DK168020B1 - PROCEDURE FOR THE PREPARATION OF FORM STABLE ARTICLES FROM A FLUIDIZED CELLULOSE FIBER MATERIAL - Google Patents
PROCEDURE FOR THE PREPARATION OF FORM STABLE ARTICLES FROM A FLUIDIZED CELLULOSE FIBER MATERIAL Download PDFInfo
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- DK168020B1 DK168020B1 DK592488A DK592488A DK168020B1 DK 168020 B1 DK168020 B1 DK 168020B1 DK 592488 A DK592488 A DK 592488A DK 592488 A DK592488 A DK 592488A DK 168020 B1 DK168020 B1 DK 168020B1
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- pulp
- raw material
- thickness
- fiber
- suction
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- 238000000034 method Methods 0.000 title claims description 33
- 239000002657 fibrous material Substances 0.000 title claims description 8
- 229920003043 Cellulose fiber Polymers 0.000 title description 5
- 238000002360 preparation method Methods 0.000 title description 3
- 239000000835 fiber Substances 0.000 claims description 43
- 239000002994 raw material Substances 0.000 claims description 27
- 239000007858 starting material Substances 0.000 claims description 17
- 230000008569 process Effects 0.000 claims description 16
- 239000000758 substrate Substances 0.000 claims description 12
- 238000009837 dry grinding Methods 0.000 claims description 11
- 238000000151 deposition Methods 0.000 claims description 8
- 230000000694 effects Effects 0.000 claims description 7
- 230000035699 permeability Effects 0.000 claims description 7
- 230000008021 deposition Effects 0.000 claims description 6
- 238000007493 shaping process Methods 0.000 claims description 5
- 230000008033 biological extinction Effects 0.000 claims description 2
- 230000001427 coherent effect Effects 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 description 24
- 238000004519 manufacturing process Methods 0.000 description 14
- 239000000123 paper Substances 0.000 description 8
- 238000000227 grinding Methods 0.000 description 7
- 239000010893 paper waste Substances 0.000 description 7
- 238000001035 drying Methods 0.000 description 5
- 239000002671 adjuvant Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 238000003754 machining Methods 0.000 description 4
- 239000002023 wood Substances 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 241000218631 Coniferophyta Species 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000010897 cardboard waste Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005137 deposition process Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 235000013601 eggs Nutrition 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 210000003097 mucus Anatomy 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000012779 reinforcing material Substances 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21J—FIBREBOARD; MANUFACTURE OF ARTICLES FROM CELLULOSIC FIBROUS SUSPENSIONS OR FROM PAPIER-MACHE
- D21J7/00—Manufacture of hollow articles from fibre suspensions or papier-mâché by deposition of fibres in or on a wire-net mould
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Paper (AREA)
- Pallets (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Description
DK 168020 B1DK 168020 B1
Den foreliggende opfindelse angår en fremgangsmåde til fremstilling af formstabile genstande ved afsætning af et fluidiseret cellulosefiberråstof på et formgivende underlag ved påsugning af en pulp af fiberråstoffet på dette 5 underlag.The present invention relates to a method for making mold-stable articles by depositing a fluidized cellulosic fibrous raw material on a shaping substrate by aspirating a pulp of the fibrous raw material onto this substrate.
Ved et fluidiseret cellulosefiberråstof skal der forstås et til fremstilling af de ønskede genstande egnet udgangsmateriale, der kan foreligge i våd form, og som har fibrøs karakter. Som et sådant udgangsmateriale kan der 10 eksempelvis henvises til et fiberpulpmateriale, således som det anvendes eksempelvis til bakker og kartoner til emballering af skøre og ømfindlige genstande såsom frugt, blomster, æg og genstande eksempelvis af glas. Pulpmaterialet består da T reglen af en opslæmmet, fibrøs cellulose.By a fluidized cellulose fiber raw material is meant a suitable starting material which can be present in wet form and which is fibrous in nature. As such a starting material, reference may be made, for example, to a fiber pulp material, such as is used, for example, for trays and cartons for packaging fragile and delicate objects such as fruits, flowers, eggs and articles, for example glass. The pulp material then comprises the rule of a slurry, fibrous cellulose.
15 Det er kendt i dette øjemed at anvende en fremstil lingsteknik, ved hvilken udgangsmaterialet i form af en pulp, ved en afsætningsproces anbringes mod den konturgivende yderside af en form, som er permeabel for at lade et luftformigt arbejdsmedium ved en sugeeffekt påvirke materialet 20 igennem formens materiale og derved suge materialet i kontur på formen.For this purpose, it is known to employ a manufacturing technique in which the starting material in the form of a pulp is applied, in a deposition process, to the contour-giving exterior of a mold which is permeable to allow an gaseous working medium to influence the material 20 through suction. the material of the mold, thereby sucking the material in contour on the mold.
Formålet med opfindelsen er at angive, hvorledes denne, i sig selv hensigtsmæssige fremstillingsteknik kan anvendes ikke alene til fremstilling af forholdsvis små og 25 lette genstande, men også til fremstilling af store, forholdsvis tunge, og særdeles bæredygtige elementer, der udmærker sig ved en formstabilitet, som i væsentlig grad er baseret på en tilsvarende tykkelse af det på det formgivende underlag afsatte materialelag. Sammenlignet hermed er materi-30 aletykkelsen ved de nævnte små og lette genstande ret ringe, og den i praksis fornødne stivhed tilvejebringes i reglen ved en bevidst udformning af vægpartier, der eksempelvis danner støtter for de nævnte genstande, idet væggene frembringer et forholdsvis stift, samlet emne ved indbyrdes at afstive 35 hinanden.The object of the invention is to indicate how this, in itself suitable manufacturing technique, can be used not only for the production of relatively small and light objects, but also for the production of large, relatively heavy, and extremely sustainable elements which are distinguished by a shape stability. which is substantially based on a corresponding thickness of the material layer deposited on the forming substrate. In comparison, the material thickness of said small and light objects is rather low, and the practically necessary stiffness is usually provided by a deliberate design of wall portions which, for example, provide support for said objects, the walls producing a relatively rigid overall subject by mutually supporting 35 each other.
