阅读说明：本技术 纤维纸浆磨浆的监测和控制 (Monitoring and control of fiber pulp refining ) 是由 L·考皮宁 于 2020-05-06 设计创作，主要内容包括：根据本发明的示例性方面,提供了一种用于监测和控制纤维纸浆的磨浆的方法,该方法包括：捕获纸浆样品的至少一幅图像；确定至少一幅图像中的所有纤维或非原纤化纤维的量；确定至少一幅图像中的原纤化纤维的量；基于至少一幅图像中的原纤化纤维的量和所有纤维或非原纤化纤维的量,确定纸浆中原纤化纤维与所有纤维或非原纤化纤维之间的关系；基于确定的纸浆中的原纤化纤维与所有纤维或非原纤化纤维之间的关系生成控制参数；并基于控制参数通过至少一个纸浆磨浆装置控制纤维磨浆。(According to an exemplary aspect of the invention, a method for monitoring and controlling refining of a fibre pulp is provided, the method comprising: capturing at least one image of a pulp sample; determining the amount of all fibers or non-fibrillated fibers in the at least one image; determining an amount of fibrillated fibers in the at least one image; determining a relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp based on the amount of fibrillated fibers and the amount of all fibers or non-fibrillated fibers in the at least one image; generating a control parameter based on the determined relationship between the fibrillated fibers and all fibers or non-fibrillated fibers in the pulp; and controlling fiber refining by at least one pulp refining device based on the control parameters.)

1. A method for monitoring and controlling refining of a fibrous pulp, the method comprising:

-capturing (200) at least one image of the pulp sample;

-determining (202) the amount of all fibers or non-fibrillated fibers in the at least one image; it is characterized in that

-determining (204) an amount of fibrillated fibers in the at least one image;

-determining (206) a relation between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp based on the amount of fibrillated fibers and the amount of all fibers or non-fibrillated fibers in the at least one image;

-generating (208) control parameters based on the determined relation between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp; and

-controlling (210) fiber refining by at least one pulp refining device based on the control parameters.

2. The method according to any of the preceding claims, wherein the amount of fibrillated fibres and/or all fibres is determined by a fibre classifier (314), the fibre classifier (314) being configured to:

-detecting fibers and fibrils of fibers in said at least one image, and

-classifying the detected fiber as fibrillated in response to fibrils attached to the fiber reaching a predetermined threshold parameter.

3. The method of any one of the preceding claims, wherein the objects identified in the at least one image are classified as fibers or fibrils based on one or more of a determined length of the objects, a width of the objects, and an area of the objects, and

classifying the fibers identified in the at least one image as non-fibrillated fibers or fibrillated fibers based on the determined area or determined circle of fibers.

4. The method according to any of the preceding claims, wherein controlling the fibre refining comprises controlling further processing of the analyzed and refined pulp batch into a further or cyclic refining stage or into a subsequent processing stage after pulp refining.

5. The method according to any of the preceding claims, wherein controlling the fiber refining comprises controlling a chemical treatment for chemical fibrillation of the fiber pulp based on the control parameter.

6. The method according to any of the preceding claims, wherein the internal fibrillation is analyzed based on the relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp and/or by the energy used in pulp refining.

7. An apparatus for monitoring and controlling refining of fibrous pulp, comprising:

-an imaging module (304) configured to capture at least one image of the pulp sample;

-a fiber analysis module (308) configured to determine the amount of all fibers or non-fibrillated fibers in the at least one image, characterized in that the apparatus comprises:

-a fiber analysis module (308) configured to determine the amount of fibrillated fibers in the at least one image and to determine a relation between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp based on the amount of fibrillated fibers and all fibers or non-fibrillated fibers in the at least one image;

-a process controller (318) configured to generate control parameters based on the determined relation between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp; and

-a mechanical refining controller (322) and/or a chemical treatment controller (324) configured to control fiber modification by at least one pulp refining device based on control parameters.

8. The apparatus according to any one of the preceding claims, wherein the apparatus is configured to determine the amount of fibrillated fibers and/or all fibers by a fiber classifier (314), the fiber classifier (314) being configured to:

-detecting fibers and fibrils of fibers in said at least one image, and

-classifying the detected fiber as fibrillated in response to fibrils attached to the fiber reaching a predetermined threshold parameter.

9. The apparatus of any preceding claim, wherein the apparatus is configured to classify an object identified in the at least one image as a fiber or fibril based on one or more of a determined length of the object, a width of the object, and an area of the object.

