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WO2011154002A2 - Procédé de régulation d'un réseau de distribution de chauffage à un seul tuyau - Google Patents

Procédé de régulation d'un réseau de distribution de chauffage à un seul tuyau Download PDF

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Publication number
WO2011154002A2
WO2011154002A2 PCT/DK2011/000056 DK2011000056W WO2011154002A2 WO 2011154002 A2 WO2011154002 A2 WO 2011154002A2 DK 2011000056 W DK2011000056 W DK 2011000056W WO 2011154002 A2 WO2011154002 A2 WO 2011154002A2
Authority
WO
WIPO (PCT)
Prior art keywords
heat exchanging
temperature
return
line
flow
Prior art date
Application number
PCT/DK2011/000056
Other languages
English (en)
Other versions
WO2011154002A3 (fr
Inventor
Michael Hartmann
Mariusz Jedrzejewski
Matjaz Osojnik
Original Assignee
Danfoss A/S
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 Danfoss A/S filed Critical Danfoss A/S
Priority to UAA201300326A priority Critical patent/UA106431C2/ru
Priority to CN201180039331.0A priority patent/CN103282722B/zh
Publication of WO2011154002A2 publication Critical patent/WO2011154002A2/fr
Publication of WO2011154002A3 publication Critical patent/WO2011154002A3/fr

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D19/00Details
    • F24D19/10Arrangement or mounting of control or safety devices
    • F24D19/1006Arrangement or mounting of control or safety devices for water heating systems
    • F24D19/1009Arrangement or mounting of control or safety devices for water heating systems for central heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D19/00Details
    • F24D19/0002Means for connecting central heating radiators to circulation pipes
    • F24D19/0004In a one pipe system
    • F24D19/0007Comprising regulation means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D19/00Details
    • F24D19/10Arrangement or mounting of control or safety devices
    • F24D19/1006Arrangement or mounting of control or safety devices for water heating systems
    • F24D19/1009Arrangement or mounting of control or safety devices for water heating systems for central heating
    • F24D19/1015Arrangement or mounting of control or safety devices for water heating systems for central heating using a valve or valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2220/00Components of central heating installations excluding heat sources
    • F24D2220/02Fluid distribution means
    • F24D2220/0271Valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2220/00Components of central heating installations excluding heat sources
    • F24D2220/04Sensors
    • F24D2220/042Temperature sensors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2220/00Components of central heating installations excluding heat sources
    • F24D2220/04Sensors
    • F24D2220/044Flow sensors

