WO1984004581A1 - A solar energy powered system for the production of cold - Google Patents

A solar energy powered system for the production of cold Download PDF

Info

Publication number
WO1984004581A1
WO1984004581A1 PCT/DK1984/000040 DK8400040W WO8404581A1 WO 1984004581 A1 WO1984004581 A1 WO 1984004581A1 DK 8400040 W DK8400040 W DK 8400040W WO 8404581 A1 WO8404581 A1 WO 8404581A1
Authority
WO
WIPO (PCT)
Prior art keywords
coolant
absorber
evaporator
tubes
condenser
Prior art date
Application number
PCT/DK1984/000040
Other languages
French (fr)
Inventor
Svend Friberg
Peter Korsgaard
Peder Worsoee-Schmidt
Original Assignee
Kaptan Aps
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kaptan Aps filed Critical Kaptan Aps
Priority to BR8406897A priority Critical patent/BR8406897A/en
Priority to AU29619/84A priority patent/AU2961984A/en
Publication of WO1984004581A1 publication Critical patent/WO1984004581A1/en
Priority to DK11685A priority patent/DK11685D0/en
Priority to FI850223A priority patent/FI850223A0/en

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B27/00—Machines, plants or systems, using particular sources of energy
    • F25B27/002—Machines, plants or systems, using particular sources of energy using solar energy
    • F25B27/007—Machines, plants or systems, using particular sources of energy using solar energy in sorption type systems
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S10/00—Solar heat collectors using working fluids
    • F24S10/70—Solar heat collectors using working fluids the working fluids being conveyed through tubular absorbing conduits
    • F24S10/75—Solar heat collectors using working fluids the working fluids being conveyed through tubular absorbing conduits with enlarged surfaces, e.g. with protrusions or corrugations
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B17/00—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type
    • F25B17/08—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type the absorbent or adsorbent being a solid, e.g. salt
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/272—Solar heating or cooling
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B10/00—Integration of renewable energy sources in buildings
    • Y02B10/20—Solar thermal
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/40—Solar thermal energy, e.g. solar towers
    • Y02E10/44—Heat exchange systems

