GB2096661A - A process for preparing waste paper - Google Patents

A process for preparing waste paper Download PDF

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Publication number
GB2096661A
GB2096661A GB8205777A GB8205777A GB2096661A GB 2096661 A GB2096661 A GB 2096661A GB 8205777 A GB8205777 A GB 8205777A GB 8205777 A GB8205777 A GB 8205777A GB 2096661 A GB2096661 A GB 2096661A
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GB
United Kingdom
Prior art keywords
breaker
pulp
paper
consistency
disc grinder
Prior art date
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Granted
Application number
GB8205777A
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GB2096661B (en
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JM Voith GmbH
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JM Voith GmbH
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Filing date
Publication date
Application filed by JM Voith GmbH filed Critical JM Voith GmbH
Publication of GB2096661A publication Critical patent/GB2096661A/en
Application granted granted Critical
Publication of GB2096661B publication Critical patent/GB2096661B/en
Expired legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30Defibrating by other means
    • D21B1/32Defibrating by other means of waste paper
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/64Paper recycling

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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)

Abstract

In order to save energy and to economise on plant components, in the process for preparing relatively clean, pre-sorted waste paper the following preparation steps are carried out: a) Pulping in the breaker (1) to a stock consistency of more than 15%, b) Delivery from the breaker (1) with the pulp stock at the consistency level established therein, c) Sorting of the pulpy paper stock by conducting it past a metal-seeking device (5), d) Introduction into a dispersion appliance (4) with an operating range which lies within the pulp stock consistency established in the breaker (1), e) Dispersion of the pulp stock in the dispersion appliance (4), f) Ensuing thinning of the pulp stock, g) Further preparation of the pulp by fine sorting and fine cleansing for the purpose of supplying it to the paper or cardboard machine. <IMAGE>

