EP1887130B1 - Verfahren zur Entfernung von Tensiden während der Herstellung von Papier in einer Papiermaschine und Papiermaschine zur Durchführung des Verfahrens - Google Patents
Verfahren zur Entfernung von Tensiden während der Herstellung von Papier in einer Papiermaschine und Papiermaschine zur Durchführung des Verfahrens Download PDFInfo
- Publication number
- EP1887130B1 EP1887130B1 EP07301077A EP07301077A EP1887130B1 EP 1887130 B1 EP1887130 B1 EP 1887130B1 EP 07301077 A EP07301077 A EP 07301077A EP 07301077 A EP07301077 A EP 07301077A EP 1887130 B1 EP1887130 B1 EP 1887130B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- papermaking machine
- paper
- flotation
- manufacturing paper
- surface active
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000004094 surface-active agent Substances 0.000 title claims abstract description 31
- 238000000034 method Methods 0.000 title claims abstract description 26
- 238000004519 manufacturing process Methods 0.000 title claims description 19
- 238000005188 flotation Methods 0.000 claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000000835 fiber Substances 0.000 claims abstract description 8
- 238000000926 separation method Methods 0.000 claims abstract description 8
- 238000001914 filtration Methods 0.000 claims abstract description 6
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000003643 water by type Substances 0.000 claims description 9
- 239000013543 active substance Substances 0.000 claims description 6
- 239000010802 sludge Substances 0.000 claims description 5
- 229920001131 Pulp (paper) Polymers 0.000 claims description 3
- 239000013505 freshwater Substances 0.000 claims description 2
- 238000011144 upstream manufacturing Methods 0.000 claims 1
- 239000006260 foam Substances 0.000 abstract description 13
- 239000003795 chemical substances by application Substances 0.000 abstract description 3
- 238000000746 purification Methods 0.000 abstract description 3
- 230000015572 biosynthetic process Effects 0.000 abstract description 2
- 239000002002 slurry Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 description 10
- 239000007787 solid Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 2
- 238000009300 dissolved air flotation Methods 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 239000007767 bonding agent Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 239000002761 deinking Substances 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000000976 ink Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 235000015927 pasta Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Images
Classifications
-
- 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
- D21F1/70—Pulp catching, de-watering, or recovering; Re-use of pulp-water by flotation
Definitions
- the present invention relates to an improved method of making paper on machine, as well as the paper machine adapted to the implementation of such a method.
- the invention uses the technique of dispersed air flotation, making it possible to rid the water used in the manufacture of paper of surfactants.
- these substances tend to stabilize any air bubble introduced into the head circuits, especially when the dough is highly sheared as in a binder, a pump, .... This therefore requires the availability of deaerators usually placed just before the headbox.
- the surfactants remain within the suspension or process water and accumulate in the top circuits.
- the document DE-A-199 14 779 discloses a method of making paper on a machine comprising, in the wet part, a white water flotation step, as well as a paper machine comprising, in its wet part, a white water flotation cell.
- the invention therefore relates to a method for producing paper on a machine comprising in the wet part at least one step of separating the surfactant substances present in the white water by dispersed air flotation.
- surfactant substances means chemical compounds which, introduced into a liquid, lower the surface tension, which has the effect of increasing the wetting properties.
- fatty acids or nonionic surfactants can for example be fatty acids or nonionic surfactants. These substances are found in large quantities in the process water when the pulp used for the manufacture of the paper is recycled pulp. Indeed, in addition to the substances added voluntarily during deinking, other surfactants are "salted out” by the recovered papers (surfactants put into the formulation of printing inks, in the formulation of the layers applied to the surface of the paper for manufacturing magazine papers) and also released by mechanical pulp fibers when they are obtained (defibration, refining) or bleaching.
- the surface-active substances have no potential beneficial effect, even if present in a small amount.
- the object of the invention is therefore the total elimination of the surface-active substances present in the waters used for papermaking, after separation.
- the step of separating the surfactant substances is carried out using the technique of dispersed air flotation.
- This technique consists in separating the surfactants from the water containing them, dragging them to the surface by the insufflation, within the liquid mass, of air bubbles having a diameter that may range from a few hundred microns a few millimeters. This results in a flotation foam rich in isolated surfactant substances. This foam is then separated from the treated liquid, for example by suction or overflow.
- Another contribution of the invention has been to determine the most judicious places of the papermaking process, where the dispersed air flotation treatment has to be carried out.
- the treatment is carried out on a stream with a low content of suspended solids.
- the surfactant removal process must concentrate the rich surfactant-rich rejection as much as possible.
