EP3749501A1 - Method for operating an extruder, and extruder - Google Patents
Method for operating an extruder, and extruderInfo
- Publication number
- EP3749501A1 EP3749501A1 EP19701835.1A EP19701835A EP3749501A1 EP 3749501 A1 EP3749501 A1 EP 3749501A1 EP 19701835 A EP19701835 A EP 19701835A EP 3749501 A1 EP3749501 A1 EP 3749501A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- flow rate
- time
- recipe identifier
- throughput
- parameter
- 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- Withdrawn
Links
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/002—Methods
- B29B7/007—Methods for continuous mixing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
- B29B7/72—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
- B29B7/72—Measuring, controlling or regulating
- B29B7/728—Measuring data of the driving system, e.g. torque, speed, power, vibration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/7466—Combinations of similar mixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/7476—Systems, i.e. flow charts or diagrams; Plants
- B29B7/7495—Systems, i.e. flow charts or diagrams; Plants for mixing rubber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/269—Extrusion in non-steady condition, e.g. start-up or shut-down
- B29C48/2692—Material change
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/404—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders the screws having non-intermeshing parts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/49—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using two or more extruders to feed one die or nozzle
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/92295—Errors or malfunctioning, e.g. for quality control
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92323—Location or phase of measurement
- B29C2948/92485—Start-up, shut-down or parameter setting phase; Emergency shut-down; Material change; Test or laboratory equipment or studies
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
- B29C2948/926—Flow or feed rate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/9298—Start-up, shut-down or parameter setting phase; Emergency shut-down; Material change; Test or laboratory equipment or studies
Definitions
- the invention relates to a method for operating an extruder. According to a second aspect, the invention relates to an extruder.
- the invention relates to a method for producing automobile tires and components of automobile tires, for example treads, by means of an extruder.
- Extruders have a screw which travels in a cylinder to convey and thereby knead optionally extruded material, which is a rubber composition according to a preferred embodiment, and optionally to heat and finally discharge under pressure to a spray head.
- the snail wears out. This increases a gap between the outer edge of the screw and an inner surface of the cylinder in which the screw is running. Through this gap flows to be extruded material against a
- the throughput is that amount of extruded material that is released to the spray head during operation of the extruder.
- the procedure is that the screw is usually changed too early.
- the invention is based on the object to reduce disadvantages in the prior art.
- the invention solves the problem by a method for operating an extruder comprising a screw, comprising the steps of (a) detecting a recipe identifier associated with material to be extruded and at least one operating quantity indicative of a desired screw rotational frequency f, the screw, (b) time-dependent detection of a flow rate parameter, from which a throughput of the extruder, in particular per revolution of the screw can be concluded, (c) detecting an error time tp, to which the Extruder is no longer operable due to excessive wear, and (d) calculating a limiting flow rate parameter Mi (tp) from the flow rate parameter M, linking the Grenz thoroughly- Parame ters Mi (tp) with the recipe identifier R, (and optionally the Error time tp) and storing the limit flow rate parameter M, ( ⁇ r).
- the recipe identifier is understood as meaning, in particular, a date, for example a number, an amount of numbers or a vector, which codes the information necessary for processing a particular material. In particular, it is determined from the recipe identifier, which material is to be extruded and thus supplied to the extruder.
- the recipe identifier also encodes a product dimension.
- the recipe code also encodes an operating variable from which the desired screw rotational frequency of the screw can be determined.
- the operating variable is the desired screw rotational frequency itself.
- the operating variable may be the output of the extruder to be set, a nominal throughput in weight per unit of time, and / or a nominal production speed.
- the recipe code encodes a corresponding operating variable. In other words, it is sufficient that the recipe identifier
- the time-dependent detection of the throughput parameter is understood in particular to mean that the throughput parameter is recorded at least once per minute, preferably at least once per 10 seconds, preferably at least once per second. It is possible that the time-dependent detection is performed on the basis of an external signal, for example from a central control unit.
