EP2234727A1 - Système de régulation de broyeur et procédé pour faire fonctionner un broyeur - Google Patents

Système de régulation de broyeur et procédé pour faire fonctionner un broyeur

Info

Publication number
EP2234727A1
EP2234727A1 EP08868833A EP08868833A EP2234727A1 EP 2234727 A1 EP2234727 A1 EP 2234727A1 EP 08868833 A EP08868833 A EP 08868833A EP 08868833 A EP08868833 A EP 08868833A EP 2234727 A1 EP2234727 A1 EP 2234727A1
Authority
EP
European Patent Office
Prior art keywords
mill
control device
fuzzy
grinding
control system
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.)
Withdrawn
Application number
EP08868833A
Other languages
German (de)
English (en)
Inventor
Dietmar Gocht
Werner Bischoff
Thomas Krause
Alfred Gwosdz
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.)
Steag GmbH
Mitsubishi Power Europe GmbH
Original Assignee
Hitachi Power Europe GmbH
Evonik Energy Services 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 Hitachi Power Europe GmbH, Evonik Energy Services GmbH filed Critical Hitachi Power Europe GmbH
Publication of EP2234727A1 publication Critical patent/EP2234727A1/fr
Withdrawn legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
    • B02C15/04—Mills with pressed pendularly-mounted rollers, e.g. spring pressed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
    • B02C15/007—Mills with rollers pressed against a rotary horizontal disc
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C25/00—Control arrangements specially adapted for crushing or disintegrating