Det angivne formål opnås ifølge opfindelsen ved, at DK 168020 B1 2 der af det fluidiserede cellulosefiberråstof fremstilles en pulp, som under anvendelse af et langfibret udgangsmateriale har forbedrede afvandingsegenskaber, at denne pulp påføres underlaget i en sådan mængde, og at påsugningen foretages 5 styret på en sådan måde, at der på underlaget ved påsugningen afsættes et fiberråstof lag med så stor en tykkelse, at denne tilvejebringer den for genstanden ønskede formstabilitet, hvorefter genstanden færdiggøres.The stated object is achieved according to the invention in that DK 168020 B1 2 produces from the fluidized cellulose fiber raw material a pulp which, using a long-fiber starting material, has improved dewatering properties, that this pulp is applied to the substrate in such an amount and that the suction is carried out in a controlled manner. in such a way that a fiber raw material layer of such thickness is deposited on the substrate upon suction to provide the desired shape stability for the article, after which the article is completed.
GB-patentskrift nr. 1.589.077 omhandler en formstøb-10 ning af genstande, der er sammensat af dele med forskellig tykkelse, hvilket opnås ved, at koncentrationen af støbeformens sugehuller, som skal fjerne væskefasen fra en fiberhol-dig suspension, varieres fordelt over formoverfladen.GB-A-1,589,077 discloses a molding of articles composed of different thickness parts, which is achieved by varying the concentration of the suction holes of the mold to remove the liquid phase from a fibrous suspension. mold surface.
SE-fremlæggelsesskrift nr. 324.498 omhandler en netdug 15 med et varieret maskemønster til tilvejebringelse af variationer af vægtykkelsen af genstande, som støbes ved påsugning af en fiberholdig masse på netdug.SE Patent Laid-Open No. 324,498 discloses a web 15 having a varied mesh pattern to provide variations in the wall thickness of articles molded by suction of a fibrous web onto the web.
US-patentskrift nr. 3.325.349 omhandler foranstaltninger til styring af den til fremstilling af en bestemt 20 genstand fornødne pulpmængde ved at formindske tykkelsen af visse dele af genstanden. I dutte øjemed gøres der brug af en specifik perforering af den anvendte sugeform.U.S. Patent No. 3,325,349 discloses measures for controlling the pulp quantity required to produce a certain amount of pulp by reducing the thickness of certain portions of the article. For nap purposes, a specific perforation of the suction mold used is made.
US-patentskrift nr. 2.079.667 omhandler foranstaltninger, der tilstræber en ensartet lagtykkelse af den støbte 25 genstand, hvilket skal opnås ved hjælp af en speciel udformning af den anvendte støbeform.U.S. Patent No. 2,079,667 discloses measures that aim at uniform layer thickness of the molded article, which must be achieved by a special design of the mold used.
I modsætning til denne kendte teknik er det væsentlige for opfindelsen at anvende en pulp, der kan afvandes særlig nemt, så at en væsentlig forøget tykkelse af det afsatte 30 fiberråstoflag er tilvejebragt ved en forøgelse af pulpmassens væskeafgivelsesevne, hvilket igen er opnået ved anvendelse af et langfibret udgangsmateriale.Contrary to this prior art, it is essential for the invention to use a pulp that can be dewatered particularly easily so that a substantially increased thickness of the deposited fiber raw material layer is provided by increasing the pulp's fluid delivery capacity, which is again achieved by using a pulp material. long-fiber starting material.
Herved vil det være muligt under udnyttelse af den ovennævnte fremstillingsteknik også at fremstille bæredygtige 35 elementer såsom lastepaller og byggeelementer, som i modsætning til de nævnte emballageeksempeler kan udvise forholdsvis DK 168020 B1 3 jævne og glatte yder flader, og som i sig selv udviser en stor formstabilitet. Afsætningen af et fiberråstof lag med den definerede tykkelse betyder, at der ved det til påsug-ningen anvendte undertryk i fiberråstoflaget kan tilveje-5 bringes en materialetæthed, der er størst ved den yderside af materialelaget, som vender mod formfladen, og som vil virke forstærkende, idet den ligger i afstand fra den afsatte genstands gennemgående midterplan.Hereby, it will be possible to make use of the aforementioned manufacturing technique to produce sustainable elements such as pallets and building elements which, in contrast to the mentioned packaging examples, can exhibit relatively smooth and smooth outer surfaces and which in themselves exhibit a large form stability. The deposition of a fiber raw material layer of the defined thickness means that, under the suction pressure applied to the suction material, a material density can be provided which is greatest at the outer surface of the material layer facing the mold surface and which will act as reinforcing material. , being at a distance from the central median plane of the deposited object.
10 EksempelExample
Som udgangsmateriale anvendes der i eksemplet "returpapir", der har et stort, i eksemplet ca. 80% indhold af cellulosefibre med en længde op til 3,5 mm (nåletræ), ca.As the starting material, in the example "recycled paper" which has a large, in the example approx. 80% content of cellulose fibers with a length up to 3.5 mm (conifer), approx.
18% kortere fibre, samt ca. 2% småpartikler.18% shorter fibers, and approx. 2% small particles.