10. The apparatus of any one of the preceding claims, wherein the apparatus is configured to classify fibers identified in the at least one image as non-fibrillated fibers or fibrillated fibers based on a determined area or a determined circle of fibers.

11. The apparatus according to any of the preceding claims, wherein controlling the fibre refining comprises controlling further processing of the analyzed and refined pulp batch into a further or cyclic refining stage or into a subsequent processing stage after pulp refining.

12. The apparatus according to any of the preceding claims, wherein controlling the fiber refining comprises controlling a chemical treatment for chemical fibrillation of the fiber pulp based on the control parameter.

13. The apparatus according to any of the preceding claims, wherein the apparatus is configured to analyze the internal fibrillation based on the relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp and/or by the energy used in pulp refining.

14. The apparatus according to any of the preceding claims 7 to 13, wherein the apparatus is further configured to perform the method according to any of the claims 1 to 6.

15. A fibre pulp treatment system, characterized in that it comprises a set of pulp treatment devices and a device according to any of the preceding claims 7-14.

Technical Field

Various exemplary embodiments relate to monitoring and control of fiber pulp refining.

Background

Refining of pulp is one of the most important stages in the manufacturing process of paper, board or towel. Refining has an impact on the operation and energy consumption of the paper, board or towel machine and on the stoichiometric strategy. It also determines the quality and final properties of the final product, such as strength and printability. Thus, many tests can be performed on pulp fibers, such as fiber length, diameter, modulus and strength, freeness and chemical purity measurements, to predict and modify the properties of the final product. However, there is still a need for improved determination of fiber properties and control of fiber modification and stoichiometry for higher quality paper, paperboard, tissue and microfibrillated cellulose (microfibrillated cellulose), nanofibrillated cellulose (nanofibrillated cellulose) and nanocrystalline cellulose (nanocrystalline cellulose).

Disclosure of Invention

The invention is defined by the features of the independent claims. Some specific embodiments are defined in the dependent claims.

According to a first aspect, there is provided a method for monitoring and controlling refining of a fibre pulp, the method comprising: capturing at least one image of a pulp sample; determining the amount of all fibers or non-fibrillated fibers in the at least one image; determining an amount of fibrillated fibers in the at least one image; determining a relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp based on the amount of fibrillated fibers and the amount of all fibers or non-fibrillated fibers in the at least one image; generating a control parameter based on the determined relationship between the fibrillated fibers and all fibers or non-fibrillated fibers in the pulp; and controlling fiber refining by at least one pulp refining device based on the control parameters.

According to a second aspect, there is provided an apparatus for monitoring and controlling refining of fiber pulp, comprising means configured to perform at least the following: capturing at least one image of a pulp sample; determining the amount of all fibers or non-fibrillated fibers in the at least one image; determining an amount of fibrillated fibers in the at least one image; determining a relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp based on the amount of fibrillated fibers and the amount of all fibers or non-fibrillated fibers in the at least one image; generating a control parameter based on the determined relationship between the fibrillated fibers and all fibers or non-fibrillated fibers in the pulp; and causing control of the modification of the fibres by the at least one pulp refining device based on the control parameters.

According to an embodiment, the pulp sample is a pulp liquid suspension.

According to an embodiment, controlling the fibre refining comprises controlling the further processing of the batch of pulp analyzed and refined into a further or cyclic refining stage or into a subsequent processing stage after pulp refining.

According to one embodiment, the device is arranged before a headbox (head box) of a paper, board or towel machine.

According to an embodiment, the pulp refining is controlled for the manufacturing process of microfibrillated cellulose, nanofibrillated cellulose and nanocrystalline cellulose.

According to an embodiment, the internal fibrillation is analyzed based on the relation between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp and/or by the energy used in pulp refining.

According to an embodiment, the device is configured to generate the control parameter further based on a canadian standard freeness parameter and/or a Schopper Riegler (Schopper Riegler) parameter.

Drawings

FIG. 1 illustrates a pulp manufacturing process in accordance with at least some embodiments of the present invention;

fig. 2 illustrates a method for monitoring and controlling refining of fiber pulp in accordance with at least some embodiments of the present invention;

fig. 3 illustrates an apparatus for monitoring and controlling refining of fiber pulp in accordance with at least some embodiments of the present invention;

FIG. 4 shows fibers in a sample of pulp prior to refining;

FIG. 5 shows fibers in a pulp sample after refining; and

figure 6 shows the fibers in the pulp sample after the second stage refining.