Definitions

  • a solar energy powered system for the production of cold A solar energy powered system for the production of cold.
  • the invention relates to a system for the produc- tion of cold with an absorption cooling system compris ⁇ ing an evaporator positioned in a thermally insulated space to which evaporator a coolant is supplied in the liquid state from a condenser through a coolant vessel and from which evaporator coolant in the vapour state is sucked by an absorber which is designed as a solar col ⁇ lector and comprises a humidity absorbing compound for the suction of said coolant at night hours at a compara ⁇ tively low temperature and delivery of said coolant in the vapour state to the condenser at day hours at a com- paratively high temperature, said coolant suction and delivery to and from the absorber taking place through one and the same tube connection to the evaporator and the condenser.
  • Such demands may exist with respect to the cooling of food, pharmaceuticals and other products which do not stand storage at elevated temperature, as well as air conditioning of living rooms for living beings, includ ⁇ ing in particular residential rooms.
  • a solar energy powered cooling system of the kind mentioned is known in principle from DE-A-609,104.
  • the humidity absorbing compound is accommo ⁇ dated in a tube coil in a solar collector unit arranged on the roof of the building and is connected with a con ⁇ denser cooled by a cold accumulator incorporated in a separate self-circulating system so that cooled liquid is collected in the cold accumulator at night hours for cooling the condenser at day hours.
  • a system for the pro ⁇ duction of cold of the kind referred to is characterized in that the absorber comprises a number of parallel ab ⁇ sorber tubes which are connected with said tube connec ⁇ tion through a manifold, and each of which comprises said humidity absorbing compound in a direct thermal contact with parallel evaporator tubes of a secondary self- circulating cooling circuit positioned coaxially in said absorber tubes, a solar energy actuated blocking valve device being arranged in a coolant supply tube between a condenser and said evaporator tubes in said secondary cooling circuit. Since the daily temperature variation i.e.
  • the temperature difference between day and night hours may be utilized to energize a periodically operating absorp ⁇ tion cooling system, the process in the system is con ⁇ ducted in the way that evaporation of coolant in the thermally insulated space takes place at night hours during which the absorber is not exposed to solar energy.
  • an intensified direct cooling of the absorber tubes by means of the secondary self- circulating cooling circuit the humidity absorbing cora- pound which may be of a known type such as calcium chlorid can be brought onto a temperature at which it will effectively absorb coolant in the vapour state from the evaporator.
  • Duting the cooling period in which the solar energy actuated blocking valve device is open for circulation of coolant in the secondary circuit substan ⁇ tially the entire quantity of coolant in the system will be absorbed in the compound in the absorber tubes.
  • the cooling of the compound in the absorber tube by means of the secondary cooling circuit is of "essential importance to the efficiency of the process it is an essential characteristic of the invention that a good direct thermal contact exists between the compound and the evaporator tubes of the secondary cooling circuit.
  • a preferred embodiment of the system according to the invention is further characterized in that the eva- porator tubes of the secondary cooling circuit are each enclosed by a heat-conducting finned tube with external longitudinal fins for dividing the space of annular cross section between the finned tube and the external wall of the absorber tube in a number of chambers for accommodating said humidity absorbing compound.
  • the absorber comprising the compound accommodated in absorber tubes may be designed as a conventional solar collector.
  • the solar energy actuated blocking valve device between the evaporator and the condenser of the seconda ⁇ ry cooling circuit may in a simple way be constituted by a so-called bubble pump which in principle functions in the same manner as a water closure, and is exposed at the outlet side to coolant in the vapour state in the evaporator tubes of the secondary circuit which by the temperature to which the bubble pump is exposed under the influence of the solar energy in day hours gives rise to a bubble generation effective to block for the flow -of coolant in the liquid state from the condenser to the evaporator tubes.
  • a so-called bubble pump which in principle functions in the same manner as a water closure, and is exposed at the outlet side to coolant in the vapour state in the evaporator tubes of the secondary circuit which by the temperature to which the bubble pump is exposed under the influence of the solar energy in day hours gives rise to a bubble generation effective to block for the flow -of coolant in the liquid state from the condenser to the evaporator tubes.
  • FIG. 1 shows a schematic diagram of an embodiment of a cold production system according to the invention
  • Fig. 2 a cross sectional view of an absorber tube in the absorber cooled periodically by a secondary cool- ant circuit.
  • the coolant evaporator 1 is positioned in a thermally insulated space 2 for which cooling is desired.
  • the space 2 may constitute for example a cooling box for food, pharmaceuticals or other products for which cold storage is desired, whereby in consideration of the periodical operation of the system to be explained in the following a cold reservoir 3 may be provided in the space 2 to maintain a low tempe- rature in the period in which no evaporation of coolant takes place.