Definitions

  • Method to control the flow rate and of a heat exchanging fluid medium to a riser in a one-pipe system being a typical pipe set up in for example building cooperatives for supplying heat to the radiators of the flats.
  • the method being to regulate the temperature of the supplied heat exchanging fluid medium in response to changes in external parameters (temperature) and the flow rate in response to the temperature of the heat exchanging fluid medium in an return line.
  • Typical set ups of the pipes supplying radiators in e.g. housings or building cooperatives are either two-pipe systems or one-pipe systems.
  • housings comprising a plural of flats, or any other places where such setups are typical.
  • a set of parallel pipes forms supply pipes (or 'lines' in more general) and return pipes (or 'lines') to a collection of heat exchanging devices such as radiators.
  • the pipes associated with each such collection of heat exchanging devices is referred to as risers, and in two-pipe systems the flow rates at each riser are in traditional systems regulated individually, thus giving dynamic flow rates in each riser matching the present loads.
  • the supply line system feeds some heat exchanging fluid medium (typically water) and a supply temperature (typically water) at a flow rate to a collection of heat exchanging devices.
  • the individual radiators are connected in series with one after the other, such that the return line of one radiator is the feeding line of a next radiator.
  • the flow rates of the heat exchanging fluid medium to each radiator are usually controlled by thermostats being set by the users of the radiators, but the overall flow in the supply and return lines is in traditional systems substantially permanent, meaning it is not reacting to changes in the load.
  • the radiator thermostats in general is closed letting most of the heat exchanging fluid medium flow through the bypass lines, such a setup leads to an undesired high temperature of the heat exchanging fluid medium in the return line(s).
  • a high temperature of the return heat exchanging fluid medium is not desired, since it leads to an uncontrolled heating of the living spaces and further to unnecessary losses of heat of the heat exchanging fluid medium in the lines, since the lines will continue to deliver heat though, the radiators are closed. This is especially the case where the lines are not well insulated. This would be a further discomfort to the inhabitants.
  • valve actuator regulating the flow is placed centrally. This is not possible in a one-pipe-system, since it will cause underflow in parts of the system still having high load, and overflow in parts / risers with low load.
  • the present invention relates to introducing a solution giving a highly energy- efficient and load dependent one-pipe system.
  • the present invention solves the problems of one-pipe systems by introducing a two-part control, one being to regulate, or control, the temperature of the supplied heat exchanging fluid medium, the supply temperature, and another to control flow through a collection of heat exchanging devices in relation to the temperature of the heat exchanging fluid medium in the return line.
  • the control of flow and return temperature is done "de-centrally" in each riser.
  • the supply temperature control is based on external conditions comprising conditions influencing the system that cannot be influenced by the system itself, this preferably includes, for example, the weather by introducing a weather compensator (more especially the external temperature, being e.g. the outdoor temperature of a housing), but could also include other factors that would influence the expected needed heat to be supplied to the houses.
  • the main, but not exclusive, embodiment is especially related to the external temperature, the system thus optionally including an external temperature sensor.
  • the system is coupled to a weather forecast system such as through the internet.
  • the present invention thus introduces a method of regulating a system comprising;
  • a heat exchanging fluid medium with a supply temperature is feed from the main supply line to the collection of heat exchanging devices at a flow rate
  • the supply temperature is regulated according to a supply set point temperature depending parameters external to the system
  • the flow rate is regulated according to a return set point temperature depending on a
  • the supply temperature is regulated according to a supply set point temperature depending on parameters external to the system, and / or the flow rate is regulated according to a return set point temperature depending on a temperature of the heat exchanging fluid medium downstream of the first heat exchanging device in the collection.
  • the return temperature set point preferably is regulated in response to a regulation of the supply temperature set point.
  • the method in a further embodiment applies to a system further comprising
  • a flow controller connected to a return line, the flow controller being adapted to control the flow rate through the return line
  • thermosensor positioned in heat exchanging connection to the heat exchanging fluid in the return line.
  • the flow controller is further adapted to maintain a constant flow despite changes in the pressure in the main supply line.
  • the system in one embodiment may comprise an external temperature sensor positioned to measure a temperature external to the system.
  • the system in one embodiment may comprise an electronic controller connected to the actuating devices and the temperature sensors connected to the return lines.
  • the electronic controller is optionally connected to a temperature sensor connected to the main supply line, and optionally also to the external temperature sensor.
  • the actuating device is pulse actuated, such as where the actuating device is an electro-magnetic, pneumatic, hydraulic or electrostrictive actuator.
  • the supply temperature is regulated according to a supply set point temperature depending on parameters external to the system, and the flow rate is regulated according to a return set point temperature depending on a temperature of the heat exchanging fluid medium downstream of the first heat exchanging device in the collection.
  • the return temperature set point is preferably regulated in response to a regulation of the supply temperature set point.
  • the actuating devices are connected directly to the temperature sensors and are self-acting and include means to adjust the return temperature set point.
  • a natural choice is that the actuating device is a thermostat.
  • Fig. 1 Illustration of a standard one-pipe, or one-line, set up
  • Fig. 2 Illustration of a number of parallel risers each associated with a collection of heat exchanging devices, and where each riser is controlled according to one embodiment of the present invention.
