EP4317878A1 - Procédé de commande d'une installation de séchage - Google Patents

Procédé de commande d'une installation de séchage Download PDF

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Publication number
EP4317878A1
EP4317878A1 EP23187769.7A EP23187769A EP4317878A1 EP 4317878 A1 EP4317878 A1 EP 4317878A1 EP 23187769 A EP23187769 A EP 23187769A EP 4317878 A1 EP4317878 A1 EP 4317878A1
Authority
EP
European Patent Office
Prior art keywords
dehumidifier
fan
performance
drying
power
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.)
Pending
Application number
EP23187769.7A
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German (de)
English (en)
Inventor
Johannes LANDRICHINGER
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
J+w Liegenschaftsverwaltungs GmbH
Original Assignee
J+w Liegenschaftsverwaltungs GmbH
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 J+w Liegenschaftsverwaltungs GmbH filed Critical J+w Liegenschaftsverwaltungs GmbH
Publication of EP4317878A1 publication Critical patent/EP4317878A1/fr
Pending legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/06—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
    • F26B21/022—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure with provisions for changing the drying gas flow pattern, e.g. by reversing gas flow, by moving the materials or objects through subsequent compartments, at least two of which have a different direction of gas flow
    • F26B21/028—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure with provisions for changing the drying gas flow pattern, e.g. by reversing gas flow, by moving the materials or objects through subsequent compartments, at least two of which have a different direction of gas flow by air valves, movable baffles or nozzle arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
    • F26B21/04—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06—Controlling, e.g. regulating, parameters of gas supply
    • F26B21/08—Humidity
    • F26B21/086—Humidity by condensing the moisture in the drying medium, which may be recycled, e.g. using a heat pump cycle
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06—Controlling, e.g. regulating, parameters of gas supply
    • F26B21/12—Velocity of flow; Quantity of flow, e.g. by varying fan speed, by modifying cross flow area
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/06—Chambers, containers, or receptacles
    • F26B25/08—Parts thereof
    • F26B25/10—Floors, roofs, or bottoms; False bottoms
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B9/00—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
    • F26B9/02—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in buildings
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
    • F26B2200/02—Biomass, e.g. waste vegetative matter, straw

Definitions

  • the invention relates to a method for controlling a drying system, in which an air flow generated by a fan and dried by a dehumidifier dries items to be dried in a drying room, with a dehumidifier control controlling the operation of the dehumidifier influenced by the air flow through the dehumidifier, so that operation in a predetermined and work area remains.
  • Drying material in the form of biomass such as wood chips or plant fibers, e.g. hay or straw
  • a drying room such as a hay box in a barn
  • the air flowing through the material to be dried can absorb moisture from the material to be dried until a sufficient degree of drying is achieved.
  • Drying systems for drying items to be dried usually have a fan to generate an air flow and an air dehumidifier to dehumidify the air flow. Drying with a dehumidifier can require a high connected load from the drying operation, for example an agricultural operation. If this connection power is not available, there is a risk of the company's power supply being overloaded.
  • a system control system detects a system performance, which includes at least the performance of the fan and the dehumidifier, and controls the performance of the fan - and thus indirectly the dehumidifier performance via the air flow - in such a way that that the system output remains below a predetermined maximum output during the drying process of the items to be dried.
  • the invention is based on the idea that in order to achieve effective drying operation it is necessary to coordinate the performance of the fan and the dehumidifier.
  • the dehumidifier should work at an effective, especially at an optimal operating point, and this depends on the amount of air that flows through the dehumidifier, i.e. on the fan performance.
  • a one-sided determination of the performance of the dehumidifier leads away from such an operating point, so that the effectiveness of the drying is unfavorably influenced.
  • An operation of the dehumidifier that is adapted to the current air flow can be achieved if the dehumidifier regulates its operation using its own dehumidifier control, so that this regulation - at least in terms of control technology - is expediently independent of a control or regulation of the fan.
  • the performance control of the dehumidifier can be carried out using an internal dehumidifier parameter, such as a temperature or the coolant pressure, advantageously in the low pressure side of the dehumidifier coolant circuit.