Detailed Description

As used herein, the term "pulp" includes, but is not limited to, pulp made from softwood, hardwood, or non-wood fibers, recycled pulp made from printed waste paper, such as newspapers, advertising leaflets, magazines, data recording paper, photocopies, computer printouts, or mixtures of such printed matter (e.g., waste magazine paper and office waste paper), and mixtures thereof. The term also includes microfibrillated cellulose (MFC), nanofibrillated cellulose (NFC) and nanocrystalline cellulose (NCC), synthetic pulp and artificial pulp.

In this context, the term "fibrillation" includes shearing pulp fibers by external fibrillation to loosen fibrils from the fiber surface and fiber walls and/or delaminating and expanding fibers by internal fibrillation.

In this context, the term "fibrillated fibers" includes fibers that have been processed to form fibers with higher surface area and/or branching structures.

In this context, the term "refining" includes mechanical and/or chemical treatment for fibrillation of fiber pulp.

In this context, the term "chemical fibrillation" includes chemical treatment for fibrillation of fiber pulp.

In this context, the term "stock flow system" includes the part of the papermaking process between the final stock preparation tank and the headbox of the paper machine.

During the refining of the pulp, fibrillation of the cellulose fibres occurs. Fibrillation is one of the most important fiber properties that control the properties of the final product. For example, it has been noted that fibrillated fibers give the final product greater strength, and thus fiber-to-fiber bonding is stronger by increased fiber bonding area. Furthermore, studies with functional paper chemicals have shown that the chemicals tend to attach more fines and fillers for more fibrillated fibers as well as microfibrillated cellulose, nanofibrillated cellulose and nanocrystalline cellulose. Therefore, it is important to measure fiber properties, particularly fibrillation, to control refining, optimize the chemometric strategy, and model the strength and other mechanical properties of the final product. However, there remains a need for improved determination and control of fibrillation. The present embodiment thus provides an improved method for monitoring and controlling refining of fibre pulp.

Fig. 1 shows a pulp manufacturing process 100. The process may include raw material preparation 102, pre-treatment 104, mechanical 106 or chemical 108 pulping, treatment 110, screening 112 and bleaching 114 of the pulp, intermediate storage 116, 122 of the pulp, refining 118, 120 of the pulp, monitoring 124 of the pulp, further refining 126 of the pulp.

After further refining 126, the pulp may be monitored 128 again. The pulp may be provided for further processing stages. In the example of fig. 1, the pulp is provided to a slurry flow system (AFS) 130. The stock approach system step 130 may include, for example, a headbox, a mixing tank, a mechanical tank, a chemical treatment, or a steam burst system of a paper machine, a board machine, or a towel machine. It should be understood that fig. 1 shows only one example of a pulp manufacturing process, and may differ at some stages or even be omitted. The pulp manufacturing process may also comprise other processing stages, such as pre-and post-treatment of the pulp and intermediate storage. Furthermore, refining and monitoring can be performed in multiple stages.

Feedstock preparation 102 may include, for example, peeling, flaking, cooking, bleaching, screening, and washing the feedstock. In the manufacture of chips, the logs (or parts of logs) are broken down into chips suitable for subsequent pulping operations. The screening may separate the fragments based on fragment length and/or thickness.

Mechanical pulping 106 or chemical pulping 108 is used to break down individual cellulosic fibers of wood (or other fibrous raw material). Mechanical pulping processes utilize mechanical energy to weaken fibers and separate fibers from wood by a grinding action. Mechanical pulping processes include, for example, Groundwood (GW) pulping, Refiner Mechanical Pulping (RMP), thermomechanical pulping (TMP), and Chemithermomechanical (CTM) pulping. Chemical pulping breaks the bulk structure of the fiber source by degrading lignin and hemicellulose into small water-soluble molecules that can be washed off the cellulose fibers. Chemical pulping processes include, for example, the kraft process and the sulfite process.

After pulp production, the pulp treatment 110 removes impurities, such as uncooked chips, and recycles any remaining cooking liquor through the pulp washing process. Screening 112 of the pulp is performed to remove oversize and unwanted particles such as lumps (knots) and coarse cellulose (shive). The pulp may then be bleached to obtain a lighter color. Bleaching 114 may also be used to purify the pulp by removing hemicellulose and wood extracts as well as lignin.

Pulp produced without any mechanical treatment in the pulp mill is generally not suitable for most paper grades. Thus, refining 118 is performed to obtain better pulp quality. During refining, the fibers become fibrillated by external fibrillation as the outer portions of the fibers are at least partially stripped. Some outer portions of the fibers may remain attached and increase the strength of the fibers. This significantly increases the surface area of the fiber. In addition, the inner wall can become delaminated by internal fibrillation, which increases the compliance (conformability), flexibility, bonding tendency, and thickness of the fiber. Due to the internal fibrillation, a larger inter-fiber bonding surface and a larger volume are obtained. In addition, due to the lower amount of fines, dewatering is more efficient and the need for drying energy is reduced.

