EP3012370B1 - Appareil de recyclage de boues de déchets et procédé de recyclage de boues résiduaires - Google Patents

Appareil de recyclage de boues de déchets et procédé de recyclage de boues résiduaires Download PDF

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Publication number
EP3012370B1
EP3012370B1 EP14189919.5A EP14189919A EP3012370B1 EP 3012370 B1 EP3012370 B1 EP 3012370B1 EP 14189919 A EP14189919 A EP 14189919A EP 3012370 B1 EP3012370 B1 EP 3012370B1
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EP
European Patent Office
Prior art keywords
waste sludge
fiber web
manifolds
waste
headbox
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EP14189919.5A
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German (de)
English (en)
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EP3012370A1 (fr
Inventor
Jin-Doo Kim
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Valmet Technologies Oy
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Valmet Technologies Oy
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Priority to EP14189919.5A priority Critical patent/EP3012370B1/fr
Priority to CN201510507454.2A priority patent/CN105544271B/zh
Publication of EP3012370A1 publication Critical patent/EP3012370A1/fr
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Publication of EP3012370B1 publication Critical patent/EP3012370B1/fr
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    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00—Wet end of machines for making continuous webs of paper
    • D21F1/02—Head boxes of Fourdrinier machines
    • D21F1/022—Means for injecting material into flow within the headbox
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00—Wet end of machines for making continuous webs of paper
    • D21F1/66—Pulp catching, de-watering, or recovering; Re-use of pulp-water
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F9/00—Complete machines for making continuous webs of paper
    • D21F9/003—Complete machines for making continuous webs of paper of the twin-wire type
    • D21F9/006—Complete machines for making continuous webs of paper of the twin-wire type paper or board consisting of two or more layers

Definitions

  • the invention relates to a waste sludge recycling apparatus according to the preamble of claim 1 for forming a multilayer fiber web, and to a waste sludge recycling method according to the preamble of claim 12 for forming a multilayer fiber web.
  • waste sludge such as reject, fines or other materials which are of low quality and are thus not used anymore in the process of manufacturing of fiber web in fiber web plants was deposited at waste dumpsites and/or used as construction material, for example as ground material, in road building.
  • waste sludge was uncomplicated and cheap since only storage places have to be provided in fiber web mills before the waste sludge is transported away by trucks and/or railway to waste dumpsites or road building facilities.
  • the building size of the fiber web plants does not increase.
  • EP 0 479 141 A1 shows a generic waste sludge recycling apparatus according to the preamble of claim 1 for a multilayer headbox being capable of supplying liquids onto a wire in a layered manner for forming a multilayer fiber web and including a plurality of manifolds to form corresponding layers of the multilayer fiber web in a forming section of a fiber web making machine, comprising: a waste sludge recirculation means configured to be connected to at least one of the manifolds of the multilayer headbox for supplying waste sludge to be recycled to the at least one of the manifolds.
  • a generic waste sludge recycling method for forming a multilayer fiber web, comprising: supplying liquids in a layered manner onto a wire of a forming section of a fiber web making machine via a multilayer headbox including a plurality of manifolds to form corresponding layers of the multilayer fiber web, and recirculating and supplying waste sludge to be recycled to at least one of the manifolds of the multilayer headbox.
  • EP 0 751 253 A2 shows a process which utilizes a "non-papermaking" portion of waste paper to produce a highly absorbent, essentially fiber-free granule which can be used, for example, as an agricultural chemical carrier.
  • the process maximizes the amount of long (papermaking) fiber sent to a paper machine.
  • the waste paper is broken up in a hydropulper, and pulp stock is screened so that papermaking fibers are retained and sent forward to the papermaking process, and solid material in a reject stream, such as kaolin clay and inorganic materials pass through a flotation clarifier to separate the solids.
  • the slurry is then dewatered by means of a belt press to form a filter cake.
  • the filter cake then enters a pin mixer where it is broken up into individual granules.
  • the granules are then dried to a solids content of greater than 95%.
  • the inventors of the present invention have surprisingly found that it is possible to maintain strength of a multilayer fiber web, for example, a multiply board web, by even directly adding waste sludge, which has not been used by now in the process of manufacturing of fiber web in fiber web plants, into the layers of the fiber web to be formed in a forming section of the fiber web plant.
  • the strength properties of the fiber web could be maintained or even slightly improved compared to the case in which only filler materials are added to the fiber web.