  • the parameter, such as the pressure can be used as a control variable to regulate the performance of the dehumidifier and is, for example, kept at a constant value or a value dependent on another parameter.
  • the pressure of the coolant in the low-pressure side depends on the energy transfer of the warm air flowing through the evaporator to the coolant. If the carryover is low, for example because the air flow is low or the air is cold, the coolant temperature may remain below the evaporation temperature of the coolant, which remains very cold and at low pressure. If the process value of the pressure is too low, there is a risk of the cooling register or the evaporator icing up. To reliably avoid this, the coolant pressure should be kept above a lower limit. However, if the coolant in the evaporator warms up significantly, it may not cool the air below its dew point, so that no water is excreted from the air and dehumidification comes to a standstill.
  • the coolant pressure is too high.
  • the operation of the dehumidifier can thus be maintained in an optimal working range of the dehumidifier, in which the air is expediently cooled to just below its dew point and reliably kept in a predetermined position above the freezing point of water.
  • the fan and the dehumidifier can both be controlled, in particular regulated, based on parameters that are independent of one another.
  • the system performance can be used as a control variable, in particular as a controlled variable.
  • An internal dehumidifier parameter such as coolant pressure, can be used for the dehumidifier.
  • joint control of the system performance can be achieved by linking the drying air routed through both devices.
  • a dehumidifier - and also a fan - is usually controlled via a frequency converter, so that, strictly speaking, there is frequency control and not power control.
  • frequency control should also include frequency or speed control or control based on an electrical quantity, such as current and/or voltage.
  • the system control is expediently superior to the dehumidifier control and can, for example, switch the dehumidifier on and off, specify performance values or limits and/or adopt one or more parameters from the dehumidifier control.
  • the system control expediently controls the fan directly, for example via a frequency converter. If the fan performance and thus the air flow through the dehumidifier changes, the dehumidifier performance is also affected.
  • the dehumidifier performance can be controlled indirectly by directly controlling the fan performance.
  • the maximum power can be a maximum power that can be used, in particular electrical power, of the system. It is also possible for the maximum power to be a value that is set or results from the maximum power that can be used or another predetermined power value, for example based on a safety distance, a control variable or the like.
  • the fan can be a centrifugal compressor.
  • the air compressed by the fan can be completely or only partially passed through the breather. For example, some of the air can be led past the compressor via a bypass become.
  • the material to be dried is expediently hay or wood chips.
  • the drying room advantageously has a ventilation floor on which the material to be dried lies and through which the drying air can expediently flow from bottom to top.
  • the drying air can be conducted in a particularly closed circuit, for example from the fan into an air duct under the drying room, from there through the drying room and from there further into an air space and an air duct to the dehumidifier and back to the fan.
  • Fresh air operation is also possible, in which the air is sucked in from outside a building, expediently led through a roof duct for heating, from there through the dehumidifier to the fan or without dehumidification directly to the fan, from which it is blown into the air duct under the drying room , from there flows through the drying room and out of the building again.
  • the output of the fan is reduced while the control of the dehumidifier remains unchanged.
  • the control can remain simple and not susceptible to errors without moving the dehumidifier away from a control system that is aimed at the predetermined operating range.
  • the performance control of the dehumidifier has priority over the performance control of the fan, so that when a performance limit is reached, the fan is reduced or controlled and not the dehumidifier.
  • the limit value is predetermined and is expediently below the maximum power, so that if the limit value is exceeded, an increase in the system output is still possible, for example in order to be able to intervene in terms of control technology.
  • the performance of the system can be used as a control variable to control the fan performance.
  • a regulation is viewed as a special case of the more general control, so that every regulation can also be described as a control, but not the other way around.
  • the electrical current supplied to the system can be measured and the current system performance can be calculated from this. For example, the current flowing through a main power supply line of the system is determined and the current system performance is calculated from this. Alternatively or additionally, it is possible for the current performance of one or more devices in the system to be determined and an at least approximate system performance to be determined from this.
