EP3861169A1 - Process for the manufacture of moulded fibre-based 3-dimensional articles and articles obtainable by said process - Google Patents
Process for the manufacture of moulded fibre-based 3-dimensional articles and articles obtainable by said processInfo
- Publication number
- EP3861169A1 EP3861169A1 EP19778556.1A EP19778556A EP3861169A1 EP 3861169 A1 EP3861169 A1 EP 3861169A1 EP 19778556 A EP19778556 A EP 19778556A EP 3861169 A1 EP3861169 A1 EP 3861169A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- furnish
- fibre
- article
- foamed
- mould
- 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.)
- Granted
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21J—FIBREBOARD; MANUFACTURE OF ARTICLES FROM CELLULOSIC FIBROUS SUSPENSIONS OR FROM PAPIER-MACHE
- D21J3/00—Manufacture of articles by pressing wet fibre pulp, or papier-mâché, between moulds
- D21J3/10—Manufacture of articles by pressing wet fibre pulp, or papier-mâché, between moulds of hollow bodies
-
- 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
Definitions
- the present disclosure relates to the production of fibre-based articles having a 3-dimensional shape, such as moulded fibre-based packaging, for example bottles and other types of hollow containers.
- the disclosure relates in particular to a method of forming a moulded fibre-based article having a 3-dimensional and a moulded article produced by said method.
- moulded fibre-based 3-dimensional articles It is possible to produce moulded fibre-based 3-dimensional articles, but with some exceptions, these have so far been rather unsophisticated in shape, and mainly limited to applications with lower requirements on surface finish.
- Such articles are generally produced using permeable moulds formed of metal mesh.
- a furnish comprising water, fibre and additives is applied to a mould or die, said furnish is dewatered and the still moist article is removed from the mould and dried.
- the construction of such moulds or dies is a lengthy and expensive procedure, so this technology is limited to items produced in very substantial numbers.
- WO 2018/020219 discloses a method of forming a moulded article comprising: preparing a fibre suspension by liquidizing fibrous material in a suspending liquid using at least one high shear mixer; feeding the fibre suspension to the moulding surface of porous mould; removing said suspending liquid via the pores of said porous mould to deposit suspended fibre on said mould surface as a moulded article, the step of removing said suspending liquid comprising pressing a bladder formed of a resilient flexible impermeable membrane against the article using pressure applied behind the membrane; removing the moulded article from the porous mould and drying the moulded article using microwave radiation.
- the concentration of fibrous material in the suspending liquid is in the range of 0.5 - 10 weight-% of paper fibre in water, but it is also noted that high concentrations make it difficult to transport the suspension and to achieve an even coating in the mould. In a preferred embodiment, the concentration of fibrous material in the suspending liquid is therefore about 1 %.
- the additive may for example comprise coloring or herbicide or germicide or fungicide or beeswax or decorative particles, or a combination thereof.
- the additive amount is no more than 20 wt% of the solids content, and in some preferred embodiments, no additives are present.
- Moulded fibre-based articles such as bottle-shaped fibre-based articles, can be manufactured for example using a system and method as disclosed in WO 2016/055073.
- This system comprises a pressure device for applying a pressure to the pulp, a first compressor, a split mould having a central first cavity, said first cavity having an opening for supplying said pulp to said first cavity, one or more further cavities together surrounding said first cavity, and a wall separating said first cavity from said one or more further cavities, said wall having a structure allowing for fluid to flow between said first cavity and said one or more further cavities), said wall having a first surface facing the interior of said first cavity and supporting a layer of said pulp deposited thereon, wherein said first compressor is configured for establishing a temporary elevated fluid pressure of more than 1 bar in said one or more further cavities.
- the dewatering of the layer of pulp deposited on the inside surface of an interior cavity of a mould is performed very rapidly, and at a temperature around 100 °C. This may make it possible to shorten or even avoid a subsequent drying step where the article must be moved to a drying station, after having been removed from the aforementioned mould.
- Moulded pulp is considered a sustainable packaging material, since it can be produced from renewable sources, or even from recycled materials, and as it can be recycled again after use.
- the present disclosure sets out to address the problems of the prior art, and makes available an improved method of producing a moulded fibre-based 3- dimensional article and a moulded article exhibiting improved properties, in particular hollow fibre-based articles such as containers and bottles.
- the present disclosure makes available a method for the production of a moulded fibre-based 3-dimensional article comprising the steps of preparing a furnish, delivering said furnish into a mould to wet-form a 3- dimensional fibre-based moulded article, and dewatering said article, wherein said furnish is foamed prior to delivery to said mould.
- the fibre concentration of said furnish - prior to foaming - is higher than traditionally used, and preferably
- the fibre concentration is preferably in the interval of about 1 to about 20 weight-%, for example about 1 to about 10 weight- %, preferably more preferably about 2 to about 10 weight-%, most preferably 3 to 10 weight-%.
- said furnish is foamed in a mixing tank, producing a foamed furnish substantially immediately before said foamed furnish is introduced into the mould.
