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Pulse purge regenerative gas dryer
   
Document Number
US Patent 7000332
Issued Date
February 21, 2006
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Abstract
A gas drying apparatus is provided having at least two desiccant-containing towers which alternately receive moisture-saturated air from an inlet to be dried during a drying phase, and then receive dry air during a regeneration phase to regenerate the desiccant which had previously adsorbed moisture from saturated air during the drying phase. The apparatus diverts a portion of dry air flowing along one of two flow paths including a first flow path having a heater and a pulse purge regeneration control valve for selectively enabling delivery of heated dry air to the tower being regenerated, and a second flow path which bypasses the first flow path and includes a bypass valve for selectively permitting delivery of unheated dry air to the tower being generated so as to cool the desiccant therein. A temperature sensing arrangement is provided for monitoring and maintaining the internal temperature of heated dry air delivered into the tower being regenerated.
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Number of Claims:
5
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Owner
Pneumatech, Inc. (Kenosha, WI)
Published
February 21, 2006
Application Number
11/100,165
Filed
April 6, 2005
US Classification
34/330   34/343 34/473 95/122 95/123 95/98
Int'l Classification
F26B   3/00   (20060101)  
Examiner
USPTO Field of Search
34/330   34/332   34/343   34/345   34/473   34/80   95/98   95/117   95/118   95/119   95/120   95/121   95/122   95/123  
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7413595 - Control scheme for hybrid PSA/TSA systems - Owned by Air Products and Chemicals, Inc. (Allentwon, PA)

An improved control scheme is set forth for an adsorption process that removes water and carbon dioxide (CO.sub.2) from a feed gas using a hybrid of both temperature swing (i.e. TSA) and pressure swing (PSA) to regenerate the adsorbent. The control scheme comprises adjusting the quantity of heat to be provided by the regeneration gas as a function of temperature data taken within a strategic portion of the water selective adsorbent zone. The strategic portion corresponds to the location for the desired transition from regeneration by temperature swing, to regeneration by pressure swing. In a preferred embodiment of the present invention, said quantity of regeneration heat is also adjusted as a function of the water content of the feed gas.

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Description
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