METHOD OF AND AN ARRANGEMENT FOR ADDING AT LEAST ONE ADDITIONAL STOCK COMPONENT TO AN APPROACH FLOW SYSTEM OF A FIBER WEB MACHINE

Abstract

A method of and an arrangement for adding at least one additional stock component to an approach flow system (30) of a fiber web machine by mixing the at least one additional stock component to a fibrous stock such that the stock flow is equalized (50) and the at least one additional stock component is introduced to the stock flow by injection mixing (80).

Claims

1. A method of adding at least one additional stock component to a stock flow in an approach flow system of a fiber web machine headbox, wherein a fibrous stock is introduced by a headbox feed pump via a headbox screen, a headbox feed pipe and a chemical mixer to the headbox of a fiber web machine, the method comprises: treating the stock flow by equalizing consistency differences prevailing in the stock flow downstream of the headbox screen to form an equalized stock flow, and mixing the at least one additional stock component with the equalized stock flow.

2. The method as recited in claim 1, further comprising providing a stock flow equalizer to perform the step of the treating the stock flow by equalizing the consistency differences prevailing in the stock flow, wherein the stock flow equalizer is between the headbox screen and the chemical mixer at a distance from the chemical mixer.

3. The method as recited in claim 1, wherein the mixing of the at least one additional stock component with the stock occurs at least before or after the equalizing of the consistency differences prevailing in the stock flow downstream of the headbox screen.

4. The method as recited in claim 1, further comprising using an injection mixing station to add the at least one additional stock component to the stock flow by using at least one of fresh pulp, recycled pulp, white water and fresh water as an injection liquid for the injection mixing station.

5. The method as recited in claim 3, further comprising using an injection liquid to carry the at least one additional stock component into the equalized stock flow.

6. The method as recited in claim 1, further comprising using an injection mixing station to add the at least one additional stock component to the stock flow, wherein the injection mixing station uses an injection liquid to carry the at least one additional stock component to the stock flow, and the injection liquid is stock from the headbox feed pipe take upstream or downstream of the stock flow equalizer and upstream of the injection mixing station.

7. The method as recited in claim 1, wherein the at least one additional stock component is at least one of: a retention chemical, sizing agent, a starch, filler, paper dye or pigment, a micro-fibrillated cellulose, a nano-fibrillated cellulose, a bio-based fiber and a synthetic fiber.

8. An approach flow system of a fiber machine headbox comprising: a headbox feed pump; a headbox screen; a chemical mixer; a headbox feed pipe, wherein a stock flow passage extends through the headbox feed pump, the headbox screen, the chemical mixer and the headbox feed pipe, and a stock flow equalizer included in the stock flow passage and configured to equalize consistency differences prevailing in a stock flow in the stock flow passage, and the stock flow equalizer is between the headbox screen and the headbox and is upstream of the chemical mixer in the stock flow passage.

9. The arrangement as recited in claim 8, wherein the chemical mixer is at least one of upstream and downstream of the stock flow equalizer.

10. The arrangement as recited in claim 8, wherein the chemical mixer is an injection mixing station comprising at least one injection mixer, and the injection mixing station is configured to inject an injection liquid carrying the at least one additional stock component into the stock flow.

11. The arrangement as recited in claim 10, wherein the injection mixing station includes an inlet channel configured to feed the injection liquid into the injection mixing station, and the inlet channel has an inlet connected to the headbox feed pipe at a location of: between the stock flow equalizer and the injection mixing station, upstream of the stock flow equalizer, and downstream of the injection mixing station.

12. The arrangement as recited in claim 10, wherein: a distance along the stock flow passage from the stock flow equalizer to the chemical mixer is in a range of 0.5 to 10 times a diameter of the headbox feed pipe, and a distance along the stock flow passage from the stock flow equalizer to the headbox is in a range of 5 to 15 times the diameter of the headbox feed pipe.

13. The arrangement as recited in claim 10, wherein the stock flow equalizer includes a tubular wall having an inside surface and form parts on the inside surface.

14. The arrangement as recited in claim 13, wherein each of the form parts has a height in a radial direction of the tubular wall of 0.1 to 0.5 times a diameter of the headbox feed pipe.

15. The arrangement as recited in claim 9, wherein the headbox feed pipe extends from the headbox screen to the fiber web machine headbox, and the headbox feed pipe is connected to each of the headbox feed pump, the chemical mixer, the stock flow equalizer and the fiber web machine headbox.

16. A method comprising: pumping a flow of stock of a suspension of fibers through a headbox pipe; screening the flow of stock in a headbox screen connected to the headbox pipe; equalizing consistency differences in the flow of stock downstream of the headbox screen and upstream of a headbox; mixing an additional stock component into the flow of stock upstream of the headbox downstream in the flow of stock from the equalizing consistency differences, and directing the flow of stock with the additional stock component through the headbox pipe and into the headbox.