  • FIG. 3 Illustration of a flow controller used in one embodiment of the present invention, the flow controller being adapted to maintain a constant flow despite pressure changes.
  • FIG. 4 Illustration of set point dependences on external conditions.
  • Figs. 5A and 5B Illustrations of how the present invention relates the flow rate to better match the actual load in the system. Illustration of the system introducing an electronic controller according to an embodiment of the present invention.
  • Fig. 1 illustrates a typical set up of a one-pipe system, where a supply line (3) system feeds some heat exchanging fluid medium (typically water) at a supply temperature and at a flow rate, to a collection of heat exchanging devices (6), such as e.g. radiators, and adapted to heating up a number of living spaces.
  • heat exchanging devices (6) are frequently referred to as radiators.
  • the individual radiators (6) are connected in series, one after the other, such that the return line (4)of one radiator (6) is the feeding line (3) of a next radiator (6).
  • the feeding line (3) and return line (4) of each radiator (6) is additionally connected by a bypass line (5).
  • a main supply line (1) is connected to the feeding line (3) of the first of the radiators (6) in the collection, seen in the flow direction, and a main return line (2) is connected to the return line (4) of last of the radiators (6) in the collection, seen in the flow direction.
  • a setup is in some places typical in houses comprising a number of rooms and flats, where e.g. a number of parallel risers are each connected to a number rooms / flats. In this text each of these rooms / flats is regarded as one heat exchanging device, the rooms / flats associated with a riser then
  • the individual radiators (6) within each room / flat may be connected according to a similar or a very different setup.
  • the heat exchanging medium may be supplied directly to the radiators (6) (in the following referred to as the direct supply setup), or the system may introduce a substation comprising a heat exchanger separating the supplier lines from e.g. a house (in the following referred to as the substation setup), thus forming a closed loop for the heat exchanging fluid to circulate to the individual radiators (6).
  • the flow rates of the heat exchanging fluid medium to each radiator (6) are controlled by flow regulating means (7), in the following being, without loss of generality, referred to as a the radiator thermostats.
  • the regulation of the flow rates to the radiators (6) in addition influences the flow in the bypass lines (5), by changing the flow to the radiators (6), the flow through the bypass lines (5) being changed accordingly.
  • the present invention solves this problem by introducing a two part control, one being to regulate, or control, the temperature of the supplied heat exchanging fluid medium, the supply temperature, and another to control the flow through a collection of heat exchanging devices (6) in relation to the temperature of the heat exchanging fluid medium in a return line (3).
  • the supply temperature control is based on external conditions comprising conditions influencing the system that cannot be influenced by the system itself, this preferably includes such as the weather (more especially the external temperature, being e.g. the outdoor temperature of a housing), by introducing a weather compensator, but could also include other factors that would influence the expected needed heat to be supplied to the houses.
  • the main, but not exclusive, embodiment is especially related to the external temperature, the system thus optionally including an external temperature sensor (8).
  • the system is coupled to a weather forecast system such as through the internet.
  • the regulation of the flow to the risers in this manner are based on the actual demand(s), or load (2), in the riser(s), in that a changing demand changes the temperature of the heat exchanging fluid medium in the return line(s) (4).
  • Fig. 2 illustrates a set up according to the present invention, where a flow controller (9) is connected to a return line (4) associated with a collection of radiators (6) for controlling the flow of heat exchanging fluid in the lines supplying these radiators )6).
  • the flow controller (9) in one preferred but not limiting embodiment has two operations in that both a flow control valve and a pressure independent balancing valve.
  • the flow controller (9) in this embodiment includes means to set a desired flow rate, and means to ensure this substantially constant flow rate despite pressure changes in the flow system.
  • Such valves are available in the market, where examples are the AB-QM product series provided by
  • Fig. 3 illustrates such a valve (9), or flow controller, consisting of two parts, a differential pressure controller and a control valve.
  • the differential pressure controller maintains a constant differential pressure across the control valve (9).
  • the control valve (9) comprises a spindle (31), stuffing box (32), plastic ring (33), control valve's cone (34), membrane (35), main spring (36), hollow cone (pressure controller) (37) and vulcanized seat (pressure controller) (38).
  • the pressure difference APcv (P2 - P3) on the membrane (35) is balanced with the force of the spring (36).
  • the control valve (9) has a linear characteristic. It features a stroke limitation function that allows adjustment of the Kv value. The stroke limitation is changed by lifting the blocking mechanism and turning the top of the valve (9) to the desired position. A blocking mechanism automatically prevents unwanted changing of the setting.
  • Introducing such a flow controller (9) has one further advantage, in that, for example, the flow in the risers is regulated / controlled mutually independently, despite being connected to common main supply (1) and return (2) lines.
  • the figure shows the flow controller attached to the return line (4) of the last of the radiators (6) seen in the direction of flow, an actuating device (10) being connected to the flow controller (9), optionally by the use of an adapter. Further seen is a temperature sensor (11) adapted to be positioned in thermal exchange connection to the return line (4).
  • the actuating devices (10) may be actuators, and may be self-acting or controlled, and operating in any manner as known in the arts, such as electromagnetic, pneumatic, hydraulic, electroactive etc.
  • Fig. 2 thus shows a system where the control is based on two parts, one being related to regulating the supply temperature in dependence of external conditions, such as the external temperature, the second being to regulate the flow associated with each collection of heat exchangers (6), in dependence of the return temperature, the temperature of the heat exchanging fluid medium in a return line (4).
