Presaturation of Supercritical CO2 with Water for Decellularization of Matrices
US-2015315540-A1 · Nov 5, 2015 · US
US10576395B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10576395-B2 |
| Application number | US-201715810766-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 13, 2017 |
| Priority date | Mar 14, 2017 |
| Publication date | Mar 3, 2020 |
| Grant date | Mar 3, 2020 |
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A system and method for removing residual glutaraldehyde from a natural polymer scaffold crosslinked with glutaraldehyde is provided. The system includes a cleaning solution comprising carbon dioxide and one or more polar solvents and an environmental chamber that can include and a treatment chamber. The environmental chamber is maintained at a temperature greater than 31.1° C. and the carbon dioxide is maintained at a pressure greater than 7.38 megapascals to form supercritical carbon dioxide. A crosslinked natural polymer scaffold treated via the glutaraldehyde removal system and method can have a glutaraldehyde content of less than about 3 parts per million. A crosslinked natural polymer scaffold cleaning solution comprising supercritical carbon dioxide and one or more polar solvents is also provided.
Opening claim text (preview).
What is claimed is: 1. A method for removing residual glutaraldehyde from a natural polymer scaffold, the method comprising: treating the natural polymer scaffold with a cleaning solution comprising carbon dioxide and one or more polar solvents at a temperature greater than 31.1° C., wherein the carbon dioxide is maintained at a pressure greater than 7.38 megapascals to form supercritical carbon dioxide, and wherein the one or more polar solvents comprises ethanol, methanol, isopropanol, acetic acid, or a combination thereof. 2. The method of claim 1 , wherein a pump compresses the carbon dioxide before the carbon dioxide is delivered to the natural polymer scaffold. 3. The method of claim 1 , wherein the carbon dioxide and the one or more polar solvents are mixed for a time period ranging from about 5 seconds to about 10 minutes prior to exposing the natural polymer scaffold to the cleaning solution. 4. The method of claim 1 , wherein the cleaning solution is delivered to a treatment chamber containing the natural polymer scaffold. 5. The method of claim 4 , wherein the cleaning solution is delivered to the treatment chamber at a flow rate ranging from about 1.5 millimeters per minute to about 3.5 milliliters per minute. 6. The method of claim 1 , wherein the cleaning solution is mixed in a presaturation chamber, wherein the cleaning solution is delivered from the presaturation chamber to a treatment chamber containing the natural polymer scaffold. 7. The method of claim 1 , wherein the natural polymer scaffold is exposed to the cleaning solution for a time period ranging from about 1 minute to about 2 hours. 8. The method of claim 1 , wherein treating the natural polymer scaffold with the cleaning solution results in the natural polymer scaffold having a denaturation temperature of greater than about 60° C. in 4% acetic acid. 9. The method of claim 1 , wherein treating the natural polymer scaffold with the cleaning solution results in the natural polymer scaffold having an ultimate tensile strength that is greater than about 40 kilopascals when the natural polymer scaffold includes collagen. 10. The method of claim 1 , wherein the method facilitates removal of the residual glutaraldehyde from the natural polymer scaffold so that glutaraldehyde is present in the natural polymer scaffold at a level of less than about 3 parts per million after the natural polymer scaffold is treated with the cleaning solution.
with a supercritical fluid · CPC title
Processes carried out under supercritical conditions · CPC title
by extraction or solubilisation · CPC title
Connective tissue peptides, e.g. collagen, elastin, laminin, fibronectin, vitronectin or cold insoluble globulin [CIG] · CPC title
Cross-Sectional Technologies · mapped topic
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