Refining 118 may be performed by, for example, a pulper or refiner (e.g., a single disc refiner, a conical disc refiner, a double disc refiner, or a flat disc refiner). The refiner may comprise two blades facing each other and rotating relatively, thus producing the mechanical action of refining.

Referring to fig. 1, the refining process may include simultaneous refining 120 and/or further refining 126 stages. In simultaneous refining, the pulp flow may be split and directed to at least two refiners, which simultaneously refine the fibers. Refining may comprise, for example, 1 to 10 stages, especially 1 to 5 stages, preferably 1 to 3 stages. The refining stage can be repeated to produce fibrillated fibers. Refining can be monitored and controlled to achieve preferred fiber properties. The pulp can be directed to further refining stages or returned to the cyclic refining stage on the basis of the fiber monitoring 124 to achieve preferred fiber properties. For example, after fiber monitoring 124, the fibers may be directed to a prior refining 118 stage or to a further refining 126 stage. The fibres can be led through the same refining stage several times, even up to 20-30 times. The fiber may then be redirected to fiber monitoring 124. The fiber monitoring and previous or further refining stages can be repeated until the preferred fiber properties are obtained. When preferred fiber properties are obtained, the pulp may be provided to further process steps.

In the following examples, the term fibrillated fiber ratio parameter is used to refer to the relationship between fibrillated fibers and all fibers or non-fibrillated fibers in a pulp.

Fig. 2 shows a method for monitoring and controlling refining of fibre pulp. The method can comprise the following steps: capturing 200 at least one image of a pulp sample; determining 202 the amount of all fibers or non-fibrillated fibers in at least one image; determining 204 an amount of fibrillated fibers in at least one image; determining 206 a relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp based on the amount of fibrillated fibers and the amount of all fibers or non-fibrillated fibers in the at least one image; generating 208 a control parameter based on the determined relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp; and controlling 210 fiber refining by at least one pulp refining device based on the control parameters. Due to the monitoring and control of the refining of the fibre pulp, a smooth operation of the paper, board or towel machine can be achieved and the final properties of the pulp or the final product can be adjusted. Furthermore, the stoichiometry strategy can be optimized according to the determined fibrillated fiber ratio parameters and the strength and other mechanical properties of the final product can be modeled.

In addition to determining the relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp, the method may be configured to generate 208 a control parameter further based on a Canadian Standard Freeness (CSF) parameter and/or a Schopper Riegler (SR) parameter. The CSF and SR parameters give a measure of the drainage performance of the pulp suspension in water. CSF parameters can be measured according to the standards TAPPI T227 and ISO 5267-2. The SR parameters may be measured according to standard 5267-1. In addition, other inputs may be used to generate 208 control parameters.

Note that since the method of fig. 2 may be implemented in a device separate from the imaging device, block 200 may refer to receiving image data of a pulp sample.

Controlling 210 fiber refining may include, for example, adjusting blade gaps between segments in the refiner. The space between the blades can be widened or shortened depending on the degree of refining suitable for the end use of the pulp, paper, board or towel to be produced. The blade gap may be measured by at least one sensor or may be measured indirectly from the refiner vibrations or other indicative measurements.

The blade gap between the sections in the refiner has a significant impact on both the yield and the pulp quality. Furthermore, an optimal blade gap reduces the refiner life cycle cost due to fewer production stoppages and better refiner performance. It is therefore very important that the refiner operates with an optimum blade gap.

In addition, controlling 210 the fiber refining may include controlling further processing of the pulp batch being analyzed and refined, either into a further refining stage or into a cyclic refining stage or into a subsequent processing stage after pulp refining. The refining stage can be repeated until the pulp meets the set requirements. The fibrillated fiber proportion parameters and other fiber properties can be determined before and/or after each refining stage.

Controlling 210 fiber refining may also include controlling replacement of refiner blades. The blade may be replaced according to an indication generated based on the fibrillated fiber ratio parameter. Blades with different patterns can be used for different refining stages. The optimal choice of blades provides the preferred fiber properties and may reduce the need for several refining stages.

