METHOD AT THE MANUFACTURE OF MECHANICAL PULP

Description

[0001] This invention relates to a method of controlling the manufacture of mechanical pulp in a refining process where cellulose-containing material in lumps, such as wood chips, is refined. The chips prior to the refining can be treated with heat and/or chemicals for manufacturing TMP (thermomechanical pulp) or CTMP (chemi-thermomechanical pulp). The refining is carried out in one or several steps by single- or double-disc refiners. These refiners are provided with opposed refiner discs rotating relative one another. The discs are provided with disc segments comprising bars and intermediate grooves. Opposed disc segments form a gap where material is refined during its passage outward.

[0002] The properties of the manufactured pulp are influenced, besides by the quality of the wood chips, by a great number of system parameters. Among them can be mentioned the distance between the disc segments (gap), the load of the motor driving a rotary refiner disc, the pressure by which the refiner discs are pressed in the direction toward each other, the pressure at the feed-in of the chips, the pressure in the housing enclosing the discs, the supply of diluting water, the material flow through the refiner (the production), the material concentration. Some of these parameters are depending on each other while other are substantially independent. For example, the motor load increases and so does the pressure by which the discs are pressed toward each other when the gap decreases.

[0003] It is impossible in practice to check and control all parameters influencing the properties of the pulp. It was found, however, that a desired pulp quality can be achieved with pretty high precision by controlling some especially important parameters, viz. the gap size, the material concentration and the production.

[0004] A great problem is that the measuring of the system parameters does not yield a direct measure of the pulp properties. For being able to determine the properties of the pulp, such as tensile strength, tearing resistance, dewatering capacity, shives content, fibre length etc., it is, of course, necessary to analyze the pulp and the paper made thereof. In a mill it takes normally several hours to obtain the results of such analysis, and sampling usually is carried out not more than 2-3 times per day. It is, therefore, impossible to rapidly discover and compensate for such variations in the pulp properties which are due to system parameters, which have not been determined, or where there is no simple relation between the system parameter and the pulp properties.

[0005] One factor causing the relation between the measured system parameters and pulp properties to change in operation is the wear of the refiner disc segments. This implies that certain pulp properties can deteriorate although the measured system parameters remain unchanged. This implies in practice, that the system parameters must be adjusted on the basis of anaysis results of a pulp, which had been manufactured several hours earlier. This is, of course, a great disadvantage.

[0006] "Further according to US-A-4 627 578 there is used an accelerometer attached to one of the refiner discs in a refiner for predicting and/or preventing the clashing of the refiner discs. This accelerometer detects the decreases in vibrations of the refiner discs due to a reduction in the quantity of material flowing between the discs. Thus, the output of the accelerometer is converted to a voltage so that a decreased vibration causes a voltage decrease. However, while disc clashing according to this arrangement can be predicted and/or prevented it is not mentioned and it would not be possible to use this output signal for controlling the manufacture of pulp, determining the condition of the refining surfaces or evaluating and comparing different disc segments."

[0007] The delay in obtaining the analysis results involves substantial disadvantages also in connection with the testing of and comparison between different refiner disc segments. It is desired, therefore, to be able during the refining process to measure such system parameters, which render it possible to predict the pulp properties with greater accuracy than it has been heretofore possible.

[0008] The present invention offers a solution of this problem. The invention implies that the vibrations arising in the refiner discs during the refining are utilized for calculating the pulp properties. The characterizing features of the invention become apparent from the attached claims.

[0009] The invention is described in greater detail in the following, with reference to embodiments and test results shown in the accompanying drawing, in which

Figure 1 shows a frequency analysis of the measured vibrations,

Figures 2 and 3 show the agreement between measured and calculated tensile strength without and, respectively, with utilization of the vibrations in the refiner discs.

[0010] One property important for the quality of pulp is the tensile strength. This applies especially to mechanical pulp intended for papermaking.

[0011] By controlling and adjusting the three system parameters gap size, material concentration and production, it is possible with pretty good precision to maintain a desired pulp quality. Experiments carried out on mill scale, however, have shown that the pulp quality deteriorates with the time due to wear of the refiner discs, without the possibility of predicting this by control of the aforesaid system parameters.

[0012] By measuring the high-frequency vibrations arising in the refiner discs due to their relative rotation and their segment design, it is possible to calculate the vibration energy over the refiner disc segment. The frequency depending on the rotation speed of the discs and the design of the disc segments can amount to several thousands c.p.s. The measuring is carried out by means of an accelerometer attached to the disc, preferably to the rear side of a segment. In a single-disc refiner the accelerometer is attached on the stationary disc. It is also imaginable to attach accelerometers to both discs in a single- or double-disc refiner, in order to obtain additional information on the vibrations of the discs.

