EP2211125A1 - Installation et procédé de production d'eau chaude et froide devant alimenter un ou plusieurs utilisateurs thermiques - Google Patents

Installation et procédé de production d'eau chaude et froide devant alimenter un ou plusieurs utilisateurs thermiques Download PDF

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Publication number
EP2211125A1
EP2211125A1 EP09425020A EP09425020A EP2211125A1 EP 2211125 A1 EP2211125 A1 EP 2211125A1 EP 09425020 A EP09425020 A EP 09425020A EP 09425020 A EP09425020 A EP 09425020A EP 2211125 A1 EP2211125 A1 EP 2211125A1
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EP
European Patent Office
Prior art keywords
working fluid
unit
circuit
conserving
room
Prior art date
Legal status (The legal status 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 status listed.)
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Application number
EP09425020A
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German (de)
English (en)
Inventor
Andrea Verondini
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Zanotti SpA
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Zanotti SpA
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Publication date
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Priority to EP09425020A priority Critical patent/EP2211125A1/fr
Publication of EP2211125A1 publication Critical patent/EP2211125A1/fr
Withdrawn legal-status Critical Current

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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
    • F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/003—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the compression type system
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D11/00—Central heating systems using heat accumulated in storage masses
    • F24D11/02—Central heating systems using heat accumulated in storage masses using heat pumps
    • F24D11/0214—Central heating systems using heat accumulated in storage masses using heat pumps water heating system
    • 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
    • F25B7/00—Compression machines, plants or systems, with cascade operation, i.e. with two or more circuits, the heat from the condenser of one circuit being absorbed by the evaporator of the next circuit
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2220/00—Components of central heating installations excluding heat sources
    • F24D2220/20—Heat consumers
    • F24D2220/2009—Radiators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2220/00—Components of central heating installations excluding heat sources
    • F24D2220/20—Heat consumers
    • F24D2220/2081—Floor or wall heating panels
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2220/00—Components of central heating installations excluding heat sources
    • F24D2220/20—Heat consumers
    • F24D2220/209—Sanitary water taps
    • 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
    • F25B2339/00—Details of evaporators; Details of condensers
    • F25B2339/04—Details of condensers
    • F25B2339/047—Water-cooled condensers

Definitions

  • the present invention refers to a thermodynamic process for producing cold and for producing hot water to be supplied to one or more thermal users, which has a preferred, although not exclusive, use in rooms wherein it is necessary to conserve frozen or deep-frozen and/or fresh foods, and at the same time air conditioning is needed.
  • the invention also refers to a thermal plant for producing cold and for producing hot water to be supplied to thermal users, operating according to the aforementioned thermodynamic process.
  • refrigerating users The operation of refrigerating users is usually ensured by special plants for producing cold; each plant is associated with a single refrigerating user or else many centralised devices to serve a plurality of refrigerating users.
  • the refrigerating users can be different in number, and/or in type, according to the number or type of units used.
  • European patent application EP 08425703.9 describes a plant comprising a closed circuit in which a working fluid completes a thermodynamic cycle.
  • the closed circuit provides a plurality of thermal users for regulating the air temperature of a room, for example air conditioners.
  • the same closed circuit also comprises different refrigerating users, and in particular at least one unit for conserving frozen or deep-frozen foods (not necessarily present) and/or at least one unit for conserving fresh foods.
  • the described plant makes it possible to simultaneously satisfy the dual need to produce cold to conserve foods and to regulate the air temperature of the room, in an efficient way and with a small number of apparatuses.
  • the users are thus distinguished according to the relative purpose: producing cold to conserve foods, or else producing cold to decrease the air temperature in rooms compared to the outside, during the summer or on hot days.
  • the purpose of the present invention is to provide a thermodynamic process, and the relative thermal plant, for producing cold and for producing a hot working fluid intended to be supplied alternately, selectively or simultaneously to one or more thermal users, which are simple and efficient in terms of energy output.
  • thermal users it is intended to identify the apparatuses and the circuits that for their relative operation must be supplied with a hot working fluid, preferably water, the temperature of which is above 35° C.
  • a hot working fluid preferably water
  • thermal users the sanitary thermal users of the building that houses the commercial structure (the sinks where the food is washed, prepared or packaged, the bathrooms, the tanks located in the rooms for storing cleaning implements, etc.), the units for heating and dehumidifying the ambient air, the possible floor heating units in rooms, etc.
  • the invention concerns a thermodynamic process according to claim 1.
  • the invention in a first aspect thereof, concerns a thermodynamic process for producing cold for refrigerating users and for producing hot water for thermal users, comprising the steps of:
  • the configuration described in relation to the heat exchange between the working fluid and the water allows to make the most of the the energy sources in the different conditions of use.
  • room we mean to generically indicate an enclosed portion of space
  • outside we mean to generically indicate any space outside of said room, even if possibly located indoors. More specifically, by room we mean to indicate the shop or the dining establishment in which the plant that operates according to the thermodynamic process is installed, irrespective of whether it contains just one or many enclosed spaces.