  • the drying specification can be a control or regulation of the fan power using a drying parameter, such as the humidity, temperature, a pressure and/or a pressure difference of the air used for drying, for example before and/or after the material to be dried.
  • the drying parameter or its control value can be changed compared to a power-unlimited drying in order to adapt the drying to the limited conditions.
  • Unlimited drying is not drying without any performance limitations. Drying only takes place with a fan power that is controlled according to the drying specification and is not influenced by the power limitation.
  • the ratio can be any relation between the two performance variables, for example which performance is higher, a quotient or another mathematical relationship.
  • the drying specification is a quantity of air per time, in particular a constant quantity of air per time.
  • the drying is controlled in such a way that the drying air is blown through the material to be dried with a predetermined air quantity progression over time, in particular with a constant air quantity per time.
  • the predetermined course can be determined in advance or dependent on a drying parameter, for example an air parameter.
  • the air volume can be measured using an air speed sensor and the measured value can be processed by the main control as a controlled variable in order to keep the air volume constant or in the desired course.
  • the items to be dried become drier, with the effect that air can flow through the items to be dried with less resistance. If the amount of air is to be kept constant, the performance of the fan can be gradually reduced over the course of the drying process, as there is ever lower flow resistance to overcome.
  • Drying can be particularly energy efficient if the drying specification is a quantity of air depending on a Moisture is.
  • Humidity can be used to control the flow of air volume over time.
  • the humidity of the air can be measured after it flows through the material to be dried, for example in the hay box above the hay.
  • the amount of air that the fan blows through the haystack is not necessarily kept constant, but its flow is expediently regulated variably.
  • the air it also makes sense for the air to flow more slowly through the items to be dried to allow more time for the water to be absorbed.
  • another parameter can also be used as a default parameter, which expediently reflects the air quantity. In this respect, it is sufficient if the drying specification is a parameter dependent on moisture.
  • the fan may make sense to initially operate the fan without the dehumidifier and to blow non-dehumidified air through the items to be dried. If the dehumidifier is then switched on, overloading the power supply should be avoided. For this purpose, it is advantageous if the fan is operated without the dehumidifier, especially at maximum output of the fan, then the output of the fan is reduced to a value at which the system output would be below the maximum output with the dehumidifier running at full load, and only then Dehumidifier is switched on. If it makes sense, a current peak when switching on the dehumidifier can also be taken into account. After switching on, the dehumidifier can be brought to full load so that its cooling register cools down quickly and dehumidification can begin quickly.
  • a future system performance is determined with the addition of a dehumidifier operation, in particular under full load, and if the calculated future system performance exceeds the maximum performance, the fan power is reduced, in particular before starting the dehumidifier.
  • the reduction can take place to the extent that a calculated future system performance is kept in a predetermined performance band even in the event of a known fluctuation in the dehumidifier performance.
  • the dehumidifier After starting the dehumidifier, it can independently adjust its performance so that its performance lies within a specified working range. This can be determined by a pressure range or by another dehumidifier parameter. If the power set in this way is the full load of the dehumidifier, the fan can continue to be operated with reduced power, in particular constantly reduced power.
  • the dehumidifier's operating point may be below full load and the dehumidifier will therefore adjust its performance to a completely below full load operating range. It is then possible for the fan to increase its performance until the system output is within a specified performance range. Increasing the fan power can be done while reducing the power of the dehumidifier or after starting work in the work area. For example, the system control receives a signal from the dehumidifier control that the working area has been reached.
  • the fan performance is expediently changed with a gradient adapted to the dehumidifier operation, i.e. raised or lowered.
  • the change in performance can occur continuously, which can also be understood as a quasi-continuous change in many steps.
  • Another possibility of not allowing the system output to exceed the maximum output when starting the dehumidifier is to determine an operating point of the fan using a drying parameter before starting the dehumidifier, at which the system output does not exceed the maximum output even when the dehumidifier is switched on.
  • Future system performance can take into account one or more drying parameters, such as temperature, humidity and/or pressure of the drying air.