  • the space or container 2 may also constitute for instance a cooling or freezing space for the production of ice blocks or a cooling chamber for an air conditioning system.
  • the evaporator 1 By means of an inlet line 4 for coolant in the liquid state the evaporator 1 is connected with a coolant vessel 5 having a capacity exceeding the total coolant quantity of the system.
  • the evapora ⁇ tor 1 is connected through an outlet line 6 for cool- " ant in the vapour state to the vessel 5 at a higher level than the liquid level when the total coolant quan- 5 tity of the system is collected in the vessel 5.
  • An inlet tube 7 for coolant in the liquid state to the vessel 5 constitutes the lowermost part of a single tube connection between the vessel 5 and the absorber of the system, since the inlet tube 7 is
  • the absorber 12 is designed as a solar collector and comprises a number of parallel absorber tubes 13 which are connected to the- tube 11 through a manifold 14 at the upper end of the absorber 12 which in this
  • a secondary cooling circuit comprises an evaporator hav-
  • each of the upper tubes 13 a coaxially extend ⁇ ing evaporator tube 15, said evaporator tube being connected through a manifold 16 at the lower end of the absorber 12 with an inlet tube 17 for coolant in the liquid state and through a manifold 18 at the
  • the circulation of coolant in the two cooling circuits is shown by arrows of which the solid arrows 22 designate coolant in the vapour state, whereas the dashed arrows 23 designate coolant in the liquid state.
  • the system is operating periodically in a day and night cycles in which the evaporation of coolant in the evaporator 1 takes place at night hours when the absorber 12 is not exposed to solar radiation on one hand, and is exposed on the other hand to further cooling by means of the se ⁇ condary cooling circuit including the evaporator tubes 15 extending coaxially in the absorber tubes 13. There ⁇ by the humidity absorbing compound in the absorber tubes 13 attains a low temperature at which it has a strong absorbing effect relative to the evaporated coola- ⁇ -t.
  • the total coolant quantity in the system which at the beginning of the evaporation period is col ⁇ lected in the coolant vessel 5 will be sucked into the humidity absorbing compound in the absorber tubes 13 in the course of the evaporation period, the absorber tubes 13 being proportioned to accomodate a compound quantity having an absorption capacity corresponding to the total coolant quantity.
  • the influence of solar radiation will cause a temperature increase in the absorber itself on one hand and act on the blocking valve device 21 very rapidly on the other hand to interrupt the coolant circulation in the secondary circuit.
  • the blocking valve device 21 is constituted in the embodiment shown of a so-called bubble pump operating, in principle, in the same way as a water closure since it is exposed to solar radiation on the inlet side whereby vapour bubbles are generated in thelliquid to force any downwards flowing liquid back into the condenser 20 by their rise Thereby, the passage of coolant, from the condenser 20 to the evaporator tubes 15 will be blocked.
  • the humidity absorbing compound in the absorber tubes 13 can no longer retain the absorbed coolant quantity, but delivers the coolant in the vapour state at increasing temperature through the tube connection 11 to the con- denser 8 from which coolant in the liquid state is supplied to the collecting vessel 5 through the tube 1. ' After the end of the day hours functioning as a re ⁇ generation period the process is repeated by cooling of the absorber no longer exposed to solar radiation, and the opening of the blocking valve device 21 for circu ⁇ lation of coolant in the secondary circuit.
  • the absorber tubes may be designed as shown in Fig. 2.
  • flat tangential fins 24 are attached to the external side of the tubes 13 to be positioned immediately below a covering sheet 25 of a type known • p er se in the absorber 12.
  • the width of the fins 24 is adjusted according to the quantity of humidity absorbing compound 26 and the coolant quantity- so that at day hours a te ⁇ pe- - rature is attained by which the compound 26 delivers in the course of the period the total coolant quantity absorbed by ⁇ t in the preceeding night period.
  • the evaporator tubes 15 are surround ⁇ ed by a heat conducting finned tube 27 having a number of longitudinal fins 28 -dividing the space of annular cross section between the tube. 27 and the external wall of the absorber tubes .13 in a number of chambers 29 accommodating each its share of the total quantity of humidity absorbing compound of the absorber tube 13 «
  • the coolant in the primary cooling circuit is pre ⁇ ferably ammonium, but it may be any coolant suitable for absorption cooling systems.
  • a hydrocarbon based coolant may be used such as one of the so-called chloro-fluoro-carbons.
  • the efficiency of the system will be determined by the efficiency of the absorber designed as a solar col ⁇ lector defined by the product of the solar collector ef*-- ficiency, the absorber area, the incoming solar radia- tion and the number of sun hours on one hand and the coolant absorption in the humidity absorbing compound defined by the product of the specific heat of reaction of the compound and the quantity of absorbed coolant per unit of length of the absorber tubes.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Sustainable Energy (AREA)
  • Sustainable Development (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Sorption Type Refrigeration Machines (AREA)
  • Photovoltaic Devices (AREA)
  • Air-Conditioning For Vehicles (AREA)
  • Charge And Discharge Circuits For Batteries Or The Like (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

