• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    In a method of operating a ventilating device having a heat exchanger (4) with an exhaust duct through which room air discharged from the inside of the building and a supply air passage through which fresh air supplied from the outside flows is set below a temperature limit for preventing closure of the fan Exhaust ducts of the heat exchanger (4) in a row icing the fresh air supplied to the supply air duct heated with at least one heating element (10). The heating of the fresh air with the at least one heating element (10) is carried out repeatedly, wherein between the heating phases in which the fresh air is heated, a formation of ice is allowed, which is melted again in the subsequent heating phase of the fresh air.
    公开号:AT510604A4
    申请号:T1759/2010
    申请日:2010-10-22
    公开日:2012-05-15
    发明作者:
    申请人:Drexel Und Weiss Energieeffiziente Haustechniksysteme Gmbh；
    IPC主号:
    专利说明:

    Patent attorneys; · Hefel scofmann 23674/33 / s 101011
    patent attorneys
    European Patent Attorneys
    European Trademark Attorneys
    Dl Herbert Hefel (until 2006)
    Dr. Ralf Hofmann Thomas Fechner 6806 Feldkirch, Austria Egelseestr 65a, PO Box 61 1
    The invention relates to a method for operating a ventilation device, which comprises a heat exchanger with an exhaust duct, flows through the air discharged from the building interior room air, and a supply air duct, flows through the fresh air supplied from the outside, below a temperature limit value for preventing a closure the exhaust air duct of the heat exchanger as a result of icing the fresh air supplied to the supply air duct is heated with at least one heating element.
    Ventilation systems are known with geothermal heat exchangers in which the fresh air to be supplied from the outside is first passed through a pipe laid in the ground, which serves as a heat exchanger The ventilation system also has a heat exchanger through which on the one hand led the air coming from the building interior and the fresh air be transferred, with heat of the room air is transferred to the fresh air. Due to the passage through the upstream geothermal heat exchanger, the temperature of the fresh air is above 0 ° C even at low outside temperatures.
    If no such geothermal heat exchanger is present, then at least one, generally electrical, heating element is provided, with which the fresh air supplied to the heat exchanger is preheated at low outside temperatures before entering the heat exchanger. If such a preheating omitted, it could be caused by the heat recovery condensate, which precipitates out of the guided through the heat exchanger room, freeze, whereby the exhaust duct of the heat exchanger would be closed.
    In practice, the preheating of the fresh air supplied is frequently regulated as a function of the temperature which the room air guided through the heat exchanger has after exiting the heat exchanger (this air is usually used as exhaust air).
    Bank bonds T +43 (0) 5522 73 137 Austrian Post Savings Bank Sparkasse of the City of Feldkirch F +43 (0) 5522 73 359
    Account No. 92.111.622, BIS 60000 Account No. 0400-006300, bank code 20604 M office@vpat.at
    Swift Code: OPSKATWW Swift Code. SPFKAT2B I www.vpat.ot • * 2 • * · · draws) to maintain this temperature above 0 ° Celsius. This type of preheating of the fresh air supplied to the heat exchanger (before entering the heat exchanger, this is usually referred to as outside air) usually leads to an energy consumption in the range of 200-300 kWh / a, but in some cases up to 1000 kWh / a.
    Another way of controlling the preheating of the outside air provides that the outside air is heated to a constant value of about -3.5 ° Celsius when the outside temperature is less than this value. At the usual efficiencies of used heat exchangers, which are in the range of 90%, then it comes to a surface temperature of the heat exchanger, which is still above freezing, so that formation of ice is prevented. The energy required for the preheating can thus be reduced to about 100-150 kWh / a, which is still a noteworthy quantity. Passive houses often come with a magnitude of 1500 kWh / a for the entire building services (heating, ventilation, hot water, including auxiliary drives). The preheating of the outside air can therefore increase the consumption by 10%.
    The object of the invention is to provide an improved method of the type mentioned by which the required for the preheating of the outside air energy consumption (if no geothermal heat exchanger is available) can be reduced. According to the invention, this is achieved by a method having the features of claim 1.
    In the method according to the invention, at low outside temperatures at which the risk of freezing the heat exchanger, the heating of the fresh air with the at least one heating element is not carried out continuously but intermittently, i. in repetitive heating phases. There is no preheating of the fresh air supplied to the heat exchanger between these heating phases and ice formation is permitted in these phases in which no fresh air is heated. In the heating phases, the ice formed in each case is defrosted again.