  • a specified amount of waste sludge can be added to the fiber web while the strength properties of the fiber web can be maintained in the required range.
  • the object of the present invention is achieved by a waste sludge recycling apparatus having the features of claim 1 and by a method for recycling of waste sludge having the features of claim 12.
  • a waste sludge recycling apparatus for a multilayer headbox being capable of supplying liquids onto a wire in a layered manner for forming a multilayer fiber web and including a plurality of manifolds to form corresponding layers of the multilayer fiber web in a forming section of a fiber web making machine.
  • the apparatus comprises a waste sludge recirculation means configured to be connected to at least one of the manifolds of the multilayer headbox for supplying waste sludge to be recycled to the at least one of the manifolds.
  • waste sludge recycling apparatus for a multilayer headbox.
  • This waste sludge recycling apparatus is directly connectable to the multilayer headbox being capable of supplying liquids (such as fiber pulp suspension including fibers, refined fibers, fillers, starch and/or water) onto a wire in a layered manner for forming the multilayer fiber web and including the plurality of manifolds to form corresponding layers of the multilayer fiber web.
  • the waste sludge recycling apparatus comprises the waste sludge recirculation means (including, for example, a piping or line system for supplying waste sludge to be recycled) configured to be connected to at least one of the manifolds of the multilayer headbox.
  • the direct connection of the waste sludge recirculation means to the at least one manifold includes any pipe or line fitting arrangement which is suitable for supplying the waste sludge to be recycled directly into the at least one of the manifolds.
  • This direct connection and supply to the manifold(s) of the multilayer headbox achieves the effect of sufficiently mixing the waste sludge with the fiber pulp suspension directly before being supplied onto the wire in a layered manner.
  • waste sludge compared to the total amount fiber pulp suspension (stock suspension) thus can be supplied and added to the respective layers of the multilayer fiber web.
  • alternative use of waste sludge can be provided and, on the other hand, the amount of pulp can be reduced by maintaining the strength of the fiber web.
  • a further preparation of the waste sludge for disposal or for adding it to a raw material in a stock preparation plant of a forming section can be avoided.
  • the cost for such a preparation can be saved.
  • the present invention will be useable with any multilayer headbox being capable of supplying liquids onto a wire in a layered manner for forming a multilayer fiber web and including a plurality of manifolds to form corresponding layers of the multilayer fiber web in a forming section of a fiber web making machine.
  • the supplied waste sludge can be suitably mixed with the respective liquids (fiber pulp suspension, water, etc.) in a feed line in and directly before the manifolds.
  • the waste sludge recirculation means is connectable (i.e.
  • the waste sludge being supplied by the waste sludge recirculation means is mixed with the white water and/or stock suspension in the feed line for the water and/or stock suspension and/or direct in the headbox.
  • the waste sludge recirculation means is configured to be directly connected (mounted, fixed, attached) to at least one of the manifolds of the multilayer headbox and/or the mentioned feed line just (directly) before the respective liquid flows into the manifold(s) for further mixing the waste sludge and the white water and/or stock suspension.
  • such a headbox has a vane construction by which at boundaries of the fiber web, suspension layers to be formed the respective layers do not get mixed with adjacent fiber web suspension layers.
  • the individual fiber web suspension layers stay separated from each other in the multilayer headbox. Accordingly, the different fiber web suspension layers can be supplied to a wire in a forming section in a layered manner, thus maintaining the purity and characteristic of the individual liquid layers.
  • the plurality of manifolds of the multilayer headbox includes at least a bottom manifold to form a bottom layer of the fiber web, a middle manifold to form a middle layer of the fiber web, and a top manifold to form a top layer of the fiber web, and the waste sludge recirculation means is configured to be connected to the middle manifold of the multilayer headbox for supplying waste sludge to be recycled to the middle manifold.
  • the waste sludge recirculation means is configured to be connected to at least the middle manifold of the multilayer headbox.
  • an amount of waste sludge of 5 - 15% in the middle layer can be achieved, since by adding such an amount of waste sludge strength of fiber web can be maintained and waste sludge is comparably cheap with respect to common fillers, starch or refined fibers.
  • the middle layer of the web is commonly a water layer
  • waste sludge in the amount of 5 - 15% of the total amount of materials of the layer can be added to the middle layer (here the water layer, for example white water layer) in order to provide a suitable recycling process for the waste sludge.
  • This adding of waste sludge to the water layer is acceptable in view of purity and quality of the multiply board, wherein the strength of the board can be maintained or slightly increased due to the adding of the waste sludge.