In a system for the production of cold comprising an absorption cooling system with an evaporator (1) from which coolant is supplied in the vapour state through an absorber (12) to a condenser (8), from which coolant is supplied in the liquid state to a coolant vessel (5) connected with the evaporator (1) the absorption cooling system is designed as a primary system operating periodically in a day and night cycle with the absorber (12) designed as a solar collector having a number of parallel absorber tubes (13) accommodating a humidity absorbing compound for the suction of coolant at night hours at a comparatively low temperature and delivery of coolant to the condenser (8) at day hours at a comparatively high temperature. The coolant transport to and from the absorber (12) takes place through a single tube connection (11). The humidity absorbing compound in the absorber tubes (13) is in a direct thermal contact with the evaporator tubes (15) of a secondary self-circulating coolant circuit, in which a solar energy actuated blocking valve device is connected in a supply line between a condenser (20) and the evaporator tubes (15).

Description

A solar energy powered system for the production of cold.
The invention relates to a system for the produc- tion of cold with an absorption cooling system compris¬ ing an evaporator positioned in a thermally insulated space to which evaporator a coolant is supplied in the liquid state from a condenser through a coolant vessel and from which evaporator coolant in the vapour state is sucked by an absorber which is designed as a solar col¬ lector and comprises a humidity absorbing compound for the suction of said coolant at night hours at a compara¬ tively low temperature and delivery of said coolant in the vapour state to the condenser at day hours at a com- paratively high temperature, said coolant suction and delivery to and from the absorber taking place through one and the same tube connection to the evaporator and the condenser.
The use of solar energy as an energy source has hitherto mainly been adopted for heating purposes where¬ by different types of solar collector systems has gained interest on an equal footing with other kinds of alterna¬ tive energy sources, as far as solar collector systems are concerned particularly for the heating of water with respect to tap water in buildings as well as swimming pool's and the likes. In connection with solar collector powered air condition systems it is known, however, to incorporate an air cooling into a total solution in con¬ nection with water heating by combining the solar collec- tor system with an absorption cooling system.
Particularly in the hotter regions of the world and in places where the access to electric power and other conventional energy sources is difficult or ex¬ pensive, there is a great and up till now badly fulfilled need for cooling systems for many different purposes.
Thus, such demands may exist with respect to the cooling of food, pharmaceuticals and other products which do not stand storage at elevated temperature, as well as air conditioning of living rooms for living beings, includ¬ ing in particular residential rooms.
A solar energy powered cooling system of the kind mentioned is known in principle from DE-A-609,104. In this system, the humidity absorbing compound is accommo¬ dated in a tube coil in a solar collector unit arranged on the roof of the building and is connected with a con¬ denser cooled by a cold accumulator incorporated in a separate self-circulating system so that cooled liquid is collected in the cold accumulator at night hours for cooling the condenser at day hours.
In conventional absorption cooling systems powered for instance by gas heating it is moreover known for iή- stance from SE-A-88,723 and US-A-1,955,612 and 2,130,503 to cool an absorber vessel by means of a separate self- circulating cooling system in which the circulation is interrupted at the start of the boiling period of the absorber by means of a valve which is closed at a pre- determined temperature in the absorber, for instance by thermostatic control.
It is the object of the invention to provide a system for the production of cold of the kind referred to,utilizing solar energy as the only energy source so that no demands are put on accessto electricity and gas or other conventional forms of energy supply, whereby a veryhigh efficiency and thus a high cooling capacity relative to the solar collector efficiency may be obtain-<- ed with a very simple design. According to the invention, a system for the pro¬ duction of cold of the kind referred to is characterized in that the absorber comprises a number of parallel ab¬ sorber tubes which are connected with said tube connec¬ tion through a manifold, and each of which comprises said humidity absorbing compound in a direct thermal contact with parallel evaporator tubes of a secondary self- circulating cooling circuit positioned coaxially in said absorber tubes, a solar energy actuated blocking valve device being arranged in a coolant supply tube between a condenser and said evaporator tubes in said secondary cooling circuit. Since the daily temperature variation i.e. the temperature difference between day and night hours may be utilized to energize a periodically operating absorp¬ tion cooling system, the process in the system is con¬ ducted in the way that evaporation of coolant in the thermally insulated space takes place at night hours during which the absorber is not exposed to solar energy. By providing in this period an intensified direct cooling of the absorber tubes by means of the secondary self- circulating cooling circuit the humidity absorbing cora- pound which may be of a known type such as calcium chlorid can be brought onto a temperature at which it will effectively absorb coolant in the vapour state from the evaporator. Duting the cooling period in which the solar energy actuated blocking valve device is open for circulation of coolant in the secondary circuit substan¬ tially the entire quantity of coolant in the system will be absorbed in the compound in the absorber tubes.
