DE102006012835B3 - Process for the treatment of pulp containing disruptive vascular cells - Google Patents
Process for the treatment of pulp containing disruptive vascular cells Download PDFInfo
- Publication number
- DE102006012835B3 DE102006012835B3 DE200610012835 DE102006012835A DE102006012835B3 DE 102006012835 B3 DE102006012835 B3 DE 102006012835B3 DE 200610012835 DE200610012835 DE 200610012835 DE 102006012835 A DE102006012835 A DE 102006012835A DE 102006012835 B3 DE102006012835 B3 DE 102006012835B3
- Authority
- DE
- Germany
- Prior art keywords
- vascular cells
- hydrocyclone
- pulp
- centrifugal forces
- chemical reaction
- 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.)
- Expired - Fee Related
Links
- 238000000034 method Methods 0.000 title claims abstract description 32
- 210000005167 vascular cell Anatomy 0.000 title claims abstract description 26
- 239000000945 filler Substances 0.000 claims abstract description 13
- 239000000725 suspension Substances 0.000 claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 7
- 239000000835 fiber Substances 0.000 claims description 20
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 8
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 6
- 239000000920 calcium hydroxide Substances 0.000 claims description 5
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 4
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 4
- 239000001569 carbon dioxide Substances 0.000 claims description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 4
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 3
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 2
- 239000000292 calcium oxide Substances 0.000 claims description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 2
- 239000013078 crystal Substances 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 239000002657 fibrous material Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 235000011116 calcium hydroxide Nutrition 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000011121 hardwood Substances 0.000 description 3
- 230000002452 interceptive effect Effects 0.000 description 3
- 230000003287 optical effect Effects 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 230000029087 digestion Effects 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 229920005610 lignin Polymers 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000003490 calendering Methods 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 230000029142 excretion Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000012764 mineral filler Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/63—Inorganic compounds
- D21H17/70—Inorganic compounds forming new compounds in situ, e.g. within the pulp or paper, by chemical reaction with other substances added separately
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D5/00—Purification of the pulp suspension by mechanical means; Apparatus therefor
- D21D5/18—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force
- D21D5/24—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force in cyclones
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
Abstract
Das Verfahren behandelt eine Zellstoffsuspension (1), die einen störenden Anteil von Gefäßzellen aufweist. Diese werden in einem Beladungsprozess (2) so behandelt, dass durch eine chemische Reaktion Füllstoffe gebildet werden, die sich an die Gefäßzellen anlagern. Diese können danach durch Zentrifugalkräfte z.B. in Hydrozyklonen (9) entfernt werden.The process treats a pulp suspension (1) which has a disruptive proportion of vascular cells. These are treated in a loading process (2) in such a way that fillers are formed through a chemical reaction that attach to the vascular cells. These can then by centrifugal forces e.g. removed in hydrocyclones (9).
Description
Die Erfindung bezieht sich auf ein Verfahren gemäß dem Oberbegriff des Anspruchs 1.The The invention relates to a method according to the preamble of the claim 1.
Bekanntlich enthalten solche Zellstoffe, zu deren Erzeugung schnell wachsende Laubhölzer, insbesondere tropische Laubhölzer verwendet werden, sogenannte Gefäßzellen (englisch: vessels), welche in Folge der klimatischen Bedingungen relativ große Abmessungen aufweisen. Ihr Mengenanteil am Zellstoff liegt zumeist bei 3 bis 5 %. Diese Gefäßzellen werden bei der Zellstofferzeugung nicht entfernt und sind bei dem aus einem solchen Zellstoff hergestellten Papier störend, da sie für bestimmte Nachteile verantwortlich sind. So kann es z.B. passieren, dass die Gefäßzellen aus dem Papiergefüge ausbrechen, wodurch sich die Oberfläche verschlechtert und die Papiereigenschaften beeinträchtigt sind.generally known contain such pulps, which produce rapidly growing Hardwoods, in particular tropical hardwoods used, so-called vascular cells (English: vessels), which in consequence of the climatic conditions relatively large Dimensions have. Their proportion of pulp is mostly at 3 to 5%. These vascular cells are not removed in pulp production and are in the interfering with paper produced from such a pulp, since she for certain disadvantages are responsible. So it can be e.g. happen, that the vascular cells break out of the paper structure, which causes the surface deteriorates and the paper properties are impaired.
