| US3070703A | 1962-12-25 | |||
| US4159017A | 1979-06-26 | |||
| US4116223A | 1978-09-26 | |||
| US4079591A | 1978-03-21 |
| 1. | A system for collecting solar energy which com¬ prises in combination: a concave reflector directed to receive radi¬ ation from the sun and to focus said energy on a focal area, means for driving said reflector to follow the diurnal course of the sun, a boiler containing a quantity of mercury dis¬ posed in said focal area, whereby said mercury is brought to a boil by energy from the sun which is focused in said focal area, a mercury turbine, a first conduit system connected between said mercury boiler and said mercury turbine for delivering mercury vapor to drive said turbine to rotate, an electrical generator coupled in driven relation to said mercury turbine, a mercury condenser connected by conduit means to receive the mercury vapor output from said mercury turbine, a fluid coil enclosed in said mercury condenser, a fluid distribution system, a second conduit system including pumping means for pumping the output from said fluid distribution system into the fluid coil in said mercury condenser for heat ex¬ change with the condenser vapor in said mercury condenser, and for pumping the heated fluid from said mercury conden¬ ser into said distribution system for dissipating the heat from said fluid in said dissipation system. |
| 2. | The combination in accordance with claim 1, in which the fluid in the coil in said mercury condenser is water. |
| 3. | The combination in accordance with claim 1, in which the fluid in the coil in said mercury condenser is steam. |
| 4. | The combination in accordance with claim 3, in which a superheater is connected into said second conduit system between said mercury condenser and said distribution system for superheating the steam from said condenser before directing it into said distribution sys¬ tem. |
| 5. | The combination in accordance with claim 1, which includes a conventional heating system having a stack through which heated waste gases escape to the atmosphere, and said first conduit system is constructed to pass through said stack in heatexchange relation with said waste gases. |
| 6. | The combination in accordance with claim 5, wherein the portion of said first conduit system con¬ structed to pass through said stack includes a coil of pipe in heat exchange with said waste gases. OMPI /. |
Background of the Invention
This relates in general to solar energy systems; and more particularly, to systems in which the sun's rays are focused for the purpose of vaporizing fluid which is utilized to generate power and supply heat for residential, industrial and commercial consumption.
Many of the prior-art systems utilize steam boilers which require high pressures in order to drive turbine or other power-generating equipment. This re¬ quires the use of systems, including boilers, conduits, turbine and condensers, which are of high strength ma¬ terials and are therefore expensive to construct and maintain.
Further, one of the disadvantages of many types of prior art solar systems is that they are completely dependent on sunlight, and do not function at all during the night, or on cloudy days. It is therefore a principal object of this invention to provide improvements in systems for fo- cusing solar energy to vaporize fluid.
A more particular object of the invention is to provide a solar energy system of the type de- scribed which is cheaper to build and maintain than the systems of the prior art. Another object of the invention is to provide a system of the type described which- is readily adapted to augment the heat derived from solar
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energy with waste heat derived from other sources.
These and other objects, features and advantages are realized in a system in which solar energy is focused on a mercury boiler by a concave or parabolic mirror, trained to follow the sun, the vapor from which boiler is pumped through a conduit system which leads into a mercury turbine. The exhaust vapor from the turbine passes into a condenser where it is condensed back to liquid by heat- exchange with a coil bearing water. The water in the coil is heated up and may be converted to steam, being pumped through an independent heat distribution system, the output from which passes back into the condenser coil. As an alternative, the conduit from the mercury boiler may be passed through the exhaust gas stack of a conventional oil, gas or coal heating system, so as to absorb heat from the exhaust gases during periods when no sunlight is available.
A particular advantage of the system of the present inventi over prior systems in which solar energy is focused to vaporize water or other low density fluids, is that the pressure of mercury vapor is substantially lower than that of steam at the high temperatures generated at the focal point of the reflector by solar radiation. Hence, the conduit systems and generating and condensing equip- ment of the present invention need not be constructed of as high-strength material, and are less expensive to build and maintain. Another advantage of the present invention is that, in the alternative, the mercury vapor conduit is constructed to pass through the stack of a conventional heating system to thereby absorb waste heat from an additional energy source, therby providing an auxiliary energy source for periods when the sun is not shining. Further advantages of the mercury vapor system of the present invention over systems employing water is that there is no danger of the system freezing up in winter; and there is less danger of leakage in the system than with conventional steam systems.
