Solar heating system

• US 4,603,685 A
• Filed: 06/21/1983
• Issued: 08/05/1986
• Est. Priority Date: 06/21/1983
• Status: Expired due to Fees

• Current Assignee: Soltrac Incorporated
• Original Assignee: Institut national de la recherche scientifique
• Inventors: Bergevin, Benoit, Rheault, Fernand, Jean, Benoit
• Primary Examiner(s): Jones, Larry
• Application Number:
  US06/506,542
• Time in Patent Office: 1,141 Days
• Field of Search: 126/433, 126/432, 126/435, 126/437, 126/417, 126/428, 126/419, 126/421, 126/423, 126/434, 165/104.19, 165/104.21, 165/104.22, 165/104.24, 165/104.25, 165/104.31
• US Class Current: 126/587
• CPC Class Codes: F24D 11/003 combined with solar energy
• CPC Class Codes: F24S 10/95 having evaporator sections and condenser sections, e.g. heat pipes
• CPC Class Codes: F28D 15/0266 with separate evaporating and condensing chambers connected by at least one conduit; Loop-type heat pipes; with multiple or common evaporating or condensing chambers F28D15/043 takes precedence
• CPC Class Codes: F28D 2020/0078 Heat exchanger arrangements
• CPC Class Codes: F28F 2250/08 Fluid driving means, e.g. pumps, fans
• CPC Class Codes: Y02B 10/20 Solar thermal
• CPC Class Codes: Y02E 10/40 Solar thermal energy, e.g. solar towers
• CPC Class Codes: Y02E 10/44 Heat exchange systems

Abstract

The present invention relates to a solar water heating system operating in a closed circuit and making use of a change of phase in a working fluid as a heat transfer medium, comprising: at least one collector to be exposed to sunlight for transmitting radiant solar energy to a working fluid and thus converting the fluid into a liquid-vapor mixture; a hot water storage reservoir connected to a heat exchanger; a pump for returning the working fluid to the collector; and a pipe means connecting all of the above mentioned components. The system according to the subject invention is characterized in that it comprises a separator connected to both ends of the collector; a pipe for returning the liquid coming from the liquid-vapor mixture to the lower end of the absorber of the collector in such a manner that it is constantly wet; and two pipes connecting the separator to the exchanger, one for circulating the vapor to the exchanger where it condenses and the other for allowing return of the condensed liquid to the separator, by means of the pump; the exchanger being of the type that allows free gravity flowing of the condensed liquid to the pump; and the system is further characterized in that the pump is placed below the mean level of the liquid in the exchanger and in that it ensures the return of the condensed liquid accumulated at the bottom of the exchanger to the separator.

Claims

1. A solar water heating system operating in a closed circuit and making use of a change of phase of a working fluid as a heat transfer medium, comprising:

at least one collector to be exposed to sunlight for transmitting radiant solar energy to the working fluid in order to convert said fluid into a liquid-vapour mixture, said collecotr having an inlet and an outlet through which the liquid-vapour mixture exits;

a heat exchanger having an inlet and an outlet, said heat exchanger being of the type that allows free gravity flowing of the liquid that condenses therein;

a hot water storage reservoir connected to the heat exchanger to recover and store the heat extracted from the working fluid in said heat exchanger;

first piping means connecting the outlet of said at least one collector to the inlet of said heat exchanger, said first piping means including a phase-separator mounted thereon adjacent the outlet of said at least one collector to extract the liquid phase from the vapour phase in the liquid-vapour mixture exiting said collector;

second piping means for returning the liquid phase extracted in said phase separator to the inlet of said at least one collector whereby said collector is constantly wet and the heat exchanger is supplied with the working fluid in vapour phase only through said first piping means;

third piping means for connecting the outlet of the heat exchanger to the inlet of said at least one collector through the phase separator and said second piping means; and

pumping means for returning the working fluid from the heat exchanger to said at least one collecotr through said third piping means, said pumping means being placed below the mean level of the liquid condensing in said heat exchanger to exclusively return the condensed liquid accumulated at the outlet of said heat exchanger to said phase separator through said third piping means wherein said pump comprises two concentric reservoirs spaced from each other so as to define a small volume therebetween, the internal reservoir being made of insulating material and the external reservoir being made of heat conducting material;

said external reservoir being closed but connected to the outlet of said heat exchanger by means of a gravity feed pipe provided with an inlet unidirectional valve and also to the third piping means via an outlet unidirectional valve, said external reservoir being further provided with a vapour exhaust valve adapted to equilibrate the pressures between the gravity feed pipe and the pump during filling thereof;

internal reservoir further enclosing a mechanism for sampling the liquid to be vaporized.