Zwar
ist aus der
In
der
Aus
der
In
der
Eine
weitere Veröffentlichung,
die
Der Erfindung liegt die Aufgabe zu Grunde, ein weiteres Verfahren zu schaffen, mit dem es möglich ist, die Nachteile, die sich aus dem Gehalt an Gefäßzellen ergeben, zu reduzieren oder ganz zu beseitigen. Es soll zumindest bei speziellen Aufbereitungsverfahren eine verbesserte Gesamtwirtschaftlichkeit haben.Of the Invention is based on the object to another method create with it possible is, the disadvantages stemming from the content of vascular cells arise, reduce or eliminate altogether. It should be at least have improved overall economy in special treatment processes.
Diese Aufgabe wird durch die im Kennzeichen des Anspruchs 1 genannten Merkmale in Verbindung mit denen des Oberbegriffs gelöst.These The object is achieved by the mentioned in the characterizing part of claim 1 Features associated with those of the preamble.
Das Verfahren wird üblicherweise in der Stoffaufbereitung einer Papierfabrik angewendet. Es kann aber auch bereits in der Zellstofffabrik nach dem Aufschluss durchgeführt werden.The Procedure becomes common used in the stock preparation of a paper mill. It can but also already be carried out in the pulp mill after digestion.
Das Beladen der Gefäßzellen und Fasern mit mineralischem Füllstoff erfolgt beispielsweise durch eine chemische Fällungsreaktion, d.h. insbesondere durch einen sogenannten „Fiber LoadingTM"-Prozess, wie er unter anderem in der US-A-5 223 090 beschrieben ist. Bei einem solchen „Fiber LoadingTM"-Prozess wird an die benetzten Faseroberflächen des Fasermaterials wenigstens ein Zusatzstoff, insbesondere Füllstoff, eingelagert. Dabei können die Fasern beispielsweise mit Calciumcarbonat beladen werden. Hierzu wird dem feuchten, desintegrierten Fasermaterial Calciumoxid und/oder Calciumhydroxid vorzugsweise in flüssiger Form (Kalkmilch) so zugesetzt, dass zumindest ein Teil davon sich mit dem im Fasermaterial vorhandenen Wasser assoziiert. Das so behandelte Fasermaterial wird anschließend mit Kohlendioxid beaufschlagt. Dadurch läuft eine chemische Reaktion, bei der das Calciumcarbonat ausfällt und sich an den benetzten Fasern und Gefäßzellen anlagert. Dieses Anlagern kann außen und innen erfolgen, da Zellstofffasern und Gefäßzellen offene Hohlkörper sind.The loading of the vascular cells and fibers with mineral filler takes place for example by a chemical precipitation reaction, ie in particular by a so-called "Fiber Loading ™ " process, as described, inter alia, in US Pat. No. 5,223,090 Loading TM "process is incorporated on the wetted fiber surfaces of the fiber material at least one additive, in particular filler. The fibers can be loaded with calcium carbonate, for example. For this purpose, the moist, disintegrated fiber material calcium oxide and / or calcium hydroxide is preferably added in liquid form (milk of lime) so that at least a part of it associates with the water present in the fiber material. The fiber material treated in this way is then treated with carbon dioxide. This causes a chemical reaction in which the calcium carbonate precipitates and attaches to the wetted fibers and vascular cells. This attachment can be done outside and inside, as pulp fibers and vascular cells are open hollow body.
Mögliche Vorteile der durch Beladen einer Fasersuspension erhaltenen Füllstoffteilchen bestehen unter anderem in folgendem:
- – Es ist nunmehr möglich, die erforderlichen Füllstoffteilchen gleichmäßig über die Faseroberfläche zu verteilen, wodurch die besten optischen Eigenschaften online in der Stoffaufbereitung erzielt werden, wobei das erreichte Füllstoffniveau unterhalb oder oberhalb 40 % liegen kann.
- – Da auch innerhalb des Faserlumens Füllstoffteilchen eingebettet sind, wird die Tendenz einer Schwärung durch Kalandrieren deutlich reduziert.