15 Ved en tørproces-behandling f.eks. i en shredder, efterfulgt af en tørproces-behandling i en hammermølle gennemføres en løsnen af udgangsmaterialets fiberstruktur i dennes bestanddele, hvilket kontrolleres eksempelvis ved valg af hulstørrelse og lysningsareal af et i hammermøllen 2 0 indbygget sold.In a dry process treatment e.g. in a shredder, followed by a dry process treatment in a hammer mill, a loosening of the starting material's fiber structure is carried out in its constituents, which is checked, for example, by selecting the hole size and luminous area of a screen built into the hammer mill.
De således frilagte fibre tilføres doseret til en pulper, således som den er kendt fra papirfabrikationen, og hvori de behandles i ca. 3 minutter, og den deraf resulterende pulp er da færdig til påføring på det formgivende 25 underlag. Denne behandlingstid udgør ca. 10-20% af den behandlingstid, som må anvendes for fremstillingen af en færdig pulp af samme udgangsmateriale, som ikke er blevet underkastet den nævnte tørproces-behandling.The fibers thus exposed are fed dosed to a pulper, as is known from the paper manufacture, and in which they are processed for approx. 3 minutes, and the resulting pulp is then ready for application to the shaping substrate. This processing time amounts to approx. 10-20% of the processing time which may be used for the preparation of a finished pulp of the same starting material which has not been subjected to said dry process treatment.
Ved den beskrevne samlede behandling bliver der opnået 30 en væsentlig forbedring af afvandingsegenskaberne, idet afvandingshastigheden under påsugningen af pulpen på det formgivende underlag blev forøget 4 gange i forhold til en påsugningsproces gennemført med en pulp, der er fremstillet uden anvendelse af den forudgående tørproces-behandling.In the overall treatment described, a significant improvement in the dewatering properties is obtained, since the dewatering rate during suction of the pulp on the shaping substrate was increased 4 times over a suction process carried out with a pulp made without the use of the previous dry process treatment. .
35 Forøgelsen af afvandingshastigheden medfører, at også produkter, der med henblik på formstabilitet skal have DK 168020 B1 4 en stor masse, f.eks. et pladeemne på 1,2 x 0,8 m og en vægt på 3 kg, har kunnet fremstilles ved en påsugningstid på 30 sekunder.The increase in the drainage rate also means that products which, for the sake of shape stability, must have a large mass, e.g. a plate blank of 1.2 x 0.8 m and a weight of 3 kg has been produced at a suction time of 30 seconds.
Under udnyttelse af lagtykkelsen af den således frem-5 stillede genstand kan dennes formstabilitet som angivet i krav 2 også forøges ved, at der fordelt over fiberråstof laget i dette tilvejebringes én eller flere variationer i lagtykkelsen ved, at påsugningseffekten under en fælles påsug-ningsproces for den til hele genstandens fremstilling for-10 nødne fiberpulpmængde varieres tilsvarende lokalt. På denne måde vil der under én og samme arbejdsoperation, dvs. fiberråstoffets afsætning på det formgivende underlag kunne formes både den for genstanden ønskede endelige yderside, og under udnyttelse af materialelagets tykkelse en formstabiliteten 15 øgende formgivet struktur i selve det genstanden dannende materialeemne. En sådan struktur vil som angivet i krav 3 eksempelvis kunne udformes som et sammenhørende strukturmønster med en i forhold til de øvrige områder af genstanden større lagtykkelse.Utilizing the layer thickness of the article thus produced, its mold stability as set forth in claim 2 can also be enhanced by providing one or more variations in the layer thickness by distributing the suction effect during a common suction process for the layer thickness thereof. the amount of fiber pulp needed for the whole article is similarly varied locally. In this way, during one and the same work operation, i.e. The deposition of the fiber raw material on the shaping substrate could be shaped both at the final outer surface desired for the article and, utilizing the thickness of the material layer, a molding stability increasing the shaped structure of the article material forming itself. Such a structure, as stated in claim 3, can, for example, be designed as a coherent structural pattern with a greater layer thickness relative to the other areas of the object.
20 En hensigtsmæssig måde til gennemførelse af fremgangs måden ifølge opfindelsen er angivet i krav 4 og er ejendommelig ved, at der til påsugning af en let afvandelig pulp af fiberråstoffet i den ønskede tykkelse anvendes en for et luftformigt, ved et undertryk virksomt arbejdsmedium gen-25 nemtrængelig form, som har en for arbejdsmediet gennemtræn-gelig formflade, hvis permeabilitet er afpasset efter tykkelsen af det fiberråstoflag, som skal af lej res ved påsugning af pulpen på denne flade.A convenient method for carrying out the method according to the invention is set forth in claim 4 and characterized in that a gaseous pulp of the fibrous raw material of the desired thickness is used for a gaseous working medium under pressure. easy-to-mold form having a permeable surface permeable to the working medium, the permeability of which is adapted to the thickness of the fiber raw material layer to be deposited by suction of the pulp on this surface.
Herved kan der opnås et sådant samspil mellem pulpens 30 af vandelighed, og formfladens påsugningsevne, at også elementer med en som følge af den ønskede formstabilitet stor fiberlagtykkelse kan fremstilles rationelt.In this way, such an interaction can be achieved between the pulpability 30 of the pulp 30 and the suction surface of the mold surface, that also elements having a high fiber layer thickness due to the desired shape stability can be produced rationally.
Til opnåelse af lokale variationer i lagtykkelsen af elementets fiberråstoflag kan der som angivet i krav 5 an-35 vendes en form, hvis formflade har en permeabilitet, der varierer i overensstemmelse med lagtykkelsen af henholdsvis DK 168020 B1 5 den eller de lokale variatoner af, eller det sammenhørende strukturmønster af det ved påsugning på formfladen afsatte, let afvandelig fiberpulplag.In order to obtain local variations in the layer thickness of the element raw material layer, as indicated in claim 5, a mold whose shape surface has a permeability which varies according to the layer thickness of the local variation or localities of or the associated structural pattern of the easily degradable fiber pulp film deposited on the mold surface.
