GB2037340A - Utilizing waste paper - Google Patents
Utilizing waste paper Download PDFInfo
- Publication number
- GB2037340A GB2037340A GB7927549A GB7927549A GB2037340A GB 2037340 A GB2037340 A GB 2037340A GB 7927549 A GB7927549 A GB 7927549A GB 7927549 A GB7927549 A GB 7927549A GB 2037340 A GB2037340 A GB 2037340A
- Authority
- GB
- United Kingdom
- Prior art keywords
- waste
- paper
- fractionizing
- milling
- waste paper
- 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.)
- Withdrawn
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
- D21B1/30—Defibrating by other means
- D21B1/32—Defibrating by other means of waste paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
- D21C5/02—Working-up waste paper
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Paper (AREA)
Abstract
Short fibers obtained by fractionating waste paper reduce in the course of processing of waste paper the bonding properties of long fiber fractions. According to this invention the short fiber fractions are first separated from the long fiber fractions, the long fiber fractions regenerated by milling, advantageously by fibrillation milling, and subsequently at least part of the earlier separated short fiber fraction added to the regenerated long fiber fraction for further processing.
Description
SPECIFICATION
Method for utilizing waste originating by fractionizing waste paper in the paper manufacture
DESCRIPTION
The invention relates to a method for utilizing waste originating by fractionizing waste paper in the
paper manufacture.
One of principle negative effects in the course of processing paper stuff obtained from collected waste paper are fine and very fine particles. They not only contribute to an increase of the degree of
milling, cause a worse dehydration but they mainly prevent a correct processing of fibers by milling and thus their full regeneration, which is for fibers obtained from waste paper the major condition required for a following processing by a paper machine.
As follows from evaluations of up to now obtained results, it is obvious, that fine particles of fibers
lower the mechanical strength of the paper in that they fill gaps between individual fibers increasing.
thus distances between fibers capable of bonding. A consequence thereof is a required increased degree of milling and a reduced capability of dehydration. The fine fractions of fibers increase due to their high stiffness the required milling pressure in the course of milling. A consequence thereof is a further increase of the amount of fine fractions, as due to the high pressure in the course of milling long fibers are disintegrating. The regeneration of long fibers is thus very impaired as for this purpose a rather smooth, mostly highly fibrillation milling is required, which proceeds at lower milling pressures.
In order to enable a maximum regeneration of fibers obtained from waste paper, the fractionizing of waste paper is very advantageous.
By fractionizing, two fractions are obtained, one with long fibers the second with short fibers waste. This waste consists of fine fractions of fibers and of fillers, of an amount up to 30 per cent. The separated long fibers are processed independently by fibrillation milling, increasing thus the bonding properties of fibers showing in increased mechanical strengths of paper sheets obtained from these fibers.
The processing of waste paper by fractionizing found however up to now no industrial application as there was no industrial utilization for the short fiber fraction, of which up to 30 per cent is originating.
Thus considerable economical losses are occuring due to the necessity of liquidation of a large amount of waste, due to worsening of environmental conditions and high requirements on power.
It is an object of this invention to provide a method leading to utilization of this waste in the paper industry. According to this invention the separated waste represented by a mixture of short fibers and of fillers is in the course of the proceeding process returned to the fraction of long fibers which has been prior to this mixing with the waste processed by milling advantageously by fibrillation milling, to required mechanical values whereby the amount of returned waste from fractionizing can be within 10 to 100 per cent of the separated waste. The separated waste can be also utilized for some other suspension of material than from which it has been fractionized in order to reduce the content of fillers or in order to obtain from the final mixture new properties for the paper.
The attached drawing indicates diagrammatically the whole process according to this invention.
With reference to the drawing, waste paper is disintegrated in a pulper 1, wherefrom it is discontinously or continuously removed to a storage bin 2, wherefrom it is conveyed by a stream of water to a separator 3 of contaminants, where the not fiberized fractions and contaminants of higher
and lower specific weight are removed. The material rid of contaminants is brought to a storage bin 4 wherefrom it is pumped to a fractionizer 5. Here fine fractions of fibers and fillers are separated at an
amount up to 30 per cent of the overall amount of paper stuff. The stream of long fibers passes from the
fractionizer 5 to a storage bin 7.From this storage bin 7 the long fiber fraction is pumped over a thickening vessel 8 and another storage bin 9 to mills 10, where it undergoes a fibrillation milling and is
collected in a mixing vessel 1 The bonding properties of fibers are regenerated by this milling and their specific surface is increased. Due to the increase of the specific surface the contact surfaces of individual fibers are increased in the course of formation of the paper sheet and fine fiber fractions the waste -- which represents due to its morphology a dead not active part of the paper stuff forms some kind of filler and does not prevent to such an extent as was the case at not regenerated fibers the creation of bonds and it is possible to return it at the whole extent back into the suspension and start its processing together with the other fractions.
The short fiber fraction -- the waste from the fractionator 5 passes to a storage bin 6, wherefrom
it is pumped to the mixing vessel 11 or alternatively to this mixing vessel 11 by way of a thickening vessel 1 2. From the mixing vessel 11 the mixed material passes for processing to a paper machine. By the amount of added short fiber fraction -- of the waste - into the mixing vessel 11 can be adjusted the dehydration, the degree of milling, the amount of fillers and other properties of the paper while
maintaining high mechanical strength obtained by correct regeneration of the long fiber fraction. See also the following table.
