• 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:

    公开号:NL2005206A
    申请号:NL2005206
    申请日:2010-08-10
    公开日:2011-02-22
    发明作者:Morten Nylykke
    申请人:Maersk Container Ind As；
    IPC主号:
    专利说明:

    DEHUMIDIFIER
    FIELD OF THE INVENTION
    The present invention relates to a dehumidifier for dehumidifying a cooling compartment in a refrigeration system especially for dehumidifying a refrigerated transportation container and a method for controlling the dehumidifying process using an economically optimized method to control the humidity in a closed cooled room by controlling the capacity of an evaporator.
    BACKGROUND OF THE INVENTION
    A common method to dehumidify air is to blow air over a cold evaporator with the temperature of the evaporator surface maintained below the frost point so the moisture in the air will deposit on the evaporator coils and freeze to ice. The ice then is removed from time to time by defrosting.
    US 4,291,542 shows an air drying apparatus comprising a refrigeration system, the evaporator of which is used for cooling an air flow to or below its dew point whereby the moisture in the air as drawn through the cooler by a fan is condensed on the cooler and drained off. The cooler can temporary be connected as a condenser whereby the cooler is heatable for defrosting. A temperature sensor mounted on the cooler serves to control the fan power for optimal economy in normal operation and to detect frost formation and control start stop of a defrosting cycle.
    The problem of common humidifiers is that the surface temperature often is lower than it has to be and therefore is not economically and that the dehumidifying process causes disturbances in the refrigeration system, especially critical is disturbance of the cooling of the goods in the cooling compartment of the refrigerator.
    SUMMERY OF THE INVENTION
    It is the object of the invention to make a dehumidifier for a cooling compartment especially for a refrigerated transportation container and a method to control the dehumidifier to remove moisture from the air in an economical optimized manner.
    It is further the object of the invention during the dehumidifying process to keep the parameters of the refrigeration system, especially the temperature in the cooling compartment within acceptable limits so the dehumidifying process do not damage the goods in the cooling compartment during dehumidification.
    It is further the object of the invention to de-ice the evaporator whenever needed during the dehumidification process.
    The refrigeration system can be operated in three different ways; Normal operation, dehumidification and defrosting. During normal operation the refrigeration system works like any normal refrigeration system, when cooling is needed refrigerant is let into the evaporator and air is blown over the evaporator and is cooled down.
    The invention provides a method for dehumidifying the air in a cooling compartment, for instance in a container in an economically optimized manner and in a way that keeps the measured parameters of the refrigeration system, especially the temperature in the cooling compartment within acceptable limits during dehumidification.
    The refrigeration system comprises a refrigeration circuit, a control unit, a cooling compartment, a re-establish mode and a dehumidification mode, a target air temperature, a target air moisture percentage; the refrigeration circuit comprises a compressor, an expansion valve, a condenser and an evaporator; the cooling compartment comprises a cooling space, and the cooling space comprises means to blow air through the cooling space, the evaporator, a temperature sensor placed close to the surface of the evaporator, a moisture sensor arranged upstream of the evaporator and heating elements arranged downstream of the evaporator;
    The control unit comprises means to determine a first shift condition and a second shift condition, and the dehumidification method comprising the steps of: a. enter the dehumidifying mode, b. when a first shift condition is reached the refrigeration system shifts to reestablish mode, c. when a second shift condition is reached the refrigeration system shifts to dehumidification mode, d. the steps b-c is repeated until the target air moisture percentage is reached.
    The advantage of this step wise dehumidification method, where there is shifts between dehumidification mode and re-establish mode, is that the measured parameters of the refrigeration system, especially the temperature in the cooling compartment is kept within acceptable limits. By regularly entering re-establish mode the parameters measured in the system, for instance the cooling compartment temperature can be checked, and if they are different from the preferred operation parameters, the system runs for a while in re-establish mode to re-establish the parameters to their preferred values. In this way the temperature in the cooling compartment can be kept basically within acceptable limits during dehumidification, so the goods in the cooling compartment are not damaged.
    The cooling compartment comprises a cooling space, the cooling space are separated from the rest of the cooling compartment in such a way that no goods can be placed in the cooling space, so there is a free flow of air in the cooling space.
    In the preferred embodiment the dehumidification mode comprises the steps of: - blowing air over the evaporator, the moisture sensor measures the air moisture percentage and air temperature before the air reaches the evaporator, determine a target surface temperature based on the measured air moisture percentage and air temperature, regulate the surface temperature of the evaporator by controlling the refrigeration circuit so the surface temperature of the evaporator correspond to the chosen target surface temperature, the heating elements warms up the air after it passed the evaporator.
