Purification of air
AssigneeAir Products and Chemicals, Inc.
InventorsMohammad Ali Kalbassi, Anthony Finot, Timothy Christopher Golden, Christopher James Raiswell, Ann Marie Botelho
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AssigneeAir Products and Chemicals, Inc.
InventorsMohammad Ali Kalbassi, Anthony Finot, Timothy Christopher Golden, Christopher James Raiswell, Ann Marie Botelho
Estimating the term…
Process of reducing water, CO2 and N2O in feed air, which: a first adsorbent such as alumina (25-40% volume) and a second adsorbent such as X zeolite (60-75% volume) are used; the online time of the adsorbent is determined by determining the concentration measured by an analyzer for CO2 concentration at a position within the length of the second adsorbent when a maximum level of N2O is simultaneously obtained at the downstream end of the second adsorbent in the feed direction, wherein the online time is the time taken from commencing passing the feed air to the first and second adsorbents to the measurement by the analyzer of the determined concentration of CO2; at least the second adsorbent is regenerated by heated regeneration gas at a temperature of 140° C.-220° C.; and the molar ratio of the regenerating gas to feed air supplied during one iteration of the cycle is 0.08-0.5.
A method for determining conditions for the reduction, prior to cryogenic distillation, of the level of water, carbon dioxide and nitrous oxide in a feed air stream in a process comprising:
A process for the reduction of the level of water, carbon dioxide and nitrous oxide in a feed air stream prior to cryogenic distillation, comprising:
An apparatus for the reduction of the level of water, carbon dioxide and nitrous oxide from a feed air stream prior to cryogenic distillation, comprising:
A method of upgrading an apparatus designed to reduce the levels of carbon dioxide, nitrous oxide and water from a feed air stream by a temperature swing adsorption process in order that it can provide a reduction in the level of nitrous oxide in the feed air stream without use of an adsorbent having a Henry's Law selectivity measured at 30° C. for nitrous oxide compared to carbon dioxide of 0.5 or more, in which the adsorbents contained in the apparatus are removed and replaced with an identical total volume of adsorbent consisting of a layer of a first adsorbent which has a Henry's Law selectivity for carbon dioxide over nitrous oxide measured at 30° C. of at least 12.5 and a second adsorbent whose Henry's Law constant for the adsorption of N2O measured at 30° C. is less than 500 mmol/g/atm and whose Henry's Law selectivity for CO2 over N2O is at most 5, wherein the first adsorbent occupies from 25% to 40% by volume of the total volume occupied by the first and second adsorbents, and in which an analyser for carbon dioxide is placed within the length of the second adsorbent.
Dependencies are inferred from the claim text.