  • closed circuit we mean to indicate the circuit in which a working fluid flows and that extends according to a closed loop in which compressors, refrigerating users, valves, pipes, heat exchangers, etc. are arranged, according to what is provided by the corresponding thermodynamic cycle.
  • the closed circuits are also sealed, in the sense that leaks of working fluid from the circuit into the atmosphere are prevented.
  • a working fluid is in heat exchange relationship with another fluid when it exchanges heat with it, for example in a special heat exchanger in which the two fluids in any case remain separate.
  • thermodynamic cycles there are two thermodynamic cycles provided in the aforementioned step aa) :
  • the first thermodynamic cycle and the second thermodynamic cycle are refrigerating cycles.
  • the first working fluid transfers heat to the second working fluid.
  • the circuit in which the second working fluid is active is subordinated to the circuit in which the first working fluid is active.
  • the heat exchange between the fluids can be direct, or else it can take place through an intermediary fluid that receives heat from the first fluid and transfers the same to the second fluid.
  • the second circuit is arranged in cascade with respect to the first circuit.
  • the second working fluid supplies one or more units for cooling the ambient air.
  • the units for cooling the air are deactivated. For this reason, and as shall be described more clearly hereafter, the heat transferred by the first working fluid to the second working fluid is greater during the cold seasons than the heat transferred during the hot seasons.
  • the second working fluid transfers heat to a water flow rate flowing in a corresponding third closed circuit subordinated to the second circuit, in cascade.
  • the heat exchange with the second working fluid causes an increase in the temperature of the water flow rate that flows in the third circuit, preferably to the heat levels at which condensation boilers operate, for example for common boilers over 35°C and more preferably between 40°C and 55°C, according to the season.
  • the water flow rate thus heated is collected in a collection tank, which directly or indirectly supplies one or more thermal users.
  • the extent of the heat exchange between the second working fluid and the water flow rate varies according to whether the units for cooling the ambient air are active or not.
  • the heat transferred by the second working fluid to the water flow rate flowing in the third circuit is greater during the cold seasons than the heat transferred during the hot seasons. This characteristic allows hot water to be made available when it is needed most.
  • thermodynamic cycle In a first operating mode, the step of implementing the first thermodynamic cycle in turn comprises the steps of:
  • the first working fluid substantially absorbs the heat transferred during said steps b) and c) and during step b) the second working fluid substantially absorbs the heat transferred during steps e) and f) .
  • the first, second and possible third thermodynamic cycle are configured in cascade, with the third cycle subordinated to the second cycle and the second cycle subordinated to the first cycle.
  • the units for cooling the air can be selectively deactivated. This characteristic allows one or more units for cooling the air to be excluded when necessary based upon the environmental conditions.
  • the second working fluid substantially absorbs the heat transferred during step e) .
  • the thermal users of the third circuit comprise at least one unit for heating the air in the room, and/or at least one unit for dehumidifying the air in the room, one or more heating systems positioned in the floor of a room and one or more circuits for distributing water for sanitary use.
  • the hot water is selectively supplied to one or more of said thermal users simultaneously.
  • Such thermal users can be selectively deactivated when there is no need to heat or dehumidify the air, or heat the floor or the water for sanitary use, or even when the units for cooling the air are operating.
  • the water for sanitary use is heated to a temperature equal to about 35-40°C, i.e. that which is commonly adopted in condensation boilers.
  • the circuit for distributing the water for sanitary use is placed in heat exchange relationship with the hot water contained in the collection tank.
  • step a) of the first thermodynamic cycle in turn comprises compressing a first flow rate of the first working fluid, suitable for ensuring the operation of the units for conserving frozen or deep-frozen foods, and compressing a second flow rate of the first working fluid, suitable for ensuring the operation of the units for conserving fresh foods.
  • the present invention concerns a thermal plant according to claim 11.
  • the thermal plant comprises:
  • the plant comprises:
  • the thermal plant according to the present invention advantageously makes it possible to satisfy the requirements of producing cold and of regulating the temperature of the air with the related thermodynamic cycles and, in addition, makes it possible to satisfy the requirement of producing hot water intended to supply different thermal users, through the utilization of the waste energy of the first thermodynamic cycle, i.e. by exploiting part of the heat collected by the first working fluid in the refrigerating users, the compression and the waste energy of the second working fluid, i.e. by exploiting part of the heat collected by the fluid that supplies the units for cooling the ambient air.
  • the water is indeed heated with part of the heat transferred by the second working fluid.
  • the circuits of the plant share corresponding heat exchangers, in practice being arranged in cascade.
  • the number of components of the plant is therefore less than the number of components of distinct (separate) plants intended for producing cold, for conditioning the air and for heating water. Therefore, both the overall bulk of the plant and the interventions necessary for its installation and maintenance are reduced. This is particularly advantageous in the case of small rooms and/or rooms located in old buildings, in which there can be a limited possibility of carrying out structural work to install plants.
