Method for operating an extruder

Claim 2

In a method for operating an extruder of an extruding system for producing profiled sections made from rubber and/or soft plastic mixtures with, relative to the extruder, a set-point Mooney viscosity (M) at a set-point operating point of the extruder with a corresponding set-point throughput value (q o ), a corresponding set-point extruder speed (n o ), and a set-point value for at least one operating variable measured at or in front of the extruder head, said method including measuring the value of at least one operating variable, and changing the speed of the extruder in the event of a deviation of the respective measured said at least one operating variable from the corresponding set-point value at predetermined time intervals; the improvement wherein said step of changing includes changing said extruder speed (n) in proportion to a proportionality factor (k) which is valid for the extruder and for the type of material mixtures to be processed in it and which has been previously determined by experimentation; and wherein said proportionality factor (k) is previously determined by: operating the extruder with various batches of the same type of material mixture to be processed, with the various batches having differing Mooney viscosities (M', M") above and/or below said set-point Mooney viscosity (M) and with the exruder speed being adjusted to a value (n') to provide said set-point throughput value (q o ) for the extruder with the respective various batches of different Mooney viscosity (M', M"); measuring said at least one operating variable at the adjusted speed (n'); and deriving said proportionality factor (k) from the quotient of the ratio of the difference between said adjusted speed (n') and said set-point speed (n o ) to said set-point speed (n o ), divided by the ratio of the difference between said measured value of said at least one operating variable at said adjusted speed (n') and the corresponding set-point value to said corresponding set-point value for the operating variable.

Claim 3

A method as defined in claim 1 wherein said predetermined time intervals are of from 2 to 30 seconds.

Claim 4

A method as defined in claim 2 wherein said predetermined time intervals are from 5 to 10 seconds.

Claim 5

A method as define in claim 1, wherein said step of varying the speed includes changing the speed by an amount corresponding to the product of the three following factors; said stored proportionality factor determined by experimentation for the particular extruder and for the type of material mixture to be processed in it; the set-point speed (n 0 ); and the difference formed between said measured value of an operating variable at a given time and the corresponding set-point value, divided by said corresponding set-point value.

Claim 6

A method as defined in claim 4 wherein said predetermined time intervals are of from 2 to 30 seconds.

Claim 7

A method as defined in claim 5 wherein said predetermined time intervals are from 5 to 10 seconds.

Claim 8

A method as defined in claim 1, wherein: said at least one operating variable which is measured for the respective Mooney viscosities (M', M") is the pressure (p) exerted upon the applicable material mixture; and said proportionality factor (k) is equal to (n'/n.sub.o -1)/(p/p.sub.o -1), wherein p o is the set-point pressure value for the extrusion process.

Claim 9

A method as defined in claim 1 wherein said extruder system is a multiple extruder system having a plurality of extruders connected to a common extruder head; and wherein said steps of method are carried out separately for each extruder of the system.

Claim 10

A method as defined in claim 1 wherein: said at least one operating variable which is measured for the respective Mooney viscosity (M', M") is the temperature (θ) of the material mixture; and wherein said proportionality factor (k) is equal to (n/n.sub.o -1)/(θ/θ.sub.o -1), where θ 0 is the set-point temperature value for the extrusion process.

Claim 11

A method as defined in claim 9 further comprising: identifying the material mixture to be processed before it is fed into the extruder; and feeding an identifying code to a computer system based on electronic data processing in which the set-point throughput (q o ), the set-point speed (n o ), the set-point pressure (p o ), the set-point temperature (θ o ) and the proportionality factor (k) for the repsective material mixture are stored.

Claim 12

A method as defined in claim 7 further comprising: identifying the material mixture to be process before it is fed into the extruder; and feeding an identifying code to a computer system based on electronic data processing in which the set-point throughput (q o ), the set-point speed (n o ), the set-point pressure (p o ), the set-point temperature (θ o ) and the proportionality factor (k) for the respective material mixture are stored.

Claim 13

A method as defined in claim 11, wherein said step of identifying the material mixture to be processed is effected by means of a material-composition reader.