2. A system as claimed in claim 1 wherein said third piping means for returning the liquid to the separator is concentric to said first piping means used for conveying the vapour to the exchanger, both of said piping means being enclosed in an insulating sheath.

3. A system as claimed in claim 1, wherein said internal reservoir has an aperture in its bottom for sampling the liquid to be vaporized and a float made of insulating material for thermally insulating the liquid surface in contact with the space above said internal reservoir;

said vapour exhaust valve and said aperture for discharging the liquid to be vaporized being opened and closed in a reverse manner by means of two obturators mechanically interconnected said obturators being actuated together by the action of the float housed in the internal reservoir.

4. A system as claimed in claim 3, wherein said obturators are provided at the ends of a rigid stem passing through the float, said stem and the lower obturator attached thereto closing by gravity the aperture at the bottom of the internal reservoir during filling of the pump, said stem having such a length that the upper obturator does not close the aperture of the vapour exhaust valve when the lower obturator closes the aperture for sampling the liquid.

5. A system as claimed in claim 4 wherein said obturators are needles cooperating with corresponding seats.

6. A system as claimed in claim 1, wherein said internal reservoir contains a siphon which is actuated only when the liquid in the internal reservoir has reached a predetermined level, said liquid flowing into the volume between the two reservoirs until said internal reservoir is empty;

said internal reservoir further containing a float made of insulating material for thermally insulating the liquid surface in contact with the space above said internal reservoir;

said vapour exhaust valve being closed by means of an obturator when the siphon is operating said obturator being actuated by the action of the float housed in the internal reservoir.

7. A system as claimed in claim 6, wherein said obturator is provided at the upper end of a rigid stem.

8. A solar water heating system operating in a closed circuit and making use of a change of phase of a working fluid as a heat transfer medium, comprising:

at least one collector to be exoosed to sublight for transmitting radiant solar energy to the working fluid in order to convert said fluid into a liquid-vapour mixture, said collector having an inlet and an outlet through which the liquid-vapour mixture exits;

a heat exchanger having an inlet and an outlet, said heat exchanger being of the type that allows free gravity flowing of the liquid that condenses therein;

a hot water storage reservoir connected to the heat exchanger to recover and store the heat extracted from the working fluid in said heat exchanger;

first piping means connecting the outlet of said at least one collector to the inlet of said heat exchanger, said first piping means including a phase-separator mounted thereon adjacent the outlet of said at least one collector to extract the liquid phase from the vapour phase in the liquid-vapour mixture exiting said collector;

second piping means for returning the liquid phase extracted in said phase separator to the inlet of said at least one collector whereby said collector is constantly wet and the heat exchanger is supplied with the working fluid in vapour phase only through said first piping means;

third piping means for connecting the outlet of the heat exchanger to the inlet of said at least one collector through the phase separator and said second piping means; and

pumping means for returning the working fluid from the heat exchanger to said at least one collector through said third piping means, said pumping means being placed below the mean level of the liquid condensing in said heat exchanger to exclusively return the condensed liquid accumulated at the outlet of said heat exchanger to said phase separator through said third piping means wherein said pump for returning the liquid accumulated at the outlet of the exchanger to the separator is a vapour pressure pump wherein vapour pressure is generated from a portion of the condensed liquid sampled only when a predetermined level of liquid into the pump is reached by means of a continuous external heat source when a predetermined level of liquid is reached in the pump.

9. A system as claimed in claim 8, wherein the external heat source is controlled by means of a thermostat.

10. System as claimed in claim 9, wherein said heat source is controlled by means of a thermostat.

11. A system as claimed in claim 9, wherein said external heat source is controlled by a sunlight intensity detector.

12. A system as claimed in claim 9, wherein said external heat source is controlled by a temperature differential sensor mounted between said at least one collector and said heat exchanger.