Further, controlling 210 fiber refining may include controlling dilution water. The increase in the introduction of dilution water reduces the consistency of the pulp. When operating with an undesirably high dilution water intake, high pulp flows may occur inside the refiner stages. This may result in low pulp quality due to short refining time and lower specific energy (specific energy) input in each section. Conversely, reducing the dilution water introduction increases consistency. This may result in a decrease in strength due to insufficient pulp flow between the stages, resulting in insufficient pulp quality and plugging of the stages. Therefore, control of the dilution water is important to obtain optimum fiber properties and pulp flow.

Controlling 210 fiber refining may also include controlling throughput. The throughput may be controlled by a screw feeder or pump. The production volume affects the residence time of the pulp and the flow of pulp and steam. Thanks to the optimum production, the refiner is stabilized due to the uniform inflow of pulp.

Controlling 210 fiber refining may include controlling chemical treatment for chemical fibrillation of the fiber pulp based on control parameters, according to some embodiments. Controlling the chemical treatment may include controlling the dosage and/or duration of the application of chemicals, controlling enzyme treatment, controlling dispersant treatment, controlling solvent treatment, controlling chemical additive or agent treatment to promote or enhance hydrolysis of cellulose, controlling post-refining treatment, controlling retention chemical treatment, and/or controlling the amount of water. The chemicals may include, for example, retention chemicals, Polyacrylamide (PAM), silica, and chemicals used in MFC or NFC production (e.g., 2,6, 6-tetramethylpiperidin-1-oxyl (TEMPO)). Enzymes may include, for example, cellulases, xylanases, laccases, and lipases.

The control of the chemical dosage can be used as a pre-treatment after and/or between stages of refining and/or mechanical refining. During the treatment stage or in the pulp flow system, chemicals may be dispensed directly into the pulp vessel. After pulping or after preliminary refining in MFC or NFC process, chemicals can be dispensed. The distribution of PAM and silica can be performed, for example, in the short circulation of the paper machine. The dispensing of the retention chemical may be performed, for example, in a slurry flow system.

The duration and dosage of the application of the chemicals can be optimized to achieve the preferred ratio of fibrillated fibers. The dosage of the chemicals can be controlled to form a hardened fiber and to soften the upper layer of fibers. The chemicals may increase the internal fibrillation of the fiber by delamination, where the walls of the fiber thicken when they separate. Controlling the dosage of the chemicals produces fibers with optimal properties (e.g., strength). In addition, enzymatic pre-treatment for refining can improve the efficiency of the refining process.

Pulp samples are prepared prior to pulp monitoring 124 and fiber properties determination. Sample preparation may be manual or automated. The pulp sample may be a pulp liquid suspension, such as an aqueous pulp suspension. The properties of the pulp sample (e.g., weight and volume of the sample) can be determined prior to controlling the consistency of the sample and determining the fiber properties of the sample. The consistency of the pulp liquid suspension may be controlled, for example, by adding a sufficient amount of liquid (e.g. water) to the suspension. A wetting agent may be added to the suspension to improve the uniform distribution of the fibers in the suspension. The wetting agent may be, for example, a surfactant or an alcohol.

The amount of fibrillation and/or all fibers may be determined 202, 204 by a fiber classifier (e.g., fiber classifier 314 shown in the apparatus of fig. 3) configured to: detecting fibers and fibrils of the fibers in the at least one image, and classifying the detected fibers as fibrillated fibers in response to fibrils attached to the fibers reaching a predetermined threshold parameter. The fiber classifier may be part of the device or connected to the device. The predetermined threshold parameter may be set, for example, according to the type of pulp used or the type of input material (e.g., tree species). The predetermined threshold parameter may be, for example, one to three fibrils, in particular one fibril. Due to the classification of the fibers, a parameter of the proportion of fibrillated fibers in the pulp can be determined.

According to some embodiments, the object identified in the at least one image may be classified as a fiber or fibril based on the determined length and/or width of the object. An object may be classified as a fiber if the length of the object is, for example, in the range of 0.5 to 15mm, and/or if the width of the object is, for example, in the range of 10 to 75 μm. An object can be classified as a fibril if its width is, for example, below 10 μm. An object may be classified as an MFC or NFC fiber if its length is for example in the range of 100nm to 100 μm and/or if its width is for example in the range of 10 to 100 nm. An object may be classified as an MFC or NFC fibril if its width is, for example, below 10nm, in particular in the range of 5 to 6 nm. The predetermined threshold parameters for the width and length of the fibres and fibrils may be set, for example, according to the type of pulp or tree species used. The classification may be done by the fiber classifier 314 determining the length and/or width of the object in the at least one image. Due to the fiber classification, a fibrillated fiber proportion parameter can be determined.