- the dispersed air flotation treatment is carried out on all or part of the white water.
- the step of separating surfactants by dispersed air flotation is carried out directly on the filtration water, from the web or table forming paper, before their recirculation and recycling.
- a second possibility, even more efficient, is to implement this air flotation dispersed on the water of the fiber recuperator, at the machine head, at the level of the white water circuit of the paper machine.
- the recovery of the fibers can be carried out either with the aid of a disk filter or with a dissolved air flotation cell.
- the water from this fiber recuperator is therefore depleted of suspended solids, which makes it possible to limit the losses in solids.
- the dispersed air flotation generates a so-called flotation foam in which the surface-active substances are trapped in concentrated form.
- these foams are intended to be eliminated after recovery, typically by overflow or by suction.
- a method according to the invention provides for the evacuation of this flotation foam directly in a purification plant.
- the flotation foam is pretreated with ozone, which facilitates the degradation of the surfactants.
- Another possibility is to introduce this flow in the middle of the sludge dewatering table, to drain the surfactants into the sludge.
- the invention relates to a paper machine adapted to the implementation of the method described above.
- a paper machine according to the invention is therefore characterized by the presence in its wet part of at least one cell adapted to dispersed air flotation allowing the separation of surfactants present in white water.
- such a cell is designed to have contact time between air bubbles and water to be treated, sufficiently long.
- all surfactants even with slow adsorption kinetics, have time to migrate to the air / water air bubble interfaces.
- the rate of air introduced into the cell must be large enough for the adsorption surface of the surfactants to be sufficient. In order to minimize water losses, several stages are necessary. One of the ways of minimizing water losses is also to have a cell with a sufficient foam thickness to dry the concentrated foam in surfactants.
- the dispersed air flotation cell as described above, is advantageously positioned at the level of the white water circuit, in particular at the level of the filtration water coming from the paper forming fabric, before it is put back into circulation and recycled.
- the flotation cell is located on the clarified water circuit from the fiber recuperator, so as to minimize material losses.
- the paper machine according to the invention is advantageously provided with a system for recovering foams generated by the dispersed air flotation cell.
- a system for recovering foams generated by the dispersed air flotation cell According to a first system, it is a connection between the flotation cell and a purification plant, preferably via an ozone treatment unit.
- the flotation cell is connected to a sludge dewatering table.
- the present invention relates to any type of paper machines. More particularly targeted by the present invention, paper machines or processes consuming small amounts of fresh water, or even operating in a closed circuit. It is in these conditions that the waters are the most loaded with surfactants.
- the invention is also very useful and efficient when the paper is formed from recycled (especially de-inked) or mechanical pasta (wood pulp, ).
- a third application also seems particularly suitable: during the manufacture of coated papers from virgin pastes, the process can be implemented on the thickening waters, generated during the recycling of the manufacturing breakages to be thickened.
- the figure 1 illustrates a paper machine according to the invention for the implementation of the advantageous paper manufacturing method as described.
- the paper machine according to the invention is conventionally equipped with a headbox (1) providing a homogeneous distribution of the paste over the entire width of the paper forming table (2), a press section ( 3) to remove water by pressing and a dryer (4) to remove the residual water by evaporation before winding the roll paper (5).
- the filtration water beneath the forming fabric is recovered for recycling and to dilute the pulp in the head circuits, before the hydrocyclones (6) and the machine head files (7) for removing contaminants with a higher density. to 1 on the one hand and the contaminants of size greater than 150 - 200 microns on the other hand.
- the filtration water under the forming fabric is either recycled directly without any treatment, or clarified by the clarifier, in this case a dissolved air flotation cell (8).
- the flotation treatment of water can then be carried out on all or part of the stream of white water recovered under the formation web (9A ), or all or part of the flow of water free of suspended matter, at the outlet of the clarifier (9B).
Landscapes
- Paper (AREA)
Claims (14)
- Verfahren zur maschinellen Papierherstellung, das im nassen Teil mindestens einen Schritt der Abtrennung der im Siebwasser vorhandenen oberflächenaktiven Substanzen durch Flotation mit dispergierter Luft umfasst.
- Verfahren zur maschinellen Papierherstellung nach Anspruch 1, dadurch gekennzeichnet, dass der Schritt der Abtrennung der oberflächenaktiven Substanzen an dem gesamten Siebwasser oder einem Teil davon durchgeführt wird.
- Verfahren zur maschinellen Papierherstellung nach einem der Ansprüche 1 und 2, dadurch gekennzeichnet, dass der Schritt der Abtrennung der oberflächenaktiven Substanzen an dem aus dem Schritt der Bildung des Papiers stammenden Filterwasser vorgenommen wird.