  • a preferable solution is that white water is fed to the middle manifold of the headbox which may be directly taken from a white water pit in the forming section.
  • the waste sludge recirculation means is connected with said manifold so that the supplied waste sludge is mixed with the white water to form the middle layer inside the fiber web.
  • the inventors have found that, since a white water layer consistency is so low (fiber consistency of white water is less than 0.5%) that it would not form a separate fiber layer but it is sufficient to separate bottom and top layers of the fiber web from each other, when adding waste sludge to this middle layer, the waste sludge stably remains in this layer and thus between the bottom and top layers. Thus, an amount of waste sludge of 5 - 15% in the middle layer can be preferably added. It is also possible to add chemicals, etc. to this "white water layer" for improving web properties and quality.
  • a typical stock suspension (fiber pulp suspension) is supplied to the middle manifold and thus the waste sludge supplied via the waste sludge recirculation means connected to said manifold of the headbox is mixed into the fiber pulp suspension to form the middle layer of the fiber web.
  • the waste sludge recirculation means includes a waste sludge recirculation line, a waste sludge recirculation control valve for adjusting an amount of waste sludge to be supplied to the respective manifold(s), and a waste sludge feeding pump for feeding the waste sludge to the manifold.
  • a waste sludge recirculation line for adjusting an amount of waste sludge to be supplied to the respective manifold(s)
  • a waste sludge feeding pump for feeding the waste sludge to the manifold.
  • the amount and flow speed of the waste sludge to be supplied to the headbox can suitably be adjusted by means of the waste sludge feeding pump and the waste sludge recirculation control valve.
  • the valve and the pump can be turned off in case the fiber pulp suspension has already a content at its lower quality range.
  • supply of waste sludge can suitably be controlled.
  • each of the manifolds of the multilayer headbox has a diffuser as a turbulence generator creating turbulence in liquids supplied into each respective manifold, each of the diffusers having an outlet into a nozzle chamber of the multilayer headbox.
  • Each of these diffusers creates turbulence in liquids supplied into each respective diffuser.
  • the waste sludge recirculation means includes a separating means for separating fines from white water of the fiber web making machine, the separating means being configured to be connected to the at least one of the manifolds of the multilayer headbox to supply the fines to the at least one of the manifolds.
  • the separated fines can directly be supplied to the at least one of the manifolds.
  • the waste sludge can already be pre-cleaned and filtered so that waste water cleaning and waste sludge disposal process of the whole fiber web making machine can be further optimized.
  • the separating means includes a clarifier, preferably a disc filter, separating the fines from the white water.
  • a clarifier preferably a disc filter
  • Commonly known disc filters have a high capacity for cleaning fines from white water so that they are preferably used for separating the fines from the white water.
  • the separating means further includes a fines recirculation line connecting the clarifier with the at least one of the manifolds of the headbox, a fines recirculation control valve for adjusting an amount of fines to be supplied to the respective manifold(s), and a fines feeding pump for feeding the fines to the manifold(s) via the fines recirculation line.
  • a desired amount of fines can be supplied to the respective manifold(s). That is, the amount and flow speed of the fines to be supplied to the headbox can suitably be adjusted by means of the fines feeding pump and the fines recirculation control valve.
  • supply of fines can be suitably controlled.
  • the waste sludge recycling apparatus further comprises a waste water treatment means in which waste water from the fiber web making machine and/or recycled fiber plant and/or stock preparation plant is collected and clarified, the waste water treatment means including a flotation means for separating the waste sludge from the waste water, and the flotation means being connected to the waste sludge recirculation means to supply the separated waste sludge to the at least one of the manifolds of the multilayer headbox.
  • a waste water treatment means in which waste water from the fiber web making machine and/or recycled fiber plant and/or stock preparation plant is collected and clarified
  • the waste water treatment means including a flotation means for separating the waste sludge from the waste water
  • the flotation means being connected to the waste sludge recirculation means to supply the separated waste sludge to the at least one of the manifolds of the multilayer headbox.
  • the waste sludge recirculation means further includes a waste sludge recirculation line connecting the flotation means with the at least one of the manifolds of the headbox, a waste sludge recirculation control valve for adjusting an amount of waste sludge to be supplied to the manifold, and a waste sludge feeding pump for feeding the waste sludge to the manifold via the waste sludge recirculation line.