  • the use of a single plant according to the present invention for producing cold, for conditioning and for producing hot water to serve different thermal users advantageously allows great flexibility of operation of the individual units of which it consists.
  • each unit for conserving frozen or deep-frozen foods is a counter, a cabinet or a cold room at a temperature of between about -14°C and about -30°C.
  • a temperature is preferably between about -14°C and about -16°C in the case of conservation of frozen foods.
  • This temperature is preferably equal to or less than about -18°C in the case of deep-frozen foods and it is preferably close to about -30°C in the case of the conservation of industrial ice-cream.
  • each unit for conserving fresh foods is a counter, a cabinet or a cold room at a temperature of between about +10°C and about -1°C.
  • a temperature is preferably between about +8°C and about +6°C in the case of the conservation of fruit and vegetables.
  • This temperature is preferably between about +5°C and about +3°C in the case of the conservation of dairy products and cold meats and it is preferably between about +2°C and about 0°C in the case of the conservation of meat, poultry and fish.
  • the room to which we have referred is a shop at least in part intended for the sale of food, or else a dining establishment.
  • the first working fluid at least partially evaporates in the units for conserving frozen or deep-frozen foods, and in the units for conserving fresh foods, absorbing heat.
  • the aforementioned units are hydraulically connected with the first closed circuit of the thermal plant, at as many refrigerating delivering points, and they operate directly with the first working fluid. The production of cold at such units takes place by direct expansion of the first working fluid, to the great advantage of the simplification of the plant and the efficiency of the aforementioned units.
  • the units for conserving frozen or deep-frozen foods, and/or the unit for conserving fresh foods to operate with a heat transfer fluid, preferably a non-freezing heat transfer fluid, distinct from the first working fluid and placed in heat exchange relationship with it.
  • a heat transfer fluid preferably a non-freezing heat transfer fluid
  • the units are inserted into one or more secondary circuits hydraulically separate from the first closed circuit of the thermal plant and in heat exchange relationship with it at one or more heat exchange elements, in said points where refrigeration is required.
  • the first closed circuit comprises a heat exchange device at which the first working fluid is in heat exchange relationship with the outside of the aforementioned room.
  • the heat exchange device comprises a condensing portion, at which the first working fluid transfers heat to the air of the outside.
  • the extent of the heat exchange of the first working fluid with the outside air depends mainly upon the amount of heat transferred downstream of the second working fluid. As the heat transferred by the first working fluid to the second working fluid increases the heat transferred by the first working fluid to the outside air decreases.
  • the first circuit comprises a plurality of compressors for circulating the first working fluid, a first group of compressors having a refrigerating capacity suitable for ensuring the operation of the units for conserving frozen or deep-frozen foods, and a second group of compressors having a refrigerating capacity suitable for ensuring the operation of the units for conserving fresh foods.
  • each unit for conserving frozen or deep-frozen foods is thus ensured by the first group of compressors dedicated to them. Such units can therefore be managed, and possibly excluded, by the first closed circuit of the thermal plant, without substantially influencing the performance of the other units.
  • the operation of the units for conserving fresh foods is ensured by a relative second group of compressors. This, in the case of failure of one of the compressors of a group, makes it possible to continue to ensure the operation of the units supported by the compressors of the other group, at least within certain limits.
  • the first circuit comprises at least one other heat exchanger, shared with the second circuit.
  • the second working fluid is in heat exchange relationship with the first working fluid at one or more heat exchangers shared between the first circuit and the second circuit of the plant (circuits in cascade).
  • Such an exchanger comprises a condensing portion, in which the first working fluid transfers heat, and an evaporating portion, in which the second working fluid can at least partially, and preferably substantially, absorb the heat transferred at the condensing portion.
  • the second circuit comprises one or more units for cooling the air in the surrounding area.
  • these are air conditioners or cold batteries for air treatment units.
  • Such units can be selectively deactivated during the cold seasons, for example in winter time when it is not necessary to condition the rooms.
  • the second working fluid operates directly in the unit for cooling the air.
  • the unit for cooling the air operates with its own heat transfer fluid, for example water, distinct from the second working fluid and in heat exchange relationship with it.
  • the units for cooling the air are preferably inserted in secondary circuit hydraulically separate from the second closed circuit of the plant.
  • the secondary circuit is placed in heat exchange relationship with the second circuit at one or more heat exchange elements, i.e. in one or more points where refrigeration is required.
  • the heat transfer fluid flowing in the unit for cooling the air when operating, can be advantageously kept at a positive temperature. This substantially avoids the formation, at the heat exchange battery of such a unit, of brine that, since it is thermally insulating, would hinder the heat exchange with the air of the room. A more comfortable climate is also obtained, since the temperature of the air emitted by the unit compared to the temperature of the room can be better controlled, therefore reducing the risk to people of thermal shocks.