At the beginning of day hours the influence of solar heating will rapidly act on the solar energy actu- ated blocking valve device for interrupting the coolant circulation in the seconday circuit and, on the other hand, bring, the compound in the absorber tubes in the absorber designed as a solar collector onto a temperature at which it can no longer retain the absorbed coolant quantity, but will deliver it in the vapour state to the condenser of the system from which coolant in the liquid state. is transferred to the coolant vessel. During day hours substantially the entire coolant quantity will be collected in the liquid state in the coolant vessel in which it is retained until evaporation starts again as a result of coolant absorption in the compound in the absorber tubes, since the vapour pressure in the tube -
f OMPI connection between the coolant vessel and the absorber prevents evaporation in the former period.
As a result of the fact that transportation of coolant to and from the coolant vessel takes place in separate periods, only one tube connection is required from the absorber through the condenser to the coolant vessel, so that the system according to the invention is simple in design.
Since the cooling of the compound in the absorber tube by means of the secondary cooling circuit is of "essential importance to the efficiency of the process it is an essential characteristic of the invention that a good direct thermal contact exists between the compound and the evaporator tubes of the secondary cooling circuit. To obtain such a good thermal contact and in addi¬ tion an optimal even distribution of the humidity ab¬ sorbing compound over the cross section of the absorber tubes a preferred embodiment of the system according to the invention is further characterized in that the eva- porator tubes of the secondary cooling circuit are each enclosed by a heat-conducting finned tube with external longitudinal fins for dividing the space of annular cross section between the finned tube and the external wall of the absorber tube in a number of chambers for accommodating said humidity absorbing compound.
The absorber comprising the compound accommodated in absorber tubes may be designed as a conventional solar collector. To ensure a high efficiency with re¬ spect to the elevated temperature necessary for the delivery of coolant in the vapour state from the humidity absorbing compound to the condenser in day hours it may be expedient, especially in case of a large absorber area with comparatively long absorber tubes, to increase the solar energy collection capacity of the absorber tubes by providing tangential flat fins on the external side of the absorber tubes. The solar energy actuated blocking valve device between the evaporator and the condenser of the seconda¬ ry cooling circuit may in a simple way be constituted by a so-called bubble pump which in principle functions in the same manner as a water closure, and is exposed at the outlet side to coolant in the vapour state in the evaporator tubes of the secondary circuit which by the temperature to which the bubble pump is exposed under the influence of the solar energy in day hours gives rise to a bubble generation effective to block for the flow -of coolant in the liquid state from the condenser to the evaporator tubes.
In the following the invention will be explained in further details with reference to the drawing in which Fig. 1 shows a schematic diagram of an embodiment of a cold production system according to the invention, and
Fig. 2 a cross sectional view of an absorber tube in the absorber cooled periodically by a secondary cool- ant circuit.
In the embodiment shown in Fig. 1 of a system ac¬ cording to the invention the coolant evaporator 1 is positioned in a thermally insulated space 2 for which cooling is desired. The space 2 may constitute for example a cooling box for food, pharmaceuticals or other products for which cold storage is desired, whereby in consideration of the periodical operation of the system to be explained in the following a cold reservoir 3 may be provided in the space 2 to maintain a low tempe- rature in the period in which no evaporation of coolant takes place. However, the space or container 2 may also constitute for instance a cooling or freezing space for the production of ice blocks or a cooling chamber for an air conditioning system. By means of an inlet line 4 for coolant in the liquid state the evaporator 1 is connected with a coolant vessel 5 having a capacity exceeding the total coolant quantity of the system. In addition the evapora¬ tor 1 is connected through an outlet line 6 for cool- " ant in the vapour state to the vessel 5 at a higher level than the liquid level when the total coolant quan- 5 tity of the system is collected in the vessel 5.
An inlet tube 7 for coolant in the liquid state to the vessel 5 constitutes the lowermost part of a single tube connection between the vessel 5 and the absorber of the system, since the inlet tube 7 is
10 connected to the bottom of a condenser 8 " having a water reservoir 9 through which the single tube con¬ nection extends as a tube coil 10. The part of the tube connection positioned at a higher level is consti¬ tuted by a tube part ' 11 between the condenser 8 arid