  • the system thereby becomes a variable flow system with individual flow control for each riser depending on the load on each of the individual risers.
  • Fig. 4 shows two curves illustrating the regulation according to the present invention.
  • the upper curve (12) illustrates a regulation dependence of the supply temperature to the external temperature. Or at least illustrates how a set point of the supply temperature changes with changing external temperature.
  • the exact curve and dependence would depend on a number of factors, such as e.g. the state of insulation of the housing, and would typically be optimized to the conditions of the actual system.
  • the lower line (13) therefore illustrates a dependence of the regulation of the return temperature set point, the curve being an update of basic return temperature control where the return temperature set point actively follows the result of the control of the supply temperature based on the external temperature. It is therefore a control of the set point of the return temperature.
  • the aim is that the performance of control where flow is adjusted to load in each riser remains perfect throughout the heating season.
  • the lower curve (13) thus changes based on two factors, supply temperature and load in riser(s), as the load in the risers is unpredictable and changes from 100% to 0%,.
  • the system of the present invention thus introduces a 'super' control being the control of the supply temperature set point in relation to external conditions, and a 'sub' control correcting the system by changing the flow according to the return temperature, being related to the load in the riser(s), and where the set point of the return temperature in embodiments of the present invention actively changes according to the change of the set point of the supply temperature.
  • Fig 5A shows a graphic representation of flow to load relation in a traditional one-pipe system without any regulation according to the present invention, where the dashed line (14) illustrates the actual flow rate fluctuating unpredictably since these systems are dynamic due to the radiator thermostat (7) actions.
  • the wavy line (16) is the actual load clearly seen to be uncorrelated to the actual flow rate.
  • the straight line (15) is caused by the introduction of the pressure independent flow controller (9) according to the present invention.
  • Fig. 5B shows the situation according to the present invention, where the flow is controlled in dependence of the return temperature, thus controlling the flow according to the demand, or load. This gives a flow rate (17) much more matching the actual demand, and thus giving a much more efficient system.
  • the illustrated system in Fig. 2 shows a simple setup of the present invention, where the actuating device (10) operating flow rate setting of the flow controller (9) is a thermostat of any kind as known in the arts, the system thus being self acting.
  • the temperature sensor (11) being directly connected to the actuating device (10).-
  • Such a setup has the advantage of not needing any additional energy source for operation, and each riser may be regulated individually.
  • actuating device (10) as known in the arts, further gives the advantages that such devices often include means to set a temperature set point, the set point of the return temperature therefore being adjustable according to a dependence as, for example, illustrated in Fig. 4.
  • Fig. 6 shows an embodiment where all sensors (8), (9) and (19) (temperature sensor measuring the temperature of the heat exchanging medium in the main supply line (1)) and flow controllers (9), or alternatively the actuating devices (10) are connected to an electronic controller (18) adapted to individually regulate the flows in response to the measured temperatures.
  • the electronic controller (18) comprises the needed means for electronic controllers (18) as they are well known in the arts of electronic controllers.
  • the set point of the return temperature is automatically adjustable according to the actual conditions by the electronic controller (18), whereas in the self-acting embodiment the set point of the return temperature is usually set manually. This gives a huge potential in saving energy, since the system would optimize the set point of the return temperature according to an optimized curve (13) as illustrated in Fig 4.
  • the supply temperature is controlled by the external temperature measurement (the 'super control'). Based on these
  • the 'sub'-controls of the flows in the risers is related to the individual collection of radiators (6) / riser loads, and thus correlates flow to heat demand, and thereby converts this one-pipe system from a traditional constant flow system into a highly energy efficient variable flow system.
  • Another advantage is that the electronic controller (18) allows monitoring and registering temperatures and flows for control and system monitoring, in order to actively optimise the system parameters over time.
  • the electronic controller (18) may in one embodiment automatically open valves / flow controllers (9) located in at least one of the risers to ensure minimum flow.
  • the illustrated system comprises an external temperature sensor (8) for measuring outdoor temperature.
  • the regulation of the supply temperature in the main supply line (1 ) may be done in any manner as it would be obvious according to the actual set up. In the illustrated substation setup system this could be by regulating the primary flow of fluid to the primary side of the heat exchanger (20) of the substation.
  • the electronic controller (18) is connected to the individual actuating devices (10), and is adapted to induce an actuation. In one embodiment the state of the actuating devices (10) is further registered by the electronic controller (18).
  • the electronic controller (18) is further connected to the temperature sensors
  • the actuating device (10) attached to the flow controller (9) is pulse actuated.
  • Pulse width modulation as mean of control uses pulses at some frequency to modulate control the flow precisely.
  • the flow controller (10) is adapted to slowly close or open the flow controller (9) in that it closes off or opens for the flow in the riser, a pulse making the actuating device (9) open or close a little for the flow.
  • the frequency of the pulses then defines the opening status of the flow controller (9).
  • the more frequent the pulses the more open a flow controller (9) or alternatively the more closed a flow controller (9).
  • the situation where the pulses make the actuating member (10) close the flow controller (9) is preferred since, in the case of a failure of the system, there would still be a flow, but the present invention is not limited to this.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Steam Or Hot-Water Central Heating Systems (AREA)