  • the fan power is increased when the dehumidifier power drops and the system power is kept in a predetermined power band. If the performance of the fan has to be reduced below the maximum performance due to the limitation of the system performance, the dehumidifier can independently adapt its performance to the reduced air volume and - depending on the current operating point - possibly also reduce its performance. This means that more power is available to the system again. Since the dehumidifier will slowly reduce its performance during the independent adjustment, it is advantageous if the released power is used early on to increase the fan performance slightly again. An excessive drop in the dehumidifier performance can be avoided, which can counteract undesirable fluctuations in the performance of the system.
  • the dehumidifier performance may increase, forcing the system control to reduce the fan performance.
  • it is advisable to take into account the performance gradient of the dehumidifier when controlling the fan performance i.e. how quickly the performance of the dehumidifier changes. The higher the performance gradient, the sooner or more strongly the fan performance should be changed, i.e. reduced or increased. This can also counteract undesirable fluctuations in system performance.
  • the performance of the dehumidifier may fluctuate somewhat until it has settled into its working range.
  • the system output is kept at a distance from the maximum output by controlling the fan output.
  • the system performance can then be brought closer and closer to maximum performance as the drying process progresses.
  • the target point of the system performance or fan performance is brought up to the maximum performance during the drying process.
  • a temporal fluctuation in the system performance is determined and, for example, processed into a fluctuation value.
  • the fan performance is adjusted depending on the fluctuation. For example, a power gradient of the fan is set depending on the fluctuation.
  • a past, current or predicted fluctuation in system performance can be a criterion. For example, it is advantageous if the system output is brought towards maximum performance depending on the fluctuation in the system output.
  • the current operating point of the dehumidifier can be read from the process value of the controlled variable of the dehumidifier, i.e. the current value of the controlled variable, which can deviate from the setpoint of the controlled variable. For example, it can be determined whether the dehumidifier is working in the intended work area or at which point inside or outside the work area it is located. If a fan power reduction is necessary, this can be made dependent on the current operating point and therefore on the process value of the dehumidifier's controlled variable in order to keep the drying process as close as possible to its optimum.
  • control of the fan can be dependent on a signal from the dehumidifier control, for example that the dehumidifier has reached its predetermined working area, or more generally: what position the process value has relative to the working area. From this, the future power consumption of the dehumidifier can be estimated.
  • the fan can be controlled depending on a drying parameter, for example the humidity of the drying air after the material to be dried flows through and/or a pressure difference in the air before and after the material to be dried.
  • a drying parameter for example the humidity of the drying air after the material to be dried flows through and/or a pressure difference in the air before and after the material to be dried.
  • a control can be stored in a drying specification in the system control.
  • a target value for the fan power can be determined from the specification, i.e. a target power according to a drying specification. Stands for this one If there is not enough power available due to the limitation to the maximum power, the target power of the fan will be a limited target power.
  • a relation between the target power according to a drying specification and the limited target power can be used to control the fan.
  • An advantageous use of this relationship is to switch from circulating air drying to fresh air drying.
  • the switchover depends on a switchover value from circulating air drying to fresh air drying, for example an outside temperature, a temperature difference between outside and inside and/or an air humidity inside.
  • “earlier” can be the change of the switching value in the direction of a current actual value of the parameter of the switching value.
  • the invention is also directed to a drying system with a fan, a dehumidifier, a drying chamber and a system control.
  • the system control is prepared to carry out a control method as described above.
  • FIG 1 shows a drying building 2 in a sectional view, so that a drying room 4 becomes visible in which drying material 6 is stored.
  • the drying building 2 can be a barn, the drying room 4 one of several hay boxes and the drying material 6 hay.
  • a drying system 8 housed with a fan 10 and a dehumidifier 12.
  • the drying system 8 includes a system control 14 for controlling the drying system 8 and a dehumidifier control 16 for controlling the dehumidifier 12.
  • FIG 2 the drying system 8 with the system control 14 and the dehumidifier control 16 is shown schematically.