    By using the air moisture percentage and air temperature of the air before it reaches the evaporator to determine a target surface temperature to regulate the surface temperature of the evaporator, an economically optimized control of the process can be obtained.
    The target temperature is determined so it is not too low; a too low temperature will not be economically optimized, energy will be wasted. The temperature of the surface of the evaporator will be chosen such that it is cold enough to give an effective condensing; the surface temperature is chosen so the moisture percentage of the air, when it passes the evaporator and is cooled down, reached 100%. The temperature for which the moisture percentage reaches 100% is called the dew-point temperature. The surface temperature of the evaporator is kept a little lower than the dew-point temperature.
    The heating elements placed downstream after the evaporator heats up the air just after the air passed the evaporator. This has the effect that when air has reached a moisture percentage of 100% the moisture condenses at the coldest surface. By having heating elements just after the evaporator it is ensured that the coldest surface is the evaporator, so the moisture condenses on the evaporator. A further advantage of having heating elements just after the evaporator is that the heating elements heats up the air before it returns to the cooling compartment, so by heating the air the moisture percentage of the air is lowered, so air with a lower moisture percentage is returned to the cooling compartment.
    After the moisture condenses on the evaporator, it drains down in a tray placed in the bottom of the container below the evaporator.
    The refrigeration system comprises means to determine the dew point temperature, when entering the dehumidification mode the dew point temperature is determined for air with the found moisture percentage and air temperature, and then a target surface temperature, lower than the dew point temperature, is determined.
    To further improve the method, the dehumidification mode can further comprise the step of reducing the amount of refrigerant in the evaporator, so the evaporation takes place in the first part of the evaporator. The first part of the evaporator is to be understood as the part closed to the refrigerant inlet of the evaporator.
    By reducing the amount of refrigerant evaporation occurs in the first part of the evaporator, this makes it easier to control the temperature of the surface of the evaporator, so it is easier to control the refrigeration system to reach the target temperature of the evaporator surface. The disadvantage of this is that by adding less of the refrigerant to the evaporator, the cooling of the air is less and therefore the temperature in the cooling compartment might rise. Therefore the method of entering the re-establish mode regularly becomes very important because the need to regularly re-establish the parameter values, like the cooling compartment temperature, increase. Likewise if the dehumidification takes place at a time, where cooling is not needed, the cooling compartment temperature will decrease and also in this case entering the reestablish mode regularly is important.
    A simple embodiment to determine the target surface temperature is to choose the target surface temperature to be less than 10 degrees lower than the dew point temperature. The dew point temperature is calculated when the system goes into dehumidification mode, and then a number of degrees are subtracted from the dew point temperature to determine the target surface temperature.
    This is a simple way to determine the target surface temperature; of course more complex algorithms can also be used. The basic idea is that the target surface temperature should not be to much lower than the dew point temperature, because that would be economically inefficient. However the target surface temperature should be so much lower than the dew point temperature that the dew point temperature does not drop to be lower than the target surface temperature before the system enters reestablish mode.
    Conditions to determine when to shift from re-establish mode to dehumidification mode and visa-versa has to be defined either by the user or by the manufacturer and entered into the control unit.
    One possible embodiment is that the conditions, called the second shift condition, for shifting from re-establish mode to dehumidification mode is that the air temperature is less than a preselected number of degrees different from the target air temperature. For instance if the temperature in the cooling compartment is within 0.5 degrees of the target air temperature, the conditions can be close enough to the preferred conditions, and the system can shift to dehumidification mode to continue dehumidifying.
    Likewise a possible embodiment is that the first shift condition, to shift from dehumidification mode to re-establish mode, is when the air temperature is more than a preselected number of degrees different from the target air temperature. This preselected number of degrees can for instance be a difference of 5° C.
    Another possible embodiment is that the first shift condition, to shift from dehumidification mode to re-establish mode, is after a preselected time period. Instead of using the temperature or another measure parameter to decide when to go into reestablish mode, re-establish mode can be entered after running dehumidification mode for a certain time period.
    The control unit can be set to start the dehumidification method, when the relative humidity RH, (based on actual value from RH sensor), percentage is higher than a predefined value. Another possibility is that the dehumidification can be initiated manually.
