PURIFICATION OF AIR

Purification of Air Process of reducing water, C0 2 and N 0 2 in feed air, which: a first adsorbent such as 5 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 anal...

Ausführliche Beschreibung

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Bibliographische Detailangaben
Hauptverfasser:	MOHAMMAD ALI KALBASSI, TIMOTHY CHRISTOPHER GOLDEN, CHRISTOPHER JAMES RAISWELL, ANN MARIE BOTELHO, ANTHONY FINOT
Format:	Patent
Sprache:	eng
Schlagworte:	BLASTING CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSEGASES [GHG] COMBINED HEATING AND REFRIGERATION SYSTEMS GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS HEAT PUMP SYSTEMS HEATING INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIRCHEMICAL OR PHYSICAL PROPERTIES LIGHTING LIQUEFACTION SOLIDIFICATION OF GASES LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS MANUFACTURE OR STORAGE OF ICE MEASURING MECHANICAL ENGINEERING MIXTURES BY PRESSURE AND COLD TREATMENT PERFORMING OPERATIONS PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL PHYSICS REFRIGERATION OR COOLING SEPARATION TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION TECHNICAL SUBJECTS COVERED BY FORMER USPC TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE TESTING TRANSPORTING WEAPONS
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Beschreibung
Zusammenfassung:	Purification of Air Process of reducing water, C0 2 and N 0 2 in feed air, which: a first adsorbent such as 5 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 analyser for C0 2 concentration at a position within the length of the second adsorbent when a maximum level of N 0 2 is simutaneously obtained at the downstream end of the second adsorbent in the feed direction, wherein the online 10 time is the time taken from commencing passing the feed air to the first and second adsorbents to the measurement by the analyser of the determined concentration of C0 ; 2 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 0.08-0,5. is 15 FIG. 3 -43-