- – Es wird ein neuer Weg zur Einlagerung von Pigmenten geschaffen, um die gewünschten optischen Eigenschaften und die gewünschte Bedruckbarkeit in und auf dem Papierblatt bei der Papierherstellung zu erreichen.
- – Da die Füllstoffteilchen an die Fasern eingelagert sind, können sie in der Sieb- oder Langsiebpartie einer Papiermaschine nicht mehr ausgewaschen werden.
- – Da die Füllstoffteilchen an die Fasern in einem Online-Prozess eingelagert, d.h. in dem Faserstoffaufbereitungssystem kristallisiert werden, können wirtschaftliche Vorteile durch Einsparungen von Retentionsmitteln, Fasern und Sludge, die Verringerung der Siebwasserverunreinigung sowie die Einsparung von Energie und Rohmaterial erzielt werden.
- – Der Einsatz von TiO2 kann verringert werden, nachdem ein höherer Weißgrad und bessere optische Eigenschaften erreicht werden können.
- It is now possible to distribute the required filler particles uniformly over the fiber surface, whereby the best optical properties are achieved online in the stock preparation, wherein the level of filler reached can be below or above 40%.
- Since filler particles are also embedded within the fiber lumen, the tendency of calendering to shrink is significantly reduced.
- A new way of incorporating pigments is provided to achieve the desired optical properties and printability in and on the paper sheet in papermaking.
- - Since the filler particles are embedded in the fibers, they can no longer be washed out in the wire or wire screening section of a paper machine.
- - Because the filler particles are incorporated into the fibers in an on-line process, ie, crystallized in the pulp preparation system, economic benefits can be gained by saving retention agents, fibers, and sludge, reducing white water pollution, and conserving energy and raw material achieved.
- - The use of TiO 2 can be reduced after a higher whiteness and better optical properties can be achieved.
Gefäßzellen haben die Aufgabe, den Wassertransport in Laubholzstämmen zu sichern. In der Regel sind diese Gefäßzellen im wasserdurchströmten Teil mit einer Ligninschicht ausgekleidet. Dadurch ergibt sich ein starker hydrophober Charakter. Durch den Aufschlussprozess wird diese Ligninschicht herausgelöst und zurück bleibt ein poröses und hydrophiles Fasermaterial. Gefäßzellen haben die Eigenschaft, auf Grund dieser Porosität besonders wirksam beladen zu werden. D.h., dass sie die ausgefällten Füllstoffe in höherem Maße anlagern und aufnehmen als die Zellstofffasern. Dadurch steigt ihre Dichte und sie lassen sich durch Zentrifugalkräfte wirksam von den Zellstofffasern abtrennen.vascular cells have the task of transporting water in hardwood logs to back up. As a rule, these vascular cells are in the water-flow part lined with a lignin layer. This results in a strong hydrophobic character. The digestion process makes this lignin layer leached and back remains a porous one and hydrophilic fiber material. Vascular cells have the property due to this porosity to be loaded particularly effectively. That is, they are the precipitated fillers in higher Attach dimensions and take up as the pulp fibers. This increases their density and they are effectively released from the pulp fibers by centrifugal forces split off.
Durch die erfindungsgemäße Kombination der Verfahrensschritte Beladen und Hydrozyklonieren wird erreicht, dass die durch die genannten Gefäßzellen drohenden Qualitätseinbußen für das aus dem Zellstoff später hergestellte Papier nicht mehr auftreten, da der weit überwiegende Teil der Gefäßzellen entfernt werden kann. Darüber hinaus bringt das Beladen eine signifikante Qualitätsverbesserung.By the inventive combination of Process steps loading and hydrocycloning is achieved that through the mentioned vascular cells imminent loss of quality for that from the Pulp later Paper produced no longer occur because of the vast majority Part of the vascular cells can be removed. About that In addition, loading brings a significant quality improvement.
Die Erfindung wird erläutert an Hand einer Zeichnung, die die wichtigsten Schritte des Verfahrens an einem typischen Beispiel schematisch darstellt.The Invention will be explained on hand of a drawing showing the main steps of the procedure schematically in a typical example.