17. The method of claim 16 wherein the equalizing of consistency differences is performed with a stock flow equalizer comprising a tube having an inside surface wetted by the flow of stock, wherein the inside surface has a diameter equal to an inner diameter of the headbox pipe, and the stock flow equalizer further comprises form parts arranged symmetrically around a circumference of the inside surface, wherein each of the form parts extends radially inward from the inside surface a distance in a range of 0.1 to 0.5 times an inner diameter of the headbox feed pipe.

18. The method of claim 17, wherein the form parts each include a ramp extending downstream from the inside surface to an apex having a height 0.1 to 0.5 times the inner diameter of the headbox feed pipe.

19. The method of claim 18, wherein each of the form parts has a downstream side parallel to a radial line and extending from the apex to the inside surface.

20. The method of claim 18, wherein each of the form parts has a first triangular shape in a first cross section parallel to a flow direction through the tube of the equalizer and a second triangular shape in a second cross section perpendicular to the flow direction.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0019] In the following the prior art and the present invention are discussed in more detail with reference to the accompanying drawings, in which

[0020] FIG. 1 illustrates a partial view of a prior art approach flow system of a fiber web machine,

[0021] FIG. 2A illustrates a partial view of a novel approach flow system of a fiber web machine in accordance with an embodiment of the present invention,

[0022] FIG. 2B illustrates a partial view of a novel approach flow system of a fiber web machine in accordance with another embodiment of the present invention

[0023] FIG. 3 illustrates a partially cut view of a stock flow equalization mixer or stock flow equalizer in accordance with an embodiment of the present invention,

[0024] FIG. 4a illustrates the operation of the form parts of the stock flow equalizer as seen from the side of the form part,

[0025] FIG. 4b illustrates the operation of the form parts of the stock flow equalizer as seen from the direction of the headbox.

DETAILED DESCRIPTION

[0026] FIG. 1 illustrates a partial view of a prior art approach flow system of a fiber web machine. In accordance with the Figure the approach flow system 10 of the fiber web machine comprises, in addition to the not-shown components, a headbox feed pump 12, a stock flow pipe 14, a headbox screen 16, a chemical mixer 18 and a headbox 20 via which the fibrous stock is delivered to the forming section of the fiber web machine, normally on the wire or forming section thereof. The chemical mixer 18 is an OptiMixer™ of Valmet Corporation discussed in more detail in US Patent Application Publication 2002/0121350. The chemical mixer 18 has a number of feed openings arranged on the circumference of the mixer, the feed openings being arranged into cooperation with the form parts of the mixer. Each feed opening may have only one feed channel for the chemical, or two feed channels 22′ and 22″, as shown in the Figure. In accordance with the US-document feed channel 22′ may be used for feeding filling agent or fiber pulp, and feed channel 22″ for feeding some other chemical such that the two components are mixed with each other before introduction via the feed opening to the stock in the stock flow pipe 14.

[0027] As discussed already above, feeding one or more chemicals to the stock flow that has not yet been completely mixed so that the consistency variations in the stock flow would have been equalized brings about problems that may be seen in both the quality of the end product and in the unnecessarily high dosage of chemicals, resulting in increased chemical costs.

[0028] FIG. 2A illustrates a partial view of an approach flow system of a fiber web machine in accordance with the present invention. The novel approach flow system 30 of the fiber web machine comprises, in addition to the not-shown components, a headbox feed pump 32, a stock flow pipe 34, a headbox screen 36, a headbox feed pipe 38 and a headbox 40 via which the fibrous stock is delivered to the forming section of the fiber web machine, normally on the wire or forming section thereof. The headbox feed pipe 38 extending from the headbox screen 36 or machine screen to the headbox 40 is provided with a stock flow equalizer 50 (discussed in more detail in FIGS. 3 and 4a-4b) and an injection mixing station 80. As shown in the FIG. 2A the injection mixing station 80 has at least one inlet channel or a set of inlet channels 82 for one or more chemicals to be introduced to the stock flow in the headbox feed pipe 38. The injection mixing station 80 has also at least one inlet channel 84 for receiving injection liquid. The injection liquid may be withdrawn from the headbox feed pipe 38 and pumped by means of a pump 86 to the injection mixing station 80. In accordance with an embodiment of the present invention, the injection liquid is taken from the headbox feed pipe 38 between the stock flow equalizer 50 and the injection mixing station 80 from such a position that the consistency variations in the stock flow have already been equalized. In accordance with another embodiment (shown by broken lines) the injection liquid is taken from the headbox feed pipe upstream of the stock flow equalizer 50. And in accordance with a yet further embodiment the injection liquid is taken from the headbox feed pipe downstream of the injection mixing station 80. The injection mixing station is preferably, but not necessarily, formed of one or more TrumpJet™ injection mixers. The TrumpJet™ injection mixer and its use are discussed in, for instance, European Patent B-1219344.