- the expression“immediately before” here means that the foamed furnish is delivered to the mould before the foam deteriorates, and preferably within about 1 minute from formation of the foam, more preferably within 1 to 30 seconds, and most preferably within 1 to 10 seconds, and most preferably within 1 to 5 seconds from formation of the foam.
- the foaming is performed in two steps, a first upstream pre- mixing step and a subsequent foaming step taking place in a mixing tank, producing a foamed furnish substantially immediately before the furnish is introduced into the mould.
- said furnish is prepared in a furnish tank located upstream, in which tank the ingredients are mixed.
- the furnish is then led, for example pumped, into a mixing tank located in close proximity to the moulding equipment.
- the furnish is then foamed in the mixing tank, and substantially immediately fed into the moulding equipment.
- the foaming is performed using vigorous mixing, pumping or by the introduction of pressurized air.
- the pre-mixing step, taking place upstream can be performed using a traditional mixer, for example an impeller, whereas the foaming step that is performed in the mixing tank, in close proximity to the moulding
- the foamed furnish has a content of air in the range of about 20 - 80 % air per volume, preferably about 30 - 70 %, more preferably 40 - 60 %.
- said furnish comprises an additive chosen from a polyvinyl alcohol, a sodium dodecyl sulphate, a carboxymethyl cellulose, a surfactant, or combinations thereof.
- said furnish comprises at least one of the following additives: a wet-strength agent; a retention agent (such as a retention polymer); and a
- said furnish comprises at least two of said additives. In one embodiment, said furnish comprises all of said additives.
- the 3-dimensional article is a container for liquids, preferably a fibre-based bottle.
- the foamed furnish comprises fibers of different origin, such as cellulose fibers and synthetic fibers.
- the foamed furnish comprises fibers of different length.
- the foamed furnish comprises a functional additive chosen from natural and synthetic polymers, pigments, fillers and combinations thereof.
- the wet-formed 3-dimensional article is dewatered by applying vacuum to the outside of the mould, or by applying pressure to the inside of the mould, or a combination of the two, and subsequently removed from the mould.
- the distribution of the furnish is improved, and according to an embodiment, freely combinable with the previous embodiments, the wet-forming of said 3-dimensional article takes place during a time period in the interval of 1 - 20 seconds.
- the 3-dimensional article has lower water content after dewatering, but before demoulding and drying, than traditionally produced articles, preferably a water content of about 50 to about 75 % after dewatering.
- a second aspect of the present disclosure relates to a 3-dimensional moulded fibre-based article, obtainable by a method according to any one of the above first aspect and embodiments thereof.
- the article is a hollow article, such as a container for liquids, preferably a fibre-based bottle.
- Fig. 1 is a schematic illustration of the process flow used in the experiments, comprising the steps of pre-mixing, mixing tank foaming, wet-forming and dewatering/drying.
- Fig. 2 shows the effect of Poval 23-88 on the stability of the foam when added in different concentrations.
- Figure 3 is a bar diagram showing an example of the reduction of wet- forming time achieved with a foamed furnish, compared to a traditional furnish and a traditional furnish in an optimized process.
- Figure 4 is a bar diagram showing an example of how the foaming disclosed herein makes it possible to use a significantly more concentrated furnish.
- Figure 5 is a bar diagram showing the Pressure Resistance Index, PRI for a number of moulded articles (fibre-based bottles), i.e. a reference (at 0.5 % furnish concentration) and four different foaming agents used with seven different settings (at 1.5 % furnish concentration).
- a furnish comprises water, cellulose fibre and additives, for example sizing, fillers, optical brighteners etc.
- the term“fibre” encompasses cellulose fibre, such as virgin fibre, for example bleached and/or unbleached kraft pulp, or chemithermomechanical pulp (CTMP), but also includes recirculated fibre, pulped recycled paper, such as pulped newsprint, de-inked pulp (DIP) etc.
- CMP chemithermomechanical pulp
- DIP de-inked pulp
- the term“fibre” also encompasses other natural fibres, as well as synthetic fibres of different composition, length and width.
- foaming agent is used to describe an additive capable of aiding and/or sustaining foaming when air is mixed into the furnish.
- Pressure Resistance denotes a measure of the strength of the bottles used in this disclosure. A method was designed specifically for the purpose of exploding bottles, and for accurately measuring the burst pressure.
- Pressure Resistance Index denotes a normalized value, obtained by dividing the measured pressure resistance with the weight of oven dry fibre (in gram) for each measured bottle.
- the present disclosure makes available a method for the production of a moulded fibre-based 3-dimensional article comprising the steps of preparing a furnish, delivering said furnish to a mould to wet-form a 3- dimensional fibre-based moulded article, and dewatering said article, wherein said furnish is foamed prior to delivery to said mould.