Description

SPECIFICATION A process for preparing waste paper The invention relates to a process for preparing relatively clean, pre-sorted waste paper, particularly paper rejected during the manufacture of paper.
Until now, waste paper has either been pulped to a low consistency in a breaker and then delivered to the further processing stages such as cleansing, sorting and thickening, or the waste paper has been pulped in a breaker to a higher consistency of more than 20%, for example, and then either thinned while still in the breaker or delivered from the breaker to the further processing stages, thinned to a consistency which can easily be pumped and sorted. In all cases when following this procedure a thickener was required, which made the whole process more expensive and also required more space.
An object of the present invention is to provide a simplified process which is particularly intended for the preparation of relatively clean papers, i.e.
either pre-sorted waste paper or papers which have been rejected during the manufacture of paper, such as waterproof portions, for example.
According to the invention, such a process is characterised by the features set out in Patent
Claim 1.
In accordance with the invention a quick and easy preparation process is achieved, which is greatly simplified compared with the known process.
It is particularly advantageous when waste paper containing few contraries is to be prepared, where specifically heavy items such as screws, stones, wires, etc. and large-surface are elements such as foils, pieces of wood, textiles, etc. are meant by the term "contraries", since in this case a very rapid preparation method is obtained for the waste paper up to re-use in the paper machine; in this case any printing inks contained are not removed but are finely dispersed in the subsequent process.
A very advantageous development of the process is realised by using a disc grinder, since the operating characteristic and effect of this can be adapted to the pulp stock consistency involved by adjusting the gap between the discs, and this leaves the choice of pulp stock consistency in the breaker relatively free.
The invention will now be explained in more detail in the following description of one embodiment example of the process, with reference to the accompanying drawing, which is a schematic view of said process.
It will be seen from the drawing that the path of the fibrous pulp from the breaker passes via a shut-off device 10, a screw conveyor 2 and a conveyor belt 3 to the disc grinder 4 in which the suspension is dispersed. Above the conveyor belt 3 there is a metal-seeking device 5 to ensure that metal parts such as screws or staples or suchlike contained in the suspension cannot reach the subsequent sorting equipment or even the paper machine. In the disc grinder the lumps are removed to bring the pulp to the necessary degree of fineness, i.e. it is broken down into individual fibres and any printing inks, for example, which may be contained are dispersed. In this process the pulp stock consistency amounts to approximately 20%, and in particular to more than 20%, and is maintained throughout without change, from the breaker up to the disc grinder.
The most favourable pulp stock consistency, which may also be less than 20%, will be chosen either according to the operating method of the breaker alone, or by also taking into account the possible range of the disc grinder, i.e. its possible spacing. Generally, however, it will be found that the operating characteristic of the disc grinder can be adapted to the consistency which is most favourable for the breaker, by adjusting its operating gap.
Naturally, instead of the disc grinder another dispersion appliance may be selected, and particularly, for example, a single-shaft grinder, which does not have an adjustable operating gap so that in this case the choice of the pulp stock consistency in the breaker may not be made freely, but must be made according to the best possible operating characteristics of the singleshaft grinder.
After the disc grinder the pulp is delivered via a continuousiy operating conveyor belt with reversible conveying direction into an intermediate tank in which thinning is carried out. This is necessary in order to meet the requirements with regard to being sorted, for the subsequent fine sorting and cleansing of the pulp stock. Extraction from the intermediate tank 8 is effected by means of a pump 9. After this, very varied sorting equipment such as strainer sorters, particularly vertical sifters, and also flotation devices may follow. Flotation devices are not necessary, of course, if unprinted waste papers and/or only offcuts (rejects) from the paper manufacturing process are used as the waste paper.When the plant is being run up the conveyor belt can run in the opposite direction and deliver the pulp leaving the disc grinder back into the breaker again via a return conveyor screw 11, as a certain amount of transition time is necessary when the plant is being run up before the pulp has the required properties when it leaves the disc grinder.
The figures also shows that the fibrous pulp is supplied onto the disc grinder 4 by a feed screw 12. If a single-shaft grinder is used a very high pulp stock consistency of, for example, possibly around 30%, and in exceptional cases up to 35%, is necessary in the breaker; however, this is quite within the capabilities of the latter. In the case of the disc grinder the consistencies are lower and, as stated, may vary within a wide range.
CLAIMS 1. A process for preparing relatively clean, presorted waste paper, such as paper rejected during the manufacture of paper, characterised by the following features:
**WARNING** end of DESC field may overlap start of CLMS **.

Claims (7)