Claim 14

In a method for operating an extruder of an extruding system for producing profiled sections made from rubber and/or soft plastic mixtures with, relative to the extruder, a set-point Mooney viscosity (M) at a set-point operating point of the extruder with a corresponding set-point point throughput value (q o ), a corresponding set-point extruder speed (n o ), and a set-point value for at least one operating variable measured at or in front of the extruder head, said method including measuring the value of at least one operating variable, and changing the speed of the extruder in the event of a deviation of the respective measured said at least one operating variable from the corresponding set-point value at predetermined time intervals; the improvement wherein said step of changing includes changing said extruder speed (n) in proportion to a proportionality factor (k) which is valid for the extruder and for the type of material mixture to be processed in it and which has been previously determined by experimentation; and wherein said proportionality factor (k) is previously determined by: operating the extruder with various batches of the same type of material mixture to be processed, with the various batches having differing Mooney viscosities (M', M") above and/or below said set-point Mooney viscosity (M) and with the extruder speed being adjusted to said set-point speed (n o ) for the extruder with the respective various batches of different Mooney viscosity (M', M"); measuring said at least one operating variable and the throughput (q) of the extruder at the set-point speed (n o ); and deriving said proportionality factor (k) from the product of (1) the set-point value of said at least one operating variable and (2) the quotient of the ratio of the different between said set-point throughput value (q o ) and said measured throughput value (q) to said measured throughput value (q), divided by the difference between said measured value of said at least one operating variable at said set-point speed (n o ) and the corresponding set-point value for the operating variable.

Claim 15

In a method for operating an extruder of an extruding system for producing profiled sections made from rubber and/or soft plastic mixtures with, relative to the extruder, a set-point Mooney viscosity (M) at a set-point operating point of the extruder with a corresponding set-point point throughput value (q o ), a corresponding set-point extruder speed (n o ), and a set-point value for at least one operating variable measured at or in front of the extruder head, said method including measuring the value of at least one operating variable, and changing the speed of the extruder in the event of a deviation of the respective measured said at least one operating variable from the corresponding set-point value at predetermined time intervals; the improvement wherein said step of changing includes changing said extruder speed (n) in proportion to a proportionality factor (k) which is valid for the extruder and for the type of material mixture to be processed in it and which has been previously determined by experimentation; and wherein said proportionality factor (k) is previously determined by: operating the extruder with various batches of the same type of material mixture to be processed, with the various batches having differing Mooney viscosities (M', M") above and/or below said set-point Mooney viscosity (M) and with the extruder speed being adjusted to said set-point speed (n o ) for the extruder with the respective various batches of different Mooney viscosity (M', M"); measuring said at least one operating variable and the throughput (q) of the extruder at the set-point speed (n o ); and deriving said proportionality factor (k) from the product of (1) the set-point value of said at least one operating variable and (2) the quotient of the ratio of the different between said set-point throughput value (q o ) and said measured throughput value (q) to said measured throughput value (q), divided by the difference between said measured value of said at least one operating variable at said set-point speed (n o ) and the corresponding set-point value for the operating variable.

Claim 16

A method as defined in claim 13, wherein: said at least one operating variable which is measured for the respective Mooney viscosity (M', M") is the pressure (p) exerted upon the applicable material mixture; and the proportionality factor (k) is equal to ##EQU2## where p o is the set-point pressure for the extrusion process.

Claim 17

A method as defined in claim 13: wherein said at least operating variable which is measured for the respective Mooney viscosities (M', M") is the temperature (θ) of the material mixture; and wherein said proportionality factor (k) is equal to ##EQU3## where θ o is the set-point temperature for the extrusion process.

Claim 18

A method as defined in claim 13 further comprising: identifying the material mixture to be processed before it is fed into the extruder and feeding an identifying code to a computer system based on electronic data processing in which the set-point throughput (q o ), the set-point speed (n o ), the set-point pressure (p o ), the set-point temperature (θ o ) and the proportionality factor (k) for the respective material mixture are stored.

Claim 19

A method as defined in claim 15 further comprising: identifying the material mixture to be processed before it is fed into the extruder and feeding an identifying code to a computer system based on electronic data processing in which set-point throughput (q o ), the set-point speed (n o ), the set-point pressure (p o ), the set-point temperature (θ o ) and the proprotionality factor (k) for the respective material mixture are stored.

Claim 20

A method as defined in claim 16, wherein said step of the identifying the material mixture to be processed is effected by means of a material-composition reader.

Claim 21

A method as defined in claim 18 wherein said predetermined time intervals are of from 2 to 30 seconds.

Claim 22

A method as defined in claim 19 wherein said predetermined time intervals are from 5 to 10 seconds.