[0013] By including the vibration energy thus measured in the calculation of the pulp properties, it was found by surprise, that these properties can be predicted with much higher precision. This applies especially to the strength properties of the pulp (tensile strength). It was found possible, thus, to predict the reduction in tensile strength caused by wear of the disc segments.

[0014] This implies simultaneously that the vibration energy also can be utilized for determining the condition of the processing surfaces of the segments. The vibration energy, furthermore, can be utilized for comparing the efficiency of disc segments of different types.

Example

[0015] In a single-disc refiner an accelerometer was mounted in a hole drilled in the rear side of a disc segment in the stationary disc. The segments were designed with three zones comprising bars and grooves of different size.

[0016] The refining was carried out with pre-heated chips for the manufacture of TMP. The system parameters and pulp properties at two test runs were as follows:

[0017] The signal from the accelerometer was simultaneously measured and analysed. The frequency range in question was 5-25 kc/s. In Figure 1 a frequency analysis of this signal is shown. The signal can be divided into three different areas corresponding to the three zones of the segments. In the inner zone comprising the coarsest bars the frequencies 5.&_-11.2 kc/s were noted. In the central zone 11.2-17.6 kc/s, and in the outer zone comprising the finest bars 17.6-25 kc/s were noted. The vibration energy is represented by the surface beneath the frequency curve in Figure 1.

[0018] After 800 operation hours new measurements of the system parameters and pulp properties were carried out. It was then found, that most of the measured pulp properties agreed well with the pulp properties, which were calculated by means of measured system parameters and results from previous tests. One exemption was the tensile strength, of which the measured values were lower than the calculated ones. In Figure 2 the measured tensile index is shown as a function of the tensile index, which was calculated by means of measured values of production, gap size and material concentration. It shows that there is a heavy systematic error. The fully drawn line designates full agreement, and the dashed lines designate an acceptable error range.

[0019] By including in the calculation of the pulp properties the vibration energy obtained from the accelerometer signal, all measured pulp properties could be predicted with high precision. In Figure 3 the measured tensile index is shown as a function of the calculated tensile index where the vibration energy has been utilized together with the adjusted production, gap size and material concentration. The agreement there lies within the error range. No systematic erros could be stated.

[0020] The deterioration in the tensile strength of the pulp can be explained by the wear of the disc segments. Heretofore it has not been possible to find a controllable relation between the tensile strength and the wear of the segments. The present invention, thus, offers such a control possibility. By measuring the vibration energy according to the invention, thus, the condition of the disc segments can be determined, which also can be utilized for determining the time when the segments have to be exchanged. The invention can also be used for comparing different segment patterns and materials.

[0021] The invention, of course, is not restricted to the embodiments described, but can be varied within the scope of the invention idea.

Claims

1. A method of controlling the manufacture of mechanical pulp in a refiner process, wherein cellulose-containing material in lumps is refined during passage between two opposed refiner dishes rotating relative to each other, vibrations of at least one refiner disc being measured by means of an accelerometer attached to the disc, characterised in that the accelerometer output is converted to a signal representing vibration energy and that this signal, together with signals representing one or more other process variables is utilised for controlling the refiner process and thereby the properties of the manufactured pulp.

2. A method as defined in claim 1 where the refiner process is carried out in a single-disc refiner, characterized in, that the vibrations are measured in a disc segment located on the stationary disc in the refiner.

3. A method as defined in claim 1 or 2, characterized in, that the control is based on the vibration energy in combination with the production, gap size and material concentration.

4. A method of determining the condition of the beating surface of the disc segments of a refiner having two opposed refiner discs rotating relative to each other, characterised in that vibrations of at least one refiner disc are measured by means of an accelerometer attached to the disc and that the output of the accelerometer is converted to a signal representing vibration energy, which is also indicative of the condition of the beating surfaces of the disc segments.

5. A method of evaluating and comparing different disc segment designs in a refiner having two opposed refiner discs rotating relative to each other, characterised in that, for each design, vibrations of at least one refiner disc are measured by means of an accelerometer attached to the disc and that the output is converted to a signal representing vibration energy, whereby a comparison of said signals obtained using different disc designs enables these different disc designs to be evaluated and compared.