  • the thermal plant comprises selective deactivation means of one or more units for conserving fresh foods, and/or one or more units for conserving frozen or deep-frozen foods, and/or one or more units for cooling the air in a room.
  • deactivation means can, for example, comprise at least one valve for intercepting a portion of the first circuit or of the second circuit and a corresponding by-pass circuit of the relative working fluid.
  • the second circuit comprises at least one compressor for circulating the second working fluid.
  • the compressor has a refrigerating capacity sufficient to ensure the operation of the units for cooling the air or in any case sufficient to support the heat exchange of all of the heat transferred between the fluids in the exchanger.
  • part of the compression work which determines an increase in the energy of the second working fluid, is recovered to heat the water in the third circuit.
  • both the first and the second circuit of the plant comprise expansion means of the respective working fluids, selected from thermal expansion valves and/or flooding supply systems of the evaporators.
  • the first working fluid and the second working fluid are refrigeration fluids selected from the group comprising hydrofluorocarbons (HFC), hydrochlorofluorocarbons (HCFC), carbon dioxide, propane, ammonia or other known technical fluids. More preferably, such refrigeration fluids are hydrofluorocarbons (HFC) selected from the group comprising R-507 A, R-134 a, R-410, R-404 A, R-407C.
  • the third working fluid is preferably demineralised water with added antifreeze or any non-freezing mixture like, for example, formates, acetates or nanoparticles.
  • the second working fluid is carbon dioxide CO 2 .
  • the third closed circuit comprises:
  • the thermal users of the third circuit are supplied directly with hot water taken from the collection tank, or else they are supplied with a corresponding working fluid placed in heat exchange relationship with the hot water collected in the tank.
  • the third working fluid is placed in circulation in the corresponding circuit by one or more pumps.
  • the thermal users of the third circuit are selected from a unit for heating ambient air, a unit for dehumidifying the ambient air, one or more panels arranged to heat a floor in said room and a circuit for distributing water for sanitary use.
  • the thermal plant comprises a microprocessor control unit programmed to control the operation of the plant in feedback, based upon the required operating conditions at:
  • the water collected in the collection tank has a temperature characteristic of condensation boilers, typically over 35°C.
  • the water is preferably mixed with glycols (20% by mass).
  • the thermal plant of the invention comprises means for switching between the different operating modes.
  • the thermal plant of the invention can therefore be used to regulate the temperature of the air both in the hot seasons and in the cold seasons, substantially without the operation of the units for conserving foods being jeopardised.
  • the switching means comprise a microprocessor control unit, suitably programmed to control the intercepting means of portions of the circuits of the plant.
  • the operation of the plant is as follows.
  • the thermal refrigerating devices of the first circuit for conserving foods is active; the units for cooling the ambient air are also active, i.e. they are supplied with the second working fluid.
  • the first working fluid condenses in the exchanger of the first circuit positioned outside of the room.
  • the second working fluid transfers heat to the water flow rate flowing in the third circuit.
  • the water, heated to a temperature characteristic of condensation boilers, typically above 35°C, is collected in the tank of the third circuit and preferably supplies the unit(s) for dehumidifying the air and transfers heat to the water for sanitary use flowing in the relative distribution circuit.
  • the unit for heating ambient air is deactivated.
  • the panels for heating the floor are deactivated, but optionally it is possible to activate one or more panels to dry the floor that has been made wet by customers of the shop on rainy days or else to heat the floor in the till area of the shop.
  • the refrigerating users of the first circuit for conserving foods are active; the units for cooling the ambient air are deactivated, i.e. they are not supplied with the second working fluid.
  • the first working fluid transfers heat to the second working fluid at the heat exchanger shared between the first and the second circuit.
  • the second working fluid substantially transfers the heat received from the first working fluid to the water flow rate flowing in the third circuit.
  • the water thus heated is collected in the tank of the third circuit and preferably supplies the unit(s) for heating the air in the room and/or the panels arranged in the floor and gives up heat to the water for sanitary use flowing in the relative distribution circuit.
  • the unit for dehumidifying the air is activated when needed.
  • FIG 1 a thermal plant in accordance with the invention for producing cold to conserve foods, to cool the air and to produce hot water to supply different thermal users is wholly indicated with reference numeral 1.
  • the same plant 1 allows the thermodynamic process according to the present invention to be described.
  • the thermal plant 1 is preferably applied in a room I where it is necessary to conserve fresh and/or frozen/deep-frozen foods, for example for the purpose of selling (retail or wholesale), or for catering.
  • Such applications comprise shops such as mini or supermarkets, food shops and similar, and dining establishments such as canteens, restaurants, snack bars and similar.
  • the thermal plant 1 comprises a first closed circuit A in which a first working fluid undergoes a first thermodynamic cycle, a second closed circuit B , subordinated to the first circuit A , in which a second working fluid undergoes a second thermodynamic cycle, and a third closed circuit C in which flows hot water, or a mixture of water and glycols (or other technical mixtures), to supply different thermal users.