- the throughput indicates which mass of extruded material per unit time or per revolution of the screw is discharged from the extruder.
- time it is either the real time or one
- Machine time meant that increases with the real time in operation strictly monotonous. However, unlike the real time, the machine time may stall, for example, when the extruder is not operated or reset, for example after a screw change.
- the error time is preferably indicated in the machine time, for example in number of hours since the last change of the screw of the corresponding extruder.
- the error time is that time at which the extruder delivers extruded material that no longer meets the required quality of the product and / or to which the extruder no longer reaches a predetermined target production speed.
- this quality refers to whether the material is completely unvulcanized. It is possible, but not necessary, for the quality of the product to be described in objectively measurable parameters.
- the error time is that time at which a predetermined maximum temperature of the extruded material is at least locally exceeded. It is possible, but not necessary, for the temperature of the extruded material to be measured and for the time of failure thereby to be determined from this temperature, in particular by setting the time of exceeding the maximum temperature as the time of error.
- the screw rotation frequency After some wear, the screw rotation frequency must be increased to reach the target production speed. If a further increase in the screw rotational frequency is not possible because this would lead to too high a thermal load, the production speed drops below the target production speed. This is one possible criterion for assuming a too worn worm.
- the cutoff parameter is calculated from the throughput parameter, it is understood, in particular, that the cutoff parameter is set equal to the throughput parameter at a time that is within a DC wear interval around the fault time.
- the DC wear interval is a time interval in which it can be assumed that the wear of the worm has not changed significantly.
- the interval length of the DC wear interval is at most three months, in particular at most one month and / or at least one day.
- the threshold flow rate parameter is linked to the recipe identifier
- the corresponding data are stored so that when querying the threshold flow rate parameter is uniquely identifiable to which recipe identifier this belongs. It is convenient, but not necessary, for the error time t P to be linked to the limiting flow rate parameter and the recipe recognition.
- the limit flow rate parameter associated with the recipe identifier and, if applicable, the time of error forms an error record.
- Material processed within the equal wear interval at the time of error the flow rate parameter associated with the corresponding recipe identifier and a timestamp for inferring the error time, as an equivalent flow rate parameter Miq q ( tp) stored.
- this throughput parameter is linked to the error time tp itself, even if the material is not processed exactly at the error time.
- Material to be extruded which belongs to different prescription identifiers, may react differently to the wear of the extruder. It is commonly known heuristically that a particular material sensitive or insensitive to wear. If it is known that the material reacts insensitive to wear, it can be processed, although the previous material could no longer be processed.
- the new material with the new recipe identifier is processed only for the purpose of determining whether even with this material, the wear of the extruder is already so great that the required throughput can not be achieved with the specified quality.
- This data results in a collection of data that can be extracted in the form of a throughput map at which specific throughput the material having a particular recipe identifier can no longer be processed.
- the method preferably comprises the steps
- the detection of the throughput parameters at the time within the DC wear interval is based on the knowledge that the wear within of the DC wear interval only to a negligibly small extent. Each time the recipe is changed, it will give an indication of the influence that the viscosity in the other properties of the material with a given recipe identifier has on the throughput at an unknown but given wear. On the basis of this data, a conclusion can be drawn as to which wear is to be expected if the material is changed over with an already presumed recipe code. In particular, by the method steps mentioned above, a throughput parameter for a material with a first, current recipe identifier can be used to infer the expected throughput parameter through the material with a second, future recipe identifier.
- Throughput parameter for the material with the current recipe identifier at the current time of change of the throughput parameters for the material with the future recipe identifier at the current change time is obtained. In this way, an estimated flow rate parameter is obtained.
- a warning message is issued if the throughput parameter, which has been calculated in this way for the material with the future recipe, falls below a predetermined minimum throughput parameter associated with the recipe identifier.