    When the evaporator surface temperature drops below the freezing point, ice can assemble on the evaporator coils, therefore defrosting can be necessary. Defrosting is performed to remove ice from the evaporator, the method comprising the steps of: the heating elements are turned on, - turning off the means to blow air over the evaporator, when the ice is removed from the evaporator and the evaporator temperature Tevap is above 20°C, previous operation resumes.
    Usually defrosting takes place as part of the re-establish mode.
    BRIEF DESCRIPTION OF THE DRAWINGS
    Fig. 1 shows an embodiment of this invention, it is a transport container with the dehumidification system.
    Fig. 2 shows an I.x-diagram displaying an example of how the dehumidifying method runs.
    DETAILED DESCRIPTION OF THE DRAWINGS
    Fig. 1 shows a transport container 1 with is the preferred embodiment of this invention. The container 1 comprises a cooling compartment 2 and a cooling space 3. The cooling space 3 is separated from the rest of the cooling compartment by a plate 4. In the cooling space 3 is placed an evaporator 5. The rest of the refrigeration circuit is placed outside the container, in Fig. 1 is shown the compressor 6 and the expansion valve 7. The condenser is not shown. In the cooling space 3 beside the evaporator 5 is placed a moisture sensor 8 and heating elements 9. In the ends of the cooling space 3 is an air inlet 10 and in the other end is an air outlet 11. And outside the container is a control unit 12.
    In this case the cooling space 3 is an air channel build into the cooling compartment 2. The cooling space 3 can be a part of the container 1 or it can in an alternative embodiment be a separate unit mounted into the cooling compartment 2.
    At the air inlet 10 there are means to blow air into the cooling space 3; this could for instance be a fan. The moisture sensor 8 is placed upstream of the evaporator 5, so the air passes the moisture sensor 8 before it reaches the evaporator 5. The moisture sensor 8 measures the moisture percentage and the air temperature. The heating elements 9 are placed downstream from the evaporator 5, so the air reaches the heating elements 9 just after the air passed the evaporator 5.
    Fig. 2 is an Ι,χ-diagram for moist air at 1013 mBar. The diagram can also be called a h,x-diagram or a Mollier chart. On the left side is air temperature Tair, the horizontal lines follows the air temperature. On the right side the relative moisture RH percentage is following the curved lines. The temperatures following the slanting lines are not relevant for this invention. The x-axis of the diagram shows the moisture content in the unit [kg water/ kg air]. The y-axis shows the Enthalpy, the Enthalpy is represented by the air temperature Tair.
    The dehumidification process is initiated at the point A and the dehumidification mode is started. The air temperature in the container is 30° Celsius and the humidity is 90%. Going from point A vertically down to the 100% moisture line, the dew point temperature Tdew is found to be 28° C. Now the target surface temperature TO of the evaporator surface is by the control unit 12 chosen to be T0_1, which is 20 0 C. It is important that the TO is lower than the found dew point temperature Tdew, so a moisture percentage of 100% is reached for the air passing the surface of the evaporator. The air passing close to the evaporator then cannot hold all the moisture in the air, and therefore moisture condenses on the surface of the evaporator.
    After a while the air temperature has dropped to 25 0 C. Then a first shift condition is reached, and the system shifts to re-establish mode. The refrigeration system is now operated in such a way that the air temperature increases to the target temperature of 30° C reaching point B in Fig. 2. Now the moisture percentage in the container has dropped to 72%. Reaching point B triggers a second shift condition and the system shifts back to dehumidification mode. A new target temperature for the evaporator surface is chosen. In this embodiment the algorithm used by the control unit 12 chooses the new target temperature T0_2 simply to be 5 0 C less than the previous target temperature.
    So the surface temperature of the evaporator is now lowered to T0_2, which is 150 C. The air temperature is now slowly dropping and when it has dropped 5 0 C, again the system shifts to re-establish mode and the temperature is increase to the target temperature of 30° C reaching point C, where the moisture percentages is now dropped to 60%.
    The procedure continues through two more steps eventually reaching point E, where the moisture percentages is dropped to lower than 50%, the target percentage is reached and the dehumidification process stops.
