A method of manufacturing a pressure vessel for containing a compressed gas is disclosed in which a thin wall cylinder is wrapped with resin impregnated reinforcing fiber and shrink wrap polymeric tape prior to being cured to eliminate voids in the cured composite and to form a protective layer on the vessel.
Compressed natural gas (CNG) and pressurized hydrogen are finding increasing application as an alternative fuel for internal combustion engines. As a result, there is a need to have relatively light weight high strength pressure vessels to contain the pressurized gas. The mechanical requirements for such pressure vessels include a relatively high burst strength on the order of 10,000 psi.
There are four general categories of pressure vessels that are used to store compressed gas. Type 1 cylinders are all metal and are mechanically inefficient since circumferential stress loads in a pressurized gas cylinder are approximately double the axial stress loads. Type 2 cylinders comprise a metal liner with a resin impregnated continuous reinforcing fiber assembly that is hoop-wrapped only over the cylindrical body of the metal liner. All axial loads are borne by the metal liner and the hoop-loads are borne by a combination of the metal liner and the composite reinforcement. Type 3 cylinders comprise a metal liner with resin impregnated continuous fiber assembly fully wrapped over the end domes and hoop wrapped over the cylinder body. Type 4 cylinders comprise a non-metallic liner with a resin impregnated fiber assembly fully wrapped over the end domes and hoop wrapped over the cylinder body. For Type 2, Type 3 and Type 4 CNG tanks, the current standard adopted by industry and government requires that the composite overwrap be designed for high reliability under sustained loading and cyclic loading. This reliability is achieved by meeting or exceeding the composite reinforcement stress ratio values of 2.25× the service pressure. For typical CNG tanks with a service pressure of 3,600 psi, this is about 8,100 psi.
Filament winding is one of the most established composite manufacturing processes, and is the method of choice for producing CNG tanks. The first winding machines were developed in the late 1960's and were initially developed to produce composite rocket casings. During 1990's the production of composite pressure vessels with the filament winding technique was further developed. Over the last 30 years, filament winding machines have been equipped with modern CNC controllers, improved machine frames, automatic start and stop modules, and robotic systems to supply the gas impermeable liners to the filament winding machines. Although these developments have reduced the winding time, the labor demand of the process is still relatively high. The main reasons are the problems associated with the use of resin baths for fiber impregnation and the relatively low winding speeds associated with fiber impregnation that is coupled with filament winding. This problem has been overcome by the use of pre-impregnated fiber assemblies (i.e., pre-preg tows).
Two winding patterns are possible for compressed gas cylinders: hoop and axial (also referred to as isotensoid). Type 2 vessels are hoop-wrapped only. Types 3 and 4 vessels are generally a combination of hoop and axial (isotensoid) wrapping. Vessels can be filament wound in the same winding machine if it is equipped more than one winding head.
In addition to the use of reinforcing fibers, the manufacture of a pressure vessel requires a polymeric resin, such as a thermosetting epoxy for example, to bond the reinforcing fibers to each other and to the cylinder liner. The resin also plays an important function of transferring stresses from fiber to fiber.
There are various methods to apply the resin to the fibers. A resin transfer molding process can be used in which layers of dry un-impregnated fibers can be wrapped onto the cylinder which is then placed into a female mold. Uncured relatively viscous resin is then infused under pressure into the mold. Once infused, the resin is heated, and the resin thus completes its polymerization cycle and hardens. The resin transfer fiber reinforced cylinder is then removed from the mold. The primary limitations of this process are the relatively high cost of the molds and tooling, and the time it takes for the resin to cure or polymerize.
CNG tanks can also be fabricated using the wet-filament winding process. This is a process in which the fiber tow is passed through a resin bath to impregnate the tow and then wrapped around a mandrel prior to curing in an oven at elevated temperature. Wet winding has substantial resin waste that is inherent to the process, and is notorious for creating substantial volatile organic compounds during the manufacturing process. Wet wound cylinders can also have non-load bearing voids in the cured composite structure.
Another method for applying resin involves the use of pre-impregnated or “prepreg” fibers that have had partially cured resin applied to them prior to the wrapping process. Since the resin is partially cured, the resin is no longer in the liquid state, and the fibers can be wound onto the liner by automated equipment.