  • an appropriate amount of waste sludge to be supplied to the manifold can be suitably adjusted, for example, on the basis of quality of raw material for forming the fiber web, the quality and content of the fiber pulp suspension being, for example, produced in a stock preparation plant, the quality of the web to be formed, etc.
  • the amount and flow speed of the waste sludge to be supplied to the headbox can be suitably controlled and adjusted by means of the waste sludge feeding pump and the waste sludge recirculation control valve.
  • the waste water treatment means and the separating means are connected with the at least one of the manifolds of the headbox via a common supply line merging the waste sludge recirculation line and the fines recirculation line.
  • a common supply line merging the waste sludge recirculation line and the fines recirculation line.
  • the separating means is configured to be connected to a twin-wire former or a fourdrinier former for recirculating white water cleaned by the separating means to the gap former or the hybrid former as process water of the forming section.
  • the thus cleaned and recirculated white water can be used as process water in the forming section, preferably it is used as so-called "shower water” in the twin-wire former or fourdrinier former in order to decrease the amount of fresh water to be used in such formers.
  • a forming section of a fiber web making machine which comprises at least one wire arranged in a wire loop for forming a fiber web from a fiber suspension, a multilayer headbox being capable of supplying liquids onto the wire in a layered manner for forming a multilayer fiber web and including a plurality of manifolds to form corresponding layers of the multilayer fiber web, and the waste sludge recycling apparatus according to the present invention.
  • any of the advantages described above with regard to the waste sludge recycling apparatus according to the invention can suitably be achieved.
  • a waste sludge recycling method for forming a multilayer fiber web comprises the steps of supplying liquids in a layered manner onto a wire of a forming section of a fiber web making machine via a multilayer headbox including a plurality of manifolds to form corresponding layers of the multilayer fiber web, and recirculating and supplying waste sludge to be recycled to at least one of the manifolds of the multilayer headbox.
  • the layers are formed onto the wire via the plurality of manifolds including at least a bottom manifold to form a bottom layer of the fiber web, a middle manifold to form a middle layer of the fiber web, and a top manifold to form a top layer of the fiber web, and thus comprising at least the bottom layer, the middle layer, and the top layer, the bottom layer and the top layer being separated by the middle layer, and the waste sludge to be recycled is recirculated and supplied to the middle manifold to form the middle layer of the fiber web.
  • waste sludge is directly added (recycled) to the at least one of the manifolds of the headbox so that the waste sludge can be directly mixed with the liquid (i.e. fiber pulp suspension, water, etc.) in said manifold(s) before supplying the thus mixed liquid including the waste sludge by means of the headbox to form corresponding layers of a multilayer web.
  • liquid i.e. fiber pulp suspension, water, etc.
  • Fig. 1 is a schematic view of a forming section of a fiber web making machine in which a waste sludge recycling apparatus for a multilayer headbox being capable of supplying liquids onto a wire in a layered manner for forming a multilayer fiber web and including a plurality of manifolds to form corresponding layers of the multilayer fiber web according to an embodiment of the invention is used.
  • Fig. 1 the forming section of a fiber web making machine is schematically shown.
  • the forming section comprises a web forming machine (liner machine) 10, in which a headbox 20 is included.
  • the web forming machine may be provided as a twin-wire former or a fourdrinier former.
  • the headbox 20 is separately illustrated from the web forming machine 10. However, it is to be understood that, in general, the headbox 20 may form an integral or separate part of the web forming machine 10.
  • the headbox 20 shown in Fig. 1 is a multilayer headbox 20 which inter alia includes a bottom manifold 201, a middle manifold 202 and a top manifold 203.
  • the multilayer headbox 20 is capable of supplying liquids (such as fiber pulp suspension including fibers, refined fibers, fillers, starch and/or water) onto a wire (not shown) in a layered manner for forming a multilayer fiber web (not shown).
  • the multilayer headbox 20 includes the bottom manifold 201 to form a bottom layer of the fiber web, the middle manifold 202 to form a middle layer of the fiber web, and the top manifold 203 to a form a top layer of the fiber web.
  • the forming section shown in Fig. 1 includes a stock preparation plant (means) 40 to which raw material 50 consisting of, for example, fresh fibers, recycled fibers, old carton boards, old papers, etc. for forming a stock preparation in the stock preparation plant 40 is supplied.
  • raw material 50 consisting of, for example, fresh fibers, recycled fibers, old carton boards, old papers, etc.