  • the circuit A comprises a plurality of refrigerating delivering points at which at least one unit for conserving foods is arranged.
  • the first circuit A comprises at least one refrigerating user selected from a unit 2 for conserving frozen or deep-frozen foods and a unit 3 for conserving fresh foods.
  • the plant has many units 2 in arrays, i.e. arranged in parallel on the same line, and many units 3 in batteries.
  • the units 2 and 3 can, for example, be refrigerated counters or cabinets, or else cold rooms. In figure 1 the numbers 2 and 3 identify batteries of refrigerating users.
  • the units 2 and 3 are hydraulically connected in the closed circuit A and operate through direct expansion of the first working fluid. More preferably, the batteries of units 2 are arranged on distinct lines of the closed circuit A with respect to the batteries of units 3, so that a failure or a maintenance intervention on a line does not simultaneously jeopardise the operation of both the batteries of units 2, 3.
  • the first working fluid on average is at a lower temperature (conventionally "low temperature") than the same fluid in the units 3 for conserving fresh foods (conventionally "normal temperature”).
  • the temperature of the first working fluid at a unit 2 for conserving frozen or deep-frozen foods is typically between about -42°C and about -20°C.
  • the temperature of the first working fluid at a unit 3 for conserving fresh foods is typically between about -15°C and about +2°C.
  • the first circuit A comprises at least one compressor having the function of circulating the first working fluid according to the flow rates and the pressures suitable for the relative refrigerating cycle.
  • the plant 1 comprises five compressors 4 divided into two groups of compressors 4a and 4b, respectively comprising two and three compressors.
  • the compressors 4 can, for example, be of the hermetic, semi-hermetic or open type, and, in relation to the way in which the compression is carried out, using pistons, screw or scroll or more generically rotary.
  • the refrigerating capacity of the compressors 4 can be the same for all of the compressors, or different for some or each of them or adjustable through partialisation of the heads and/or through the variation of the number of revolutions of the relative electric motor.
  • the intake of the compressors 4 of the group of compressors 4a is connected with the output line from the units 2 for conserving frozen or deep-frozen foods. Downstream of the compressors 4a with respect to the running direction of the fluid, the line arriving from the units 3 for conserving fresh foods converges. Downstream of this convergence there is preferably an anti-liquid bottle equipped with internal heat exchanger 5, and a lamination system of the coolant; the whole assembly works as an intercooler, in turn in connection with a tank 6 for collecting the first working fluid. The tank 6 directly supplies the units 3 by means of the line 31.
  • an evaporator 313 is provided downstream of the units 3 , having the function of making it easier to start up the plant 1 during the cold seasons, after being switched off a prolonged period.
  • the heat exchange device 7 preferably consists of an assembly arranged outside E of the room I inside which the units 2 and 3 are active, preferably outside of the building comprising the room I.
  • the heat exchange device 7 allows the heat exchange of the first working fluid with the air or other fluid available outside E, like water (for example, according to availability and/or requirements, river water, aquifer water, runoff water) or another suitable fluid.
  • the heat exchange device 7 also comprises means for the forced circulation of air or of another fluid available outside and of the conventional type, such as one or more fans, for example of the helical or centrifugal type, typically electrically actuated.
  • Such means are arranged so as to increase the air flow through the heat exchange device 7 in a preferred direction.
  • the exchanger 9 can in turn comprise one or more heat exchange units.
  • the first working fluid in part transfers heat to the second working fluid. In this circumstance the first fluid can undergo a partial condensation.
  • the exchanger 9 is shared between the first circuit A and the second circuit B.
  • the first working fluid Downstream of the heat exchange device 7 the first working fluid is conveyed into the collection tank 6, at which the circuit A closes.
  • a conventional check valve 8 and means for separating and recovering oil of the compressors 4 dispersed in the working fluid are preferably arranged downstream of each compressor 4 .
  • Such means can, for example, comprise an oil separator, filters and a recovery line for the separated and filtered oil.
  • the second closed circuit B shall now be described in detail, in which a second working fluid undergoes a second thermodynamic cycle.
  • the second closed circuit B shares the heat exchanger 9 with the first circuit A to which it is subordinated.
  • the exchanger 9 comprises a condensing portion, at which the first working fluid undergoes a partial or total condensation and releases heat, and an evaporating portion, separate and distinct from the condensing portion, in which the second working fluid heats up substantially accumulating the heat released by the first working fluid.
  • the exchanger 9 comprises one or more evaporating sections and means for selectively excluding one or more of such portions. The exclusion of one or more evaporating portions is used to limit the amount of heat transferred to the second working fluid when necessary based upon the operating conditions of the plant 1.
  • first circuit A and the second circuit B are hydraulically separate.