**WARNING** start of CLMS field may overlap end of DESC **. SPECIFICATION A process for preparing waste paper The invention relates to a process for preparing relatively clean, pre-sorted waste paper, particularly paper rejected during the manufacture of paper. Until now, waste paper has either been pulped to a low consistency in a breaker and then delivered to the further processing stages such as cleansing, sorting and thickening, or the waste paper has been pulped in a breaker to a higher consistency of more than 20%, for example, and then either thinned while still in the breaker or delivered from the breaker to the further processing stages, thinned to a consistency which can easily be pumped and sorted. In all cases when following this procedure a thickener was required, which made the whole process more expensive and also required more space. An object of the present invention is to provide a simplified process which is particularly intended for the preparation of relatively clean papers, i.e. either pre-sorted waste paper or papers which have been rejected during the manufacture of paper, such as waterproof portions, for example. According to the invention, such a process is characterised by the features set out in Patent Claim 1. In accordance with the invention a quick and easy preparation process is achieved, which is greatly simplified compared with the known process. It is particularly advantageous when waste paper containing few contraries is to be prepared, where specifically heavy items such as screws, stones, wires, etc. and large-surface are elements such as foils, pieces of wood, textiles, etc. are meant by the term "contraries", since in this case a very rapid preparation method is obtained for the waste paper up to re-use in the paper machine; in this case any printing inks contained are not removed but are finely dispersed in the subsequent process. A very advantageous development of the process is realised by using a disc grinder, since the operating characteristic and effect of this can be adapted to the pulp stock consistency involved by adjusting the gap between the discs, and this leaves the choice of pulp stock consistency in the breaker relatively free. The invention will now be explained in more detail in the following description of one embodiment example of the process, with reference to the accompanying drawing, which is a schematic view of said process. It will be seen from the drawing that the path of the fibrous pulp from the breaker passes via a shut-off device 10, a screw conveyor 2 and a conveyor belt 3 to the disc grinder 4 in which the suspension is dispersed. Above the conveyor belt 3 there is a metal-seeking device 5 to ensure that metal parts such as screws or staples or suchlike contained in the suspension cannot reach the subsequent sorting equipment or even the paper machine. In the disc grinder the lumps are removed to bring the pulp to the necessary degree of fineness, i.e. it is broken down into individual fibres and any printing inks, for example, which may be contained are dispersed. In this process the pulp stock consistency amounts to approximately 20%, and in particular to more than 20%, and is maintained throughout without change, from the breaker up to the disc grinder. The most favourable pulp stock consistency, which may also be less than 20%, will be chosen either according to the operating method of the breaker alone, or by also taking into account the possible range of the disc grinder, i.e. its possible spacing. Generally, however, it will be found that the operating characteristic of the disc grinder can be adapted to the consistency which is most favourable for the breaker, by adjusting its operating gap. Naturally, instead of the disc grinder another dispersion appliance may be selected, and particularly, for example, a single-shaft grinder, which does not have an adjustable operating gap so that in this case the choice of the pulp stock consistency in the breaker may not be made freely, but must be made according to the best possible operating characteristics of the singleshaft grinder. After the disc grinder the pulp is delivered via a continuousiy operating conveyor belt with reversible conveying direction into an intermediate tank in which thinning is carried out. This is necessary in order to meet the requirements with regard to being sorted, for the subsequent fine sorting and cleansing of the pulp stock. Extraction from the intermediate tank 8 is effected by means of a pump 9. After this, very varied sorting equipment such as strainer sorters, particularly vertical sifters, and also flotation devices may follow. Flotation devices are not necessary, of course, if unprinted waste papers and/or only offcuts (rejects) from the paper manufacturing process are used as the waste paper.When the plant is being run up the conveyor belt can run in the opposite direction and deliver the pulp leaving the disc grinder back into the breaker again via a return conveyor screw 11, as a certain amount of transition time is necessary when the plant is being run up before the pulp has the required properties when it leaves the disc grinder. The figures also shows that the fibrous pulp is supplied onto the disc grinder 4 by a feed screw 12. If a single-shaft grinder is used a very high pulp stock consistency of, for example, possibly around 30%, and in exceptional cases up to 35%, is necessary in the breaker; however, this is quite within the capabilities of the latter. In the case of the disc grinder the consistencies are lower and, as stated, may vary within a wide range. CLAIMS
1. A process for preparing relatively clean, presorted waste paper, such as paper rejected during the manufacture of paper, characterised by the following features: a) pulping in the breaker to a stock consistency of more than 15%, b) delivery from the breaker with the pulp stock at the consistency level established therein, c) sorting of the pulpy paper stock by conducting it past a metal-seeking device, d) introduction into a dispersion appliance with an operating range which lies within the pulp stock consistency established in the breaker, e) dispersion of the pulp stock in the dispersion appliance, f) ensuing thinning of the pulp stock, g) further preparation of the pulp by fine sorting and fine cleansing for the purpose of supplying it to a paper or cardboard machine.
2. A process according to Claim 1, characterised in that the pulp stock consistency in the breaker is established according to the (optimum possible) operating characteristic of the dispersion appliance.
3. A process according to Claim 1 or 2, characterised by the use of a dispersion appliance with an adjustable operating gap (a disc grinder), the operating gap being set according to the pulp consistency, for the optimum operation of the dispersion appliance.
4. A process according to one of Claims 1 to 3, characterised in that delivery from the breaker is carried out by means of a feed screw or a bucket chain conveyor or a belt conveyor.
5. Apparatus for carrying out the process according to one of Claims 1, 2 or 4, characterised in that the dispersion appliance is a single-shaft grinder.
6. Apparatus for carrying out the process according to one of Claims 1, 3 or 4, characterised in that the dispersion appliance is a double disc grinder, with an adjustable operating gap between the discs.
7. A process for preparing relatively clean, presorted waste paper, or apparatus therefor substantially as hereinbefore described with reference to the accompanying schematic drawing.
GB8205777A 1981-04-10 1982-02-26 A process for preparing waste paper Expired GB2096661B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE3114527A DE3114527C1 (en) 1981-04-10 1981-04-10 Process for the treatment of waste paper