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These, and other objects, features, and advantages of the present invention will be better understood from a detailed study of the specification hereinafter with reference to the attached drawing. Fig. 1, which is a schematic showing of a preferred embodiment of the present invention. Detailed Description of the Invention
Referring to Fig. 1, there is shown a solar reflector 1 which may, for example, be in the form of a parabolic dish of a type well-known in prior art practice. The parabolic dish reflector 1 is mounted on a bearing member 2a, which, for example, may take the form of a metal semisphere, preferably of steel which is drilled with a cylindrical bore perpendicular to the plane of the drawing which accommodates and is disposed to rotate or swivel about a rod mounted in the support member 2. In accordance with well-known prior art practice, the reflector 1 may be always trained on the sun, and may be driven to rotate in such a manner that the sun's rays as received, are always substantially perpendicular to its principal axis, and will thus concentrate the rays at the focal area of the reflector.
The- solar collector system comprising the para¬ bolic dish 1 and associated driving means Is designed to cooperate with a πercury-vapor-steam electric generating system of the general form disclosed in Mechanical En¬ gineers Handbook, 1941 Edition, edited by Lionel S. Marks, published by McGraw Hill Book Company, Sect. 9, Power Generation, Chap. 4, Steam Turbines by F. Hodgkins, Fig. 28, pages 1247, 1248 and 1249.
The mercury boiler 3, which rests at the focal area of reflector 1 on a conventional open support, not shown, comprises, for example, a retort of platinum of general spherical form, the upper end of which takes the form of a neck 3a. The mercury boiler 3 holds a quantity of liquid mercury, which is heated to a temperature of about 975 degress Fahrenheit, and generates mercury vapor
at a pressure of about 140 pounds per square inch gauge. These values are indicated in the Mechanical Engineers' Handbook, 1941 Edition, supra, Sect. 4, in the Chapter entitled Thermal Properties of Bodies and Thermodynamics by H. C. Weber, page 336, Table 23.
At top speed, assuming mercury vapor at a pressure of 125 pounds per square inch gauge at the turbine, and 3 inches of mercury absolute at the tur¬ bine exhaust, the turbine 5 drives the shaft 5a at the rate of 900 revolutions per minute. Shaft 5a, in turn, is coupled to operate a conventional electrical generator 10 of a form well-known in prior art practice. When the shaft 5a operates at the rate of 900 revolutions per minute, the generator 10 will produce alternating current electricity across the terminals 10a, 10b.
The output vapor from the mercury turbine 5 passes into the condenser 7 through the conduit 4d, which may be of substantially similar cross-section and material as the conduits 4a, 4b and 4c. The er- σury condenser 7, may be of any of the forms well- known in prior art practice.
A coil 8a, of stainless steel pipe is cen¬ trally disposed in the condenser 7. Water is pumped into coil 8a by a hot water pump 12, which may be of a type well-known in prior art practice.
The water is further heated by a heat-exchange with the mercury vapor, which gives out heat as it is again reduced to liquid mercury. The latter passes from conduit 4d leading from mercury condenser 4d' through the mercury pump 13, out through the conduit 4e, and into the mercury boiler 3 where it is reconverted to mercury vapor. The mercury pump 13 is of a type well- known in prior art practice.
The water from coil 8a of the condenser 7 which has been heated in a heat exchange with the con¬ densed mercury vapor, is passed out through the conduit 8b. In a preferred embodiment, this water (or steam if
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it has been heated hot enough) passes into a conventional super-heater 9 which may be of the general form well-known in prior art practice.
The hot water or superheated steam, as the case may be, then passes into a conventional utilization sys¬ tem 11 which may be a residential, industrial or commer¬ cial heating plant, the output water (or condensed steam) returning from which passes through the conduit 8d and the hot water pump 12, and back into the condenser coil 8a through the conduit 8e.
It will be understood that the invention is not limited to the specific form of system, shown by way of illustration, but only by the scope of the ap¬ pended claims.