  • the second circuit B also comprises a compression section, in which there is at least one compressor 10 (in practice a heat pump), as shown in figure 1 , for the forced circulation of the second working fluid.
  • the second working fluid leaving the exchanger 9 is sent to a further exchanger 11 shared with a third closed circuit C, as shown in figure 1 .
  • the second working fluid transfers heat to a water flow rate that flows in the third circuit C.
  • a tank 13 for collecting the fluid Downstream of the exchanger 11 with respect to the direction of the circulation of the second working fluid a tank 13 for collecting the fluid is preferably provided. More preferably, such a tank is of the stratified type.
  • the tank 13, in delivery, serves a line 131 and a line 132.
  • the line 132 supplies the exchanger 9 shared with the first circuit A.
  • the line 131 supplies one or more units 12 for cooling the air in the room A.
  • Each unit 12 represents a point where refrigeration is required of the second circuit B, at which the second working fluid is at a temperature suitable for the heat exchange with at least the corresponding unit 12.
  • the units 12 are cold batteries for air treatment units.
  • the overall cooling power delivered by the units 12, measured in kW, is established a the design step and depends upon the size of the room I, upon the degree of insulation of the building, upon the number and heat sources present in it and upon the average number of people located in the room I.
  • the air temperature of the room I must be able to be regulated at about 25°C, typically when the room I is cooled.
  • the second working fluid at the units 12 must have a temperature equal to about +7°C.
  • the second circuit B preferably comprises interception means 14, for example solenoid valves, arranged to allow the activation or exclusion of the individual units 12 both during normal operation, for example to carry out adjustments to the plant 1 according to the season, and in conditions of failure or of partial shut-down of the same plant 1.
  • the interception means are preferably controlled remotely by a control unit of the plant 1.
  • the circuit B preferably also comprises expansion means 15 of the second working fluid.
  • expansion means 15 are preferably conventional, for example mechanical or electronic thermal expansion valves, or flooding systems of the evaporator, but more preferably thermal expansion valves.
  • the valves 15 are arranged at the points where refrigeration is required, i.e. at the units 12 , as shown in figure 1 .
  • the second working fluid output from the units 12 is sent to the compressor 10 (the circuit B is in a closed loop).
  • the first and second working fluid are refrigeration fluids, for example hydrofluorocarbons (HFC) known by the name ASHRAE R-507 A, R-134 a, R-410, R-404 A, R-407C.
  • HFC hydrofluorocarbons
  • the second working fluid can be CO 2 , ammonia or any other coolant known in the field.
  • the plant 1 comprises a third closed circuit C in which flows a water flow rate, or a mixture of water and glycols (or another technical fluid) heated by the second working fluid.
  • the third circuit C comprises a tank for collecting the hot water and one or more thermal users 18, 23, 24, 26 selectively served with the hot water.
  • the third circuit C shares the exchanger 11 with the second circuit B, to which it is subordinated in cascade. At the exchanger 11 the water flowing in the third circuit C receives heat from the second working fluid. Despite this, the third circuit C is hydraulically separate from the second circuit B.
  • the third circuit C comprises at least one pump 16 for circulating the water.
  • the water, heated in the exchanger 11, is sent by the pump 16 to a collection tank 17, in which it is preferably at a temperature typical of condensation boilers, for example above 35°C.
  • One of the thermal users of the third circuit C is a circuit 18 for distributing water for sanitary use.
  • the circuit 18 supplies thermal users external to the plant 1, for example showers, taps, baths, etc., and it is arranged in heat exchange relationship with the water contained in the tank 17, as shown in figure 1 .
  • a tank 20 can be arranged along the outer line 18, downstream of a pump 19 for circulating the water, as shown in figure 1 , to collect the water before delivery to the relative thermal sanitary devices.
  • Two pumps 21 and 22 take the hot water from the tank 17 and send it to corresponding thermal users; in particular they send it to at least one unit 23 for heating the air in the room I and at least one unit 24 for dehumidifying the air in the room I.
  • the water is in heat exchange relationship with the air of the room I.
  • the water output from the units 23 and 24, after having heated and/or dehumidified the air, is sent back to the collection tank 17. From the tank 17 a delivery side sends a water flow rate into the exchanger 11, closing the cycle.
  • the third circuit C also comprises another thermal user consisting of one or more heating units using heating panels 26 arranged in a floor of the room I.
  • the diagram shown in figure 1 shows a unit with panels 26 supplied by a corresponding pump 27 and by a three-way valve with fixed point temperature adjustment with hot water taken from the tank 17.
  • the panels 26 allow a floor made wet by the shoes of customers in the shop to be quickly dried during wet days or allow some points of the supermarket to be heated more, like for example, at the till area.
  • the third circuit C also comprises means for selectively excluding units 23, 24 and 26, for example in the summer or else during maintenance of the third circuit C.
  • Such means are preferably controlled by a control unit of the plant and can, for example, be interception valves provided upstream of the pumps 21, 22 and 27.