- Verfahren zur maschinellen Papierherstellung nach einem der Ansprüche 1 und 2, dadurch gekennzeichnet, dass der Schritt der Abtrennung der oberflächenaktiven Substanzen an dem gesamten von einer Fasern-Rückgewinnungseinrichtung kommenden geklärten Wasser oder einem Teil davon vorgenommen wird.
- Verfahren zur maschinellen Papierherstellung, dadurch gekennzeichnet, dass Altpapierstoff oder Holzschliff verwendet wird.
- Verfahren zur maschinellen Papierherstellung nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass es einen Schritt der Entfernung des Flotationsschaums, der die abgetrennten oberflächenaktiven Substanzen enthält, uinfasst.
- Verfahren zur maschinellen Papierherstellung nach Anspruch 6, dadurch gekennzeichnet, dass der Flotationsschaum mit Ozon behandelt wird, bevor er in eine Reinigungsstation abgeführt wird.
- Verfahren zur maschinellen Papierherstellung nach Anspruch 6, dadurch gekennzeichnet, dass der Flotationsschaum auf Höhe eines Schlammabtropftisches abgeführt wird.
- Papiermaschine, die in ihrem nassen Teil eine Zelle zur Flotation mit dispergierter Luft (9A, 9B) umfasst, die die Abtrennung der im Siebwasser vorhandenen oberflächenaktiven Substanzen gestattet.
- Papiermaschine nach Anspruch 9, dadurch gekennzeichnet, dass die Flotationszelle (9A) am Austritt des Papierbildungstisches (2) und stromauf des Siebwasser-Rezyklierungskreises gelegen ist.
- Papiermaschine nach Anspruch 9, dadurch gekennzeichnet, dass die Flotationszelle (9B) im Kreis des geklärten Wassers am Austritt der Fasern-Rückgewinnungseinrichtung (8) gelegen ist.
- Papiermaschine nach einem der Ansprüche 9 bis 11, dadurch gekennzeichnet, dass sie geringe Mengen an Frischwasser verbraucht oder sogar im geschlossenen Kreis arbeitet.
- Papiermaschine nach einem der Ansprüche 9 bis 12, dadurch gekennzeichnet, dass die Flotationszelle (9A, 9B) mit einer Reinigungsstation für die Abfuhr des Flotationsschaums verbunden ist.
- Papiermaschine nach einem der Ansprüche 9 bis 12, dadurch gekennzeichnet, dass die Flotationszelle (9A, 9B) mit einem Schlammabtropftisch verbunden ist.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0653059A FR2904012B1 (fr) | 2006-07-21 | 2006-07-21 | Procede d'elimination des tensioactifs au cours de la fabrication du papier sur machine et machine a papier mettant en oeuvre ce procede. |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1887130A1 EP1887130A1 (de) | 2008-02-13 |
EP1887130B1 true EP1887130B1 (de) | 2009-03-04 |
Family
ID=37198808
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP07301077A Active EP1887130B1 (de) | 2006-07-21 | 2007-05-31 | Verfahren zur Entfernung von Tensiden während der Herstellung von Papier in einer Papiermaschine und Papiermaschine zur Durchführung des Verfahrens |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP1887130B1 (de) |
AT (1) | ATE424476T1 (de) |
DE (1) | DE602007000630D1 (de) |
ES (1) | ES2321990T3 (de) |
FR (1) | FR2904012B1 (de) |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3610939C2 (de) * | 1985-12-23 | 1997-11-20 | Voith Sulzer Stoffaufbereitung | Verfahren zur Behandlung des Siebwassers einer Papiermaschine |
DE19914779A1 (de) * | 1999-03-31 | 2000-10-05 | Meri Entsorgungstech Papierind | Wasserkreislaufaufbereitung für Papiermaschinen |
-
2006
- 2006-07-21 FR FR0653059A patent/FR2904012B1/fr active Active
-
2007
- 2007-05-31 ES ES07301077T patent/ES2321990T3/es active Active
- 2007-05-31 DE DE602007000630T patent/DE602007000630D1/de active Active
- 2007-05-31 EP EP07301077A patent/EP1887130B1/de active Active
- 2007-05-31 AT AT07301077T patent/ATE424476T1/de not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
FR2904012A1 (fr) | 2008-01-25 |
ATE424476T1 (de) | 2009-03-15 |
ES2321990T3 (es) | 2009-06-15 |
FR2904012B1 (fr) | 2008-09-12 |
DE602007000630D1 (de) | 2009-04-16 |
EP1887130A1 (de) | 2008-02-13 |
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