  • a fiber pulp including fibers, refined fibers, fillers, starch and/or water or the like is generated in a known manner. Therefore, the supply of the raw material 50 to the stock preparation plant 40 as well as the structure and functions of the stock preparation plant 40 for generating the fiber pulp are generally known and are not further described.
  • the web forming section shown in Fig. 1 also includes a waste water treatment means 60 including a flotation means 601 and an aerobic treatment means 602.
  • the stock preparation plant 40 is connected with the waste water treatment means 60 via a waste water and sludge feeding line 401 (see thin solid line in Fig. 1 reaching from the stock preparation plant 40 to the waste water treatment means 60).
  • This waste water and sludge feeding line 401 supplies waste water including waste sludge (fiber web waste sludge) generated as excess material in the stock preparation plant 40 to the flotation means 601 of the waste water treatment means 60.
  • the flotation means 601 separates the waste sludge from the waste water in a usual flotation process.
  • the web forming machine 10 is connected to the waste water treatment means 60, in particular to the flotation means 601 of the waste water treatment means 60, via a waste water and sludge feeding line 305 (see thick solid line in Fig. 1 reaching from the web forming machine 10 to the waste water treatment means 60).
  • This waste water and sludge feeding line 305 supplies waste water and waste sludge from the web forming machine 10 to the flotation means 601 in order to separate the waste sludge from the waste water within the flotation means 601.
  • the waste sludge has been separated from the waste water and the waste water is further supplied to the aerobic treatment means 602 in order to clarify the waste water under aerobic conditions within the aerobic treatment means 602.
  • the thus clarified water can be fed again as process water into the forming section of the fiber web making machine, for example.
  • the waste water treatment means 60 is (directly) connected to the headbox 20 via a waste sludge recirculation means (forming a "waste sludge recycling apparatus") for supplying waste sludge to be recycled from the waste water treatment means 60 to the headbox 20.
  • a waste sludge recirculation line 603 is provided between the waste water treatment means 60 and the headbox 20.
  • the waste sludge recirculation line 603 is connected to a white water and/or stock suspension feeding line 30 in which white water and/or stock suspension (fiber suspension) is fed to the headbox 20, in particular, to the middle manifold 202 of the headbox 20.
  • the waste sludge recirculation line 603 contains the waste sludge supplied from the flotation means 601 and is mixed with the white water and/or stock suspension fed in the white water and/or stock suspension feeding line 30 upstream of the headbox 20, i.e. directly (immediately) before the manifold 202.
  • the waste sludge recirculation line 603 is connected to the flotation means 601 and to the middle manifold 202 of the headbox 20.
  • the waste sludge recirculation line 603 may be directly connected to at least one of the manifolds 201 to 203 of the headbox 20.
  • the waste sludge recirculation means is connected to at least one of the manifolds 201 to 203 of the headbox 20 for supplying the waste sludge to be recycled to the at least one of the manifolds 201 to 203.
  • a separating means for separating fines from excess white water (waste water) from the web forming machine 10 can be provided.
  • this separating means includes a clarifier 301 or filter means 301 for separating the fines from the white water.
  • the clarifier may be a commonly known disc filter having a high capacity for cleaning fines from white water so that such a filter constitution is preferably used for separating the fines from the white water.
  • the clarifier 301 is connected to the web forming machine 10 via an excess white water feeding line 304 for feeding the excess white water from the web forming machine 10 to the clarifier 301.
  • the excess white water is separated into fines (which are part of "fine sludge" of the waste sludge) and clarified white water.
  • the clarified white water can be supplied (recycled, recirculated) back to the web forming machine 10 via a white water recirculation line 303.
  • This white water recirculation line 303 acts as a process water recirculation line.
  • the separating means is configured to be connected to a twin-wire former or a fourdrinier former as the web forming machine for recirculating white water cleaned by the separating means to the gap former or the hybrid former as process water of the forming section.
  • the cleaned and recirculated white water can be used as process water in the forming section; preferably it is used as so-called "shower water” in the twin-wire former or fourdrinier former in order to decrease the amount of fresh water to be used in such formers.
  • the fines being separated within the clarifier 301 from the white water (process water) can directly be supplied to the headbox 20 via a fines recirculation line 302.
  • the fines are supplied to the headbox via the fines recirculation line 302 being connected to the white water and/or stock suspension feeding line 30 so that the fines can be mixed in a similar way as the waste sludge solely or in addition to the mixing of the waste sludge with the white water and/or stock suspension directly before feeding the thus mixed liquid to the headbox 20.