    It has been found that this approach, which differs from the state of the art, in that, instead of preventing ice formation by constant sufficient preheating of the supplied outside air, such ice formation is permitted to a limited extent and this ice is then thawed again, a considerable energy saving can be achieved can, for example, amount to more than half of the heat energy otherwise required for ice maintenance. 3 * · # * ·
    Advantageously, the volume of air (= the volume flow of air) through the heat exchanger per unit time is reduced over the duration of a respective heating phase over the volume flow present between the heating phases both for the room air passed through the heat exchanger and for the fresh air passed through the heat exchanger to a value for the two volume flows, which is in the range of 70-100 m3 / h. It can thereby be achieved at a favorable (not too high) value of the heating power of the at least one heating element sufficient preheating of the heat exchanger supplied fresh air. By heat transfer in the heat exchanger, the room air passed through the heat exchanger can optionally also be heated in order to melt the ice formed in the exhaust duct of the heat exchanger. It should be noted here that of the temperature difference around which the fresh air is heated, only that portion of the temperature difference for the defrosting of the ice formed can be exploited, by which the surface of the heat exchanger is heated to a value above 0 ° Celsius. In order to achieve a sufficiently large increase above 0 ° Celsius even with correspondingly low outside temperatures, the fresh air must be heated by a sufficiently large temperature difference, which is preferably at least 30 ° Celsius, more preferably at least 40 ° Celsius. For example, the heating power with which the preheating of the fresh air is carried out in the range of 1 kW to 1.5 kW.
    Depending in particular on the outside temperature, the temperature increase during the preheating, the room air humidity and the volume flows through the heat exchanger (which are preferably the same for the fresh air and the room air), the ratio of the duration of a heating phase (= defrost) to the duration of the preceding phase changes without Preheating the fresh air supplied to the heat exchanger. Preferably, this ratio is less than 0.25, i. the duration of each heating phase is shorter than one quarter of the duration of the preceding phase without preheating the outside air. For example, a defrosting period of usually 1-3 minutes per hour, in extreme cases of a maximum of 10 minutes may be required. If a reduction in the volume flows of the room air and the fresh air through the heat exchanger takes place over this time, this generally leads to a total of completely negligible air volume reduction of the ventilation, which can be for example in the range of usually 1% and in extreme cases 5%.
    The starting times of the heating phases can be set periodically, for example, repetitively. But it could also be used another measure, for example, the pressure drop in the exhaust duct of the heat exchanger.
    Heating phases of the fresh air are only carried out at outside temperatures where there is a danger of icing. For this purpose, a temperature limit is set, below which repetitive heating phases are carried out. This temperature limit may be based on the temperature of the fresh air supplied to the heat exchanger prior to entry into the heat exchanger and against heating by the at least one heating element (= outside temperature or outside air temperature) and / or on the temperature of the Raumiuft passed through the heat exchanger after leaving the heat exchanger {= Exhaust air temperature) refer.
    For example, can be used as a temperature limit, a value of the outside temperature, the temperature limit then at least below -10 Celsius, for example, at -4 ° Celsius. Instead, a value of the exhaust air temperature (= temperature of the room air after leaving the heat exchanger) or a combination of the outside temperature and the exhaust air temperature can be used as the limit value. It is particularly advantageous for the limit value to use the mean value between the temperature of the fresh air supplied to the heat exchanger (before preheating and before entering the heat exchanger) and the temperature of the room air passed through the heat exchanger after leaving the heat exchanger (= exhaust air temperature), wherein heating phases are performed if and only if this average value is less than 0 ° Celsius. At lower temperatures, surface temperatures of areas of the exhaust duct of the heat exchanger will be below freezing. In the case of such a mean temperature value of the temperatures mentioned below 0 ° Celsius, the temperature of the fresh air supplied to the heat exchanger is less than -1 ° Celsius (with respect to normal room temperatures in the range of 18 ° C to 23 ° Celsius and the usual efficiency of such a heat exchanger in the range of 90%).
    Further advantages and details of the invention are explained below with reference to the accompanying drawings: In the drawing, the single FIGURE shows a schematic representation of an exemplary embodiment of a ventilation device for carrying out the method according to the invention.
    The ventilation device shown in the figure comprises an input 1 for the derived from the building interior air. This is usually referred to in their supply to the ventilation device as exhaust air and their flow is indicated in the figure by an arrow. The room air is guided by a fan 2 through a filter 3 and an exhaust duct of the heat exchanger 4 and leaves the ventilation unit at an output 5 as exhaust air. The exhaust air is discharged to the outside. The volume flow of the exhaust air is indicated in the figure by an arrow.