    权利要求:
    Claims (11)
    [1]
    A dehumidification method for a cooling system, wherein the cooling system comprises a cooling circuit, a control unit (12), a cooling compartment (2), a desired air temperature, a desired humidity percentage; wherein the cooling circuit comprises - a compressor (6), - an expansion valve (7), - a condenser, - an evaporator (5); wherein the cooling compartment (2) comprises a cooling space (3), and the cooling space (3) comprises - means for blowing air through the cooling space (3), - the evaporator (5), - a temperature sensor close to the surface of the evaporator (5) is placed, - a moisture sensor (8) which is arranged upstream of the evaporator (5), - heating elements (9) which are arranged downstream of the evaporator (5); characterized in that the cooling system further comprises a recovery mode and a dehumidification mode, and the control unit (12) comprises means for determining a first shift condition and a second shift condition, and the dehumidification method comprises the steps of: a. entering the dehumidification mode, b . when a first shift condition is reached, the cooling system shifts to recovery mode, c. when a second shift condition is reached, the cooling system shifts to dehumidification mode, d. steps b-c are repeated until the desired humidity percentage is reached.
    [2]
    A dehumidification method for a cooling system according to claim 1, wherein the dehumidification mode comprises the steps of: - blowing air over the evaporator (5), - the moisture sensor (8) measures the humidity percentage and the air temperature before the air reaches the evaporator (5) - determining a target surface temperature on the basis of the measured humidity percentage and the measured air temperature, - regulating the surface temperature of the evaporator (5) by controlling the cooling circuit so that the surface temperature of the evaporator (5) corresponds to the chosen target surface temperature, - the heating elements (9) heat the air after it has passed the evaporator (5).
    [3]
    The dehumidification method for a cooling system according to claim 2, wherein the cooling system further comprises means for determining the dew point temperature and the dehumidification mode determining the dew point temperature for air with the found humidity percentage and the found air temperature, and determining a target surface temperature lower than the dew point temperature .
    [4]
    The dehumidification method according to claims 2 or 3, wherein the dehumidification mode further comprises the steps of reducing the amount of coolant in the evaporator (5) so that the evaporation takes place in the first portion of the evaporator (5).
    [5]
    The dehumidification method according to claims 2-4, wherein the selected target surface temperature is less than 10 ° C lower than the dew point temperature.
    [6]
    The dehumidification method according to any of claims 1-5, wherein the second shift condition to shift from the recovery mode to the dehumidification mode is that the air temperature is less than a preselected number of degrees Celsius different from the desired air temperature.
    [7]
    The dehumidification method according to any of claims 1-6, wherein the first shift condition to shift from the dehumidification mode to the recovery mode is when the air temperature is more than a preselected number of degrees Celsius different from the target air temperature.
    [8]
    The dehumidification method according to any of claims 1-7, wherein the first shift condition is to shift from the dehumidification mode to the recovery mode after a preselected period of time.
    [9]
    The dehumidification method according to any of claims 1-8, wherein the dehumidification starts when the moisture percentage or the moisture content is higher than a predefined value.
    [10]
    The dehumidification method according to any of claims 1-9, wherein the dehumidification begins when it is manually activated.
    [11]
    The dehumidification method according to claims 1 to 10, wherein defrosting is carried out to remove ice from the evaporator, the method comprising the steps of: - switching on the heating elements (9), - switching off the means for transferring air over the evaporator (5) ) - when the ice has been removed from the evaporator and the evaporator temperature Tevap is above 20 ° C.
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3831663A|1973-04-05|1974-08-27|Philco Ford Corp|Air conditioner|
    GB1596171A|1977-01-19|1981-08-19|Dantherm As|Air conditioning apparatuses|
    SE418829B|1979-11-12|1981-06-29|Volvo Ab|AIR CONDITIONING DEVICE FOR MOTOR VEHICLES|