Publications (2)

Publication Number Publication Date
GB2096661A true GB2096661A (en) 1982-10-20
GB2096661B GB2096661B (en) 1985-01-16

Family

ID=6129867

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8205777A Expired GB2096661B (en) 1981-04-10 1982-02-26 A process for preparing waste paper

Country Status (6)

Country Link
JP (1) JPS57183485A (en)
AT (1) AT381124B (en)
DE (1) DE3114527C1 (en)
FI (1) FI73748C (en)
FR (1) FR2503748B1 (en)
GB (1) GB2096661B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0345234A2 (en) * 1988-05-20 1989-12-06 Yhtyneet Paperitehtaat Oy Walkisoft Engineering Feeding system for the former of a dry-paper machine
US5334285A (en) * 1990-11-23 1994-08-02 J. M. Voith Gmbh Process for the treatment of wastepaper using drum soaker

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0397983A (en) * 1989-09-05 1991-04-23 Aikawa Tekko Kk Pulper device of paper making and braking dust remover therefor
DE4211545C1 (en) * 1992-04-06 1993-08-05 Hans-Juergen 7400 Tuebingen De Maier
JP7269631B2 (en) * 2019-07-16 2023-05-09 株式会社大善 Fiber recovery method from screen reject

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1097802B (en) * 1957-07-30 1961-01-19 Condux Werk Process for dissolving waste fibers, especially waste paper
FR2184176A5 (en) * 1972-05-10 1973-12-21 Delemme Marcel
CH574538A5 (en) * 1974-02-26 1976-04-15 Escher Wyss Gmbh
DE2514162B2 (en) * 1975-03-29 1977-02-03 Anlage zur Aufbereitung von Altpapier J.M. Voith GmbH, 7920 Heidenheim PLANT FOR THE PROCESSING OF WASTE PAPER
DE2818779A1 (en) * 1978-03-07 1979-09-13 Escher Wyss Gmbh METHOD FOR TREATMENT OF WASTE PAPER FOR THE RECOVERY OF SUBSTANCE LIQUID FOR THE PRODUCTION OF NEW PAPER AND DEVICE FOR CARRYING OUT THE METHOD

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0345234A2 (en) * 1988-05-20 1989-12-06 Yhtyneet Paperitehtaat Oy Walkisoft Engineering Feeding system for the former of a dry-paper machine
EP0345234A3 (en) * 1988-05-20 1991-08-07 Yhtyneet Paperitehtaat Oy Walkisoft Engineering Feeding system for the former of a dry-paper machine
US5334285A (en) * 1990-11-23 1994-08-02 J. M. Voith Gmbh Process for the treatment of wastepaper using drum soaker

Also Published As

Publication number Publication date
ATA44082A (en) 1986-01-15
AT381124B (en) 1986-08-25
GB2096661B (en) 1985-01-16
FR2503748A1 (en) 1982-10-15
FR2503748B1 (en) 1986-04-11
FI821272L (en) 1982-10-11
FI73748C (en) 1987-11-09
JPS57183485A (en) 1982-11-11
DE3114527C1 (en) 1982-10-14
FI821272A0 (en) 1982-04-08
FI73748B (en) 1987-07-31

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PCNP Patent ceased through non-payment of renewal fee