  • the fines recirculation line 302 may be directly connected to at least one of the manifolds 201 to 203 of the headbox 20.
  • the fines recirculation line 302 is connected to the waste sludge recirculation line 603 at an upstream part of the middle manifold 202 of the headbox 20. That is, the waste water treatment means 60 and the separating means are connected with at least one of the manifolds 201 to 203 of the headbox 20 via a common supply line 400 merging the waste sludge recirculation line 603 and the fines recirculation line 302.
  • the fines can be separated in the separate clarifier 301 without being supplied to the waste water treatment means 60 so that the fines to be separated in the clarifier 301 can directly be supplied to the headbox 20.
  • the common supply line 400 the amounts of fines and waste sludge can be pre-mixed before they are entering the respective manifold of the headbox 20.
  • the waste sludge recirculation means including the waste sludge recirculation line 603 may also include a waste sludge recirculation control valve (not shown) for adjusting an amount of waste sludge to be supplied to the manifold 202 and a waste sludge feeding pump (not shown) for feeding the waste sludge to the manifold 202.
  • an appropriate amount of waste sludge to be supplied to the manifold 201 can suitably be adjusted in a known manner, for example, on the basis of quality of raw material for forming the fiber web, the quality and content of the fiber pulp suspension being, for example, produced in the stock preparation plant 40, the quality of the web to be formed, etc. That is, the amount and flow speed of the waste sludge to be supplied to the headbox 20 can suitably be adjusted by means of the waste sludge feeding pump and the waste sludge recirculation control valve. Thus, supply of waste sludge can suitably be controlled.
  • the separating means including the fines recirculation line 302 connecting the clarifier 301 with the headbox 20 may include a fines recirculation control valve (not shown) for adjusting an amount of fines to be supplied to the manifold 201 and a fines feeding pump (not shown) for feeding the fines to the manifold 201 via the fines recirculation line 302.
  • a fines recirculation control valve (not shown) for adjusting an amount of fines to be supplied to the manifold 201
  • a fines feeding pump (not shown) for feeding the fines to the manifold 201 via the fines recirculation line 302.
  • the feeding amount of fines can be controlled from 0 to 100% by adjusting the valve position of the fines recirculation control valve and/or the feeding amount of waste sludge can be controlled from 0 to 100% by adjusting the waste sludge recirculation control valve as well.
  • the forming section may further comprise at least one wire arranged in a wire loop for forming a fiber web from a fiber suspension, onto which wire the headbox is capable of supplying liquids onto the wire in a layered manner for forming a fiber web on the wire.
  • the above described multilayer headbox according to the present embodiment is a three-layer headbox.
  • the multilayer headbox may also be formed as a two-layer headbox or as a headbox suitable for forming more than three layered fiber web.
  • the waste sludge may come directly, i.e. may be supplied from a recycled fiber plant (for example from OCC-/DIP-plants) via the waste sludge recycling apparatus (forming) as the waste sludge recirculation means to the manifold(s) of the headbox.
  • this waste sludge may be separated before the waste water treatment means and directly supplied to the manifold(s) via, for example, separate waste sludge recirculation lines of the waste sludge recirculation means.
  • a structure for direct connection between the web forming machine (liner machine), the recycled fiber plant and/or the waste water treatment means or the like for supplying waste sludge to at least one of the manifolds of the multilayer headbox is provided.

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Claims (12)

  1. Appareil de recyclage de boues excédentaires destiné à un réservoir d'alimentation à couches multiples (20) capable de fournir des liquides à une toile, de manière hiérarchisée, afin de former une bande de fibres à plusieurs couches et comprenant une pluralité de collecteurs (201, 202, 203) destinés à former des couches correspondantes de la bande de fibres à plusieurs couches dans une section de formation d'une machine de fabrication de bande de fibres, comprenant :
    un moyen de recirculation de boues excédentaires configuré pour être relié à au moins l'un des collecteurs (201, 202, 203) du réservoir d'alimentation à couches multiples (20) destiné à fournir des boues excédentaires à recycler à l'un des collecteurs (201, 202, 203) au moins,
    dans lequel
    la pluralité de collecteurs (201, 202, 203) du réservoir d'alimentation à couches multiples (20) comprend au moins un collecteur inférieur (201) destiné à former une couche inférieure de la bande de fibres, un collecteur intermédiaire (202) destiné à former une couche intermédiaire de la bande de fibres, et un collecteur supérieur (203) destiné à former une couche supérieure de la bande de fibres, caractérisé en ce que le moyen de recirculation de boues excédentaires est configuré pour être relié au collecteur intermédiaire (202) du réservoir d'alimentation à couches multiples (20) destiné à fournir des boues excédentaires à recycler au collecteur intermédiaire (202).