Abstract

L'invention concerne un procédé de régulation du débit d'un fluide d'échange de chaleur qui est acheminé dans une colonne montante d'un réseau à un seul tuyau, qui est une configuration traditionnelle de tuyauterie dans des coopératives d'habitation, par exemple, afin d'amener la chaleur dans les radiateurs d'appartements. Le procédé permet de réguler la température du fluide d'échange de chaleur distribué en réponse à des variations de paramètres externes (température), et le débit en réponse à la température du fluide d'échange de chaleur dans une conduite de retour.
PCT/DK2011/000056 2010-06-10 2011-06-08 Procédé de régulation d'un réseau de distribution de chauffage à un seul tuyau WO2011154002A2 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
UAA201300326A UA106431C2 (ru) 2010-06-10 2011-06-08 Способ регулировки однотрубной системы теплоснабжения
CN201180039331.0A CN103282722B (zh) 2010-06-10 2011-06-08 调节单管热量供应系统的方法

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DKPA201000503 2010-06-10
DKPA201000503 2010-06-10

Publications (2)

Publication Number Publication Date
WO2011154002A2 true WO2011154002A2 (fr) 2011-12-15
WO2011154002A3 WO2011154002A3 (fr) 2013-07-25

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PCT/DK2011/000056 WO2011154002A2 (fr) 2010-06-10 2011-06-08 Procédé de régulation d'un réseau de distribution de chauffage à un seul tuyau

Country Status (8)

Country Link
EP (2) EP2395289B1 (fr)
CN (1) CN103282722B (fr)
HU (1) HUE027364T2 (fr)
PL (1) PL2395289T3 (fr)
RU (1) RU2473014C1 (fr)
SI (1) SI2395289T1 (fr)
UA (1) UA106431C2 (fr)
WO (1) WO2011154002A2 (fr)

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ITBO20120041A1 (it) * 2012-01-27 2013-07-28 Irsap Spa Metodo per regolare la temperatura di ritorno del fluido circolante in un impianto di riscaldamento
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PL2395289T3 (pl) 2016-09-30
HUE027364T2 (en) 2016-09-28
WO2011154002A3 (fr) 2013-07-25
EP3009750A1 (fr) 2016-04-20
EP2395289A2 (fr) 2011-12-14
CN103282722B (zh) 2016-10-26
CN103282722A (zh) 2013-09-04
SI2395289T1 (sl) 2016-09-30
EP2395289A3 (fr) 2013-06-05
UA106431C2 (ru) 2014-08-26
EP2395289B1 (fr) 2016-03-23

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