This invention relates generally to the field of composite materials and, more particularly, to gas-impermeable composite materials which include carbon fibers and are intended for use in high pressure applications.
Pressure vessels are used in many industries to store gasses under high pressures. These pressure vessels are generally constructed out of carbon-based composites, namely, a high strength plastic reinforced with carbon fiber filaments. A separate plastic or aluminum, thick-walled, rigid liner is used as the form on which the carbon fiber filaments are wound during the manufacturing process.
The metal and plastic liners are costly to manufacture and must go through a variety of resource-intensive processes. The manufacturing process involves a filament winding process in which a fiber tow is first impregnated with a matrix resin and then applied at predetermined angles to a rotating liner or mandrel (which is typically made of aluminum or high-density polyethylene). After the impregnated fibers are applied, the structure must be cured, usually by heat.
The plastic or aluminum liner is permanently trapped within the vessel to achieve a permeation barrier. This adds unnecessary weight to the vessel and reduces its usable volume. Additionally, the liner can become detached from the composite shell, thereby eroding its structural integrity and causing leaks. Furthermore, these metal and polymeric liners experience cyclical fatigue which decreases the useful life of the vessel.
By way of example, a composite pressure vessel used for high pressure cryogenic storage is disclosed in U.S. Pat. No. 7,867,589 to DeLay, the subject matter of which is hereby incorporated by reference. The inner layer of the vessel is a matrix of fiber (e.g., aramid fiber) and polyurethane resin. The outer layer encapsulates the inner layer, provides structural support to that layer, and is a matrix of fiber (e.g., aramid or carbon fiber) and resin (e.g., high ductability resin or polyurethane matrix that performs well at low temperature). Once the inner and outer layers are cured, the mandrel is removed. Because this vessel is designed to contain a liquid stored at low temperatures, it does not require an impermeable barrier. Therefore, the vessel can make use of carbon (or aramid) fibers and forego a metal or polymeric liner.
Adsorbed natural gas provides a method of storing a lot more natural gas per volume of storage than can be achieved with simple compression. Using this method, the vessel includes a sorbent. The sorbent, which is typically an active carbon with a high surface area, adsorbs the natural gas and allows the vessel to store well over 100 times the volume of gas than it could otherwise store, and do so at pressures less than ⅕ of those otherwise and at ambient temperatures.
Prior art ANG pressure vessels are metal pressure vessels with an adsorbent core (see e.g. US Pat. App. Pub. No. 2014/0166664 A1 to Lin et al.). The vessels are relatively heavy—thereby reducing fuel efficiency when used in motor vehicle applications—and can corrode and experience cyclical fatigue, thereby leading to failure.
There is a need for a high pressure, liner-free vessel for storing compressed natural gas that is more easily manufactured than prior art carbon- and aramid-fiber based vessels, does not involve a metallic or polymeric liner, and is lighter weight and smaller than metal pressure vessels of equivalent size and pressure ratings.
A pressure vessel made according to this invention includes a carbon fiber reinforced plastic with an integrated permeation barrier as its innermost layers. The barrier can be metal-free impermeable film or metallic additives could be used in the film. In one embodiment of the vessel, a removable tooling process is employed in the manufacture of the vessel. In another embodiment of the invention, the tooling remains as an integral part of the vessel and serves as a sorbent. During the manufacturing of both embodiments, the permeation barrier is sprayed on and integrated into the composite.
The vessel, which is well-suited for high pressure gas storage (100-10,000 psig), is lighter weight than prior art vessels and has more usable volume (in a range of about 8-10%) than a same-dimensioned prior art vessel. The permeation barrier encapsulates one or more ports or fittings of the vessel to reduce or eliminate the potential for gaps through which gas can escape.
Objectives of this invention are to provide a pressure vessel or tank which (1) is plastic liner- and aluminum liner-free; (2) avoids the use of a separate, rigid liner and incorporates impermeability layers or strata into the composite structure; (3) provides a reinforced plastic having superior strength, durability and gas barrier properties when compared to that used in current art pressure vessels; (4) can be used for pressure vessels in gas storage applications in a range of about 100 psi and up; (5) can provide a liner-less or liner-free pressure vessel (e.g. a type III or IV tank) for use in non-cryogenic storage applications above 100 psi; (6) can be used to store gases, liquids or powder; (7) is formed (in a non-adsorbed natural gas embodiment) using water-soluble tooling; (8) can be non-spherical or non-cylindrical in shape (in addition to being spherical- or cylindrical-shaped; and (9) is easier to manufacture, more cost effective and more environmentally friendly than lined tanks.