Definitions

  • the invention is directed to a mill control system, in particular a roller mill, comprising: a mill control device which is configured to regulate at least one mill parameter based on an associated desired size, and a fuzzy control device which is connected to the mill control device and which is arranged Setpoint size of the at least one mill parameter to be controlled in case of deviation of at least one mill operating parameter from a predefined normal range as a function of fuzzy rules based on this at least one mill operating parameter until the at least one mill operating parameter has again reached the predefined normal range. It is further directed to a mill with such a mill control system and the use of the mill and a method for operating a mill, in particular roller mill.
  • Roller mills have a rotating grinding table and a plurality of rolling elements, which are pressed against the grinding table, for example via hydraulic cylinders.
  • the millbase is placed centrally on the rotating grinding table and moved by the centrifugal forces acting between the turntable and rolling elements through to Mahltellerau inforand. There it is blown up by a separat Kunststoffström or Tragluftstrom and transported to a sifter. Coarse particles are retained in the sifter and returned to the grinding table, fine particles leave the mill or sifter with the prepare slaughter.
  • Mahlgut Mrs grinding bed
  • a mill control device 11 which includes a mill load control unit IIa, a classifying air flow control unit IIb, a classifying temperature control unit 11c, a grinding pressure control unit 11a.
  • Control unit Hd and a classifier speed control unit He includes.
  • the load controller IIa measures the mill load, for example in the form of the millbase mass flow supplied to a mill, compares the measured mill load with a mill load setpoint and then adjusts the allocator speed if necessary.
  • the classifying airflow control unit Hb measures the classifying airflow supplied to a mill 1, compares the measured classifying airflow with a classifying airflow target amount determined depending on the current mill load, and then switches the classifying air hot air regulating damper 15.
  • the classifier temperature control unit Hc measures the temperature of the air separator leaving a separator 7, compares the measured temperature with a temperature setpoint, which is determined as a function of the instantaneous mill load, and then switches the classifying air cold air regulating flap 17.
  • the grinding pressure regulating unit Hd measures the grinding pressure in the mill 1 the measured pressure with a grinding pressure target size, which is determined as a function of the instantaneous mill load, and then possibly changes the contact pressure of the rolling elements.
  • the air pressure difference is the pressure difference between mill inlet and outlet of the hot drying air flowing through the mill, including the entrained fine dried pulverized coal particles and the evaporated water from the coal (vapors). If the pressure difference is high, then the amount of hot air has a high dust load. If the difference is low, the air is less laden with dust.
  • the air pressure difference is also still dependent on the mill load.
  • the classifier speed control unit He measures the number of revolutions of the classifier 7, compares the measured number of revolutions with a classifier nominal rate of setpoint, which is determined as a function of the instantaneous mill load, and then changes the classifier speed if necessary.
  • mills tend to "rumble", i. to a very restless run with shocks. This may be due to changed or changing operating conditions, e.g. caused by a change to a regrind with other grinding properties and / or wear of the grinding tools (turntable and rolling elements) and / or a change in the Mahlgut21.
  • a change in the grinding bed thickness can be caused, which may lead to a Mühlenrumpeln.
  • DE 44 44 794 A1 discloses a mill control method in which the vibration level of the mill is detected continuously by means of a vibration pickup, wherein a long-term mean value and a short-term average value are formed from the detected values, by means of which a first fuzzy logic function calculates a degree of stability , and wherein a second fuzzy logic function calculates the setpoint of a control quantity based on the calculated degree of stability so as to achieve a desired degree of stability and to control the mill for optimal operation.
  • 44 44 794 Al only control interventions are possible with a method according to DE, which can be derived from a long-term average.
  • the invention has for its object to provide a solution that allows, even with changing
  • Mill operation in particular a "mill rumbling" avoiding mill operation to ensure.
  • the solution should also make it possible to facilitate the commissioning of a mill, in particular a roller mill.
  • the invention provides a mill control system according to claim 1, a mill according to claim 14, the use of a mill according to claim 17 and a method for
  • Mill control system, mill and method of the invention are described in the respective dependent claims. Due to the invention, it is possible to largely automate the mill with the help of the special fuzzy control and automated to ensure optimized mill operation. In particular, with the aid of the invention, the so-called "mill rumble" during mill operation can be avoided, whereby the air pressure difference across the mill represents the advantageous mill operating parameter which is kept within its predetermined standard range To avoid mill, since with this scheme, the adjusting mill bed grinding bed thickness regulate and influence on grinding material and can hold and set in a range in which no "mill rumble" occurs. Furthermore, the thickness of the Mahlgut für between the grinding rollers and the grinding plate (grinding bed thickness) can be measured and maintained as mill operating parameters in their predetermined normal range.
  • the mill control system comprises a mill control device, which regulates at least one mill parameter on the basis of an associated desired size, and an associated fuzzy control device, which supplements the mill control device.