  2. Appareil de recyclage de boues excédentaires selon la revendication 1, dans lequel le moyen de recirculation de boues excédentaires comprend une conduite de recirculation de boues excédentaires (30), une soupape de commande de recirculation de boues excédentaires destinée à ajuster une quantité de boues excédentaires à fournir à l'un des collecteurs (201, 202, 203) au moins, et une pompe d'alimentation en boues excédentaires destinée à fournir les boues excédentaires à au moins l'un des collecteurs (201, 202, 203).
  3. Appareil de recyclage de boues excédentaires selon la revendication 1 ou 2, dans lequel chacun des collecteurs (201, 202, 203) du réservoir d'alimentation à couches multiples (20) possède un diffuseur en guise de générateur de turbulence qui crée une turbulence dans les liquides fournis à chaque collecteur respectif (201, 202, 203), chacun des diffuseurs ayant une évacuation dans une chambre de buse du réservoir d'alimentation à couches multiples (20).
  4. Appareil de recyclage de boues excédentaires selon l'une quelconque des revendications précédentes, dans lequel le moyen de recirculation de boues excédentaires comprend un moyen de séparation (301) destiné à séparer les fines de l'eau blanche de la machine de fabrication de bande de fibres, le moyen de séparation (301) étant configuré pour être relié à au moins l'un des collecteurs (201, 202, 203) du réservoir d'alimentation à couches multiples (20) destiné à fournir les fines à l'un des collecteurs (201, 202, 203) au moins.
  5. Appareil de recyclage de boues excédentaires selon la revendication 4, dans lequel le moyen de séparation (301) comprend un clarificateur, de préférence un filtre à disque, qui sépare les fines de l'eau blanche.
  6. Appareil de recyclage de boues excédentaires selon la revendication 5, dans lequel le moyen de séparation (301) comprend en outre une conduite de recirculation de fines (302) qui relie le clarificateur à au moins l'un des collecteurs (201, 202, 203) du réservoir d'alimentation (20), une soupape de commande de recirculation de fines destinée à ajuster une quantité de fines à fournir à au moins l'un des collecteurs (201, 202, 203), et une pompe d'alimentation en fines destinée à fournir les fines à l'un des collecteurs (201, 202, 203) au moins via la conduite de recirculation de fines (302).
  7. Appareil de recyclage de boues excédentaires selon l'une quelconque des revendications précédentes, comprenant en outre un moyen de traitement d'eaux usées (60) dans lequel les eaux usées provenant de la machine de fabrication de bande de fibres et/ou de l'unité de fibres recyclées et/ou de l'unité de préparation de stock sont collectées et clarifiées, le moyen de traitement d'eaux usées (60) comprenant un moyen de flottation (601) destiné à séparer les boues excédentaires des eaux usées, et le moyen de flottation (601) étant relié au moyen de recirculation de boues excédentaires afin de fournir les boues excédentaires séparées à l'un des collecteurs (201, 202, 203) au moins du réservoir d'alimentation à couches multiples (20).
  8. Appareil de recyclage de boues excédentaires selon la revendication 7, dans lequel le moyen de recirculation de boues excédentaires comprend en outre une conduite de recirculation de boues excédentaires (30) qui relie le moyen de flottation (601) à l'un des collecteurs (201, 202, 203) au moins du réservoir d'alimentation (20), une soupape de commande de recirculation de boues excédentaires destinée à ajuster une quantité de boues excédentaires à fournir à l'un des collecteurs au moins (201, 202, 203), et une pompe d'alimentation en boues excédentaires destinée à fournir les boues excédentaires à l'un des collecteurs au moins (201, 202, 203) via la conduite de recirculation de boues excédentaires (30).
  9. Appareil de recyclage de boues excédentaires selon la revendication 8, dans lequel le moyen de traitement d'eaux usées (60) et le moyen de séparation (301) sont reliés à l'un des collecteurs (201, 202, 203) au moins du réservoir d'alimentation (20) via une conduite d'alimentation commune (400) qui fusionne la conduite de recirculation de boues excédentaires (30) et la conduite de recirculation de fines (302).