An adsorbed natural gas (“ANG”) pressure vessel made according to this invention is a formed by an all-composite shell formed around a rigid porous structure that serves as a mandrel when forming the shell and as a sorbent when the vessel is in use. The rigid porous structure may be any suitable, moldable or formable sorbent or structure for adsorbing natural gas, preferably an activated carbon or its equivalent.
In its final form, the composite shell and rigid porous structure comprise a single monolithic, liner-less structure. In one embodiment, the vessel is able to withstand internal pressures in range of 500 to 1,500 psi. In other embodiments, the vessel is able to withstand internal pressures in a range of 100 to 500 psi or 1,500 to 3,600 psi or more.
Other objectives of this invention include providing an ANG pressure vessel or tank that: (1) is all-composite material and metal-free; (2) uses the sorbent material as the mandrel when forming the vessel; (3) improves the volumetric and gravimetric efficiencies relative to existing adsorbed natural gas tanks; (4) reduces the effective pressure needed to store a volume of gas; (5) is conformable shaped (cylindrical or non-cylindrical); (6) avoids the use of a separate, rigid liner; (7) incorporates impermeability layers or strata into the composite structure; (8) can be used for pressure vessels in gas storage applications in a range of about 100 psi and up; and (9) can be used for cryogenic storage applications.
Non-cylindrical shaped vessels can also be made using a non-cylindrical shaped mandrel.
A composite vessel made according to this invention is especially well-suited for use in high-pressure storage of gaseous matter such industrial and fuel gasses in compressed natural gas applications and compressed hydrogen fuel applications. A composite material made according to this invention also can be used in vessels to store other types of gasses, liquids and powders under pressure (or not under pressure) and can be used in one of its embodiments for adsorbed natural gas (“ANG”) applications.
The pressure vessel includes a carbon fiber reinforced plastic with an integrated permeation barrier as its innermost layer. Alternating layers of permeation barrier and carbon fiber reinforced plastic may also be used for the vessel's shell. During manufacturing, the permeation barrier is sprayed on and integrated into (entrained in or drawn into) the composite. The vessel, which is well suited for high pressure gas storage is lighter weight than prior art vessels and has more usable volume than same-dimensioned prior art vessel. The permeation barrier encapsulates one or more ports or fittings of the vessel to reduce or eliminate the potential for gaps through which gas can escape. In one embodiment, a removable tooling process is employed in the manufacture of the vessel. In another embodiment, a permanent tooling process is employed and the tooling serves as a sorbent material for the vessel.
Referring to
Alternatively, composite material 10 can include alternating layers of the impermeable film layer 13 and carbon fiber roving and resin layer 15 (see
Referring to
A first application step 107 applies one or more layers 11 of impermeable film 13 to the fittings 23 and mandrel 30 to create a seamless barrier. Preferably, the film 13 is applied manually or by spraying. A second application step 109 makes use of a filament winder (not shown) and applies one or more layers 15 of carbon fiber roving and resin at preprogrammed angles to fully encapsulate, and bond to, the layer or layers 11 of impermeable film 13. Preferably, each layer 15 is applied at a different preprogrammed angle than its adjacent layer 15 or 11 (see e.g.
The assembled structure 41 consisting of the shell 21, fittings 23, and mandrel 30 is removed from the filament winder and cured, preferably at room temperature for about 4 hours, during a curing step 111. A post-curing step 113 then takes place in an oven at a desired temperature and duration.
A mandrel removing step 115 is accomplished by removing the post-cured material 37 from the oven and flushing the mandrel 30 with warm water, thereby removing the mandrel.
Referring to
A first application step 107 applies an impermeable film 11 to the fittings 53 and mandrel 60 to create a seamless barrier. Preferably, the film 13 is applied manually. A second application step 109 makes use of a filament winder (not shown) and applies carbon fiber roving and resin layer 15 at preprogrammed angles to fully encapsulate, and bond to, the layer or layers 11 of impermeable film 13. Each layer 15 is preferably at a different preprogrammed angle than its adjacent layer 15 or 11 (see e.g.
The assembled structure 71 consisting of shell 51, fittings 51, and sorbent mandrel 60 is removed from the filament winder and cured, preferably at room temperature for about 4 hours, during a curing step 111. A post-curing step 113 then takes place in an oven at a desired temperature and duration.