- This minimum throughput parameter is preferably the limit flow rate parameter that is obtained when a time of error has been detected for the corresponding recipe identifier. If no error time has been detected, a predetermined estimated value which was estimated, for example, is preferably used as the minimum throughput parameter.
- the following steps are performed: (a) determining the closest time to which the throughput parameter with the current recipe identifier is equivalent Throughput parameter for the future recipe identifier exists, (b) determining a difference between the throughput parameters, (c) adding a wear progress value calculated from this difference to the throughput parameter of the current one
- the wear progress value is equal to the difference.
- this difference is multiplied by a correction value, which is calculated for example from the wear curves for the two recipe identifiers.
- the basis for this method is the assumption that the differences in the throughputs change little with increasing wear.
- warning message By issuing a warning message, it is understood, in particular, that a signal perceivable or imperceptible by humans is emitted, which encodes the circumstance that it is to be expected that the predefined quality will not be reached when the future material is extruded. It is possible that the warning message will be sent to a remote central computer, such as a computer that is in the hands of or serviced by a manufacturer or maintenance company of the extruder, so that the
- Delivery of a new snail can be triggered.
- the closest point in time is determined, to which for the Throughput parameter with the current recipe identifier an equivalent throughput parameter for the future recipe identifier exists, then the quotient of the throughput parameters is determined. This quotient becomes a
- the wear progress factor may be the quotient itself.
- the wear progress factor is multiplied by the flow rate parameter of the current recipe identifier to obtain a second estimated flow rate parameter. If the second estimated flow rate parameter is below the threshold flow rate parameter of the future material with the future recipe flag, the warning message is issued.
- Flow rate parameter does not necessarily mean that the first flow rate parameter must be calculated. It is just a simpler form of naming. It is also possible that the first and the second estimated flow rate parameters are calculated, and for the comparison with the
- Boundary flow rate parameter is used from both estimated flow rate parameters.
- the method comprises the steps (a) for at least one
- predetermined recipe identifier which may be referred to as a reference recipe, determining the throughput parameter as a function of time, in particular also throughput parameters when extruding materials and other recipe identifiers, and (b) calculating a defect time estimate to which the Minimal throughput parameters for the given recipe identifier would be less than the minimum throughput parameter associated with the recipe identifier, by extrapolating the throughput parameter versus time. It is favorable if the error time estimated value is output in the form of a message.
- the method comprises the step of obtaining fit parameters for a given set of recipes which are fitted according to the throughput parameter with a parameterized model function, whereby the extrapolation of the throughput parameter takes place on the basis of the model function with the fit parameters.
- the model function can be a linear function.
- the throughput parameter is described as a linear function versus time measured in operating hours.
- the model function contains terms of higher order, in particular those which depend on the quadratic or third power of the time.
- the method comprises the step of zeroing the time after replacement of the screw. It is possible to carry out said process only over the period over which a given screw is used. But it can be assumed with good reasons that the wear behavior of the screw is substantially the same, so from the wear behavior of a screw on the wear behavior of the following
- Snail can be closed.
- the invention also solves the problem by a method of operating an extruder having a screw, comprising the steps of: (a) detecting a recipe ID Ri associated with material to be extruded and at least one operating quantity indicative of a desired screw rotational frequency f , which is determinable of the screw to be preset in the extrusion, encodes (b) time-dependent
- the throughput parameters for the corresponding recipes are accordingly recorded in the procedure for the material with the second recipe identifier and stored in the equivalent enforcement characteristic field.
- the method preferably comprises the steps of (a) determining a recipe as reference recipe identifier and (b) determining the DC wear interval from the change times t Wk of the recipe reference recipe identifier.
- a recipe which is preferably the most commonly used recipe relative to which the enforcement parameters are referenced.