Ansprüche

1. Verfahren zur Kontrolle und Steuerung der Herstellung mechanischer Pülpe in einem Mahlverfahren, bei dem zellulosehältiges, stückiges Material beim Durchgang durch den Spalt zwischen zwei einander gegenüberstehenden Mahlscheiben, die relativ zueinander rotieren, zerkleinert wird, wobei die Vibrationen zumindest einer Mahlscheibe mittels eines an der Scheibe befestigten Beschleunigungsaufnehmers gemessen werden, dadurch gekennzeichnet, daß der Meßwert des Beschleunigungsaufnehmers in ein Signal umfgesetzt wird, das die Vibrationsenergie repräsentiert und daß dieses Signal gemeinsam mit Signalen, die eine oder mehrere Prozeßvariable kennzeichnen, zur Regelung des Mahlprozesses und so der Eigenschaften der hergestellten Pülpe verwendet wird.

2. Verfahren nach Anspruch 1, wobei der Mahlprozeß in einem Einscheibenmahlwerk ausgeführt wird, dadurch gekennzeichnet, daß die Vibrationen in einem Scheibensegment der stationären Scheibe des Mahlwerkes gemessen werden.

3. Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß der Regelung die Vibrationsenergie in Kombination mit der Produktion, der Spaltgröße und der Materialkonzentration zugrundegelegt wird.

4. Verfahren. zur Bestimmung des Zustandes der Schlagoberfläche der Scheibensegmente eines Mahlwerkes, das zwei einander gegenüberstehende Mahlscheiben aufweist, die relativ zueinander rotieren, dadurch gekennzeichnet, daß die Vibrationen zumindest einer Mahlscheibe mittels eines an der Scheibe befestigten Beschleunigungsaufnehmers gemessen werden und daß der Meßwert des Beschleunigungsaufnehmers in ein Signal umgewandelt wird, das der Vibrationsenergie entspricht, die auch ein Indikator für den Zustand der Schlagoberflächen der Scheibensegmente ist.

5. Verfahren zur Bewertung und zum Vergleichen verschieden gestalteter Scheibensegmente in einem Mahlwerk, das zwei einander gegenüberstehende Mahlscheiben aufweist, die relativ zueinander rotieren, dadurch gekennzeichnet, daß für jede Gestaltung die Vibrationen zumindest einer Mahlscheibe mittels eines Beschleunigungsaufnehmers, der auf der Scheibe befestigt ist, gemessen werden und daß der Meßwert in ein Signal umgewandelt wird, das der Vibrationsenergie entspricht, wobei ein Vergleich der bei Verwendung verschiedener Scheibengestaltungen erhaltener Signale die Bewertung und den Vergleich der verschiedenen Scheibengestaltungen erlaubt.

Revendications

1. Procédé de commande de la fabrication de pulpe mécanique dans un procédé de raffinage selon lequel le matériau en morceaux contenant de la cellulose est raffiné durant son passage entre des disques de raffinage opposés tournant l'un par rapport à l'autre, des vibrations de l'un au moins des disques de raffinage étant mesurées à l'aide d'un accéléromètre fixé au disque, caractérisé en ce que le signal de sortie de l'accéléromètre est transformé en un signal représentant l'énergie vibratoire et en ce que ce signal, avec des signaux représentant une ou plusieurs autres variables du procédé, est utilisé pour commander le procédé de raffinage et par conséquent les propriétés de la pulpe fabriquée.

2. Procédé selon la revendication 1 selon lequel le procédé de raffinage est mis en oeuvre à l'aide d'une raffineuse à disque unique, caractérisé en ce que les vibrations sont mesurées dans un segment de disque situé sur le disque fixe de la raffineuse.

3. Procédé selon l'une des revendications 1 ou 2, caractérisé en ce que la commande est basée sur l'énergie vibratoire en combinaison avec la production, les dimensions de l'intervalle et la concentration des matériaux.

4. Procédé pour déterminer les conditions de la surface de raffinage des segments de disques d'une raffineuse comportant deux disques opposés de raffinage tournant l'un par rapport à l'autre, caractérisé en ce que l'on mesure les vibrations de l'un au moins des disques de raffinage à l'aide d'un accéléromètre fixé au disque et en ce que le signal de sortie de l'accéléromètre est transformé en un signal représentant l'énergie vibratoire, qui constitue également une information concernant les conditions des surfaces de raffinage des segments du disque.

5. Procédé pour évaluer et comparer différentes conceptions de segments de disques dans une raffineuse comportant deux disques de raffinage opposés tournant l'un pr rapport à l'autre caractérisé en ce que, pour chaque conception, on mesure les vibrations d'au moins un disque de raffinage avec un accéléromètre fixé au disque et en ce que le signal de sortie est transformé en un signal représentant l'énergie vibratoire, de manière qu'une comparaison desdits signaux obtenus en utilisant des conceptions différentes de disques permet d'évaluer et de comparer ces différentes conceptions de disques.

Drawing