The mandrel 60 remains a part of the vessel 50.
Preferred embodiments of the pressure vessel have been described so as to enable of person of ordinary skill in the art to make and use the invention, which is defined by the claims listed below. The claims cover designs that substitute one or more of the elements listed with equivalent elements.
This application claims the benefit of U.S. Prov. Pat. Appl. No. 61/907,809 for a Composite Pressure Vessel for Gas Storage and a Method for Its Production, filed Nov. 22, 2013.
Number | Name | Date | Kind |
---|---|---|---|
2127712 | Blaslus | Aug 1938 | A |
2363967 | McLean | Nov 1944 | A |
2629354 | Gay | Feb 1953 | A |
2933214 | Douyard | Apr 1960 | A |
3047191 | Young | Jul 1962 | A |
3508677 | Laibson | Apr 1970 | A |
3598275 | Francois | Aug 1971 | A |
3866792 | Minke | Feb 1975 | A |
4004706 | Guldenfels | Jan 1977 | A |
4053081 | Minke | Oct 1977 | A |
RE30489 | Abbott | Jan 1981 | E |
4244482 | Baumgart | Jan 1981 | A |
4252244 | Christian | Feb 1981 | A |
4296869 | Jawad | Oct 1981 | A |
4398646 | Pechacek | Aug 1983 | A |
4671831 | Mohan | Jun 1987 | A |
4699288 | Mohan | Oct 1987 | A |
4925044 | Hembert | May 1990 | A |
5004120 | Hembert | Apr 1991 | A |
5012950 | Knappe | May 1991 | A |
5025943 | Forsman | Jun 1991 | A |
5419139 | Blum | May 1995 | A |
5476189 | Duvall | Dec 1995 | A |
5518140 | Lenz | May 1996 | A |
5534318 | Andre De La Porte | Jul 1996 | A |
5653358 | Sneddon | Aug 1997 | A |
5758796 | Nishimura | Jun 1998 | A |
5772938 | Sharp | Jun 1998 | A |
5822838 | Seal | Oct 1998 | A |
5875648 | Boye | Mar 1999 | A |
6015065 | McAlister | Jan 2000 | A |
6022435 | Palazzo | Feb 2000 | A |
6138861 | Palazzo | Oct 2000 | A |
6145692 | Cherevatsky | Nov 2000 | A |
6145693 | Berglund | Nov 2000 | A |
6230922 | Rasche | May 2001 | B1 |
6547092 | Chervatsky | Apr 2003 | B1 |
6708502 | Aceves | Mar 2004 | B1 |
6989198 | Masuda | Jan 2006 | B2 |
7255904 | Tai | Aug 2007 | B2 |
7641949 | DeLay | Jan 2010 | B2 |
7867589 | DeLay | Jan 2011 | B2 |
8074826 | Cronin | Dec 2011 | B2 |
8297468 | DeLay | Oct 2012 | B1 |
8308017 | Schlag | Nov 2012 | B2 |
8377529 | Bekele | Feb 2013 | B2 |
8481136 | Sneddon | Jul 2013 | B2 |
8561829 | DeLay | Oct 2013 | B1 |
8740009 | Otsuka | Jun 2014 | B2 |
8815360 | Beckwith | Aug 2014 | B2 |
8932695 | Villarreal | Jan 2015 | B1 |
20030111473 | Carter | Jun 2003 | A1 |
20030175457 | Jousse | Sep 2003 | A1 |
20050087536 | Caudill | Apr 2005 | A1 |
20060054628 | Matsuoka | Mar 2006 | A1 |
20060096993 | Takashima | May 2006 | A1 |
20060163261 | Sugiura | Jul 2006 | A1 |
20080121643 | Blencoe | May 2008 | A1 |
20090057319 | Schlag | Mar 2009 | A1 |
20090308874 | Lindner | Dec 2009 | A1 |
20100276434 | Berger | Nov 2010 | A1 |
20110240655 | Lindner | Oct 2011 | A1 |
20120048865 | Eihusen | Mar 2012 | A1 |
20130306651 | Markert | Nov 2013 | A1 |
20140166664 | Lin et al. | Jun 2014 | A1 |
20150240993 | DeLay | Aug 2015 | A1 |
20150316207 | Laney | Nov 2015 | A1 |
Number | Date | Country | |
---|---|---|---|
61907809 | Nov 2013 | US |