Demnach
wird eine Zellstoffsuspension
- 11
- ZellstoffsuspensionPulp suspension
- 22
- Beladungsprozessloading process
- 33
- Calciumhydroxidcalcium hydroxide
- 44
- Kohlendioxidcarbon dioxide
- 55
- Filtratfiltrate
- 66
- Wasserwater
- 77
- beladene Suspensionloaded suspension
- 88th
- Pumpepump
- 99
- Hydrozyklonhydrocyclone
- 1010
- Gutstoffstromaccepts stream
- 1111
- Rejektstromreject flow
Claims (7)
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE200610012835 DE102006012835B3 (en) | 2006-03-21 | 2006-03-21 | Process for the treatment of pulp containing disruptive vascular cells |
| PCT/EP2006/012158 WO2007107179A1 (en) | 2006-03-21 | 2006-12-16 | Method for treating cellulose which contains disruptive vessel cells |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE200610012835 DE102006012835B3 (en) | 2006-03-21 | 2006-03-21 | Process for the treatment of pulp containing disruptive vascular cells |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE102006012835B3 true DE102006012835B3 (en) | 2007-11-15 |
Family
ID=37898815
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE200610012835 Expired - Fee Related DE102006012835B3 (en) | 2006-03-21 | 2006-03-21 | Process for the treatment of pulp containing disruptive vascular cells |
Country Status (2)
| Country | Link |
|---|---|
| DE (1) | DE102006012835B3 (en) |
| WO (1) | WO2007107179A1 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10385508B2 (en) * | 2016-03-24 | 2019-08-20 | The Procter & Gamble Company | Process for producing strong and soft tissue and towel products |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0042234B1 (en) * | 1980-06-12 | 1983-05-11 | Pulp and Paper Research Institute of Canada | Lumen-loaded paper pulp, its production and use |
| US5770012A (en) * | 1994-11-18 | 1998-06-23 | P. H. Glatfelter Co. | Process for treating paper machine stock containing bleached hardwood pulp with an enzyme mixture to reduce vessel element picking |
| DE10337821B3 (en) * | 2003-08-18 | 2005-01-13 | Voith Paper Patent Gmbh | Process to remove non-cellular matter from cellular paper pulp cellulose and foreign matter are dispersed and fractionated |
| DE10347920A1 (en) * | 2003-10-15 | 2005-05-19 | Voith Paper Patent Gmbh | Method and device for loading a pulp suspension |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5223090A (en) * | 1991-03-06 | 1993-06-29 | The United States Of America As Represented By The Secretary Of Agriculture | Method for fiber loading a chemical compound |
| DE19816621A1 (en) * | 1998-04-15 | 1999-11-04 | Voith Sulzer Papiertech Patent | Reducing tropical, hardwood cellulose using rotary blade refiner |
| DE10033979A1 (en) * | 2000-07-13 | 2002-01-24 | Voith Paper Patent Gmbh | Method for loading fibers with calcium carbonate |
| US6413365B1 (en) * | 2001-07-11 | 2002-07-02 | Voith Paper Patent Gmbh | Method of loading a fiber suspension with calcium carbonate |
| DE10204254A1 (en) * | 2002-02-02 | 2003-08-14 | Voith Paper Patent Gmbh | Online production of crystalline precipitation particles in fiber suspension processes is preferably effected using precipitated calcium carbonate |
-
2006
- 2006-03-21 DE DE200610012835 patent/DE102006012835B3/en not_active Expired - Fee Related
- 2006-12-16 WO PCT/EP2006/012158 patent/WO2007107179A1/en not_active Ceased
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0042234B1 (en) * | 1980-06-12 | 1983-05-11 | Pulp and Paper Research Institute of Canada | Lumen-loaded paper pulp, its production and use |
| US5770012A (en) * | 1994-11-18 | 1998-06-23 | P. H. Glatfelter Co. | Process for treating paper machine stock containing bleached hardwood pulp with an enzyme mixture to reduce vessel element picking |
| DE10337821B3 (en) * | 2003-08-18 | 2005-01-13 | Voith Paper Patent Gmbh | Process to remove non-cellular matter from cellular paper pulp cellulose and foreign matter are dispersed and fractionated |
| DE10347920A1 (en) * | 2003-10-15 | 2005-05-19 | Voith Paper Patent Gmbh | Method and device for loading a pulp suspension |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2007107179A1 (en) | 2007-09-27 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 8364 | No opposition during term of opposition | ||
| 8339 | Ceased/non-payment of the annual fee |