Dette betyder, at afsætningen af fiberråstof på form-5 fladen vil være forskellig alt efter selve denne flades permeabilitet, hvorved påsugningseffekten vil variere lokalt, således at der ved områder, hvor formfladens permeabilitet er ringe, vil ske en formindsket afsætning af fiberråstof på formfladen, medens afsætningen vil være stor i områder, 10 hvor formfladens permeabilitet er stor.This means that the deposition of fibrous raw material on the mold surface will be different according to the permeability of this surface itself, whereby the suction effect will vary locally, so that in areas where the mold surface permeability is poor, a reduced deposition of fibrous material on the mold surface will occur. while the deposition will be large in areas where the permeability of the mold surface is high.
Til fremstilling af en pulp, der skal være let afvandelig, kan der som angivet i krav 6 som fiberråstof anvendes et udgangsmateriale, der indeholder lange fibre, og som forarbejdes til en pulp ved anvendelse dels af en udslagning 15 i en pulper, dels af en forudgående, separat, styret tørfor-maling, ved hvilken udgangsmaterialet opdeles i doserbare mængder og findeles i sine fibre, hvorefter genstanden fremstilles af den således dannede pulp.For the preparation of a pulp which is to be easily degradable, as indicated in claim 6, as a fiber raw material, a starting material containing long fibers can be used which is processed into a pulp using a cutout 15 in a pulp and partly by a pulp. prior, separately, controlled dry milling, in which the starting material is divided into dosed quantities and comminuted into its fibers, after which the article is made of the pulp thus formed.
Anvendelsen af en pulper som et væsentligt bearbejd-20 ningstrin af fiberråstofferne til dannelse af en pulp, hvoraf de ønskede genstande skal fremstilles, sker bl.a. i tilfælde, hvor fiberråstofferne modtages som tørre masser i baller, eksempelvis som papiraffald.The use of a pulp as an essential machining step of the fiber raw materials to form a pulp from which the desired articles are to be made, inter alia in cases where the fiber raw materials are received as dry masses in bales, for example as paper waste.
I pulperen fremkaldes en kraftig hvirveldannelse, 25 hvorved materialets enkeltdele gnider mod hinanden, og derved bliver findelt, hvorved råstofferne opdeles i fibre.In the pulper a vigorous vortex is produced, whereby the individual parts of the material rub against each other, thereby being finely divided, whereby the raw materials are divided into fibers.
Især ved heterogent materiale såsom affalds- eller genbrugspapir må der regnes med, at denne opdeling foregår successivt, således at de fibre, der frigøres først, udsættes 30 for en yderligere, væsentlig bearbejdning fremfor de senere frigjorte fibre. Med andre ord vil bearbejdningen i pulperen i sit forløb således være ukontrolleret, og derved uensartet. Nævnte yderligere bearbejdning medfører, at både formalingsgraden (°SR-Schopper-Riegler), og dermed slimdannelsen i 35 pulperen forøges, hvilket har en negativ indflydelse på den senere afvanding af den af pulpen fremstillede genstand, DK 168020 B1 6 samt forøger krympningen af genstanden under afvandingen og tørringen af dennes materiale.Especially with heterogeneous materials such as waste or recycled paper, it is to be expected that this division takes place successively, so that the fibers that are first released are subjected to further substantial processing over the later released fibers. In other words, the machining of the pulper in its course will thus be uncontrolled, and thus uneven. Said further machining results in both the degree of grinding (° SR-Schopper-Riegler) and thus the mucus formation in the pulp being increased, which has a negative effect on the later dewatering of the pulp made article, DK 168020 B1 6 and increases the shrinkage of the article. during the dewatering and drying of its material.
Ved fremgangsmåden ifølge krav 6 opnås, at der til pulperen i det mindste delvis tilføres et fiberråstofmate-5 riale, hvis fibre allerede i en væsentlig grad er opdelt i enkeltfibre, hvorfor de er mere umiddelbart og samtidig modtagelige for den i pulperen tilvejebragte selvformalings-påvirkning og sammenblandingseffekt. Idet pulperen forarbejder et mere ensartet råstofmateriale, kan også den i pulperen 10 ved selvformaling tilvejebragte formalingsgrad styres til at være mere ensartet, og den føromtalte binding af vand i den fra pulperen afgående pulp vil dermed være bedre styrbar.By the method of claim 6, it is achieved that at least partially a fiber raw material is supplied to the pulper, the fibers of which are already substantially divided into single fibers, which is why they are more immediately and simultaneously susceptible to the self-grinding effect provided in the pulper. and mixing effect. As the pulper processes a more uniform feedstock, the degree of grinding provided in the pulper 10 can also be controlled to be more uniform, and the aforementioned bonding of water in the pulp exiting the pulper will thus be better controllable.
Samme fremgangsmåde vil imidlertid også medføre andre fordele, som er særlig værdifulde ved genanvendelse af pa-15 piraffald.However, the same approach will also bring other benefits which are particularly valuable in recycling paper waste.
Genbrugs-papiraffald forefindes i mange forskellige kvaliteter og sorteringer. Underkastes dette materiale forud for udslagningen i pulperen en separat, styret tørformaling, vil man ofte kunne anvende en dårligere, og dermed billigere 20 materialekvalitet, end hvis opdelingsprocessen udelukkende blev gennemført som en udslagning i pulperen.Recycled paper waste is available in many different grades and grades. If this material is subjected to a separate controlled dry grinding prior to the pulverization, it will often be possible to use a poorer, and thus cheaper, material quality than if the partitioning process was carried out solely as a pulverization.