  • the controller 14 controls the fan 10 and the controller 16 controls the dehumidifier 12 via a frequency converter 18, 20, which converts the control commands of its controller 14 and 16 into electrical voltages for operating the fan 10 and the dehumidifier 12, respectively.
  • the frequency converter 18 feeds the fan motor of the fan 10 and the frequency converter 20 feeds the motor of the compressor 22 of the dehumidifier 12.
  • the dehumidifier 12 has a cooling register 24 and a heating register 26, also called an evaporator or condenser, in which the drying air 28 is cooled or . is heated.
  • the drying line 28 is sucked by the fan 10 through both registers 24, 26, compressed in the radial compressor of the fan 10 and blown into the drying room 4, as in FIG 1 is shown.
  • the drying air 28 is blown through the material to be dried 6 from below by the fan 10.
  • the drying room 4 is equipped with a grid floor 30, which is in FIG 1 is indicated by dots on which the material to be dried 6 is stored.
  • a channel 34 from the fan 10 leads into the area 32 under the grid floor 30, so that the drying air 28 can be blown into the area 32 through the channel 34.
  • the drying air 28 is blown through the material to be dried 6 and absorbs moisture from it, so that it emerges wet again at the top of the material to be dried 6, as in FIG 1 is shown.
  • the drying air 28 is led back to the fan 10 in a circuit, as in FIG 1 is shown by the solid arrows. It passes through an opening in a wall, behind which the dehumidifier 12 is located, and is sucked back to the fan 10 through its two registers 24, 26 and, for example, an opening in the floor.
  • the drying air 28 is sucked in from outside, as in FIG 1 is shown by the dashed arrows. It is guided along a roof channel 36 under the roof 38 and absorbs solar heat from the roof 38.
  • Warmed up in this way it enters a collecting channel 40 and from there is passed through a closable air barrier 42, for example a slatted blind, as in FIG 1 is shown, sucked to the fan 10.
  • the warm drying air 28 is blown under the material to be dried 6, flows through it and absorbs moisture and then reaches the space above the material to be dried 6. From there it is blown out of the drying building 2 through a window 44.
  • the dehumidifier 12 can remain out of operation.
  • recirculation or fresh air mode is automatically selected by the system control 14, which uses data from sensors 46 ( FIG 2 ) receives, such as temperature and / or humidity of the drying air 28 and / or outside air.
  • a switch is made between recirculated air and fresh air mode.
  • the drying air 28 can be guided through the dehumidifier 12 or past it via the air barrier 42.
  • the fan 10 and the dehumidifier 12 are operated, which places a high load on the electrical energy supply of the company, part of which is the drying building 2 is, can lead.
  • the system control 14 detects a system performance that includes at least the performance of the fan 10 and the dehumidifier 12.
  • the drying system 8 is equipped, for example, with a sensor 50 ( FIG 2 ), which records the current flow of the main electrical supply line 52 to the drying system 8 and possibly to other systems 54, which are in FIG 2 are only indicated, for example a milking system, a heating system, a hay crane and/or a feeding system in a stable.
  • the maximum power or the maximum current that is allowed to flow through the main supply line 52 is known and stored in the system control 14. This performance should not be exceeded during drying operation.
  • the system control 14 throttles the power of the fan 10 if necessary so that the system power remains below the predetermined maximum power or the maximum power is not exceeded.
  • the dehumidifier control 16 is independent of this performance limitation, ie it does not control the performance of the compressor 22 based on the system performance or any other performance external to the dehumidifier.
  • the dehumidifier control 16 detects a coolant pressure 56 of the coolant in the low-pressure side of the coolant circuit of the dehumidifier 12. If this rises above an upper limit value, the dehumidifier control 16 increases the performance of the compressor 22 - if it is not already running at full load - and reduces it when the coolant pressure falls below a lower limit. By maintaining the process value of the coolant pressure between the two limit values, the operating point of the dehumidifier is maintained within a predetermined operating range.
  • this pressure regulation of the dehumidifier 12 is independent of the control of the fan 10.