  • the third circuit C preferably comprises a heat exchanger 25, installed outside E of the room I, having the function of cooling the water contained in the tank 17, giving up heat to the outside air, when necessary following excessive heating.
  • the exchanger 25 is used in the summer when the thermal users 23, 24 and 26 are deactivated and the water collected in the tank 17 can reach high temperatures, for example 55°C.
  • thermodynamic process of the invention we shall now describe the operation of the thermal plant 1, in accordance with a preferred embodiment of the thermodynamic process of the invention.
  • the first thermodynamic cycle is active for producing cold at the units 2 for conserving frozen or deep-frozen foods and at the units 3 for conserving fresh foods
  • the second thermodynamic cycle is active, i.e. the compressor (or the compressors) 10 is switched on, to circulate the second working fluid, to receive heat from the first working fluid, compress it and transfer heat to the water flowing in the third circuit C; the heated water is supplied to the thermal users 23 and/or 24 and/or 26 and/or 18; the units 12 for cooling the air are excluded, i.e. switched off.
  • the heat given up by the first working fluid to the outside air through the exchanger 7 is minimal.
  • the plant 1 can be made easier to start in the winter by temporarily actuating the evaporator 31.
  • the first thermodynamic cycle is active for producing cold at the units 2 for conserving frozen or deep-frozen foods and a the units 3 for conserving fresh foods;
  • the second thermodynamic cycle is active, i.e. the compressor 10 is switched on, to supply the units 12 for cooling the air and to transfers heat to the water flowing in the third circuit C;
  • the water heated in the third circuit C is supplied to the circuit 18 for distributing sanitary water and possibly to the units 24 for dehumidifying the air in the room I.
  • the other thermal users 23 and 26 are excluded, i.e. switched off.
  • the heat given up by the first working fluid to the outside air through the exchanger 7 is minimal. If the water of the third circuit heats to above the predetermined value, for example over 55°C, the exchanger 25 is activated to give up heat to the outside air and cool the water collected in the tank 17.
  • thermodynamic cycle comprises the steps of:
  • the first circuit A and the second circuit B are configured in cascade, during step d) the first working fluid substantially absorbs the heat transferred during said steps b) and c) and during step b) the second working fluid substantially absorbs the heat transferred during steps e) and f).
  • the second working fluid substantially absorbs the heat given up during step e).
  • Both the changes in operating modes, and the adjustment of the thermal plant 1 between the various seasons are preferably controlled by a specially programmed microprocessor control unit (not shown in the figures).
  • control unit receives the following signals in input:
  • control unit Based upon the signals received, the control unit adjusts the thermal plant 1 in feedback, modifying the number of unit 2, 3, 12, 23, 24 and 26 to activate or deactivate and acting upon the valves 8, 14 and upon the pumps 16, 19, 21, 22 and 27.
  • the thermal plant 1 is intended to be sold without the thermal users (units 2, 3, 12, 23, 24 and 26 ).
  • the different units can indeed be purchased on the market from various suppliers.
  • the thermal plant 1 is characterised by high energy efficiency. The heat that in other plants would be released into the atmosphere, in the plant 1 is exploited in the circuits B and C subordinated to the circuit A.
  • FIG 2 shows an alternative embodiment of the plant 1 according to the present invention.
  • the same reference numerals as those used in figure 1 indicate identical or equivalent elements.
  • the plant does not provide two distinct circuits A and B to supply the units for conserving foods and the units for cooling the air. Instead, there is a single closed circuit D in which the same working fluid undergoes a thermodynamic cycle to selectively supply the units 2, 3 and 12.
  • the plant comprises a closed circuit D in which flows a corresponding working fluid that undergoes a thermodynamic cycle and supplies, simultaneously or alternately, at least one unit 2 for conserving frozen or deep-frozen foods (or else an array of such units), and/or at least one unit 3 for conserving fresh foods (or a battery of such units), and/or at least one unit 12 for cooling the air in the room I (three units 12 are shown).
  • the plant also comprises a circuit C, equivalent to the one described earlier in relation to figure 1 , intended for the circulation of hot water, and one or more thermal users 17, 23, 24, 26 able to be selectively supplied with such water.
  • the circuit C for circulating the hot water is subordinated, in cascade, to the circuit D for circulating the working fluid.
  • the working fluid of the circuit D is placed in heat exchange relationship with the water flowing in the circuit C.
  • the operation of the plant shown in figure 2 is similar to that of the plant shown in figure 1 .