    The fresh air supplied from the outside is fed to an inlet 6 of the ventilation unit. The fresh air is usually referred to when entering the ventilation unit as outside air and its flow is indicated in the figure by an arrow. By means of a fan 7, the fresh air is passed through the filter 8, a heating station 9 with an electric heating element 10 and through the supply air duct of the heat exchanger 4 to the output 11. The outlet 11 leaving air is usually referred to as supply air and its flow is indicated in the figure by an arrow.
    The ventilation device further comprises a controller 12, which are supplied to various measured variables explained below and which controls the ventilation device in the manner also to be described. This control can be done for one or more variables in a closed loop (= loop), i. the terms "control" and "steer " should also the terms "regulation" and "regulate" include.
    The inputs and outputs 1, 6; 5, 11 are formed by pipe connection flanges.
    In the heat exchanger 4 is carried out in the usual way an energy recovery from the guided through the ventilation unit room air by heat of the room air is transferred to the fresh air. At low temperatures, where surface temperatures of walls of the exhaust duct of the heat exchanger 4 are below freezing, to prevent closure of the exhaust duct of the heat exchanger by freezing condensate, the "freeze-free" method described in more detail below is described. the heat exchanger 4 performed:
    In repetitive heating phases, which can also be referred to as dewing phases, the fresh air supplied to the supply air duct of the heat exchanger 4 is preheated in the heating station 9, specifically to a temperature above freezing, preferably to a temperature above 10 ° C. As a result, frozen condensate, which has formed in the exhaust duct of the heat exchanger 4 in the phase before the heating phase, in which no preheating of the fresh air supplied has been formed, again defrosted. Over the period of a respective heating phase or defrosting phase, the volume flows of the guided through the heat exchanger 4 room air and guided through the heat exchanger 4 fresh air are preferably reduced. The volumetric flows through the supply air and exhaust air duct of the heat exchanger 4 hereby favorably have the same (higher) value both during the heating phases and the same (lower) value during the heating phases.
    The volume flows of the room air and the fresh air can be adjusted by the fans 2, 7, which are controlled by the controller 12 accordingly.
    For example, the volume flows are reduced during the heating phases to a value of 80 m3 / h and the fresh air is heated in the heating station 9 with a power of 1.2 kW, this leads to a temperature increase At the fresh air as it passes through the heating station 9 of about 45 Kelvin (K).
    Such a heating of the fresh air, the temperature of the guided through the heat exchanger room air at its exit from the heat exchanger (= exhaust air temperature), for example in the range of 20 ° Celsius to 40 ° Celsius (depending on the outside temperature) and after a few minutes, the required amount of energy brought in to melt all the ice.
    How much ice is actually formed between two heating phases depends on the amount of air (ie the volume flow times the time between the two defrosting phases), the outside temperature and the exhaust air humidity. From these variables, the maximum amount of condensate and thus the maximum amount of ice to be defrosted can be determined, for which purpose, for example, an empirical formula can be determined (this may be somewhat different depending on the type of heat exchanger used). From the maximum amount of ice expected, the amount of heat required for defrosting Q_abtau results from the product of this maximum expected amount of ice and the heat of fusion of the water, which is 0.093 Wh / g (the heating of the ice to 0 ° Celsius can be neglected). •: ι
    To determine the air humidity of the exhaust air, the determination of the difference between the temperature of the room air after passing through the heat exchanger 4 (= exhaust air temperature) and the outside air temperature can be used instead of a (relatively expensive) humidity sensor. The greater this temperature difference, the higher the humidity of the exhaust air and the greater is the amount of condensate, with an at least approximately linear relationship exists.
    The exhaust air capacity available as a function of the outside temperature is calculated as follows: P_air air = (t_raumluft - 0.9 x (t_ra recirculated air - (t_outside air + Δΐ)}) x V x 0.33 where t_raumluft is the temperature of the room air before entering into At the temperature difference by which the fresh air (in m3 / h) of the heating station is heated, and V corresponds to the volume flow of the room air and the fresh air, the heat exchanger, t_outdoor air, the temperature of the fresh air before entering the heat exchanger and preheating , 9 is used for the typical efficiency of such heat exchangers and 0.33 denotes the specific heat capacity of the air (in Wh / m3K) .The required defrost duration (= duration of the heating phase) in seconds then results:
    Defrost duration = (Q_abtau [Wh] / P_abluft [W]) x 3600 [s / h]
    The general prerequisite for ice formation is that at least a portion of the wall of the exhaust duct of the heat exchanger has a surface temperature which is below 0 ° C. The lowest surface temperature of the heat exchanger occurs at the entrance of the outside air and outlet of the exhaust air and therefore results from the average of these two temperatures. This mean value can thus be used as the limit value for carrying out the intermittent preheating of the fresh air, wherein the intermittent preheating is carried out only if this mean value (t_outdoorair + t_fortluft) / 2 < 0 is.