Dehydration Length of fracture Stress Tearing .SR km kPa mN 500 ml 700 ml 800 ml waste paper, classical technology 44.05 98.9 148.3 55 2.85 120 665 waste paper, short fibers removed 7.6 17.2 26.0 20 2.4 110 950 waste paper. short fibers removed. milled 24.2 53.9 83.7 39 3.9 150 495 to milled material 10% of short fibers added 27.9 62.9 93.6 42 4.0 130 455 to milled material 30% short fibers added 31.3 70.1 104 47 3.95 130 470 to milled material 80% short fibers added 39.3 90.3 133.7 54 4.15 140 490 to milled material 50% short fibers added 35.0 80 118.3 50 4.0 140 505 to milled material 100% short fibers added 33.7 76.9 114.3 59 4.1 140 490
Claims (5)
1. A method of utilizing waste originating by fractionizing waste paper in the paper industry wherein the collected waste paper undergoes fractionizing, separating the long fiber fraction and the waste the short fiberfraction and fillers regenerating the long fiber fraction by milling to required mechanical values and returning thereafter at least a part of the earlier separated waste to the long fiber fraction, whereby the amount of returned waste from fractionizing is within 10 to 100 per cent of the separated waste.
2. A method as claimed in claim 1, wherein the milling step is fibrillation milling.
3. A method as claimed in claim 1 or 2 wherein the separated waste from fractionizing waste paper is added to a suspension other than that from which it has been fractionized in order to reduce the amount of fresh fillers.
4. A method as claimed in claim 1 or 2 wherein the separated waste from fractionizing waste paper is added to a suspension other than that from which it has been fractionized in order to obtain new properties of the final mixture.
5. A method for utilizing waste originating by fractionizing waste paper in the paper industry, substantially as herein before described with reference to the accompanying drawing.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CS788056A CS220858B1 (en) | 1978-12-06 | 1978-12-06 | Method of treating the waste paper |
Publications (1)
Publication Number | Publication Date |
---|---|
GB2037340A true GB2037340A (en) | 1980-07-09 |
Family
ID=5430642
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB7927549A Withdrawn GB2037340A (en) | 1978-12-06 | 1979-08-07 | Utilizing waste paper |
Country Status (9)
Country | Link |
---|---|
JP (1) | JPS5580588A (en) |
CS (1) | CS220858B1 (en) |
DD (1) | DD145293A1 (en) |
DE (1) | DE2926185A1 (en) |
ES (1) | ES483485A1 (en) |
FR (1) | FR2443528A1 (en) |
GB (1) | GB2037340A (en) |
IT (1) | IT1125398B (en) |
NL (1) | NL7904845A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3536337C1 (en) * | 1985-10-11 | 1987-05-27 | Voith Gmbh J M | Process and device for stock preparation for ash-containing raw material in waste paper processing |
EP0582042A1 (en) * | 1992-07-23 | 1994-02-09 | J.M. Voith GmbH | Process for modifying the properties of deinked waste paper pulps, especially the fiber classification and installation for carrying out the process |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2331455A (en) * | 1937-06-09 | 1943-10-12 | Cowles Co | Process for the preparation of paper stock |
SE7613057L (en) * | 1976-03-17 | 1977-09-18 | Black Clawson Co | SETS AND APPARATUS FOR RECYCLING PAPER FIBERS FROM WASTE MATERIAL CONTAINING PAPER |
DE2759113C2 (en) * | 1977-12-30 | 1979-05-17 | J.M. Voith Gmbh, 7920 Heidenheim | Process and system for processing waste paper |
DE2836186C2 (en) * | 1978-08-18 | 1980-02-07 | J.M. Voith Gmbh, 7920 Heidenheim | Process and device for ash removal from pulp suspensions in waste paper processing |
US4676910A (en) * | 1986-08-11 | 1987-06-30 | Nalco Chemical Company | Means of controlling precipitation of Na2 SO4 from solutions of NaHSO3 oxygen scavengers |
-
1978
- 1978-12-06 CS CS788056A patent/CS220858B1/en unknown
-
1979
- 1979-06-21 NL NL7904845A patent/NL7904845A/en not_active Application Discontinuation
- 1979-06-28 DE DE19792926185 patent/DE2926185A1/en not_active Withdrawn
- 1979-06-28 IT IT2396479A patent/IT1125398B/en active
- 1979-08-06 DD DD79214822A patent/DD145293A1/en unknown
- 1979-08-07 GB GB7927549A patent/GB2037340A/en not_active Withdrawn
- 1979-08-20 ES ES483485A patent/ES483485A1/en not_active Expired
- 1979-10-12 FR FR7925509A patent/FR2443528A1/en not_active Withdrawn
- 1979-12-04 JP JP15645479A patent/JPS5580588A/en active Pending
Also Published As
Publication number | Publication date |
---|---|
CS220858B1 (en) | 1983-04-29 |
IT7923964A0 (en) | 1979-06-28 |
IT1125398B (en) | 1986-05-14 |
ES483485A1 (en) | 1980-03-01 |
DD145293A1 (en) | 1980-12-03 |
NL7904845A (en) | 1980-06-10 |
FR2443528A1 (en) | 1980-07-04 |
DE2926185A1 (en) | 1980-06-26 |
JPS5580588A (en) | 1980-06-17 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
WAP | Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1) |