Det ligger inden for opfindelsens rammer at gennemføre den nævnte forudgående, separate tørformaling som en flertrinsproces, hvorved man på særlig effektiv måde vil kunne 25 opdele udgangsmaterialet i doserbare mængder.It is within the scope of the invention to carry out the aforementioned, separate dry milling process as a multi-stage process, whereby the starting material can be divided into dosable quantities in a particularly effective manner.
På denne måde vil eksempelvis også et affaldspapirmateriale, som indeholder plast, vådstærkt papir, plastlamineret karton og papir, i ønsket omfang kunne opdeles i fibre og andre partikler. Opdelte bestanddele, der ikke er papir, 30 kan da forud for tilførselen til pulperen frasepareres, eller også vil disse bestanddele, da de foreligger i findelt stand, kunne indgå i den efterfølgende produktionsproces.In this way, for example, a waste paper material containing plastics, wet-strength paper, plastic laminated cardboard and paper can also be divided into fibers and other particles to the desired extent. Non-paper split components may then be separated prior to delivery to the pulper or, as they are in finely divided condition, these components may be included in the subsequent production process.
Ved en udførelsesform for den nævnte fremgangsmåde kan et, en separat, styret tørformaling underkastet lang-35 fibret udgangsmateriale tilsættes en allerede i pulperen dannet pulp og underkastes en fælles tidsbegrænset udslagning DK 168020 B1 7 med denne.In one embodiment of the aforementioned method, a separately controlled dry grind subjected to long-fiber starting material may be added to a pulp already formed in the pulper and subjected to a common time-limited extinction thereof.
På denne måde kan der produceres en genstand, hvis fibermateriale dels hovedsagelig er bundet ved hydrogene fiberbindinger, dels har fået iblandet i luft suspenderet 5 fibermateriale, til hvis binding der i reglen anvendes lim.In this way, an article can be produced, the fiber material of which is mainly bonded by hydrogen-bonded fiber, and partly mixed with air-suspended fiber material, to which bonding is usually used glue.
Det har vist sig, at man på denne måde kan give afkald på en traditionel, fuldstændig hydrogen binding af hele pulpen, hvilket betyder, at afvandingen, og dermed produktionstiden for genstanden kan afkortes væsentligt. Endvidere giver 10 metoden mulighed for en nøje kontrol med de for genstanden ønskede stabiliserende styrkeegenskaber, idet disse vil kunne styres nøje ved tilsætning af lim.It has been found that in this way a traditional, completely hydrogen bonding of the whole pulp can be dispensed, which means that the dewatering, and thus the production time of the object, can be significantly shortened. Furthermore, the method allows for close control of the stabilizing strength properties desired for the object, which can be controlled precisely by the addition of glue.
Disse fordele er af væsentlig betydning for en rationel" og dermed økonomisk industriel fremstilling også af 15 store, formstabile genstande ved anvendelse af den beskrevne påsugningsteknik.These advantages are essential to a rational "and thus economically industrial manufacture" also of 15 large, shape-stable objects using the described suction technique.
En i flere trin opdelt tørformaling vil eksempelvis kunne gennemføres ved anvendelse af en flængemaskine, også kaldet shredder, efterfulgt af en behandling i en hammermøl-20 le, som således kan modtage materialet fra shredderen i doserbare mængder, og som udsætter materialet for en yderligere findelingspåvirkning, før det, om ønsket ligeledes i specielt doserbare mængder, tilføres pulperen til den egentlige udslagningsbearbejdning.For example, a multi-stage dry milling can be carried out using a blender, also called shredder, followed by a treatment in a hammer mill which can thus receive the material from the shredder in dosed quantities and subject the material to a further comminution effect. before, if desired, also in especially dispensable amounts, the pulper is fed to the actual knockout operation.
25 Den ovennævnte separate, styrede tørformaling af fiberråstofferne forud for deres udslagning i pulperen åbner ligeledes muligheden for medanvendelse af genbrugs-affaldspapir i tilfælde, hvor de genstande, der skal fremstilles, skal være krympefrie og målfaste. Et udgangsmateriale med 30 et højt indhold af træholdige fibre medfører mindre krympning, end hvis fibrene var cellulosefibre. Det har vist sig, at der ved anvendelse af fremgangsmåden ifølge opfindelsen til et træholdigt papirråmateriale endda kan tilsættes en væsentlig mængde prisbilligt genbrugs-affaldspapir, her-35 under papaffald, som ikke nødvendigvis er træholdigt, idet der i pulperen på grund af den forudgående separate, styrede DK 168020 B1 8 tørformaling af råmaterialet vil kunne fremstilles en pulp, som ikke medfører nogen uønsket krympning af de fremstillede genstande.25 The aforementioned separate, controlled dry milling of the fiber raw materials prior to their scraping in the pulper also opens up the possibility of reuse waste paper in cases where the articles to be manufactured must be shrink-free and target-proof. A starting material with a high content of wood-containing fibers causes less shrinkage than if the fibers were cellulose fibers. It has been found that by applying the method of the invention to a wood-containing paper raw material, a substantial amount of affordable recycled waste paper can be added, including cardboard waste, which is not necessarily wood-containing, because of the prior separate , controlled dry grinding of the raw material will be able to produce a pulp which does not cause any unwanted shrinkage of the manufactured articles.
Det er i princippet kendt til fremstilling af gen-5 stande af et fluidiseret fiberråstof at anvende hjælpestoffer i form af fyldstoffer og kemikalier, samt bindemidler. Hjælpestofferne bestemmer, hvorvidet de fremstillede genstande skal være mere eller mindre stærke, hårde og transparente, eller svage, bløde og sugende. Den foreliggende opfindelse 10 medfører også fordele i forbindelse med anvendelsen af sådanne hjælpestoffer.In principle, it is known to produce articles of a fluidized fibrous material to use adjuvants in the form of fillers and chemicals, as well as binders. The adjuvants determine whether the manufactured articles should be more or less strong, hard and transparent, or weak, soft and absorbent. The present invention 10 also provides advantages in using such auxiliaries.