- the method comprises the steps of (a) detecting an error time point tp at which the extruder is no longer operable with the desired screw rotational frequency due to excessive wear (because otherwise the required quality of the product is no longer guaranteed), (b ) Determining the flow rate parameter Mi (tp) at a time t P in the equal wear interval l a , (c) determining the minimum flow rate parameter M n from this flow rate parameter M i ( ⁇ r), in particular by setting minimum flow rate equal Parameters Mi min and throughput parameters Mj (t P ).
- a throughput parameter is obtained which is known that the material with the associated recipe identifier can not be processed at the given wear.
- inventive method there is also a method for operating an extrusion line which has a first extruder, a second extruder and at least one third extruder, the method being carried out for the majority of the extruders, in particular for all extruders.
- an extruder is also provided with a cylinder, at least one screw running in the cylinder, and a control unit which is arranged to automatically carry out a method according to the invention.
- the control unit has a digital memory in which a program is stored, which encodes the method.
- control unit is provided with a
- Data network connected or connectable to send the throughput parameters or parameters calculated therefrom, in particular Fit parameters, to a spatially spaced central computer.
- the central computer may, for example, be located more than one kilometer away from the control unit nearest to it. This allows the manufacturer of the extruder or a
- an extrusion system with at least three extruders, each having at least one screw, as well as a control unit, which is set up for automatically performing an inventive
- Figure 1 shows an inventive extrusion system with inventive
- FIG. 2 shows a diagram in which the course of the throughput parameters for a plurality of recipe identifiers is plotted over time
- FIG. 3 shows a diagram similar to that according to FIG. 2, wherein the time over which a recipe is processed in each case is shorter than in the case of FIG. 2.
- FIG. 1 shows an extrusion system 10 according to the invention with a first extruder 12.1, a second extruder 12.2 and a third extruder 12.3.
- the first extruder has a first screw 14.1, which runs in a cylinder 16.1.
- a material supply 18.1 to be extruded material 20.1 is fed to the extruder 12.1.
- the extruder 12.1 has a drive 22.1 in the form of an electric motor for rotating the worm 14.1.
- a control unit 24.1 controls the drive 22.1 so that it causes a predetermined screw rotational frequency f.
- the control unit 24.1 can communicate with a central computer 26. It is possible that an intermediate computer 28 is used for this purpose.
- the control unit 24 comprises a digital memory in which a program is stored which, when working, causes the method described below to be executed.
- a recipe identifier R is detected by extruded material.
- the index i is a run index, which could also be referred to as a recipe index, as it numbers the different recipes.
- a recipe contains, for example, an indication of the constituents of the material 20.1 which is fed to the extruder 14.1.
- the recipe R also includes an indication of a desired screw rotational frequency fi. soii , which should be preset when extruding material 20.1.
- this desired screw rotational frequency f.sub.o.sub.ii refers to a predetermined throughput m, which relates to the amount of material which is discharged by the extruder 12.1 per revolution of the screw 14.1. From the throughput m and the screw rotational frequency f, it is thus possible to calculate a mass throughput which is measured in kilograms per unit of time and indicates how many kilograms of extruded material per unit of time is output by the extruder 12.1.
- the extruder 12.1 delivers the extruded material by means of a line 30.1 to a spray head 32.
- the other extruders of the extrusion system 10 in the present case, the extruder 12.2 and 12.3, via corresponding lines 30.2, 30.3 each extruded material to the spray head 32, where from the combined streams a profile 34 is injected.
- the profile 34 runs on a conveyor 36, for example a belt conveyor, for further processing.
- a scale 38 determines the weight of a portion of the profile 34 so that a line weight G, also called the meter weight, of the profile 34 can be determined. Since the proportion of the material coming from a specific extruder is known on the profile, from this information and the measured meter weight and a speed with which the profile 34 moves, the throughput in kilograms per unit time of all extruders can be determined. The speed at which the profile 34 moves is also measured, for example, by measuring a rotational speed of a roller over which the profile 34 rolls.
- the extruders 12.2 and 12.3 and any further existing extruders are each constructed the same, but it is also possible that they differ in their design. However, the essential characteristics of the extruders relevant to the invention are those described above.
