Claims
- 1. A process for selecting cellulose acetate butyrate for use in an osmotic delivery device, wherein the process comprises:
- 1) generating differential scanning calorimetry ("DSC") profiles for representative samples from lots of cellulose acetate butyrate ("CAB") being considered for use in the osmotic delivery device, said profiles having primary and secondary DSC minimum temperature peaks and
- 2) selecting for use in the manufacture of said osmotic delivery devices those lots of CAB for which the samples exhibit an acceptable DSC profile, which, if analyzed on a Du Pont 2100 Thermal Analyzer set to equilibrate the sample at a temperature of 30.degree. C., and heat the sample to 270.degree. C. at 20.degree. C. per minute, would exhibit a DSC profile wherein the profile has a minimum temperature peak above 228.degree. C. and an area under the secondary minimum temperature peak which is equal to or less than 30% of the total combined areas under the primary and secondary DSC peaks.
- 2. The process of claim 1, further including
- 1) determining the butyryl, acetyl and hydroxyl content of the cellulose acetate butyrate; and
- 2) selecting for use in the osmotic delivery device those lots of the cellulose acetate butyrate that have a butyryl content of between 16.5% and 18.2%, an acetyl content between 29.1% and 31.0% and a hyroxyl content that is less than or equal to 1.0%.
- 3. A process according to claim 2 wherein the cellulose acetate butyrate has a hydroxyl content of between 0.55% and 0.95%.
- 4. A process for making an improved semi-permeable membrane component formed from cellulose acetate butyrate, said process comprising:
- 1) generating DSC profiles for representative samples from lots of cellulose acetate butyrate ("CAB") being considered for use in the device, said profiles having a primary and secondary minimum temperature peaks; and
- 2) forming said membrane component from those lots of CAB for which the samples exhibit an acceptable DSC profile, which, if tested on a Du Pont Thermal Analyzer 2100 set to equilibrate the sample at a temperature of 30.degree. C. and heat the sample to 270.degree. C. at 20.degree. C. per minute, would exhibit a DSC profile wherein the profile has a minimum temperature peak above 228.degree. C. and an area under the secondary peak which is equal to or less than 30% of the total combined areas under the primary and secondary minimum temperature peaks.
- 5. A process for making an osmotic delivery device having acceptable start-up characteristics and comprising a semipermeable membrane component formed from cellulose acetate butyrate, said process comprising:
- 1) generating DSC profiles for representative samples from lots of the cellulose acetate butyrate ("CAB") being considered for use in the device, said profiles having a primary and secondary minimum temperature peaks; and
- 2) forming said membrane component from those lots of CAB for which the samples exhibit an acceptable DSC profile, which, if tested on a Du Pont Thermal Analyzer 2100 set to equilibrate the sample 30.degree. C. and heat the sample to 270.degree. C. at 20.degree. C. per minute, would exhibit a DSC profile wherein the profile has a minimum temperature peak above 228 C. and an area under the secondary minimum temperature peak which is equal to or less than 30% of the total combined areas under the primary and secondary peak.
- 6. A process for selecting CAB for use in the manufacture of osmotic delivery devices having acceptable start-up characteristics comprising:
- a) determining endothermic properties for representative samples from lots of CAB being considered for use in the device; and
- b) selecting for use in the device those lots of CAB for which the endothermic properties of the samples correspond to the endothermic properties of CAB known to produce acceptable start-up characteristics.
- 7. A process for manufacturing an osmotic delivery device having acceptable start-up characteristics and comprising a semipermeable membrane component formed from cellulose acetate butyrate ("CAB"), said process comprising:
- a) determining endothermic properties for representative samples from lots of CAB being considered for use in the device; and
- b) forming said membrane component from those lots of CAB for which the endothermic properties of the samples correspond to the endothermic properties of CAB known to produce acceptable start-up characteristics.
- 8. A process according to claim 7 wherein the cellulose acetate butyrate has a hydroxyl content of between 0.55% and 0.95%.
Parent Case Info
This application is a continuation of application Ser. No. 07/945,082, filed Sep. 15, 1992, abandoned and benefit of the filing date of said earlier filed application is claimed under 35 U.S.C. .sctn.120.
US Referenced Citations (24)
Continuations (1)
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Number |
Date |
Country |
Parent |
945082 |
Sep 1992 |
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