Opdelingen af fremstillingsprocessen i flere fremstillingstrin giver nemlig forøget mulighed for at tilsætte hjælpestofferne på forskellige stadier af den samlede frem-15 stillingsproces. Den som følge af den for opfindelsen ejendommelige bearbejdning opnåede åbne struktur af den endelige pulp gør endda denne i forøget grad tilgængelig for hjælpestofferne, således at eksempelvis et bindemiddel kan påføres mere eller mindre integrerende i de fremstillede genstandes 20 overflade til tilvejebringelse af en forøget vægstyrke. Tilsætningen af hjælpestofferne under den forudgående separate, styrede tørformaling vil på særlig god måde kunne fremme en særdeles ensartet fordeling af hjælpestofferne i den fremstillede fibermasse. Naturligvis kan hjælpestofferne 25 også stadig tilsættes i pulperen.Namely, the division of the manufacturing process into several manufacturing stages allows for increased additives at various stages of the overall manufacturing process. The resultant open structure of the final pulp obtained by the machining of the invention even makes it increasingly available to the auxiliaries, so that, for example, a binder can be applied more or less integrally in the surface of the manufactured articles 20 to provide an increased wall strength. The addition of the adjuvants during the preceding separate controlled dry milling may, in a particularly good way, promote a very uniform distribution of the adjuvants in the produced pulp. Of course, the auxiliaries 25 can also still be added to the pulper.
Det ligger endvidere inden for opfindelsens rammer, at udslagningen i pulperen gennemføres som en i afhængighed af den forudgående separate formaling styret forarbejdningsproces. Med andre ord kan den i pulperen tilvejebragte grad 30 af selvformaling tilpasses efter graden af den formaling, som alt efter forholdene er blevet gennemført ved det eller de forudgående formalingstrin. Eksempelvis kan en papirpulp, der i pulperen er opdelt til en normalt, ved selvformaling tilvejebragt formalingsgrad på 60“SR (Schopper-Riegler), 35 tilsættes et ved tørformaling tilvejebragt fibermateriale, hvorefter blandingen bearbejdes i pulperen i yderligere 5 i l DK 168020 Bl 9 minutter. Genstande fremstillet af en sådan blandingspulp kan gives en særlig stor tykkelse, porøsitet og permeabili tet. Dette betyder, at produkterne kan have gode afvandingsegenskaber, og derfor kan fremstilles også med store godstyk-5 kelser.Furthermore, it is within the scope of the invention that the knockout in the pulper is carried out as a processing process controlled in dependence on the prior separate milling. In other words, the degree of self-grinding provided in the pulper can be adjusted to the degree of grinding which has been carried out according to the conditions at the preceding grinding step (s). For example, a paper pulp divided into the pulper to a normal grinding degree of 60 "SR (Schopper-Riegler), 35 can be added to a dry grinding fiber material, after which the mixture is processed in the pulper for a further 5 to 16 minutes. . Objects made from such blending pulp can be given a particularly large thickness, porosity and permeability. This means that the products can have good dewatering properties and therefore can also be manufactured with large thicknesses of material.
En til anvendelse ved fremgangsmåden ifølge opfindelsen fremstillet let afvandelig pulp muliggør problemløst en ensartet tilførsel af fibersuspensionen over formen, selv i tilfælde af fremstillingen af genstande med stor vægtykkelse.A readily degradable pulp made for use in the process of the invention allows for a uniform application of the fiber suspension over the mold, even in the case of the manufacture of articles of high wall thickness.
10 Affaldspapir, også kaldet returpapir, kan være meget sammensat, og indeholde fibre med mange forskellige læng der. Alligevel har det vist sig, at gennemsnitsfiberlængden er så stor, at de ovenfor anførte især afvandingsmæssige og strukturelle fordele kan opnås, når dette papirmateriale 15 indgår i fremstillingsprocessen.10 Waste paper, also called recycled paper, can be very complex and contain fibers of many different lengths. Nevertheless, it has been found that the average fiber length is so large that the above mentioned dewatering and structural advantages can be obtained when this paper material 15 forms part of the manufacturing process.
Fremgangsmåden ifølge opfindelsen vil kunne anvendes til forarbejdning også af såkaldt virgin-materiale.The process according to the invention can be used for processing also so-called virgin material.