  • the fuzzy control device may include the mill control device, but also be placed on this.
  • the fuzzy control device can thus be simply "placed" on an already existing mill control device, for example, so that existing mills can be retrofitted with the fuzzy control device to form the mill control system according to the invention.
  • the fuzzy control device is set up here, the setpoint size of the at least one mill parameter to be controlled if at least one deviation occurs Mill operating parameters of a predefined normal range as a function of fuzzy rules, which are based on this at least one mill operating parameters, to be adjusted until the at least one mill operating parameter has again reached the predefined normal range.
  • the mill control device is configured to control at least one mill parameter based on an associated target size.
  • the mill control device may be configured to control at least one of the mill parameters or one of the mill operating parameters air flow, sifter, sifter grain size, mill load, mill plate speed, grinding pressure, grinding bed thickness, or a combination of these or such mill characteristics.
  • the predefined norm (al) range of the at least one mill operating parameter is determined as a function of the mill load.
  • an absolute control variable is immediately available and not just a relative control variable, such as a comparison between a short-term average and a long-term mean according to DE 44 44 794 A1. It is also advantageous if the
  • Mill control device the at least one
  • Standard (al) state or standard (al) range deviating operating state of the mill adjusts itself.
  • the mill control device determines the associated nominal value of the at least one mill parameter to be controlled on the basis of another measured or recorded mill parameter, the other measured mill parameter being e.g. may be selected from the group consisting of the classifying air stream, the classifier temperature, the classifier grain size, the mill load, the grinding pressure, the air pressure difference across the mill, the grinding bed thickness, and a characteristic derived from one or more of these mill parameters and combinations thereof consists.
  • the mill control device the respective target size, in particular the view (er) air flow, the classifier, the separator grain size, the Mahltellerwindiere and / or the Mahldrucks determined depending on the mill load.
  • the fuzzy control device connected to or attached to the mill control device is set up to control the setpoint variable of the at least one mill parameter to be controlled in the event of a deviation from at least one
  • Mill operating parameters from a predefined standard range as a function of fuzzy rules, until the at least one mill operating parameter has again reached the predefined normal range. Subsequently, ie after the deviated mill operating parameter has returned to the predefined range, the mill control device preferably regulates the mill parameter without further intervention of the fuzzy control device on the basis of the newly set nominal value, ie the mill control device adopts the offset nominal value as a new nominal value. In other words, the setpoint is permanently or permanently adjusted by the fuzzy control device.
  • the fuzzy rules are based at least on the at least one mill operating parameter, optionally on several mill operating parameters.
  • the desired size of the at least one mill parameter to be controlled is adjusted or guided by the fuzzy control device on the basis of fuzzy rules and in dependence on the at least one mill operating parameter, i. the mill control device receives a nominal size guide from the fuzzy control device. It can be provided according to a further development of the invention that the desired value is adjusted successively and / or by a certain increment per unit of time. This takes place until the responsible fuzzy rule is no longer effective, i. until the at least one mill operating parameter has again reached the predefined normal range.
  • the fuzzy control device may comprise a control block which links at least one fuzzy input variable with at least one fuzzy output variable via the fuzzy rules.
  • the at least one fuzzy input includes the at least one mill operating parameter, and via the fuzzy output variable, the adjustment of the desired size of the at least one to be controlled mill parameter.
  • the at least one mill operating parameter comprises at least the air pressure difference across the mill.
  • the predefined normal range may e.g. be determined depending on the current mill load.
  • a predefined characteristic curve can be stored, which reproduces the profile of an air pressure difference standard value as a function of the mill load.
  • the standard range can then be determined with the given air pressure difference standard value given a specific mill load. It is also possible to change the predefined characteristic in dependence on certain other variables, in particular to shift or to increase / reduce the slope thereof. If the predefined normal range is determined as a function of the current mill load, it is possible to respond quickly and efficiently to changing grinding characteristics of the material to be ground.
  • the invention therefore further provides that the mill control device regulates the at least one mill parameter to be controlled based on a predetermined nominal value characteristic, wherein the fuzzy control device is set up to change, in particular to shift, the nominal value characteristic as a function of the fuzzy rules.
  • the at least one mill operating parameter in addition to the air pressure difference above the mill further comprise a further Mühlenkennlism and / or at least one Mahlgutkennatii and / or at least one characteristic of the mill downstream and their Mahlgut recycling plant.
  • the mill operating parameter in addition to the air pressure difference above the Further, the mill (s) air stream, sifter temperature, sifter grain size, mill load, grinding pressure, mill plate speed, mill electric power (mill power consumption), grinding bed thickness, at least one regrind milling property (grindability, water content , etc.), the storage volume (the amount / volume of millbase stored in the mill), or at least an exhaust gas concentration (eg, NO x emission) or an emission or flame pattern of a mill downstream burner, or a combination of or with these Sizes include.