- the respective control units 24 detect the respective worm rotational speed. f ,.
- the throughput in mass per unit time is given and according to a preferred embodiment is part of the recipe, can be calculated from the screw rotational frequency f, the throughput per screw revolution, namely as a quotient of throughput in weight or mass per unit time at the target throughput according to recipe.
- the nominal flow rate is given in mass or weight per minute. If it comes to wear, then the screw rotation frequency f, must be increased in order to achieve the desired throughput. This is usually done manually, but can also be done automatically.
- FIG. 2 shows schematically that the throughput parameter M decreases with the time t measured in operating hours.
- material with the recipe identifier Ri is first extruded. It can be seen that the target throughput is just under 500 grams per screw revolution.
- This recipe identifier is detected by the control unit 24, for example, by being entered by an operator via an operator interface. From the recipe identifier Ri, the control unit 24 determines the first to be selected screw rotational frequency - During the extrusion of the throughput parameter M in the form of mass penetration per screw revolution is detected continuously, for example once a second or once per 10 seconds.
- the respective current throughput parameter Mi (tw-i) is initially stored. Thereafter, the material according to a second recipe identifier R 2 is processed. At the beginning of processing, the throughput parameter M 2 (t Wi ) is determined. The same occurs at a time t W 2 when changing from the material with the second recipe identifier to the material with the third recipe identifier R 3 .
- the screw rotational frequency f 2 would have to be selected to be so high, In order to achieve the predetermined target throughput that would lead to excessive heating of the material to be extruded and local vulcanization.
- the flow rate parameter M is M 2 (t P ) at this time. It is stored as a limit flow rate parameter. For a later recurring processing of the material according to the recipe identifier R 2, it is then known that it must be ensured that the throughput parameter M 2 is always above this limit flow rate parameter M 2 min .
- FIG. 1 shows the case in which the materials are exchanged so rarely with respect to the corresponding recipe identifiers that the wear already clearly advances during the processing of only one material.
- different materials with different recipe identifications are changed so frequently that wear during processing of the material with a particular recipe identifier is small.
- This case is schematically indicated in the diagram according to FIG. It can be seen that during a DC wear interval l a, the wear decreases only so little that it can be regarded as constant. For this reason, in good approximation, the throughput parameters M 3, eq (tp), M 2 (tp), M 4, etc. q (tp) are considered to belong to the same wear condition as.
- the quotient of the throughput parameters is formed instead of the difference, in the present case this would be M 3 (t W n) / M 4 (t W n). If material with a recipe ID is used very often, it makes sense to regard this recipe ID as the reference recipe ID.
- FIG. 2 schematically shows the measuring points at which the throughput parameters are determined at least for the recipe with the recipe identifier R 2 . If a large number of these parameters exist, then the wear curve can be adapted with a model curve, which in the present case is shown with dashed lines. For example, as in the case shown in FIG. 2, it is a straight line. With sufficiently many measuring points, the parameters of the model function can be selected so that the model function is optimally adapted to the measured data. This curve fitting belongs to the prior art and will therefore not be described further.