The identified objects in the at least one image may be classified as fibers or fibrils based on the determined area of the objects. The classification may be performed by the fiber classifier 314 detecting an object in at least one image and determining the area of the object. For example, the predetermined threshold parameter of the area of the fibers and fibrils may be set according to the type of pulp or tree species used.

According to some embodiments, fibers identified in at least one image may be classified as non-fibrillated fibers or fibrillated fibers based on a determined area or a determined circle (circle) of the fibers. The classification may be performed by the fiber classifier 314 determining the area or circle of the fibers in at least one image. Due to the fiber classification, a fibrillated fiber proportion parameter can be determined.

After fiber classification, a fibrillated fiber proportion parameter in at least one image may be determined. The determination may be made by calculating the proportion of fibrillated fibers using the following equation:

the above-mentioned new parameters for measuring fiber properties provide useful tools for controlling refining, modeling paper, board or tissue strength, and other mechanical properties, and optimizing the stoichiometric strategy. Due to this parameter, the refining of the pulp can be controlled to adjust the proportion of fibrillated fibers to obtain preferred pulp and/or end product properties. Controlling fiber refining based on this ratio enables more accurate control of refining and pulp properties than controlling a fiber pulp process based on the fibrillation index based on the surface or circumference of the fibers and fibrils, since the effect of non-fibrillated fibers on the properties of the pulp or the final product can also be taken into account. For example, fibrillated fibers and non-fibrillated fibers may have different chemical treatment responses. Therefore, also detecting non-fibrillated fibers and calculating fibrillated fiber proportion parameters is crucial for achieving optimal pulp properties in e.g. MFC, NFC and NCC production, as well as higher web strength (web strength), lower porosity, higher smoothness and higher gloss in papermaking. This fibrillated fiber ratio parameter is also critical to optimize the amount of non-fibrillated fibers to achieve adequate water removal performance.

The method of fig. 2 may be provided before, after and/or during the manufacturing process of the paper, paperboard or towel. For example, the method may be provided after the chemical pulping 106 or the mechanical pulping 108, and before and/or after the refining 118, 120, 126. The method may thus give useful information about the fibre properties in different stages of the manufacturing process of paper, board or towel, and the manufacturing process may be controlled in accordance with the fibre properties to achieve a final product with optimal properties.

The method of fig. 2 may be provided before the headbox in a paper, board or towel machine instead of waiting for a time-lapse laboratory test to be performed after the manufacture of the paper, board or towel. Thus, the method can give useful information about the properties of the fibres before the web information and can control the refining of the fibres in accordance with the properties of the fibres to obtain a final product with preferred properties.

Pulp refining can be controlled for MFC, NFC and NCC manufacturing processes. Thus, the method may give useful information about the properties of the fibres during the manufacture of the cellulose and before the formation of a product comprising cellulose. Furthermore, the refining of MFC, NFC and NCC fibers can be controlled according to the fibrillated fiber ratio parameters to achieve MFC, NFC and NCC or MFC, NFC and NCC products with preferred properties.

The method may be configured to generate 208 control parameters further based on the internal fibrillation. In some embodiments, internal fibrillation may be analyzed based on the relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp and/or by the energy used in pulp refining. If the width of a fiber reaches a predetermined threshold, the fiber may be classified as an internally fibrillated fiber. The amount of internal fibrillation may increase when the energy consumption during refining increases. Thus, internal fibrillation can be controlled by the fibrillation fiber ratio parameters and/or energy consumption to achieve a final product with preferred properties.

Fig. 3 shows an apparatus 300 for monitoring and controlling refining of a fibre pulp, comprising means configured to perform at least the following operations: capturing at least one image of a pulp sample; determining the amount of all fibers or non-fibrillated fibers in the at least one image; determining an amount of fibrillated fibers in the at least one image; determining a relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp based on the amount of fibrillated fibers and the amount of all fibers or non-fibrillated fibers in the at least one image; generating a control parameter based on the determined relationship between fibrillated fibers and all fibers or non-fibrillated fibers in the pulp; and controlling the modification of the fibres by at least one pulp refining device based on the control parameters. It should be understood that fig. 3 only shows one example of a suitable device for monitoring and controlling refining of the fibre pulp.

The device may include or be connected to a network 326. Thus, refining can be monitored and controlled quickly and accurately already during refining.

The pulp sample may be prepared in the sample processing unit 302 of the apparatus 300. The sample processing unit may comprise a plurality of auto-samplers, for example 1 to 20 samplers, in particular 12 samplers. Properties of the pulp sample, such as weight, volume, and pH of the sample, may be measured by the sample processing unit, and the pulp sample may be prepared for imaging by the sample processing unit. The consistency of the pulp sample can be controlled by adding a sufficient amount of liquid (e.g., water) to the suspension.