    CA1228139A|1984-03-06|1987-10-13|John Polkinghorne|Appliance control system|
    JPS6036839A|1984-07-09|1985-02-26|Toshiba Corp|Humidity and temperature control process in air conditioning machine|
    JPH03279727A|1990-03-28|1991-12-10|Hitachi Ltd|Temperature and humidity control method for temperature and humidity control unit|
    US5119571A|1990-08-01|1992-06-09|Richard Beasley|Dehydration apparatus and process of dehydration|
    US5129234A|1991-01-14|1992-07-14|Lennox Industries Inc.|Humidity control for regulating compressor speed|
    JP3262288B2|1992-08-26|2002-03-04|東芝キヤリア株式会社|Air conditioner humidity control device|
    WO1996029555A2|1995-03-14|1996-09-26|Hussmann Corporation|Refrigerated merchandiser with modular evaporator coils and eepr control|
    US5578753A|1995-05-23|1996-11-26|Micro Weiss Electronics, Inc.|Humidity and/or temperature control device|
    US6070110A|1997-06-23|2000-05-30|Carrier Corporation|Humidity control thermostat and method for an air conditioning system|
    DE19728577C2|1997-07-04|1999-11-25|Daimler Chrysler Ag|Method for controlling the evaporator temperature of an air conditioning system depending on the dew point|
    DE19728578C2|1997-07-04|1999-11-25|Daimler Chrysler Ag|Process for evaporator temperature control depending on the dew point|
    JP3443521B2|1997-12-01|2003-09-02|株式会社東芝|refrigerator|
    JP2000274916A|1999-03-26|2000-10-06|Sanyo Electric Co Ltd|Cooling storage chamber|
    JP2002130863A|2000-10-19|2002-05-09|Chikayoshi Sato|Dehumidifying method|
    DE10161306A1|2001-12-13|2003-06-26|Bsh Bosch Siemens Hausgeraete|Method for controlling the moisture content of the air in a domestic frost-free refrigerator/freezer has a selector switch to vary the switching of the fan and compressor|
    DE10228334B4|2002-06-25|2006-04-20|BSH Bosch und Siemens Hausgeräte GmbH|Refrigerating appliance with switchable heat source|
    DE10235781A1|2002-08-05|2004-03-04|BSH Bosch und Siemens Hausgeräte GmbH|The refrigerator|
    DE10326329A1|2003-06-11|2004-12-30|BSH Bosch und Siemens Hausgeräte GmbH|Refrigeration device with controlled dehumidification|
    US6763677B1|2003-10-20|2004-07-20|Carrier Corporation|Fresh air vent position monitoring system|
    JP4052319B2|2005-05-24|2008-02-27|ダイキン工業株式会社|Air conditioning system|
    JP3988780B2|2005-09-09|2007-10-10|ダイキン工業株式会社|Refrigeration equipment|
    CN100445658C|2005-12-19|2008-12-24|上海约顿机房设备有限公司|Air conditioner for accurately control temperature and humidity|
    US8757506B2|2007-01-03|2014-06-24|Trane International Inc.|PTAC dehumidification without reheat and without a humidistat|
    ITVA20070020A1|2007-02-16|2008-08-17|Whirlpool Co|METHOD TO ADJUST HUMIDITY WITHIN A REFRIGERATOR AND REFRIGERATOR SUITABLE FOR THE IMPLEMENTATION OF THIS METHOD|
    CN101294733A|2007-04-25|2008-10-29|东元电机股份有限公司|Air conditioner and method thereof|
    DE102008051748B4|2008-10-15|2019-09-19|Liebherr-Hausgeräte Lienz Gmbh|Method for dehumidifying the air in the interior of a device|JP5110192B1|2011-06-10|2012-12-26|ダイキン工業株式会社|Refrigeration equipment|
    WO2013007627A1|2011-07-12|2013-01-17|A.P. Møller - Mærsk A/S|Humidity control in a refrigerated transport container with an intermittently operated compressor|
    US20130014522A1|2011-07-12|2013-01-17|A.P. Moller - Maersk A/S|Humidity control in a refrigerated transport container with an intermittently operated compressor|
    EP2546084A1|2011-07-12|2013-01-16|A.P. Møller - Mærsk A/S|Humidity control in a refrigerated transport container with an intermittently operated compressor|
    CN102338443B|2011-08-31|2013-09-11|奇瑞汽车股份有限公司|Device for preventing evaporator of automobile air conditioner from being mildewed and control method thereof|
    US20150338135A1|2012-11-22|2015-11-26|Daikin Industries, Ltd.|Refrigeration device for container|
    CN105526770B|2014-09-29|2020-04-24|青岛海尔智能技术研发有限公司|Control method of multifunctional chamber in refrigerator and refrigerator|
    KR20160116776A|2015-03-31|2016-10-10|엘지이노텍 주식회사|Dehumidifier|
    FI20160068A|2016-03-21|2017-09-22|Juha Virtanen|Measurement and control procedure with which condensation that occurs on a surface is prevented|
    US10295216B2|2016-03-23|2019-05-21|Defang Yuan|Modular assembly for regulating moisture and temperature of content in a container|
    US10837686B2|2016-03-24|2020-11-17|Lg Electronics Inc.|Control method for refrigerator|
    DE102016220163A1|2016-10-14|2018-04-19|BSH Hausgeräte GmbH|Refrigeration unit with dehydrating function and operating method for it|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DKPA200900944A|DK177003B1|2009-08-20|2009-08-20|Dehumidifier|
    DK200900944|2009-08-20|
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