  10. Appareil de recyclage de boues excédentaires selon l'une quelconque des revendications 4 à 9, dans lequel le moyen de séparation (301) est configuré pour être relié à un formeur à double toile (10) ou une table de fabrication (10) afin de remettre en circulation l'eau blanche épurée par le moyen de séparation (301) vers le formeur à espace (10) ou le formeur hybride (10) sous forme d'eau de traitement de la section de formation.
  11. Section de formation d'une machine de fabrication de bande de fibres, comprenant :
    au moins une toile prévue dans une boucle destinée à former une bande de fibres à partir d'une suspension de fibres,
    un réservoir d'alimentation à couches multiples (20) capable de fournir des liquides à la toile, de manière hiérarchisée, afin de former une bande de fibres à plusieurs couches et comprenant une pluralité de collecteurs (201, 202, 203) destinés à former les couches correspondantes de la bande de fibres à couches multiples, et
    l'appareil de recyclage de boues excédentaires selon l'une quelconque des revendications précédentes.
  12. Procédé de recyclage de boues excédentaires destiné à former une bande de fibres à plusieurs couches, comprenant :
    la fourniture de liquides, de manière hiérarchisée, à une toile d'une section de formation d'une machine de fabrication de bande de fibres via un réservoir d'alimentation à couches multiples (20) comprenant une pluralité de collecteurs (201, 202, 203) destinés à former les couches correspondantes de la bande de fibres à plusieurs couches, et
    la recirculation et la fourniture de boues excédentaires à recycler à au moins l'un des collecteurs (201, 202, 203) du réservoir d'alimentation à couches multiples (20),
    dans lequel
    les couches sont formées sur la toile via la pluralité de collecteurs (201, 202, 203) comprenant au moins un collecteur inférieur (201) destiné à former une couche inférieure de la bande de fibres, un collecteur intermédiaire (202) destiné à former une couche intermédiaire de la bande de fibres, et un collecteur supérieur destiné à former une couche supérieure (203) de la bande de fibres, et comprenant ainsi au moins la couche inférieure (201), la couche intermédiaire (202) et la couche supérieure (203), la couche inférieure (201) et la couche supérieure (203) étant séparées par la couche intermédiaire (202), et
    les boues excédentaires à recycler sont remises en circulation et fournies au collecteur intermédiaire (202) afin de former la couche intermédiaire de la bande de fibres.
EP14189919.5A 2014-10-22 2014-10-22 Appareil de recyclage de boues de déchets et procédé de recyclage de boues résiduaires Active EP3012370B1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP14189919.5A EP3012370B1 (fr) 2014-10-22 2014-10-22 Appareil de recyclage de boues de déchets et procédé de recyclage de boues résiduaires
CN201510507454.2A CN105544271B (zh) 2014-10-22 2015-08-18 污泥回收设备和废污泥的回收方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP14189919.5A EP3012370B1 (fr) 2014-10-22 2014-10-22 Appareil de recyclage de boues de déchets et procédé de recyclage de boues résiduaires

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EP3012370A1 EP3012370A1 (fr) 2016-04-27
EP3012370B1 true EP3012370B1 (fr) 2018-08-15

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CN106245400B (zh) * 2016-08-26 2018-01-02 盐城市光华卫星设备有限公司 一种浆渣与回用白水分离装置

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DE4031310C2 (de) * 1990-10-04 1994-08-25 Escher Wyss Gmbh Verfahren zur Erzeugung von mindestens zwei Sorten wässriger Stoffsuspensionen
US5882480A (en) * 1993-09-09 1999-03-16 Marcal Paper Mills, Inc. Process for making granular material
CA2176435C (fr) * 1995-06-07 2002-01-22 Edward G. Knapick Materiau granulaire absorbant et procede et appareil de fabrication
SE506322C2 (sv) * 1996-03-08 1997-12-01 Valmet Karlstad Ab Anordning för matning av mäld till en inloppslåda i en pappersmaskin
FI110704B (fi) * 1996-10-18 2003-03-14 Metso Paper Inc Monikerrosperälaatikon massansyöttöjärjestelmä ja menetelmä monikerrosperälaatikkokäytössä
FI125215B (fi) * 2011-11-02 2015-07-15 Valmet Technologies Inc Kuiturainakoneen perälaatikko
EP2784213B1 (fr) * 2013-03-28 2016-05-18 Valmet Technologies, Inc. Caisse de tête pour une machine de production d'une bande de matière fibreuse

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CN105544271B (zh) 2018-01-02
EP3012370A1 (fr) 2016-04-27

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