1. Field of the Invention
The invention relates to the long-term storage of hydrogen generated from wind power or solar energy, and more specifically to the supply, by hydrogen, of winter heat to farm buildings and harvest-time heat to crop dryers.
2. Description of the Invention Background
Generating hydrogen from wind power by water electrolysis is not a new concept, nor is storing the resulting hydrogen for later use (see U.S. Pat. Nos. 5,592,028; 5,900,330; 4,716,736; 6,459,231; 4,462,213; 4,311,011; and 6,591,617).
However, the storage devices and systems proposed so far are all uneconomical for long-term storage on farms. For instance, generating a large volume of hydrogen during the warm months and storing it for house-heating in winter has been economically impractical because of the high initial and operating costs of the means hitherto suggested. Devices like compressed hydrogen cylinders, reversible metal hydrides, liquid hydrogen systems, carbon nanotubes initially loaded with liquid hydrogen, water towers, and other proposed concepts are not cost-effective in the large volumes needed for summer-to-winter or spring-to-fall storage. For example, compressed hydrogen cylinders cost about $75 per standard cubic meter of hydrogen storage capacity; water towers, using pumped water to occupy the space not filled by hydrogen, cost about $500 per standard cubic meter of hydrogen; while reversible metal hydrides currently cost almost $5,000 per standard cubic meter of stored hydrogen. The one economical scheme that has been proposed for the long-term storage of hydrogen is to store it in a sealed cavern. However, most farms do not have caverns on their land or near-by, so this scheme lacks general applicability to the heating of farm buildings and structures. Yet the need for a low-cost, renewable energy source for farmhouse heating and crop drying is growing quite rapidly as fossil fuels get scarcer and ever more expensive.
The main reason why storage means like compressed gas cylinders and water towers are uneconomical for long-term hydrogen storage is the high cost of the relatively heavy enclosures needed to withstand the pressures of gas, liquid, or both. One object of the present invention is to overcome these cost problems so that hydrogen generated at any time of the year can be economically stored on-site and saved for a time when hydrogen's heat of combustion is most needed and therefore most valuable. An installed cost range of about $3 to $6 per standard cubic meter, representing a saving of 92% to 96% of the installed cost of the present state of the art, is a purpose of this invention.
The present invention provides a relatively inexpensive means of storing on farms, at near-ambient temperature and pressure, hydrogen generated from wind power or solar energy. The means are cost-effective despite their bulk because they can be made from relatively cheap, lightweight materials and because they rest on relatively cheap rural land. The main reason for the low cost of the materials is that the invention eliminates the stresses due to gas or liquid pressures, thus allowing inexpensive, lightweight structures to be used.
The invention comprises means of storing hydrogen in inflatable and deflatable balloons made of metallized polyethalene phthalate polymer film or some other suitable material. The balloons are protected against the elements, including ground water, by shields made of relatively thin-gauge steel or other suitable materials. The shields are ventilated to prevent the build-up of hydrogen from slow leakage through the balloon skins.
The relatively thin gauge, inexpensive steel construction of the shields is made possible because the invention drastically reduces the loads on the structures and the resulting stresses.
A complete understanding of the present invention may be obtained by reference to the accompanying drawings, when considered in conjunction with the subsequent detailed description, in which:
Referring to the drawings, which are for the purpose of illustrating the present preferred embodiment of the invention and not for the purpose of limiting the same,
The balloon is made of 88-gauge heat-sealable, metallized polyethylene phthalate polymer film (brand name Melinex) with a thickness of 0.00088 inch. The film is a commercial item made by, among others, the Dunmore Corporation in Bristol, Pa. and is sold as type DC040 Melinex. It comes in a width of 74 inches and in any desired length up to 20,000 yards. Its tensile strength is 37,000 poi, its rated elongation is 100%, it is metallized to an optical density of 2.5 to 3.0 using a Tobias TBX densitometer, it weighs one pound per 286 square feet, and it currently costs about 30 cents per linear yard. For the 30 ft. diameter by 125 ft. length of the preferred embodiment, the film costs less than $250. This is economically negligible compared to the total cost of the storage device and system.
The balloon can be assembled on site by heat-sealing horizontal strips of film along the intended length of the balloon and vertical strips to form the end surfaces. To facilitate the heat-sealing process, the strips can be assembled with the help of a supporting frame, also known as a “buck”, over which the strips are pulled to slide horizontally during the sealing process. The preferred cross-section of the buck is a circle about 10% smaller than the cross-section of the fully assembled balloon.
The balloon is protected by a lightweight shield 12 preferentially assembled from thin-gauge steel sheets (27 or 28 gauge) bolted or riveted together by means of long, narrow steel angles (not shown) placed along the length of shield 12. The sheets thus cover the entire perimeter of the shield which preferentially has an octagonal cross-section and is about 30 ft high & about 125 ft long. The spaces between adjacent steel sheets are lightly sealed with a commercial-type sprayed sealant (not shown), a type widely available and well-known to those skilled in the art. The function of the seals is to help shield the balloon from the elements, not to provide hermetic closure or pressurized containment, neither of which is necessary for this invention and either of which would be too expensive.
The two octagonal ends 26 of the shield are also made of thin-gauge steel sheets bolted or riveted together and spray-sealed like the steel sheets covering the length of the shield.
Hydrogen gas is blown into or out of the balloon through pipes 14 and 15. Gas flowmeter 16 feeds flow rate data electrically to gas volume totalizer 17. Flowmeter 16 measures both inflating and deflating flow rates, allowing the totalizer to keep track of the total net flow of hydrogen.
The air space 32 between the outside of the balloon and the inside of the shield is ventilated with outside air by means of blower 18 to prevent the possible accumulation of small amounts of hydrogen leaking into the air space. The ventilating air exhausts through pipe 19. Excessive accumulation of hydrogen in the air space is detected by means of hydrogen gas detector 20; excessive accumulation of oxygen within the balloon is detected by means of oxygen gas detector 21; and rapid evacuation of the balloon is effected, when either of the mixture compositions approaches the flammability threshold, by means of rapid release valve 22. Detectors 20 and 21 and valve 22 are commercial items well known to those skilled in the art.
For economic reasons, the leakage of hydrogen must be kept small over the period, typically months, during which hydrogen has to be stored. In the embodiment of
The shield is anchored to the ground by means of anchors 23, 24, and 25, which are preferentially made of heavy-gauge steel. The shield is further secured by means of anchoring steel rods 9 and 10 and other similar one (not shown) along the length of the shield.
When both the electrolyzer 31 and the heat source 34 are active, the oxygen produced by the electrolyzer flows directly to the heat source. When the heat source is active but the electrolyzer is not, air blower 35 supplies combustion air to support the burning within the heat source of hydrogen coming out of storage. When the electrolyzer is active but the heat source is not, hydrogen flows into the storage device 33 while oxygen from the electrolyzer is vented and discarded.
When the heat source is active, heat is conveyed by conventional heat-transfer means, not shown but well-known in the art, to either farmhouse 37 or crop dryer 38 or in rare cases to both at the same time. Water vapor produced by the combustion of hydrogen in heat source 34 is condensed and collected in vapor condenser 36, a common type of commercial device; the resulting pure water is pumped to the electrolyzer 31 where it provides the renewable part of the pure water required for electrolysis to take place.
Since modifications and changes varied to fit particular operating requirements and environments will be apparent to those skilled in the art, the invention is not considered limited to the preferred embodiment chosen for purposes of disclosure, and covers all changes and modifications which do not constitute departures from the true spirit and scope of this invention.
Having thus described the invention, what is desired to be protected by Letters of Patent is presented in the subsequently appended claims.