IS the absorber 12.
The absorber 12 is designed as a solar collector and comprises a number of parallel absorber tubes 13 which are connected to the- tube 11 through a manifold 14 at the upper end of the absorber 12 which in this
20 case is shown to be inclined for the arrangement against an inclined roof face.
The individual absorber, tubes 13 are filled with a humidity absorbing compound, such as calcium chloride. A secondary cooling circuit comprises an evaporator hav-
25. ing in each of the upper tubes 13 a coaxially extend¬ ing evaporator tube 15, said evaporator tube being connected through a manifold 16 at the lower end of the absorber 12 with an inlet tube 17 for coolant in the liquid state and through a manifold 18 at the
30 upper end of the absorber .12 with an outlet line 19 for coolant in the vapour state. The inlet line 17 and the outlet line 19 are connected to a condenser 20, whereby a solar energy actuated blocking valve device 21 is connected into the inlet line 17.
35 The circulation of coolant in the two cooling circuits is shown by arrows of which the solid arrows 22 designate coolant in the vapour state, whereas the dashed arrows 23 designate coolant in the liquid state. The system is operating periodically in a day and night cycles in which the evaporation of coolant in the evaporator 1 takes place at night hours when the absorber 12 is not exposed to solar radiation on one hand, and is exposed on the other hand to further cooling by means of the se¬ condary cooling circuit including the evaporator tubes 15 extending coaxially in the absorber tubes 13. There¬ by the humidity absorbing compound in the absorber tubes 13 attains a low temperature at which it has a strong absorbing effect relative to the evaporated coola-ή-t. As a result thereof the total coolant quantity in the system, which at the beginning of the evaporation period is col¬ lected in the coolant vessel 5 will be sucked into the humidity absorbing compound in the absorber tubes 13 in the course of the evaporation period, the absorber tubes 13 being proportioned to accomodate a compound quantity having an absorption capacity corresponding to the total coolant quantity. During day hours the influence of solar radiation will cause a temperature increase in the absorber itself on one hand and act on the blocking valve device 21 very rapidly on the other hand to interrupt the coolant circulation in the secondary circuit. The blocking valve device 21 is constituted in the embodiment shown of a so-called bubble pump operating, in principle, in the same way as a water closure since it is exposed to solar radiation on the inlet side whereby vapour bubbles are generated in thelliquid to force any downwards flowing liquid back into the condenser 20 by their rise Thereby, the passage of coolant, from the condenser 20 to the evaporator tubes 15 will be blocked.
With the temperature increase caused thereby the humidity absorbing compound in the absorber tubes 13 can no longer retain the absorbed coolant quantity, but delivers the coolant in the vapour state at increasing temperature through the tube connection 11 to the con- denser 8 from which coolant in the liquid state is supplied to the collecting vessel 5 through the tube 1.' After the end of the day hours functioning as a re¬ generation period the process is repeated by cooling of the absorber no longer exposed to solar radiation, and the opening of the blocking valve device 21 for circu¬ lation of coolant in the secondary circuit.
In order to obtain a high efficiency for the cool¬ ing at night hours and the temperature increase at day hours the absorber tubes may be designed as shown in Fig. 2. To increase the solar energy collection flat tangential fins 24 are attached to the external side of the tubes 13 to be positioned immediately below a covering sheet 25 of a type known • per se in the absorber 12. The width of the fins 24 is adjusted according to the quantity of humidity absorbing compound 26 and the coolant quantity- so that at day hours a teπpe- - rature is attained by which the compound 26 delivers in the course of the period the total coolant quantity absorbed by άt in the preceeding night period.
In order to ensure an even distribution of the humidity absorbing compound 26 throughout the cross section of the absorber tubes 13 as well as a good thermal contact to the evaporator tubes 15 of the se- condary soolant circuit extending coaxially in the ab¬ sorber tubes 13 the evaporator tubes 15 are surround¬ ed by a heat conducting finned tube 27 having a number of longitudinal fins 28 -dividing the space of annular cross section between the tube. 27 and the external wall of the absorber tubes .13 in a number of chambers 29 accommodating each its share of the total quantity of humidity absorbing compound of the absorber tube 13«
The coolant in the primary cooling circuit is pre¬ ferably ammonium, but it may be any coolant suitable for absorption cooling systems. In the secondary circuit a hydrocarbon based coolant may be used such as one of the so-called chloro-fluoro-carbons. The efficiency of the system will be determined by the efficiency of the absorber designed as a solar col¬ lector defined by the product of the solar collector ef*-- ficiency, the absorber area, the incoming solar radia- tion and the number of sun hours on one hand and the coolant absorption in the humidity absorbing compound defined by the product of the specific heat of reaction of the compound and the quantity of absorbed coolant per unit of length of the absorber tubes.

