprised of polyisobutylene and an active pharmaceutical ingredient.
1. A continuous process for the production of an adhesive composition comprising:
a) pre-processing a non-granulated high molecular weight polyisobutylene (HMW PIB) having a molecular weight ranging from about 200,000 g/mol to about 425,000 g/mol in a single-screw extruder to form a bulk HMW PIB material, wherein said bulk HMW PIB material is in a compressed, continuous feed form;
b) extruding said bulk HMW PIB material in an extruding apparatus, wherein said HMW PIB is extruded;
c) simultaneously extruding said extruded HMW PIB with low molecular weight polyisobutylene (LMW PIB) in said extruding apparatus to produce high shear so as to form an extruded melt, wherein a ratio of the amount of HMW PIB to LMW PIB in said melt is about 65:35;
d) adding an active pharmaceutical ingredient (API) to said extruded melt to produce an extruded API/PIB melt; and
e) discharging said extruded API/PIB melt to a die to form said adhesive composition, wherein said adhesive composition comprises about 93% to about 97% PIB and about 3% to about 7% API.
2. The process of claim 1 , wherein said single screw extruder is heated to a temperature between about 85° F. and about 500° F.
3. The process of claim 1 , wherein said high molecular weight polyisobutylene has a molecular weight ranging from about 250,000 g/mol to about 425,000 g/mol.
4. The process of claim 1 , wherein said HMW PIB and said LMW PIB are simultaneously extruded in a twin-screw extruder.
5. The process of claim 1 , wherein said low molecular weight polyisobutylene has a molecular weight ranging from about 35,000 g/mol to about 100,000 g/mol.
6. The process of claim 1 , wherein said low molecular weight polyisobutylene has a molecular weight ranging from about 36,000 g/mol to about 75,000 g/mol.
7. The process of claim 1 , wherein said low molecular weight polyisobutylene is heated to a temperature between about 65° F. and about 500° F.
8. The process of claim 1 , wherein said active pharmaceutical ingredient is selected from the group consisting of an opioid receptor antagonist, anesthetics, local anesthetics, anti-asthmatics, anti-inflammatory substances, opiates, bronchodilators, analgesics, anti-hypertensive drugs, hormones, contraceptives, anti-nauseants, anti-histamines, stimulants, anti-anginal drugs, opiate receptor agonists, dopamine agonists, anticholinergics, neuromuscular drugs, anabolic drugs, anti-emetics, decongestants, vasoconstrictors, sedatives, psychotropics, diuretics, vasodilators, hypnotics, anti-pyretics, and anti-spasmodics.
9. The process of claim 1 , wherein said active pharmaceutical ingredient is selected from the group consisting of lidocaine, piroxicam, fentanyl, sufentanyl, albuterol, buprenorphine, clonidine, diclofenac, estradiol, ethinyl estradiol, granisetron, ketoprofen, loratadine, memantine, methylphenidate, naltrexone, nicotine, nitroglycerin, norelgestromin, oxybutynin, risperidone, rivastigmine, rotigotine, scopolamine, selegiline, testosterone, desloratadine, dexmethylphenidate, and tulobuterol.
10. The process of claim 1 , further comprising adding one or more additives to said API/PIB melt.
11. The process of claim 1 , further comprising laminating said adhesive composition between a backing layer and a release liner to produce a transdermal delivery device.
12. A continuous process for the production of an adhesive composition comprising:
a) pre-processing a non-granulated high molecular weight polyisobutylene (HMW PIB) having a molecular weight ranging from about 200,000 g/mol to about 425,000 g/mol in a single-screw extruder to form a bulk HMW PIB material, wherein said bulk HMW PIB material is in a compressed, continuous feed form;
b) extruding said bulk HMW PIB material having a molecular weight ranging from about 200,000 g/mol to about 425,000 g/mol in a twin-screw extruding apparatus, wherein said HMW PIB is extruded;
c) simultaneously extruding said extruded HMW PIB with low molecular weight polyisobutylene (LMW PIB) in said extruding apparatus to produce high shear so as to form an extruded melt; wherein said LMW PIB has a molecular weight ranging from about 35,000 g/mol to about 100,000 g/mol; and wherein a ratio of the amount of HMW PIB to LMW PIB in said melt is about 65:35;
d) adding an active pharmaceutical ingredient to said extruded melt to produce an extruded API/PIB melt; and
e) discharging said extruded API/PIB melt to a die to form said adhesive composition, wherein said adhesive composition comprises about 93% to about 97% PIB and about 3% to about 7% API.
13. The process of claim 12 , wherein said HMW PIB has a number average molecular weight of about 250,000, said LMW PIB has a number average molecular weight of about 51,000 and said API is lidocaine.
14. The process of claim 1 , wherein the HMW PIB is free from fillers.
15. The process of claim 1 , wherein the API is lidocaine, and said adhesive composition comprises lidocaine in an amount of about 5%.