- fit parameters are obtained which describe the time course of the throughput parameter M for the material with the recipe identifier R. As soon as these have been obtained, it is possible to determine from that time that the preset or determined minimum flow rate parameter Mi min would also be undershot. This value can be queried automatically or on a corresponding request from the user via the user interface of the respective control unit 24 or via the intermediate computer 28 or by the central computer 26.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
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Application Number | Priority Date | Filing Date | Title |
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DE102018102738.9A DE102018102738B4 (en) | 2018-02-07 | 2018-02-07 | Method of operating an extruder and extruder |
PCT/EP2019/051786 WO2019154631A1 (en) | 2018-02-07 | 2019-01-24 | Method for operating an extruder, and extruder |
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EP3749501A1 true EP3749501A1 (en) | 2020-12-16 |
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EP19701835.1A Withdrawn EP3749501A1 (en) | 2018-02-07 | 2019-01-24 | Method for operating an extruder, and extruder |
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US (1) | US20200361131A1 (en) |
EP (1) | EP3749501A1 (en) |
CN (1) | CN111670103B (en) |
DE (1) | DE102018102738B4 (en) |
TW (1) | TWI785181B (en) |
WO (1) | WO2019154631A1 (en) |
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DE102019127042A1 (en) * | 2019-10-08 | 2021-04-08 | Rehau Ag + Co | Method for monitoring wear and / or contamination phenomena in a plastic extrusion plant |
CN113459464A (en) * | 2021-07-16 | 2021-10-01 | 孟祥书 | Recycled plastic twins equipment |
CN114274483B (en) * | 2021-12-15 | 2024-06-14 | 青岛双星轮胎工业有限公司 | Method for preventing extrusion and mixing, electronic equipment and readable storage medium |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
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US4604251A (en) * | 1985-06-14 | 1986-08-05 | Kuhman Jeffrey A | Method and apparatus for indicating dimensional relationships in plastic material feeding device during operation |
JPS6283027A (en) * | 1985-10-07 | 1987-04-16 | Toyota Motor Corp | Apparatus for detecting abrasion of kneader |
JPH05309721A (en) * | 1992-05-06 | 1993-11-22 | Japan Steel Works Ltd:The | Method for detection of friction between extruder's screw and cylinder and its apparatus |
DE19736979C1 (en) * | 1997-08-25 | 1999-04-08 | Windmoeller & Hoelscher | Process for feeding plastic granulate into the inlet opening of a plastic extruder |
US6306319B1 (en) * | 1999-07-19 | 2001-10-23 | Chroma Corporation | Method of determining wear |
DE10048826B4 (en) * | 2000-09-29 | 2012-03-01 | Robert Bosch Gmbh | Method and device for detecting age-related changes in technical systems such as electric motors |
EP1507182A1 (en) * | 2003-08-14 | 2005-02-16 | Battenfeld Extrusionstechnik GmbH | Method for determining wear in extrusion machines |
DE102007021037B4 (en) * | 2007-05-04 | 2009-11-05 | Battenfeld Extrusionstechnik Gmbh | Method for detecting wear in extruder machines |
CN101863115B (en) * | 2010-05-18 | 2013-04-24 | 大连海事大学 | Molding control device of circular bar extruder and control method |
DE102016002967A1 (en) * | 2016-02-29 | 2017-08-31 | Reifenhäuser GmbH & Co. KG Maschinenfabrik | Extruder, plastic-forming plant or compounding plant and method for operating such a plant |
JP6517728B2 (en) * | 2016-05-12 | 2019-05-22 | ファナック株式会社 | Device and method for estimating wear amount of check valve of injection molding machine |
-
2018
- 2018-02-07 DE DE102018102738.9A patent/DE102018102738B4/en active Active
-
2019
- 2019-01-07 TW TW108100526A patent/TWI785181B/en active
- 2019-01-24 US US16/963,876 patent/US20200361131A1/en not_active Abandoned
- 2019-01-24 EP EP19701835.1A patent/EP3749501A1/en not_active Withdrawn
- 2019-01-24 WO PCT/EP2019/051786 patent/WO2019154631A1/en unknown
- 2019-01-24 CN CN201980010951.8A patent/CN111670103B/en active Active
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TW201934307A (en) | 2019-09-01 |
CN111670103B (en) | 2022-05-24 |
US20200361131A1 (en) | 2020-11-19 |
DE102018102738A1 (en) | 2019-08-08 |
DE102018102738B4 (en) | 2019-09-05 |
WO2019154631A1 (en) | 2019-08-15 |
CN111670103A (en) | 2020-09-15 |
TWI785181B (en) | 2022-12-01 |
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