This application relates to a heated blanket to be incorporated in an air separation module.
Air separation modules are utilized, and in particular, in aircraft environments. In an air separation module, air is passed into a separation tank. In one type of separation tank, tube sheets are spaced from each other, and connected by hollow fibers. The hollow fibers are constructed such that oxygen can permeate the fiber and move into a chamber surrounding the fiber. Nitrogen passes through the fiber to a downstream chamber. The nitrogen may be utilized to create an inert environment in a fuel tank, resisting flame. The oxygen may be utilized such as for passenger or pilot air supply.
In this known type of air separation module, heat makes the process occur more efficiently. Presently, to provide additional heat, an air compressor supplying the air is run at higher speeds such that the air is hotter when it reaches the air separation module. However, running the compressor at higher speeds decreases efficiency of the overall system. Increasing the speed of the compressor to increase the heat is not a cost-effective way to provide additional heat.
Other methods of increasing heat have been proposed. In general, they require an additional component, such as a valve, etc.
An air separation module and blanket has an air separation module having an air inlet, an oxygen outlet and a nitrogen outlet. At least one tank has air separation elements for separating oxygen from air, and delivers the separated oxygen to the oxygen outlet, and delivers nitrogen to the nitrogen outlet. A resistance heating element is positioned between the blanket and the air separation module. Further, an inventive blanket for use with the air separation module is also disclosed and claimed.
These and other features of the present invention can be best understood from the following specification and drawings, the following of which is a brief description.
The blanket 22 is known, and is utilized to retain heat within the module 20. The air separation process occurs most efficiently when a higher temperature is maintained within the module tanks, as will be described below. The insulation blanket as known may be rubber on the outside, with some insulating polymer on an inner surface. Still, as mentioned above, additional heat is typically required to make the separation process occur most efficiently. As also shown in phantom, the blanket 22 can extend over a portion of the input port 24. Further, the term “blanket” as utilized in this application could extend to a separate blanket portion which covers the inlet portion 24 or other portions. As can be appreciated, air enters the space within the blanket 22 through the air inlet 24.
As shown in
As shown in
Oxygen permeates outwardly through the hollow fibers 42, and will be received in a chamber 46 surrounding the fibers. That oxygen is then delivered to the oxygen outlet line 25. Nitrogen will pass through the fibers, and will not permeate the fibers, instead being delivered to the nitrogen outlet 26.
Terminals 62 and 64 are connected to a voltage, and a resultant resistance within the resistance heating element 60 will then increase the temperature adjacent to the element 100, and thus improve the efficiency of the process. Further, the resistance element may only extend along a portion of the tanks 30, or may extend along the entire length of the tanks 30. The greater the length of the area along which heat is added, the greater the increased efficiency that will be achieved will also be.
In general, the resistance element can be positioned at any location between an inner wall of the blanket 22, and an outer surface of the air separation module itself.
Although an embodiment of this invention has been disclosed, a worker of ordinary skill in this art would recognize that certain modifications would come within the scope of this invention. For that reason, the following claims should be studied to determine the true scope and content of this invention.
Number | Name | Date | Kind |
---|---|---|---|
4225542 | Wall et al. | Sep 1980 | A |
4787919 | Campbell et al. | Nov 1988 | A |
4822659 | Anderson et al. | Apr 1989 | A |
4944776 | Keyser et al. | Jul 1990 | A |
5302189 | Barbe et al. | Apr 1994 | A |
5429662 | Fillet | Jul 1995 | A |
5688306 | Verini | Nov 1997 | A |
6491739 | Crome et al. | Dec 2002 | B1 |
6554261 | Katagiri et al. | Apr 2003 | B2 |
6729359 | Jones | May 2004 | B2 |
6739359 | Jones et al. | May 2004 | B2 |
6913636 | Defrancesco et al. | Jul 2005 | B2 |
6997970 | Crome | Feb 2006 | B2 |
7081153 | Leigh | Jul 2006 | B2 |
7152635 | Moravec et al. | Dec 2006 | B2 |
7159620 | Kissell | Jan 2007 | B2 |
7175692 | Schwalm | Feb 2007 | B2 |
7273507 | Schwalm | Sep 2007 | B2 |
7300494 | Schwalm et al. | Nov 2007 | B2 |
7306646 | Wong | Dec 2007 | B2 |
7445659 | Schwalm | Nov 2008 | B2 |
7833314 | Lane et al. | Nov 2010 | B2 |
7892321 | Aagesen et al. | Feb 2011 | B2 |
20010000380 | Buxbaum | Apr 2001 | A1 |
20070137478 | Stein et al. | Jun 2007 | A1 |
Number | Date | Country |
---|---|---|
63258620 | Oct 1988 | JP |
2102710 | Apr 1990 | JP |
7185253 | Jul 1995 | JP |
2003291894 | Oct 2003 | JP |
Number | Date | Country | |
---|---|---|---|
20100263537 A1 | Oct 2010 | US |