Claims (9)
Priority Applications (21)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DK592488A DK168020B1 (en) | 1988-10-25 | 1988-10-25 | PROCEDURE FOR THE PREPARATION OF FORM STABLE ARTICLES FROM A FLUIDIZED CELLULOSE FIBER MATERIAL |
| CA002001296A CA2001296A1 (en) | 1988-10-25 | 1989-10-24 | Method for the manufacture of countour-stable objects |
| NZ231149A NZ231149A (en) | 1988-10-25 | 1989-10-25 | Manufacturing form-stable articles from fibrous material by de-watering on a mould |
| CN89108946A CN1025060C (en) | 1988-10-25 | 1989-10-25 | Method for manufacture of contour stable objects |
| PCT/DK1989/000250 WO1990004678A1 (en) | 1988-10-25 | 1989-10-25 | Method for the manufacture of contour-stable objects |
| AT0903089A AT398093B (en) | 1988-10-25 | 1989-10-25 | METHOD FOR PRODUCING SHAPE-RESISTANT ITEMS |
| CH2211/90A CH677944A5 (en) | 1988-10-25 | 1989-10-25 | |
| EP89912229A EP0441835B1 (en) | 1988-10-25 | 1989-10-25 | Method for the manufacture of contour-stable objects |
| AU44950/89A AU636585B2 (en) | 1988-10-25 | 1989-10-25 | Method for the manufacture of contour-stable objects |
| GR890100687A GR890100687A (en) | 1988-10-25 | 1989-10-25 | Method for the construction of objects having a stable outline |
| PT92098A PT92098A (en) | 1988-10-25 | 1989-10-25 | PROCESS OF MANUFACTURE OF STABLE CONTOUR OBJECTS |
| NL8921150A NL8921150A (en) | 1988-10-25 | 1989-10-25 | Method for fabricating shape-retaining articles |
| BR898905455A BR8905455A (en) | 1988-10-25 | 1989-10-25 | PROCESS FOR THE MANUFACTURE OF STABLE CONTOUR OBJECTS |
| DE19893991216 DE3991216T (en) | 1988-10-25 | 1989-10-25 | |
| ES8903596A ES2017055A6 (en) | 1988-10-25 | 1989-10-25 | Method for the manufacture of contour-stable objects. |
| MX018108A MX169792B (en) | 1988-10-25 | 1989-10-25 | METHOD FOR THE MANUFACTURE OF REINFORCED STABLE OBJECTS |
| NO91911634A NO911634L (en) | 1988-10-25 | 1991-04-24 | PROCEDURE FOR MANUFACTURE OF CONTOUR STABLE OBJECTS. |
| GB9108932A GB2251402B (en) | 1988-10-25 | 1991-04-24 | Procedure for the manufacture of contour-stable objects |
| SE9101242A SE467469B (en) | 1988-10-25 | 1991-04-24 | SET FOR PREPARATION OF CONTOUR STABLE PRODUCTS |
| GB9108931A GB2243575B (en) | 1988-10-25 | 1991-04-24 | Method for the manufacture of load-carrying elements including pallets |
| FI912005A FI98549C (en) | 1988-10-25 | 1991-04-25 | Method for the manufacture of permanent products |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DK592488 | 1988-10-25 | ||
| DK592488A DK168020B1 (en) | 1988-10-25 | 1988-10-25 | PROCEDURE FOR THE PREPARATION OF FORM STABLE ARTICLES FROM A FLUIDIZED CELLULOSE FIBER MATERIAL |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| DK592488D0 DK592488D0 (en) | 1988-10-25 |
| DK592488A DK592488A (en) | 1990-04-26 |
| DK168020B1 true DK168020B1 (en) | 1994-01-17 |
Family
ID=8146198
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DK592488A DK168020B1 (en) | 1988-10-25 | 1988-10-25 | PROCEDURE FOR THE PREPARATION OF FORM STABLE ARTICLES FROM A FLUIDIZED CELLULOSE FIBER MATERIAL |
Country Status (20)
| Country | Link |
|---|---|
| EP (1) | EP0441835B1 (en) |
| CN (1) | CN1025060C (en) |
| AT (1) | AT398093B (en) |
| AU (1) | AU636585B2 (en) |
| BR (1) | BR8905455A (en) |
| CA (1) | CA2001296A1 (en) |
| CH (1) | CH677944A5 (en) |
| DE (1) | DE3991216T (en) |
| DK (1) | DK168020B1 (en) |
| ES (1) | ES2017055A6 (en) |
| FI (1) | FI98549C (en) |
| GB (2) | GB2251402B (en) |
| GR (1) | GR890100687A (en) |
| MX (1) | MX169792B (en) |
| NL (1) | NL8921150A (en) |
| NO (1) | NO911634L (en) |
| NZ (1) | NZ231149A (en) |
| PT (1) | PT92098A (en) |
| SE (1) | SE467469B (en) |
| WO (1) | WO1990004678A1 (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2667882B1 (en) * | 1990-10-12 | 1993-01-22 | Anacellulose | PROCESS FOR MANUFACTURING CONFORMED PARTS FROM PAPER PULP AND DEVICE FOR IMPLEMENTING SAME. |
| JP2836801B2 (en) * | 1992-03-06 | 1998-12-14 | 日本碍子株式会社 | Papermaking mold, papermaking method and papermaking apparatus for fiber molded product, and paper made fiber molded product |
| JP2836800B2 (en) * | 1992-03-06 | 1998-12-14 | 日本碍子株式会社 | Papermaking mold, papermaking method and papermaking apparatus for fiber molded product, and paper made fiber molded product |
| DE4402318A1 (en) * | 1994-01-27 | 1995-08-03 | Gerhard Dipl Chem Huber | Simple, economic process for prodn. of high quality tubes from paper |
| FR2776224B1 (en) * | 1998-03-20 | 2000-05-26 | Kerlane | THIN PARTS OF MINERAL FIBERS, METHOD AND MOLD FOR THEIR MANUFACTURE BY VACUUM SUCTION |
| CN1167851C (en) | 1998-12-28 | 2004-09-22 | 花王株式会社 | shaped body |
| US11970823B2 (en) * | 2019-01-24 | 2024-04-30 | Varden Process Pty Ltd | Moulded pulp fibre product forming system, apparatus, and process |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE900261C (en) * | 1944-07-04 | 1953-12-21 | Schiess Ag | Molding process |