  • the fuzzy rules are based on several mill operating parameters or on several fuzzy input variables, this can increase the performance of the fuzzy control device.
  • the target size of the at least one to be controlled mill parameter is adjusted as soon as one of the mill operating parameters deviates from its predefined normal range.
  • the setpoint variable of the at least one mill parameter to be controlled is adjusted only if several of the mill operating parameters deviate from their predefined standard range.
  • the at least one mill parameter to be controlled comprises the classifier separation grain size and / or the grinding pressure
  • the fuzzy control apparatus is set up, the nominal size of the separator grain size and / or the target size of the grinding pressure as a function from the air pressure difference across the mill and / or depending on the grinding bed thickness and at least one of the sizes - Mahldruck or - adjust classifier grain size.
  • the fuzzy control device is also set up to determine another mill parameter and / or a millbase characteristic as a function of at least one measured mill parameter on the basis of fuzzy rules, which the invention also provides.
  • a particularly expedient development of the invention further consists in that the fuzzy control device is set up, the grindability of the ground material and / or a
  • the mill control system according to the invention With the help of the mill control system according to the invention or the method according to the invention, it is possible to operate the mill always in its at least approximately optimal operating point or the mill when leaving the optimum operating point (eg due to a Mahlgutuncis or a change in Mahlgut whatsoever) in a new to regulate the optimum operating point.
  • the mill control system according to the invention a rumble of the mill due to varying coal qualities can be avoided, ie a quiet mill run can be ensured.
  • the running time of the mill or the mill components can be increased and the energy requirements of the mill can be reduced, since the mill always runs in its approximately optimal operating range / operating condition, and the range of application of the mill can be extended, since the mill, for example Grindings of varying millbase quality can be loaded.
  • the commissioning of a mill with the mill control system according to the invention can be substantially simplified because the mill is automatically adjusted by the mill control system to the optimum operating point, so that it may be possible to completely dispense with commissioning engineers.
  • the mill control system according to the invention can be used to detect, for example due to necessary readjustments, whether certain parts of the mill are subject to wear so far that they need to be replaced soon.
  • the mill can - if not optimal - possibly just continue to be operated conventionally.
  • the mill according to the invention comprises a mill control system according to the invention and may e.g. in a roller mill, in particular a roller mill, are used, the mill for cement production, but especially for the grinding of coal or cement, in particular cement clinker, can be designed.
  • the invention therefore also provides that the mill is used as a coal or cement mill.
  • the method according to the invention for operating a mill is characterized by the same combination of features according to the invention as the mill control system according to the invention, so that the same advantages as with the mill control system can be achieved therewith.
  • the method provides that the predefined standard (al) range of the at least one mill operating parameter is determined as a function of the mill load, it being expedient according to the invention that the desired value be successive and / or by a specific increment per unit of time is adjusted.
  • the at least one Mühlenkenniere is then regulated, preferably up to a new deviation from the normal range, based on the newly set target size.
  • FIG. 1 shows a flow chart of a conventional mill control system of a roller mill
  • FIG. 2 shows a flow chart of a mill control system according to the invention
  • FIG. 3 shows the system structure of a fuzzy controller which can be used in the mill control system according to FIG. 2
  • FIG. 4 shows the control block of a fuzzy controller of a mill control system according to FIG. 2 with a system structure according to FIG.
  • FIG. 5 shows the system structure of the fuzzy control device of the mill control system according to FIG. 2,
  • FIG. 6 shows the control block of the fuzzy control device according to FIG. 5
  • FIG. 7 and FIG. 8 show the behavior of the fuzzy control device according to FIGS. 5 and 6 with a deterioration of the coal quality
  • FIG. 9 shows an overview of influencing factors on the mill rumble
  • FIG. 10 shows an overview of the control task of the load change speed
  • FIG. 11 shows a control block for a fuzzy control device for determining the Hardgroveiere.
  • FIG. 2 shows a mill control system controlled by fuzzy controllers 13a and 13b, wherein identical elements to the conventional control system according to FIG. 1 are provided with the same reference numerals.
  • FIG. 2 shows a roller mill 1.
  • An allocator or mill feeder 5, z. B. formed as a trough chain conveyor, Plattenbandzuteiler or belt conveyor, promotes a regrind, in the present case coal as a fuel to be crushed, from a storage or bunker 3 in the mill 1.
  • the Mahlguteinspeisung takes place centrally on a rotating grinding table of the roller mill.
  • the roller mill is a roller mill.
  • the classifier 7 can be designed as a mill internal or external classifier. In the separator 7 coarse particles are retained and returned to the roller mill 1 and the grinding table. Fine particles leave the mill 1 or the classifier 7 with the classifying air stream and will not be downstream fed shown system. This can for example be a silo but also directly a burner of a coal dust-fired combustion chamber of a large power plant.