One way to overcome voids in the finished product is to apply pressure by means of a flexible sleeve to the outer surface of the fibers prior to the final resin cure. This is commonly done by using a “bagging process” whereby the pre-impregnated fiber covered cylinder is placed in a relatively flexible polymer bag and then placed in a heated autoclave. While this approach is mechanically feasible, the relatively high cost of autoclave equipment increases the cost of the finished product.
A liner is wrapped with pre-impregnated fiber tow using a conventional filament winding process. The prepreg tow provides a more controlled resin content and less variation in the cured part than other processes, and provides a cleaner process than a wet process, with little or no emission of volatile gas compounds. The resin may contain a nano material that increases the strength of the resulting composite structure. A shrink wrap tape is wrapped over the reinforcing fibers, and heat is applied to the tape to apply a compressive force to the reinforcing fibers in order to preclude the formation of voids in the cured resin and to cure the resin itself. The tape can be perforated to allow resin to weep onto the outer surface of the shrink wrap tape, forming a protective layer on the finished product.
A wide variety of reinforcement materials can be used for the fiber 14, including, but not limited to, carbon fiber, aramid fiber, high strength polyethylene fiber, and fiberglass fiber. In one embodiment, carbon fibers were employed. The reinforcement materials may take the form of tow or slit tape. The tow may be round or oval or flattened in cross-section.
The pre-preg materials coated onto the fiber 14 may comprise either conventional thermoset resins, or newly developed nano-material infused thermoset resin. Nano-materials resin has improved tensile strength permitting the use of less carbon fiber based material than that required with conventional prepregs. The reduced carbon fiber reduces the cost of the wrap, and enables the wrap to be completed in less time.
By heating the shrink wrapped cylinder 12 in an oven at atmospheric pressure, the shrink tape layers 18 and 20 shrink, and provide substantial compressive forces to consolidate the filament wound pressure vessel and eliminate voids in the final product. The heat shrink tape may be left on after curing to provide a protective covering for the tank. Suitable shrink tape for this purpose is sold under the name Dunstone Hi-Shrink Tape. The tape may be perforated or un-perforated.
It has been determined that by wrapping high shrink polyester tape over the finished wound cylinder, the cylinder can be heated to the relatively low temperature of 300° F. using a fast cure time of approximately one hour to obtain an essentially void free cured composite. The polyester tape is known to have excellent resistance to most substances. It is resistant to acids, oxidizers such as hydrogen peroxide and most solvents. Polyester also has excellent resistance to hydrocarbon fuels, oils and lubricants. Accordingly, the protective polyester layers provided by the tape layers 18 and 20 will add to the durability and environmental resistance of the resulting compressed gas tanks.
The heat shrink tape used in the layers 18 and 20 may also be perforated. The perforations allow excess resin to weep through the tape and after curing provide a protective layer of resin over the tape, thus obviating the need to apply a protective coating on the final composite cylinder through by means of a separate process step. A suitable perforated shrink tape is produced by Dunstone Company, Inc and is sold under the name Perforated Hi-Shrink Tape 220. The tape will begin to shrink at about 65° C., and has been used in applications up to 180° C. If unrestrained, the tape will shrink 20% after 15 minutes at 150° C. Layers of shrink tape are wound onto the outer surface of the fiber wrapped tank to form a longitudinal wrap layer 18 as shown in
The high pressure composite storage tank disclosed herein is manufactured using a new pressure application system that is coupled with a conventional filament winding system. The manufacturing system is capable of being highly automated, and is able to deposit prepreg carbon fiber on either Type 3 or Type 4 liners in an expedited manner. Further, the proposed manufacturing system enables “moldless” curing and a relatively fast resin cure cycle. The tanks may be manufactured using novel nano-material carbon-fiber based prepregs that offer improved mechanical properties. The use of these materials can reduce weight and manufacturing time by lessening the number of winding layers that are required to achieve the desired strength, leading to cost reductions.
Having thus described the device, various modifications and alterations will occur to those skilled in the art, which modifications and alterations will be within the scope of the device as defined by the appended claims.
This application claims priority of U.S. provisional application Ser. No. 61/614,207 filed Mar. 22, 2012 and international application PCT/US2013/030725 filed Mar. 13, 2013.
Filing Document | Filing Date | Country | Kind |
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PCT/US2013/030725 | 3/13/2013 | WO | 00 |
Number | Date | Country | |
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61614207 | Mar 2012 | US |