| DE803085C (en) * | 1948-12-09 | 1951-02-26 | Kurt Mueller Dr | Method and device for the production of thick-walled molded fibrous material |
| US2718826A (en) * | 1952-01-17 | 1955-09-27 | Central Fibre Products Company | Pulp molding dies |
| US2851931A (en) * | 1955-04-04 | 1958-09-16 | Pacific Pulp Molding Company | Porous sintered metal molding die |
| DE1061670B (en) * | 1955-04-07 | 1959-07-16 | Hausser O & M | Process for the production of hollow bodies of figurative formation from malleable moisture-containing mass |
| US2981330A (en) * | 1956-12-20 | 1961-04-25 | Diamond National Corp | Pulp molding die |
| GB954305A (en) * | 1960-03-30 | 1964-04-02 | Diamond National Corp | Improvements in or relating to the molding of pulp articles |
| GB898416A (en) * | 1960-04-13 | 1962-06-06 | Bemis Bro Bag Co | Molding forms and method of making them |
| FR1284406A (en) * | 1961-03-21 | 1962-02-09 | Diamond National Corp | Method and device for molding objects of paper pulp |
| US3325349A (en) * | 1964-03-18 | 1967-06-13 | Diamond Int Corp | Method and mold for controlling stock thickness in a pulp molding operation |
| US3325345A (en) * | 1966-02-21 | 1967-06-13 | Owens Illinois Inc | Process of forming water-laid products from cellulosic pulp containing polymeric thermoplastic particles |
| US3533906A (en) * | 1967-10-11 | 1970-10-13 | Haigh M Reiniger | Permanently reacted lignocellulose products and process for making the same |
| FR2356488A1 (en) * | 1976-06-29 | 1978-01-27 | Sepr | PROCESS AND APPARATUS FOR OBTAINING HIGH-PRECISION MOLDED PARTS IN FIBROUS MATERIALS |
| FR2489738A1 (en) * | 1980-09-11 | 1982-03-12 | Isobox Sa | NEW MOLDS DESIGNED FOR THE MANUFACTURE OF EXPANDED, NON-POLAR PLASTIC MATERIALS USING ULTRA-HIGH FREQUENCY RADIATION |
| LU83899A1 (en) * | 1982-01-26 | 1983-09-02 | Terre Asbl | INSULATING PANEL |
| FR2573845B1 (en) * | 1984-11-28 | 1988-02-12 | Lafarge Refractaires | METHOD AND DEVICE FOR OBTAINING A THERMAL INSULATION PART FOR A CYLINDRICAL OBJECT, AND PART OBTAINED BY THE PROCESS |
-
1988
- 1988-10-25 DK DK592488A patent/DK168020B1/en not_active IP Right Cessation
-
1989
- 1989-10-24 CA CA002001296A patent/CA2001296A1/en not_active Abandoned
- 1989-10-25 NL NL8921150A patent/NL8921150A/en unknown
- 1989-10-25 DE DE19893991216 patent/DE3991216T/de not_active Withdrawn
- 1989-10-25 WO PCT/DK1989/000250 patent/WO1990004678A1/en not_active Ceased
- 1989-10-25 GR GR890100687A patent/GR890100687A/en unknown
- 1989-10-25 CN CN89108946A patent/CN1025060C/en not_active Expired - Fee Related
- 1989-10-25 ES ES8903596A patent/ES2017055A6/en not_active Expired - Lifetime
- 1989-10-25 BR BR898905455A patent/BR8905455A/en not_active Application Discontinuation
- 1989-10-25 EP EP89912229A patent/EP0441835B1/en not_active Expired - Lifetime
- 1989-10-25 NZ NZ231149A patent/NZ231149A/en unknown
- 1989-10-25 MX MX018108A patent/MX169792B/en unknown
- 1989-10-25 CH CH2211/90A patent/CH677944A5/de not_active IP Right Cessation
- 1989-10-25 AU AU44950/89A patent/AU636585B2/en not_active Ceased
- 1989-10-25 AT AT0903089A patent/AT398093B/en not_active IP Right Cessation
- 1989-10-25 PT PT92098A patent/PT92098A/en not_active IP Right Cessation
-
1991
- 1991-04-24 GB GB9108932A patent/GB2251402B/en not_active Expired - Fee Related
- 1991-04-24 SE SE9101242A patent/SE467469B/en not_active IP Right Cessation
- 1991-04-24 GB GB9108931A patent/GB2243575B/en not_active Expired - Fee Related
- 1991-04-24 NO NO91911634A patent/NO911634L/en unknown
- 1991-04-25 FI FI912005A patent/FI98549C/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| SE467469B (en) | 1992-07-20 |
| DK592488D0 (en) | 1988-10-25 |
| GB9108932D0 (en) | 1991-06-19 |
| SE9101242L (en) | 1991-04-24 |
| EP0441835A1 (en) | 1991-08-21 |
| FI98549C (en) | 1997-07-10 |
| MX169792B (en) | 1993-07-26 |
| CN1042389A (en) | 1990-05-23 |
| GB2243575A (en) | 1991-11-06 |
| CA2001296A1 (en) | 1990-04-25 |
| BR8905455A (en) | 1990-05-29 |
| AU4495089A (en) | 1990-05-14 |
| NO911634D0 (en) | 1991-04-24 |
| ATA903089A (en) | 1994-01-15 |
| GR890100687A (en) | 1990-11-29 |
| GB2251402A (en) | 1992-07-08 |
| GB2251402B (en) | 1993-06-23 |
| CH677944A5 (en) | 1991-07-15 |
| EP0441835B1 (en) | 1996-01-03 |
| DK592488A (en) | 1990-04-26 |
| AT398093B (en) | 1994-09-26 |
| NZ231149A (en) | 1992-10-28 |
| PT92098A (en) | 1990-04-30 |
| FI98549B (en) | 1997-03-27 |
| WO1990004678A1 (en) | 1990-05-03 |
| CN1025060C (en) | 1994-06-15 |
| FI912005A0 (en) | 1991-04-25 |
| NO911634L (en) | 1991-06-24 |
| GB9108931D0 (en) | 1991-06-19 |
| NL8921150A (en) | 1991-08-01 |
| ES2017055A6 (en) | 1990-12-16 |
| AU636585B2 (en) | 1993-05-06 |
| DE3991216T (en) | 1991-11-21 |
| GB2243575B (en) | 1992-11-18 |
| SE9101242D0 (en) | 1991-04-24 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| B1 | Patent granted (law 1993) | ||
| PBP | Patent lapsed |