    For detecting the temperature of the room air supplied to the heat exchanger (t_raumluft) before entering the heat exchanger 4, a temperature sensor 13 is shown in the figure, the output signal of the controller 12 is supplied. The temperature sensor 14 is used to detect the temperature of the room air after leaving the heat exchanger 4 (= t_fortluft) and the output signal of this temperature sensor 14 is also supplied to the controller 12. The temperature sensor 15 serves to detect the fresh air supplied to the heat exchanger 4, before passing through the heating station 9 (= t_außenluft) and the output signal of the temperature sensor 15 is in turn fed to the controller 12.
    Depending on the detected variables, the controller 12 determines the duration of a respective heating phase and heats the fresh air over the corresponding heating period in the heating station 9. The heating phases are carried out in the embodiment at periodically repeating start times, for example every hour.
    Further or other measured variables for controlling the method, for example for controlling the duration of the respective heating phase, can be provided. For example, the power with which the air is heated in the heating station 9, could be controlled. For example, instead of the temperature sensor 14 for detecting the temperature of the exhaust air, a moisture sensor for detecting the humidity of the room air supplied to the heat exchanger could be provided.
    For example, the temperature difference by which the fresh air in the heating station 9 is heated, could be changed depending on the outside temperature. In this case, it would be possible to heat up the fresh air in the heating station 9 to a value which is at least largely constant, independent of the outside temperature, for example to a value lying in the range between 35 ° Celsius and 45 ° Celsius.
    The reduction of the volume flow could also be carried out, for example, as a function of the temperature of the outside air.
    An energy saving also results from a controller that takes into account fewer input variables, for example, the actual air humidity of the exhaust air is ignored and is designed for a maximum expected value of this humidity.
    Entrance room air
    fan
    Filter Heat exchanger Output Room air Input Fresh air Fan Filter
    heating station
    heating element
    Output fresh air
    control
    temperature sensor
    temperature sensor
    temperature sensor
    Legend to the hints
    权利要求:
    Claims (10)
    [1]
    PatentanwälteHefelScHofmann 2 3674/3 3 / ss 101011 * · I ··· * * · »» · Patent Attorneys European Patent Attorneys European Trademark Attorneys Dl Herbert Hefel (until 2006) Ralf Hofmann Thomas Fechner 6806 Feldkirch, Austria Egelseestr 65a, PO Box 61 1. A method for operating a ventilation device having a heat exchanger (4) with an exhaust duct through which flows out of the building interior air, and a supply air duct, through which fed from the outside Fresh air flows, wherein below a temperature limit value for preventing a closure of the exhaust air duct of the heat exchanger (4) due to icing the fresh air supplied to the supply air duct is heated with at least one heating element (10), characterized in that the heating of the fresh air with the at least one heating element ( 10) is carried out in repetitive heating phases, wherein between the heating phases, in which the fresh air is heated, a formation of ice is allowed, which is melted again in the following heating phase of the fresh air.
    [2]
    2. The method according to claim 1, characterized in that during the heating phases in which the heating of the fresh air with the at least one heating element (10) is carried out, the volume flows through the heat exchanger (4) guided room air and through the heat exchanger (4 ) guided fresh air can be reduced.
    [3]
    3. The method according to claim 2, characterized in that the volume flows of the heat exchanger (4) supplied room air and the heat exchanger (4) supplied fresh air during the heating phases are reduced to a value which is in the range of 70m3 / h to 100m7h.
    [4]
    4. The method according to claim 1 or 2, characterized in that the heating phases are carried out at periodically repeating start times. Bank details T +43 (0) 5522 73 137 Österreichische Postsparkasse Sparkasse der Stadt Feldkirch F +43 (0) 5522 73 359 Account no. 92.111.622, bank code 60000 Account no. 0400-006300, bank code 20604 M office@vpat.at Swift Code: OPSKATWW Swift Code: SPFKAT2B 1 www.vpat at 5.