  • the heat input of the air into the cooling register 24 also changes, for example the temperature of the coolant drops and therefore, under certain circumstances, also their pressure. If this drops below the lower limit, the dehumidifier control 16 reduces the performance of the compressor 22.
  • an increase in the amount of air flowing through the dehumidifier can increase the heat input into the cooling register 24, so that the coolant pressure rises above the upper limit and the compressor 22 thereby becomes Performance increased. In this way, the performance of the dehumidifier 12 can be dependent on the performance of the fan 10 - even if not in terms of control technology, at least physically - due to the amount of air conveyed by the fan 10.
  • the fan 10 When starting a drying process, the fan 10 is usually first switched on in order to ventilate the material 6 to be dried. A similar situation occurs when switching from a fresh air mode without dehumidification to a recirculation mode with dehumidification and the fan 10 runs without the dehumidifier 12.
  • the temperature and humidity of the drying air 28 emerging from the material to be dried 6 can be measured, and the drying process can be adapted to the measured conditions. For example, a decision is made as to whether the dehumidifier 12 is needed or whether the air is already sufficiently dry. When starting drying, it may make sense to use fresh air mode without a dehumidifier. If you choose recirculation mode with dehumidification, the dehumidifier 12 is switched on. Because the dehumidifier 12 usually requires more power than the fan 10 or any other unit the system 8, it may be that the available electrical power is not sufficient to be able to operate the dehumidifier 12 in an optimal manner, for example under full load.
  • the system control 14 records the current system performance and determines whether the maximum performance is exceeded when dehumidifier operation is added, for example under full load. If not, the dehumidifier 12 is switched on without affecting the fan control. If so, the system control 14 calculates a maximum possible fan performance for a predetermined dehumidifier operation and reduces the fan performance before it switches on the dehumidifier 12 and this begins the predetermined dehumidifier operation. The reduction takes place in such a way that the calculated future system performance remains within a predetermined performance band. Generally speaking, before the dehumidifier 12 is started, an operating point of the fan 10 can be determined at which the system output does not exceed the maximum output even when the dehumidifier 12 is switched on.
  • the operating point of the fan 10 can be set in various ways. It can be set depending on a drying specification and/or a drying parameter, for example a temperature and/or a pressure or a pressure difference. It is also possible to set the operating point depending on a future dehumidifier performance, which does not have to be the full load operation of the dehumidifier 12 but can be. For example, if only a low maximum power is available, the fan power will initially be low when the dehumidifier 12 is at full load. Accordingly, the air flow through the dehumidifier 12 will be low and the dehumidifier 12 will be Reduce power quickly to avoid icing up. Now there is more power available for the fan 10, which can start up again. Accordingly, the dehumidifier 12 will increase its performance, which, if the maximum performance is exceeded, will result in the fan performance being throttled again, so that the entire system fluctuates.
  • a drying specification and/or a drying parameter for example a temperature and/or a pressure or a pressure difference.
  • a system operating point can be determined, for example iteratively, which contains the coordinated operating points of fan 10 or air quantity and dehumidifier 12. Drying parameters should be taken into account here, in particular a counter pressure or a pressure difference before and after the material to be dried 6 and/or air humidity. After determining the system operating point, the fan 10 can be brought to its operating point and the dehumidifier 12 is started, which finds its operating point independently due to the pressure control.
  • the power of the fan 10 can be controlled according to a drying specification.
  • the amount of air is measured and used as a control variable. It can be regulated to a constant value or made dependent on another parameter, such as the humidity of the drying air 28 after the material to be dried 6 has flowed through. If there is now not enough power available, the fan power limited by the maximum power is lower than the actual one Target power, i.e. the fan power according to the drying specification. If this is known, the drying process can be adapted to this reduced condition. For example, earlier on one Fresh air mode switched over to drying without the power limitation.
  • the operating points of the fan 10 and dehumidifier 12 are calculated by the system control 14 are, for example iteratively, and adapted to one another, of course depending on the maximum power of the system 8, and both units are brought to this operating point in particular simultaneously.
  • the two working points should be made dependent on one or more drying parameters and/or a drying specification.