[0029] FIG. 2B illustrates a partial view of an approach flow system of a fiber web machine in accordance with the present invention. The parts as similar to FIG. 2A but the FIG. 2B presents the other option to perform the method for mixing the at least one additional stock component with the stock before and/or after equalizing consistency differences prevailing in the stock flow downstream of the headbox screen. The arrangement as shown in FIG. 2B presents that the chemical mixer 80 is arranged upstream of the stock flow equalizer 50. For certain type of additional stock components (as fibrous components may be) this is the preferred option while the embodiment of FIG. 2A is the preferred one for some additional stock components. A combination of embodiments of FIGS. 2A and 2B is also possible (not shown in Figures), then the chemical mixer 80 is arranged upstream and downstream of the stock flow equalizer 50. Then at least one but likely a number of additional stock component(s) is mixed with the stock before and after equalizing consistency differences prevailing in the stock flow downstream of the headbox screen 36. This arrangement may be preferred for example for mixing cationic and anionic additional stock components in selected order. It is also possible to double or triple one of chemical mixers if even more additional stock components are needed to be mixed.

[0030] FIG. 3 illustrates a partial cut view of the stock flow equalizer 50 of the present invention. In the embodiment shown in the Figure the stock flow equalizer 50 is fastened by means of flanges 52′ and 52″ to the headbox feed pipe 38. The stock flow equalizer 50 has a tubular wall 54 the diameter of which corresponds to that of the headbox feed pipe 38. The inside surface 56 of the tubular wall 54 is provided with form parts 58, which are, in this embodiment, arranged on the same periphery of the inside surface 56. In another embodiment the form parts are attached directly to the inside surface of the headbox feed pipe so that no additional pipeline flanges are needed, but only the headbox feed pipe is fastened at its first end to the machine screen and at its second end to the headbox. Each form part 58 has a leading surface 60 that is fastened to the inside surface 56 of the tubular wall 54 along its leading edge 62. Arrow F indicates the stock flow direction through the stock flow equalizer 50. Downstream of the leading edge 62 the leading surface 60 is raised from the inside surface 56 such that triangular side surfaces 64′ and 64″ may be provided between the side edges of the leading surface 60 and the inside surface 56. The leading surface 60 tapers towards its trailing tip 66 such that the side surfaces 64′ and 64″ may be fastened to one another at the trailing edge 68 of the form part 58.

[0031] The form parts 58 function (see FIGS. 3, 4a and 4b) such that their leading surfaces 60 raise the stock flow, which is at a lower consistency, from the near-hood of the inside surface 56 closer to the center of the tubular flow pipe to mix the low consistency stock with the higher consistency stock closer to the axis of the flow pipe. At the same time a part of the stock flowing along the leading surfaces 60 meets the side edges 70 between each leading surface 60 and the side surfaces 64′ and 64″, whereby such parts of the stock flow create two counter-rotating vortices at both sides of each form part 58. First the vortices get mixed with the low consistency stock flow that still flows along the inner surface 56 passing the form parts. Later, when the vortices of two neighboring form parts meet one another, the vortices get mixed to one another and create a chaos-like turbulent zone extending downstream of the form parts. Such a turbulent zone extends over the entire diameter of the stock flow equalizer and equalizes the consistency differences there have been. In performed experiments it has been learned that the full equalization of the stock flow requires a distance of at least 1×D, such as 3×D, where D is the diameter of the headbox feed pipe,

[0032] As to the stock flow equalizer 50 it should be understood that the number of form parts 58 thereof may vary from 3-15, the form parts may be arranged on the same circumference of the inside surface 56 of the stock flow equalizer 50, or they may be divided in several groups on several circumferences, or they may be freely arranged in arbitrary positions on the inside surface. Naturally, their axial distance from one another should not be too long, which would reduce the efficiency of the stock flow equalization function. A length of the stock flow equalizer, i.e. from the leading edge of the upstream form part to the trailing tip of the downstream form part may be in a range of 0.5 to 3×D, where D is the diameter of the headbox feed pipe. The radial height of the form parts 58 is may be in a range of 0.1 to 0.5×D, where D is the diameter of the headbox feed pipe. A width of the form part may be in a range of 0.1 to 1×length of the form part. Also the leading surface 60 of the form part is not necessarily planar, but it may be curved, i.e. convex or concave, in either radial or axial cross sections thereof, or in both.