  • the mill control system comprises a mill control device 11 and a fuzzy control device 13.
  • the mill control device 11 is set up to regulate the following mill parameters on the basis of a respectively associated desired variable:
  • the mill control device 11 has a mill load control unit IIa, a classifying air flow control unit IIb, a classifier temperature control unit 11c, a grinding pressure control unit Hd, and a separator cutoff size control unit He.
  • the sifter cut size is set above the classifier speed.
  • Adjusting the classifier flap and / or baffles can be adjusted.
  • the classifying-air flow control unit Hb measures the classifying-air flow fed into the mill 1, compares the measured classifying-air flow with a nominal-flow of visual-flow current, which is determined as a function of the instantaneous mill load and thereupon switches on a classifying air hot air control flap 15.
  • the classifier temperature control unit 11c measures the temperature of the stream leaving the classifier 7 (classifying air stream and fine material), compares the measured temperature with a set temperature value
  • the grinding pressure control unit Hd measures the grinding pressure (or the grinding force), compares the measured pressure with a grinding pressure target size, which depends on the current mill load is determined, and then possibly changed the contact pressure of the rolling elements.
  • the classifier speed control unit He measures the number of revolutions of the classifier 7, compares the measured number of revolutions with a classifier speed reference value, which is determined as a function of the instantaneous mill load, and then changes the classifier speed if necessary.
  • the load regulator Ha measures the coal mass flow supplied to the mill, compares the measured mass flow with a desired mass flow target quantity and then adjusts the allocator speed, if necessary.
  • the mass flow setpoint can be determined or adjusted, for example, as a function of a characteristic of a plant downstream of the mill, for example as a function of the boiler load or steam quantity of a steam boiler device connected downstream of the mill.
  • the respective target size of the classifying air stream, the classifier temperature, the classifier speed and the grinding pressure determined as a function of the mill load, wherein the setpoints are stored in the form of setpoint characteristics / setpoint characteristic curves.
  • the fuzzy control device 13 has a first fuzzy control unit 13a and a second fuzzy control unit 13b.
  • the first fuzzy control unit 13a is connected to and communicates with the grinding pressure control unit Hd of the mill control device 11, and the second fuzzy control unit 13b is connected to and communicates with the classifier speed control unit He of the mill control device 11.
  • the first fuzzy control unit 13a is placed on the grinding pressure control unit Hd and the second fuzzy control unit 13b is mounted on the classifier speed control unit He, i. the control units Hd and He are supplemented by the respective associated fuzzy control unit 13a or 13b.
  • the first fuzzy control unit 13a is arranged to guide the grinding pressure target size, i. to adjust or adjust these depending on at least one mill operating parameter based on fuzzy rules.
  • the second fuzzy control unit 13b is set up to guide the classifier speed setpoint or the classifier cutoff size setpoint in dependence on at least one mill operating parameter.
  • mill operating parameters in addition to the air pressure difference across the mill, for example, one or more of the following parameters can be selected:
  • the fuzzy control device 13 is arranged to adjust the target size of the separator grain size and the target size of the grinding pressure respectively in response to the air pressure difference across the mill, the grinding pressure and the classifier speed, as indicated by the dashed lines is indicated in Figure 2.
  • the air pressure difference across the mill is defined as the pressure difference between mill inlet and mill exit / sifter exit of the hot drying air passing through the mill including the entrained fine dried carbon dust particles and the vaporized water from the coal (vapors). If the pressure difference is large, the drying air has a high dust load (i.e., the circulating fluid in the mill is high); if the pressure difference is low, the dust load is low (i.e., the circulating fluid in the mill is low). With the grinding pressure, the grinding material comminution and thus the dust load (the circulation of solids in the mill) can be influenced.
  • the fuzzy control device 13 is set up to change the respective setpoint characteristic based on the fuzzy rules, in particular to move.
  • FIG. 3 illustrating a demonstration example and serving to explain a fuzzy controller which can be used in a mill control system according to FIG.
  • the system structure describes the data flow in the fuzzy system.
  • Input interfaces fuzzify the input quantity (s).
  • the input variables here are, for example, the time change of the back pressure, the fuel mass flow, the electrical power of the mill, the classifier speed, the air pressure in front of the mill, and the water content of the millbase / coal selected from the mill drying calculation.
  • analog values are converted into degrees of membership.
  • the fuzzification is followed by the fuzzy inference.
  • one or more linguistically described output variables in this case grinding pressure and hardgrove number of coal
  • fuzzy rules fuzzy rules
  • control blocks see FIG.
  • FIG. 4 shows an example of a control block of the fuzzy controller with the system structure according to FIG
  • the behavior of the controller in the various process situations is determined by the control block.
  • the rule block contains rules for a fixed set of input and output quantities.
  • the "if" part of each rule describes the situation in which each rule is to apply or apply (in other words, the prerequisite (s) / premise (s)), the “then” part describes the regulator's response to the respective process situation (in other words the conclusion (s)).