    [5]
    5th

    Method according to one of Claims 1 to 4, characterized in that the heating phases are of different lengths, depending on at least one measured variable correlating with the amount of ice formed, preferably at least as a function of the volume flow of the room air passed through the heat exchanger (4).
    [6]
    6. The method according to claim 5, characterized in that the duration of a respective heating phase further in dependence on the difference between the temperature of the fresh air before entering the heat exchanger and against heating by the at least one heating element (10) and the temperature of the heat exchanger (4) guided room air is carried out after its exit from the heat exchanger.
    [7]
    7. The method according to claim 5 or 6, characterized in that the duration of a respective heating phase in dependence on the temperature of the heat exchanger (4) supplied room air is performed prior to their entry into the heat exchanger (4).
    [8]
    8. The method according to any one of claims 1 to 7, characterized in that the duration of each heating phase is shorter than a quarter of the duration of the phase before the heating phase, in which no heating of the fresh air with the at least one heating element (10) is performed ,
    [9]
    9. The method according to any one of claims 1 to 8, characterized in that the fresh air is heated in the heating phases with the at least one heating element (10) by at least 30 K, preferably by at least 40 K.
    [10]
    10. The method according to any one of claims 1 to 9, characterized in that the temperature limit, below which the repeated heating of the heat exchanger (4) supplied fresh air with the at least one heating element (10) is performed, to the temperature of the Heat exchanger supplied fresh air before entering the heat exchanger (4) and before heating by the at least one heating element (10) and / or on the temperature of the heat exchanger (4) guided room air after leaving the heat exchanger (4) relates, preferably on the mean value between the temperature of the fresh air supplied to the heat exchanger before entry into the heat exchanger (4) and before heating by the at least one heating element (10) and the temperature of the heat exchanger (4) guided room air after leaving the heat exchanger, wherein repetitive heating phases are carried out only, we nn this mean is less than 0 ° Celsius.
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    同族专利:
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    EP2444755A2|2012-04-25|
    AT510604B1|2012-05-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    JPS6219632A|1985-07-18|1987-01-28|Mitsubishi Electric Corp|Ventilator of heat exchange type|
    SE402486B|1976-11-09|1978-07-03|Svenska Flaektfabriken Ab|VERMEAT RECYCLING FACILITY|
    US5257736A|1992-08-06|1993-11-02|Donald Roy|Self-regulating air ventilation apparatus|
    EP1616133B1|2003-04-23|2008-10-22|Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V.|Combined fluid-air evaporator and novel switching concept for a heat pump in a ventilating apparatus|
    US7942193B2|2007-11-21|2011-05-17|Nu-Air Ventilation Systems Inc.|Heat recovery ventilator with defrost|DE102013018938A1|2013-11-12|2015-05-28|Gea Air Treatment Gmbh|Plant for heat recovery|
    PL3077734T3|2013-12-02|2020-02-28|Zehnder Group International Ag|System and process for fixing a heating or cooling body|
    US10337758B2|2014-09-25|2019-07-02|Panasonic Intellectual Property Management Co., Ltd.|Heat exchanger ventilator|
    AT516753B1|2015-02-23|2016-08-15|Drexel Und Weiss Energieeffiziente Haustechniksysteme Gmbh|ventilation|
    GB2536428B|2015-03-13|2017-05-31|Redring Xpelair Group Ltd|Building ventilator|
    WO2016147147A2|2015-03-17|2016-09-22|Zehnder Group International Ag|Exchanger element for passenger compartment and passenger compartment equipped with such an exchanger element|
    CN111503815A|2020-04-29|2020-08-07|广东美的制冷设备有限公司|Defrosting control method of air conditioning system and air conditioning system|
    CN111503826A|2020-04-29|2020-08-07|广东美的制冷设备有限公司|Defrosting control method of air conditioning system and air conditioning system|
    EP3964763A1|2020-09-04|2022-03-09|Aereco|Improved heat exchanger for dual-flow ventilation system|
    法律状态:
    2018-06-15| MM01| Lapse because of not paying annual fees|Effective date: 20171022 |
    优先权:
    申请号 | 申请日 | 专利标题
    ATA1759/2010A|AT510604B1|2010-10-22|2010-10-22|METHOD FOR OPERATING A VENTILATION DEVICE|ATA1759/2010A| AT510604B1|2010-10-22|2010-10-22|METHOD FOR OPERATING A VENTILATION DEVICE|
    EP11008262.5A| EP2444755A3|2010-10-22|2011-10-13|Method for operating a ventilation device|
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