[0033] As already discussed above in connection with FIG. 2A the stock flow optimizer 50 is followed on the headbox feed pipe 38 by an injection mixing station 80. The distance between the stock flow equalizer and the injection mixing station should be arranged such that the chaos-like turbulence has already equalized the consistency but has not dampened to such a degree that the consistency differences had already started forming. In practice the distance from the trailing tip of the last (in the stock flow direction) form part to the injection mixing station may be in a range of 0.5 to 10 times, such as 2 to 5 times, the diameter D of the headbox feed pipe 38. Also, for the optimization of the headbox feed pipe and additional stock component mixing, the stock flow equalizer 50 may be arranged at a distance from the headbox 40. The distance from the injection mixing station 80 to the headbox 20 need to be considered carefully. Naturally, if the stock flow equalizer 50, and the injection mixing station 80 therewith, is brought too close to the headbox, the turbulence caused by the equalizer would have an effect on the stock flows in the headbox, and would make it more difficult to achieve an even basis weight profile to the web to be formed. And if the stock flow equalizer 50, and the injection mixing station therewith, are left too far from the headbox, the stock flow in the headbox feed pipe 38 would have time to start forming consistency differences in the stock flow. Therefore, the distance from the stock flow equalizer 50 to the headbox 20 may be in a range of 5×D to 15×D, where D is the diameter of the headbox feed pipe 38.

[0034] The chemical mixer 80 may be an injection mixing station, which may be formed of a single injection mixer or a set of injection mixers. In narrow pipes a single injection mixer may suffice, but with larger pipes an injection mixing station with several injection mixers on the periphery of the headbox feed pipe are needed. In operation, at least one additional stock component and an injection liquid is brought to the injection mixer, each along its own feed channel. The additional stock component and the injection liquid are introduced with one another via a common nozzle to the equalized stock flow such that the additional stock component is mixed with the injection liquid and the injection liquid, due to its high speed and injection pressure, ensures that the mixture of a relatively small amount of the additional stock component and the injection liquid penetrates deep enough in the equalized stock flow in the headbox feed pipe. The injection liquid may be the same stock to which the additional stock component is to be mixed. Such an injection liquid may be taken upstream of the mixer to be injected by means of the mixer together with the additional stock component to the stock flow in the headbox feed pipe. It was already earlier mentioned that the injection liquid may be taken from the headbox feed pipe either upstream of the stock flow equalizer, between the equalizer and the injection mixing station or downstream of the injection mixing station. Other options for the injection liquid are fresh pulp, recycled pulp, white water, fresh water, etc. just to name a few options without any intention of limiting the applicable liquids to the listed alternatives only.

[0035] It should also be understood that the present invention covers mixing either a single additional stock component or two or more additional stock components to the stock upstream and/or downstream of the stock flow equalizer. In other words, it is possible that in cases where more than one additional stock component is used (in addition to the one mixed downstream of the stock flow equalizer), one additional stock component is mixed to the stock between the headbox screen and the stock flow equalizer and/or one additional stock component is mixed to the stock upstream of the headbox screen. Naturally, it is preferable in these two latter alternatives that the additional stock component is such a slowly reacting one that it functions or forms agglomerations only after the stock flow equalizer.

[0036] And finally, it should also be understood that at least one additional stock component is at least one of retention chemical, sizing agent, like alkenyl succinic anhydride (ASA) or alkyl ketene dimer (AKD), starch, filler, paper dye or pigment, micro- or nano-fibrillated cellulose (MFC, NFC) or other natural/bio-based fiber or synthetic fiber, just to name a few options. These additional stock components may be mixed with the stock either together with another additional stock component(s) or independently thereof. If introduced together with some other additional stock component these may be either premixed with the additional stock component(s) prior to being injected to the stock or just injected together with the additional stock component(s) to the stock.

[0037] It should be also understood that the above presented dimensions in different embodiments in relation to the headbox feed pipe diameter D may vary significantly depending on the actual application. In a small size approach flow systems of a fiber web machine headbox, the diameter D may be 50 to 100 mm. In large fiber web machine, the diameter D may be approximately 1200 mm.

[0038] Although the invention has been described with reference to specific illustrated embodiments, it is emphasized that it also covers equivalents to the disclosed features, as well as changes and variants obvious to a man skilled in the art, and the scope of the invention is only limited by the appended claims.

[0039] While at least one exemplary embodiment of the present invention(s) is disclosed herein, it should be understood that modifications, substitutions and alternatives may be apparent to one of ordinary skill in the art and can be made without departing from the scope of this disclosure. This disclosure is intended to cover any adaptations or variations of the exemplary embodiment(s). In addition, in this disclosure, the terms “comprise” or “comprising” do not exclude other elements or steps, the terms “a” or “one” do not exclude a plural number, and the term “or” means either or both. Furthermore, characteristics or steps which have been described may also be used in combination with other characteristics or steps and in any order unless the disclosure or context suggests otherwise. This disclosure hereby incorporates by reference the complete disclosure of any patent or application from which it claims benefit or priority.