  • DOS Degree of Support
  • the individual rules can be given a different weight.
  • the rules may be specified by the mill manufacturer, with the number of rules set as required.
  • the software program has corresponding input options.
  • a fuzzy controller provided with the system structure according to FIG. 3 and the control block according to FIG. 4 is set up in order to determine the grinding pressure and the hardgrove number of the coal depending on the above-mentioned input variables and, if desired, be used in the mill control system according to FIG.
  • Figure 5 shows the system structure of the fuzzy control device 13 of the mill control system of Figure 2 and Figure 6 shows the control block of the fuzzy control device 13 of Figure 5, wherein for the grinding pressure control and the classifier speed control alternatively separate control blocks can be formed.
  • the premises include the input quantities (the fuzzy input values correspond to or include the mill operating parameters) (IF %) - Air pressure difference across the mill dp_Luft_Mühle
  • the number of rules shown in Figure 6 is exemplary and can be easily changed, with the number shown as shown below, a substantial improvement in mill operation can be achieved. In particular, the operating parameter grinding bed thickness can additionally be taken into account.
  • the fuzzy control device 13 shown in FIGS. 5 and 6 is applicable to all roller mills, in particular roller mills, and any kind of milled material ground therein. An individual adaptation, with the exception of the predefined standard ranges of the fuzzy controller, is generally not required.
  • the fuzzy control device 13 sets the target size for the grinding pressure (and / or the target size for the separator grain size) by a certain increment per hour as the air pressure difference across the mill increases or deviates from the standard (al) range Time unit higher, resulting in a better grind and a lesser Griesschlauf be achieved until the responsible rule is no longer effective, ie the air pressure difference across the mill is back in the standard (al) range.
  • FIG. 9 shows a graphic overview for avoiding the mill rumble with the aid of a fuzzy control device 13 used according to the invention.
  • the cause of the rumble may be, in addition to an altered grinding stock quality, for example a too low carrying air quantity, resulting in an increase in the grinding bed thickness.
  • FIG. 9 illustrates, mill rumble can be avoided according to the invention in that a fuzzy control unit is placed on at least one (eg several) of the control units in order to control the nominal value of at least one of the mill parameters listed under "Remedy" by means of the fuzzy control unit.
  • FIG. 9 shows, by way of example, a fuzzy control device 13, each of which provides a set point control for the ground pressure control, the classifier speed control and the classifier temperature control.
  • the fuzzy control device 13 shown in FIG. 9 contains, in addition to the air pressure difference across the mill (not shown), precisely one further input variable, namely the degree of dryness of the ground material or of the coal. Alternatively, however, the fuzzy control device 13 shown in FIG.
  • the fuzzy control device 13 may also comprise further input variables, eg further millbase parameters and / or one of the mill parameters and / or further mill parameters and / or a parameter of a mill downstream of the mill and recycling the millbase , such as exhaust gas concentrations or emissions or the flame pattern of a downstream burner.
  • further input variables eg further millbase parameters and / or one of the mill parameters and / or further mill parameters and / or a parameter of a mill downstream of the mill and recycling the millbase , such as exhaust gas concentrations or emissions or the flame pattern of a downstream burner.
  • the fuzzy control device 13 can operate besides the measured values (such as Electricity consumption of the mill "electricity", allocator speed
  • Air pressure difference across the mill “dpL” and grinding pressure or grinding force "F Ma hi") also calculated by a mill module
  • FIG. 10 shows an overview of the control task of the load change speed and classifier temperature control.
  • the load change speed depends on the grinding bed thickness. It can be expected that fuzzy-stabilized control can predict the permissible load change rate.
  • the regulation aims at a certain level for the grinding pressure and the classifier speed via corresponding setpoint specifications, depending on the respective grinding properties of the fuel. These aforementioned values ultimately influence the grinding bed thickness and thus the Eintechnisch- or Aus notes the mill.
  • It is possible to formulate a further fuzzy block for the rate of load change in which this quantity is positively influenced by the set values grinding pressure and classifier speed.
  • the existing load change rate can be incorporated as a further measured value.
  • the corresponding fuzzy rules are extended accordingly by additional rules.
  • the fuzzy control device 13 can additionally be set up to determine a different mill parameter and / or a millbase characteristic as a function of at least one measured mill parameter.
  • the fuzzy control device 13 may be configured to determine the grind-mullability HGI depending on the grinding pressure, the air-pressure difference across the mill, and the classifier speed based on fuzzy rules. In other words, in order to determine the grindability HGI, it may be sufficient to follow the premises listed in FIG. 11 during operation of the mill, in order to derive the grindability therefrom.
  • the fuzzy control device 13 may be configured to determine the milling tool wear.
  • the mean time-related change in the grinding-roll piston height determined from measured values can be compared with the coal properties Hardgrove number and / or ash determined with a mill module or the fuzzy control device 13 in order to predict the course of wear on the basis of these variables.
  • the mill control is in all Wälzmühlenart and also any ground millable material, such as cement clinker, applicable.