Claims

PATENT CLAIMS
1. A system for the production of cold with an ab¬ sorption cooling system comprising an evaporator (1) positioned in a thermally insulated space (2) to which evaporator a coolant is supplied in the liquid state from a condenser (8) through a coolant vessel (5) and from which evaporator coolant in the vapour state is sucked by an absorber (12) which is designed as a solar collector and comprises a humidity absorbing compound for the suction of said coolant at night hours of a com¬ paratively low temperature and delivery of said coolant in the vapour state to the condenser (8) at day hours at a comparatively high temperature, said coolant suction- and delivery to and from the absorber taking place through one and the same tube connection (11) to the evaporator (1) and the condenser (8), characterized in that the absorber (12) comprises a number of parallel absorber tubes (13) which are connected with said tube - connection (11) through a manifold (14) , and each of which comprises said humidity absorbing compound in a direct thermal contact with parallel evaporator tubes (15) of a secondary self-circulating cooling circuit positioned coaxially in said absorber tube (13) , a solar energy actuated blocking valve device (21) being arrang- ed in a coolant supply tube (17) between a condenser (201 and said evaporator tubes (15) in said secondary cooling circuit.
2. A system as claimed in claim 1, characterized in that the evaporator tubes (15) of the secondary cool- ing circuit are each enclosed by a heat-conducting finned tube (27) with external longitudinal fins (28) for divid¬ ing the space of annular cross section between the finned tube (27) and the external wall of the absorber tube (13) in a number of chambers (29) for accommodating said humi- dity absorbing compound (26) .
3. A system as claimed in claim 1 or 2, character¬ ized in that tangential flat fins (24) are provided on the external side of said absorber tubes (13) to increase the solar energy collecting capacity thereof.
4. A system as claimed in claim 1, 2 or 3, charact¬ erized in that said solar energy actuated blocking valve device (21) is constituted by a bubble pump.
PCT/DK1984/000040 1983-05-18 1984-05-17 A solar energy powered system for the production of cold WO1984004581A1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
BR8406897A BR8406897A (en) 1983-05-18 1984-05-17 SYSTEM SOLVED TO SOLAR ENERGY FOR COLD PRODUCTION
AU29619/84A AU2961984A (en) 1983-05-18 1984-05-17 A solar energy powered system for the production of cold
DK11685A DK11685D0 (en) 1983-05-18 1985-01-10 Solar Powered Plant for Cold Generation
FI850223A FI850223A0 (en) 1983-05-18 1985-01-17 MED SOLENERGI DRIVET SYSTEM FOER ALSTRANDE AV KYLA.