  • the energy efficiency of the plant of figure 2 is lower than the efficiency of the plant of figure 1 , even if it may in any case be acceptable for some applications.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)
EP09425020A 2009-01-27 2009-01-27 Installation et procédé de production d'eau chaude et froide devant alimenter un ou plusieurs utilisateurs thermiques Withdrawn EP2211125A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP09425020A EP2211125A1 (fr) 2009-01-27 2009-01-27 Installation et procédé de production d'eau chaude et froide devant alimenter un ou plusieurs utilisateurs thermiques

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP09425020A EP2211125A1 (fr) 2009-01-27 2009-01-27 Installation et procédé de production d'eau chaude et froide devant alimenter un ou plusieurs utilisateurs thermiques

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EP2211125A1 true EP2211125A1 (fr) 2010-07-28

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2486646A (en) * 2010-12-20 2012-06-27 Sublogic Mfg Ltd Method and Apparatus for Cascade Refrigeration and for Central Heating Hot Water Supply
EP3117161A4 (fr) * 2014-03-14 2018-02-21 Hussmann Corporation Système frigorifique à hydrocarbures représentant une faible charge

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4041724A (en) * 1975-02-18 1977-08-16 Projectus Industriprodukter Ab Installation for heating a fluid, preferably water, in a conventional central heating system, using the waste heat produced by a number of refrigerators
GB2062831A (en) * 1979-11-07 1981-05-28 Indair Ltd Waste heat recovery
EP0056780A2 (fr) * 1981-01-19 1982-07-28 Andreas Dr.-Ing. Hampe Disposition de pompes à chaleur
US4507938A (en) * 1982-09-10 1985-04-02 Mitsubishi Denki Kabushiki Kaisha System for air-conditioning and hot water supplying
JPH04263758A (ja) * 1991-02-18 1992-09-18 Kansai Electric Power Co Inc:The ヒートポンプ式給湯装置
WO2001020234A1 (fr) * 1999-09-15 2001-03-22 Ut-Battelle, Llc. Ensemble combine refrigerateur, pompe a chaleur et dispositif de chauffage d'eau
JP2004340533A (ja) * 2003-05-19 2004-12-02 Matsushita Electric Ind Co Ltd ヒートポンプ給湯空調装置
WO2006100709A1 (fr) * 2005-03-24 2006-09-28 Lambda S.P.A. Systeme integre de production de chaud et de froid pour leur utilisation simultanee par des dispositifs de refroidissement et de chauffage
EP1734318A1 (fr) * 2005-06-13 2006-12-20 Zanotti S.p.A. Installation et procédé de production de froid et de réglage de température de l'air et dispositif d'échange thermique utilisable dans cette installation
EP1780476A1 (fr) * 2004-07-01 2007-05-02 Daikin Industries, Ltd. Dispositif d"approvisionnement en eau chaude
EP1826510A2 (fr) * 2006-02-27 2007-08-29 Sanyo Electric Co., Ltd. Dispositif de circuit de réfrigération

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4041724A (en) * 1975-02-18 1977-08-16 Projectus Industriprodukter Ab Installation for heating a fluid, preferably water, in a conventional central heating system, using the waste heat produced by a number of refrigerators
GB2062831A (en) * 1979-11-07 1981-05-28 Indair Ltd Waste heat recovery
EP0056780A2 (fr) * 1981-01-19 1982-07-28 Andreas Dr.-Ing. Hampe Disposition de pompes à chaleur
US4507938A (en) * 1982-09-10 1985-04-02 Mitsubishi Denki Kabushiki Kaisha System for air-conditioning and hot water supplying
JPH04263758A (ja) * 1991-02-18 1992-09-18 Kansai Electric Power Co Inc:The ヒートポンプ式給湯装置
WO2001020234A1 (fr) * 1999-09-15 2001-03-22 Ut-Battelle, Llc. Ensemble combine refrigerateur, pompe a chaleur et dispositif de chauffage d'eau
JP2004340533A (ja) * 2003-05-19 2004-12-02 Matsushita Electric Ind Co Ltd ヒートポンプ給湯空調装置
EP1780476A1 (fr) * 2004-07-01 2007-05-02 Daikin Industries, Ltd. Dispositif d"approvisionnement en eau chaude
WO2006100709A1 (fr) * 2005-03-24 2006-09-28 Lambda S.P.A. Systeme integre de production de chaud et de froid pour leur utilisation simultanee par des dispositifs de refroidissement et de chauffage
EP1734318A1 (fr) * 2005-06-13 2006-12-20 Zanotti S.p.A. Installation et procédé de production de froid et de réglage de température de l'air et dispositif d'échange thermique utilisable dans cette installation
EP1826510A2 (fr) * 2006-02-27 2007-08-29 Sanyo Electric Co., Ltd. Dispositif de circuit de réfrigération

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2486646A (en) * 2010-12-20 2012-06-27 Sublogic Mfg Ltd Method and Apparatus for Cascade Refrigeration and for Central Heating Hot Water Supply
EP3117161A4 (fr) * 2014-03-14 2018-02-21 Hussmann Corporation Système frigorifique à hydrocarbures représentant une faible charge
AU2015230002B2 (en) * 2014-03-14 2018-06-28 Hussmann Corporation Low charge hydrocarbon refrigeration system

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