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  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Disintegrating Or Milling (AREA)
  • Feedback Control In General (AREA)
  • Crushing And Grinding (AREA)

Abstract

L'invention concerne un système de régulation de broyeur, en particulier d'un broyeur à rouleaux, comprenant : un dispositif de régulation de broyeur (11), qui est conçu pour réguler au moins une caractéristique de broyage sur la base d'une variable de consigne associée; et un dispositif de régulation à logique floue (13), qui est relié au dispositif de régulation de broyeur (11) et qui est conçu pour, en cas d'écart d'au moins un paramètre de fonctionnement du broyeur par rapport à une plage normalisée prédéfinie, ajuster la variable de consigne de la ou des caractéristiques de broyage à réguler, en fonction de règles de logique floue qui se fondent sur ce ou ces paramètres de fonctionnement du broyeur, jusqu'à ce que le ou les paramètres de fonctionnement du broyeur soient revenus dans la plage normalisée prédéfinie. L'invention vise à fournir une solution permettant d'assurer de façon automatisée un fonctionnement optimisé du broyeur même en cas de fluctuations des conditions de fonctionnement, en particulier un fonctionnement évitant le = ronflement =. A cet effet, le ou les paramètres de fonctionnement du broyeur comprennent au moins la différence de pression d'air via le broyeur.
EP08868833A 2007-12-21 2008-12-06 Système de régulation de broyeur et procédé pour faire fonctionner un broyeur Withdrawn EP2234727A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102007062820A DE102007062820A1 (de) 2007-12-21 2007-12-21 Mühlenregelungssystem und Verfahren zum Betreiben einer Mühle
PCT/EP2008/010365 WO2009083096A1 (fr) 2007-12-21 2008-12-06 Système de régulation de broyeur et procédé pour faire fonctionner un broyeur

Publications (1)

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EP2234727A1 true EP2234727A1 (fr) 2010-10-06

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EP08868833A Withdrawn EP2234727A1 (fr) 2007-12-21 2008-12-06 Système de régulation de broyeur et procédé pour faire fonctionner un broyeur

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WO2009083096A8 (fr) 2009-08-27
JP2011506085A (ja) 2011-03-03
US8706287B2 (en) 2014-04-22
ZA201004318B (en) 2011-02-23
AU2008342359B2 (en) 2012-03-29
CA2710317A1 (fr) 2009-07-09
DE102007062820A1 (de) 2009-08-06
WO2009083096A1 (fr) 2009-07-09
AU2008342359A1 (en) 2009-07-09

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