Pulp samples may be taken at several points (e.g., 1 to 20 points) of the pulp slurry. The measurement cycle time may be, for example, 0.5 to 10 minutes, preferably 3 to 6 minutes.

The means for capturing at least one image of the pulp sample may comprise an imaging module 304. The imaging module means may comprise recording means which can record the image in a digital format. The imaging module may capture, for example, 30-70 frames/second. The size of the image may be, for example, 30 × 20mm, 8 × 6mm for High Definition (HD) images and 16 × 13mm for Ultra High Definition (UHD) images.

The apparatus may also include additional modules or units, such as freeness measurement module 306. The main goal of freeness control is to produce pulp that is consistently discharged and performs well on a paper, board or towel machine. The consistency of the sample can be automatically controlled. The freeness of the pulp can be measured according to the Canadian Standard freeness method (CSF) described in Standard TAPPI T227 and ISO 5267-2. In addition, the Shoebur (SR) parameter can be measured in the freeness module according to standard 5267-1.

After image capture, the image may be processed by image processing software. Image processing may include, for example, filtering, noise reduction, changes in the sharpness, brightness, and/or contrast of the image, and/or color adjustment of the image. Image processing facilitates detection and fiber classification of objects.

The device 300 or imaging module 304 may also include an illumination device to help capture an image of the fiber. The illumination device may comprise an illumination device such as a Light Emitting Diode (LED) or an Organic Light Emitting Diode (OLED) lamp. The illumination device may be positioned such that light is transmitted through the sample. In another aspect, the illumination device may be positioned such that light is reflected from the sample. The illumination device assists the imaging module in image capture and assists the fiber classifier 314 in detecting objects and classifying fibers.

The means for determining the amount of all fibers or non-fibrillated fibers in the at least one image and the means for determining the amount of fibrillated fibers in the at least one image may comprise a fiber analysis module 308. The fiber analysis module may be part of the device or connected to the device. The fiber analysis module may include a fibrillation analyzer 310, which fibrillation analyzer 310 may include or may be connected to a fiber detector 312, a fiber classifier 314, and a fibrillation-relation parameter generator 316.

The sample can be automatically diluted to a set consistency depending on the type of pulp. The sample suspension may then flow through the imaging module 304 as a continuous flow. Images may be taken from the sample stream at regular intervals over a predetermined time until a calculation of image quantity or confidence interval is obtained. The fiber detector 312 may identify and count various objects from the captured images, such as fiber size, fine particles, fiber fibrillation, fiber bundles, tube cells, and/or rods. The fiber classifier 314 may classify fibers by automated computer image analysis. A suitable algorithm stored in the computer may cause the fiber classifier to determine the size of the object detected in the at least one image. Image analysis is a fast and reliable method of determining fibers. The amount of non-fibrillated fibers and fibrillated fibers may be counted by the fiber classifier 314 of the fibrillation relationship parameter generator 316. Finally, the fibrillation relationship parameter generator 316 may determine a fibrillation fiber ratio parameter.

The fiber analysis module 308 may also be used to determine other properties of the fibers, such as fineness, kink (kink), curl, size distribution, fraction, and details of hardwood and softwood ratios. The determination of the proportion of fibrillated fibers parameter can be processed together with possible other fiber properties measured by the apparatus in a modeling tool that helps to predict how the fiber properties will affect the final sheet properties.

The apparatus 300 and/or the fiber analysis module 308 may include a processor, a communication unit, and a memory. The fiber analysis module may include a transmitter and/or receiver that may be configured to operate in accordance with, for example, global system for mobile communications GSM, wideband code division multiple access WCDMA, long term evolution LTE, 5G or other cellular communication systems, wireless local area network WLAN, and/or ethernet standards.

The memory may store computer program code and parameters to cause the fiber analysis module 308 to perform at least some of the presently disclosed features, such as determining a fibrillated fiber ratio parameter and at least some other features in fig. 2, when the computer program code is executed by the processor. Thus, the memory, processor and computer program code may be means for causing the fiber analysis module to perform at least some of the presently disclosed features relating to the new fibrillated fiber ratio parameter.

The means for generating control parameters based on the determined fibrillated fiber ratio parameter may include a process controller 318. The process controller may comprise a refining controller 320 for generating 208 control parameters and/or controlling 210 the refining process by applying at least some of the features described above.