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DK8300055 1983-05-18

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US (1) US4586345A (en)
EP (1) EP0142536A1 (en)
AU (1) AU2961984A (en)
BR (1) BR8406897A (en)
DE (1) DE8490084U1 (en)
DK (1) DK11685D0 (en)
FI (1) FI850223A0 (en)
GR (1) GR82075B (en)
IT (1) IT1176145B (en)
NO (1) NO850165L (en)
WO (1) WO1984004581A1 (en)
ZA (1) ZA843664B (en)

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EP0203558A2 (en) * 1985-05-28 1986-12-03 ZEO-TECH Zeolith Technologie GmbH Apparatus for and method of water heating by an intermittent adsorption process
WO1988008109A1 (en) * 1987-04-06 1988-10-20 Henry Søby A/S A solar collector absorption cooling system
CN105465924A (en) * 2015-12-02 2016-04-06 云南师范大学 Solar adsorption type refrigerating air conditioner system

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US4981019A (en) * 1989-11-14 1991-01-01 Hicks Carole L Solar powered portable food container
AU649913B1 (en) * 1993-02-26 1994-06-02 Stanley Neil Foxcroft Simplified air cooler
GB2449523A (en) * 2007-05-22 2008-11-26 4Energy Ltd Absorption refrigerator system comprising a condenser pipe surrounded by a tapered fluid filled enclosure
DE102009007232A1 (en) * 2009-02-03 2010-08-05 Siemens Aktiengesellschaft Thermal power plant, in particular solar thermal power plant
US9772127B2 (en) 2011-03-08 2017-09-26 JOI Scientific, Inc. Solar turbo pump—hybrid heating-air conditioning and method of operation
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WO2013069063A1 (en) * 2011-11-10 2013-05-16 Three Eye Co., Ltd. Sorption air conditioner
WO2013130350A1 (en) * 2012-02-27 2013-09-06 Yan Kunczynski Direct flow solar collector
CN103062971B (en) * 2013-01-08 2015-01-07 青岛大学 Adsorption type solar refrigerator
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KR101580797B1 (en) * 2014-09-04 2015-12-30 한국에너지기술연구원 Solar hybrid absorption cooling system
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US11029064B2 (en) * 2018-04-09 2021-06-08 Arizona Board Of Regents On Behalf Of Arizona State University Solar adsorption heat pump and evacuated tube adsorption heat pump and desalination system

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EP0203558A2 (en) * 1985-05-28 1986-12-03 ZEO-TECH Zeolith Technologie GmbH Apparatus for and method of water heating by an intermittent adsorption process
EP0203558B1 (en) * 1985-05-28 1991-10-09 ZEO-TECH Zeolith Technologie GmbH Apparatus for and method of water heating by an intermittent adsorption process
WO1988008109A1 (en) * 1987-04-06 1988-10-20 Henry Søby A/S A solar collector absorption cooling system
CN105465924A (en) * 2015-12-02 2016-04-06 云南师范大学 Solar adsorption type refrigerating air conditioner system

Also Published As

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DK11685A (en) 1985-01-10
FI850223L (en) 1985-01-17
US4586345A (en) 1986-05-06
NO850165L (en) 1985-01-15
IT1176145B (en) 1987-08-12
DK11685D0 (en) 1985-01-10
FI850223A0 (en) 1985-01-17
IT8421002A0 (en) 1984-05-18
GR82075B (en) 1984-12-13
BR8406897A (en) 1985-04-16
IT8421002A1 (en) 1985-11-18
EP0142536A1 (en) 1985-05-29
AU2961984A (en) 1984-12-04
DE8490084U1 (en) 1985-11-07
ZA843664B (en) 1984-12-24

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