  • the dehumidifier 12 cools the drying air below the dew point in order to eliminate moisture from the air. If the dew point is well above the freezing point of the water, a reduction in the air volume does not necessarily lead to icing up of the cooling register 24. A reduction in the fan output therefore does not have to result in a simultaneous reduction in the dehumidifier output in order to prevent icing. However, if the dew point is close to the freezing point and therefore the operating point of the dehumidifier 12 is below the dew point, the performance of the dehumidifier 12 should be reduced quickly when the amount of air is reduced in order to prevent icing. It is therefore expedient if, in the event of a reduction in fan power caused in particular by the limited maximum power, an intervention in the dehumidifier control is made dependent on the position of the current operating point of the dehumidifier 12.
  • the system control 14 can check whether the fan power would have to be increased in order to achieve drying according to a drying specification, for example when operating with intended air volume.
  • the operating point of the dehumidifier 12 can be recorded. Because if the dehumidifier 12 only runs at partial load, it may be that its performance increases when the Air volume also increases and the system output exceeds the maximum output. There are several options to prevent this: On the one hand, the two future operating points of fan 10 and dehumidifier 12 can be mathematically adjusted to one another before the fan performance is increased.
  • the fan output is then increased and the dehumidifier output adapts to the increased air volume in a pressure-controlled and independent manner. It is also possible for the system control 14 to move both units to their new operating points simultaneously. In general, the system control 14 should check whether further adjustment of the fan performance makes sense in order to better utilize the maximum performance.
  • the fan 10 - controlled by the system control 14 - increases its performance with a gradient adapted to the dehumidifier operation until the system performance is in a predetermined working range. If the dehumidifier 12 is already operating at or near full load, the fan can quickly increase its performance since there will be no significant increase in the dehumidifier performance that could swell the system. However, if the dehumidifier performance is further away from full load, the gradient should be smaller, i.e. the fan performance should increase more slowly so that the system can adapt and its system performance can slowly and without fluctuations approach the maximum performance. It is also possible here for the system control to control the performance of the fan 10 depending on a process value of the controlled variable of the dehumidifier 12.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Drying Of Solid Materials (AREA)
EP23187769.7A 2022-08-02 2023-07-26 Procédé de commande d'une installation de séchage Pending EP4317878A1 (fr)

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DE102022119368.3A DE102022119368A1 (de) 2022-08-02 2022-08-02 Verfahren zum Steuern einer Trocknungsanlage

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8959794B2 (en) * 2011-10-18 2015-02-24 Roderich W. Graeff Process and apparatus to control the airflow in dehumidifying dryers
EP2876396B1 (fr) 2013-11-22 2019-01-02 Heutrocknung SR GmbH Procédé de séchage de matières à sécher
EP3187807B1 (fr) * 2013-11-22 2020-04-15 Heutrocknung SR GmbH Dispositif de séchage de foin
DE102019116898A1 (de) * 2019-06-24 2020-12-24 Lasco Heutechnik Gmbh Trocknungssystem und Trocknungsverfahren
EP3757307A1 (fr) * 2019-06-24 2020-12-30 LASCO Heutechnik GmbH Dispositif et procédé de séchage

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5984666B2 (ja) 2010-03-09 2016-09-06 三菱電機株式会社 除湿機

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8959794B2 (en) * 2011-10-18 2015-02-24 Roderich W. Graeff Process and apparatus to control the airflow in dehumidifying dryers
EP2876396B1 (fr) 2013-11-22 2019-01-02 Heutrocknung SR GmbH Procédé de séchage de matières à sécher
EP3187807B1 (fr) * 2013-11-22 2020-04-15 Heutrocknung SR GmbH Dispositif de séchage de foin
DE102019116898A1 (de) * 2019-06-24 2020-12-24 Lasco Heutechnik Gmbh Trocknungssystem und Trocknungsverfahren
EP3757307A1 (fr) * 2019-06-24 2020-12-30 LASCO Heutechnik GmbH Dispositif et procédé de séchage

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