The means for causing control of fiber modification by at least one pulp refining device based on control parameters may include or be connected to a mechanical refining controller 322 and/or a chemical process controller 324 to implement at least some of the above-described mechanical and/or chemical fiber refining actions. The mechanical refining controller may be a control unit in the mechanical refiner and control e.g. adjusting the blade gap between the sections in the refiner, pulp batch entering further or cyclic refining stages or subsequent process stages after pulp refining, changing the blades of the refiner, dilution water and/or throughput. The chemical process controller may control, for example, the dosage of chemicals.

The device may also include one or more User Interface (UI)326 devices, for example, a display and input devices, such as one or more of a keyboard, touch screen, mouse, gesture input device, or other type of input/output device. The UI may be configured to display the analysis results and provide user input for controlling the computing unit. It will be understood that various other data related to monitoring and control of refining of the fibre pulp may be displayed and/or controlled via the UI.

Figure 4 shows the fibers in a pulp sample prior to refining. The amount of fibrillation is very low. The pulp comprises almost exclusively ordinary non-fibrillated fibres. Figure 5 shows the refined pulp. Fibrillation can be seen due to the refining action, but there are still many common non-fibrillated fibers in the pulp. Fig. 6 shows the fibers after the second stage of refining. More fibrillation is naturally observed due to further refining. However, there are also non-fibrillated fibres that have (almost) passed the refining stage without damage.

This embodiment has several advantages. Previous methods for monitoring pulp are not sufficient to control refining. In contrast, this example gives a new fibrillated fiber ratio parameter that can be used to effectively control refining and achieve optimal final product performance. Since the refining is controlled by new parameters, higher web strength can be obtained by higher fiber-to-fiber bonding. An optimal relationship between fibrillated and non-fibrillated fibres can be achieved by this parameter, which results in excellent mechanical properties due to a suitable amount of fibrillated fibres and sufficient water removal properties due to a suitable amount of non-fibrillated fibres. In addition, better formation of the paper web, lower porosity of the final product, better printability, higher smoothness and higher gloss can be achieved. Furthermore, as the refining is controlled by parameters, the stoichiometric strategy and energy consumption can be optimized and the strength of the web can be modeled.

It is to be understood that the disclosed embodiments of the invention are not limited to the particular structures, process steps, or materials disclosed herein, but are extended to equivalents thereof as would be recognized by those ordinarily skilled in the relevant arts. It is also to be understood that the terminology used herein is for the purpose of describing particular embodiments only, and is not intended to be limiting.

Reference throughout this specification to "one embodiment" or "an embodiment" means that a particular feature, structure, or characteristic described in connection with the embodiment is included in at least one embodiment of the present invention. Thus, the appearances of the phrases "in one embodiment" or "in an embodiment" in various places throughout this specification are not necessarily all referring to the same embodiment.

As used herein, a plurality of items, structural elements, compositional elements, and/or materials may be presented in a common list for convenience. However, these lists should be construed as though each member of the list is individually identified as a separate and unique member. Thus, no single member of such list should be construed as a de facto equivalent of any other member of the same list solely based on their presentation in a common group without indications to the contrary. In addition, reference may be made herein to various embodiments and examples of the invention and alternatives for various components thereof. It should be understood that such embodiments, examples, and alternatives are not to be construed as being virtually equivalents to one another, but are to be considered as independent and autonomous representations of the present invention.

Furthermore, the described features, structures, or characteristics may be combined in any suitable manner in one or more embodiments. In the following description, numerous specific details are provided, such as examples of lengths, widths, shapes, etc., to provide a thorough understanding of embodiments of the invention. One skilled in the relevant art will recognize, however, that the invention may be practiced without one or more of the specific details, or with other methods, components, materials, and so forth. In other instances, well-known structures, materials, or operations are not shown or described in detail to avoid obscuring aspects of the invention.

While the above examples illustrate the principles of the invention in one or more particular applications, it will be apparent to those of ordinary skill in the art that numerous modifications in form, usage and implementation details can be made without the exercise of inventive faculty, and without departing from the principles and concepts of the invention. Accordingly, it is not intended that the invention be limited, except as by the claims set forth below.

The verbs "comprise" and "comprise" are used herein as open-ended limitations that neither exclude nor require the presence of unrecited features. The features recited in the dependent claims may be freely combined with each other, unless explicitly stated otherwise. Furthermore, it should be understood that the use of "a" or "an" (i.e., singular forms) herein does not exclude a plurality.

INDUSTRIAL APPLICABILITY

At least some embodiments are feasible in monitoring and controlling refining of fiber pulp.