Adsorbents and fluid supply packages and apparatus comprising same
US-2020206717-A1 · Jul 2, 2020 · US
US12140272B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12140272-B2 |
| Application number | US-202318102259-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 27, 2023 |
| Priority date | Jan 27, 2022 |
| Publication date | Nov 12, 2024 |
| Grant date | Nov 12, 2024 |
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Described are systems and methods of storing adsorbing diborane on carbon adsorption medium. The invention discloses a vessel for storing diborane. The vessel includes: a vessel interior; microporous carbon adsorbent in the vessel interior; diborane in the vessel interior at least partially adsorbed on the microporous adsorbent. The microporous adsorbent includes slit pores between graphite layers at a graphite layer spacing that increases an activation energy required for diborane degradation relative to an activation energy of degradation of non-adsorbed gaseous diborane at ambient pressure, and at the same temperature.
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The invention claimed is: 1. A vessel for storing diborane, the vessel comprising: a vessel interior, microporous carbon adsorbent in the vessel interior, diborane in the vessel interior at least partially adsorbed on the microporous adsorbent, and the microporous adsorbent comprises slit pores between graphite layers at a graphite layer spacing that increases an activation energy required for diborane degradation relative to an activation energy of degradation of non-adsorbed gaseous diborane at ambient pressure, and wherein the activation energy is a total of: one-half the activation energy of reaction (i), plus the activation energy of reaction (ii): B 2 H 6 →2BH 3 (i), B 2 H 6 +BH 3 ,→B 3 H 9 . (ii) 2. The vessel of claim 1 , comprising diborane at a concentration of at least 50 percent (atomic) based on a total amount of adsorbed and gaseous chemical species in the vessel interior. 3. The vessel of claim 1 , wherein the graphite sheets have a graphite layer spacing equal to or less than 0.8 nanometers. 4. The vessel of claim 1 , wherein at least 50 percent of pores of the adsorbent have a graphite layer spacing in a range from 0.4 to 0.8 nanometers. 5. The vessel of claim 1 , wherein at least 80 percent of pores of the adsorbent have a graphite layer spacing in a range from 0.4 to 0.8 nanometers. 6. The vessel of claim 1 , wherein at least 80 percent of pores of the adsorbent have a graphite layer spacing in a range from 0.4 to 0.7 nanometers. 7. The vessel of claim 4 , wherein the stored gaseous molecular diborane exhibits a reduced rate of degradation during storage at 22 degrees Celsius, compared to diborane stored on microporous carbon adsorbent having a lower percentage of pores that have a graphite layer spacing in a range from 0.4 to 0.8 nanometers. 8. The vessel of claim 5 , wherein the stored gaseous molecular diborane exhibits a reduced rate of degradation during storage at 22 degrees Celsius, compared to diborane stored on microporous carbon adsorbent having a lower percentage of pores that have a graphite layer spacing in a range from 0.4 to 0.8 nanometers. 9. The vessel of claim 6 , wherein the stored gaseous molecular diborane exhibits a reduced rate of degradation during storage at 22 degrees Celsius, compared to diborane stored on microporous carbon adsorbent having a lower percentage of pores that have a graphite layer spacing in a range from 0.4 to 0.7 nanometers. 10. A method of reversibly storing diborane in a vessel, the method comprising: to a storage vessel comprising microporous carbon adsorbent that comprises slit pores between graphite sheets that have a graphite layer spacing that increases an activation energy required for diborane degradation relative to an activation energy of degradation of non-adsorbed gaseous diborane, adding to the vessel diborane gas, the diborane becoming adsorbed onto the microporous carbon adsorbent, and storing the adsorbed diborane in the vessel, and wherein the activation energy is the total of: one-half the activation energy of reaction (i), plus the activation energy of reaction (ii): B 2 H 6 →2BH 3 , (i) B 2 H 6 +BH 3 ,→B 3 H 9 . (ii) 11. The method of claim 10 , wherein the vessel contains diborane at a concentration of at least 50 percent (atomic) based on a total amount of adsorbed and gaseous chemical species in the vessel interior. 12. The method of claim 10 , wherein the stored diborane experiences reduced degradation during storage compared to an amount of degradation of gaseous molecular diborane stored on microporous carbon adsorbent having a lower percentage of pores that have a graphite layer spacing in a range from 0.4 to 0.8 nanometers.
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