- Foaming the furnish offers many advantages, such as a more even distribution of the fibre, and a lower water content, reducing the dewatering time of the article in the mould. A shortened dewatering time reduces the cycle time and increases throughput. A more even distribution of fibre reduces flocculation and results in more uniform and smoother surfaces in the 3-dimensional article. These advantages are even more pronounced when a 3-dimensional article having a complicated shape, such as a hollow shape, is produced.
- the fibre concentration of the furnish is higher than traditionally used, and preferably significantly higher such as at least 1 weight-%, more preferably at least 2 weight-%, most preferably at least 3 weight-% or higher.
- the fibre concentration is preferably in the interval of about 1 to 20 weight-%, for example about 1 to 10 weight-%, preferably more preferably 2 to 10 weight-%, most preferably 3 to 10 weight-%.
- a higher fibre concentration in the furnish is very advantageous also because it reduces the water consumption and thus the environmental impact of the process. Possibly also the energy requirement is reduced, both as less water needs to be pumped in the process flows, and as less energy is required for dewatering and drying the 3-dimensional article.
- said furnish is foamed in a mixing tank, producing a foamed furnish substantially immediately before said foamed furnish is introduced into the mould.
- the expression“immediately before” means that the foamed pulp is delivered to the mould before the foam deteriorates, and preferably within about 1 minute from formation of the foam, more preferably within 1 to 30 seconds, and most preferably within 1 to 10 seconds, and most preferably within 1 to 5 seconds from formation of the foam.
- the foaming is performed in two steps, a first upstream pre- foaming step and a second subsequent foaming step taking place in a mixing tank, producing a foamed furnish substantially immediately before the furnish is introduced into the mould.
- the furnish is prepared in a furnish tank located upstream, in which tank the ingredients are mixed and the furnish optionally is pre- foamed.
- the furnish is then led, for example pumped, into a mixing tank located in close proximity to the moulding equipment.
- the furnish is then foamed in the mixing tank, and substantially immediately fed into the moulding equipment.
- a pre-mixing step, taking place upstream, can be performed using a traditional mixer, for example an impeller, whereas the foaming step that is performed in the mixing tank, in close proximity to the moulding equipment, is more vigorous, and performed for example using an injector mixer.
- a traditional mixer for example an impeller
- foaming step that is performed in the mixing tank, in close proximity to the moulding equipment is more vigorous, and performed for example using an injector mixer.
- other types of mixing equipment are contemplated, such as but not limited to impeller-based mixers, a pump or re-circulation based mixers, and mixing based on the injection of
- the foamed furnish has a content of air in the range of about 20 - 80 % air per volume, such as about 30 - 70 %, and preferably about 40 - 60 %.
- the inclusion of such a high proportion of air has many advantages, among others that the tiny bubbles in the foam encase individual fibre and particles included in the furnish, resulting in a homogenous distribution and stabilizing the mixture.
- functional additives such as natural and synthetic polymers, fibre of varying length, fillers, etc.
- the furnish comprises an additive chosen from a polyvinyl alcohol (PVOH), sodium dodecyl sulphate (SDS), carboxymethyl cellulose (CMC), a surfactant, such as a non-ionic surfactant, or combinations thereof.
- the additive is added in a concentration sufficient to produce stable foam, i.e. foam which retains at least about 60 % of its volume at 60 seconds from formation.
- the concentration of additive is in the interval of 0.05 - 0.15 g/g fibre.
- the exact amount of additive is dependent on the type of additive chosen, and the character of other additives and components used in the furnish. It is
- said furnish may comprise at least one of the following additives (which are all commonly used in the field of papermaking): a wet-strength agent; a retention agent (such as a retention polymer); and a
- said furnish comprises at least two of said additives (i.e. wet-strength agent + retention agent, wet-strength agent + hydrophobic sizing agent or retention agent + hydrophobic sizing agent).
- said furnish comprises all of said additives. The exact amount of additive is dependent on the type of additive chosen, and the character of other additives and components used in the furnish.
- the 3-dimensional fibre-based article is a container for liquids, preferably a fibre-based bottle.
- the inventors have shown that the method where a foamed furnish is used to produce paper bottles results in strong and smooth bottles, with good handling properties immediately after dewatering, and with a good finish and high strength after drying.
- the foamed furnish comprises fibers of different origin, such as cellulose fibers and synthetic fibers.
- synthetic polymer fibre could be added, and the type of polymer chosen such, that it melts at least partially at the drying temperature of the 3-dimensional article, thus reinforcing said 3-dimensional article.
- other functional additives are used, for example additives increasing the dry strength of the finished product.
- Synthetic fillers which melt at the drying temperatures used can also be added, providing added strength and possibly barrier properties or improved printability to the finished article.
- the foamed furnish comprises fibers of different length, different width, or with other desired properties.
- longer fibre can be added to function as reinforcement in the resulting 3-dimensional article.
- a fibre is considered to be“long” if the average fibre length is more than 100 times the average outer diameter of the fibre.
- the foamed furnish comprises a functional additive chosen from natural and synthetic polymers, pigments, fillers and combinations thereof.
- the wet-formed 3-dimensional article is dewatered by applying vacuum to the outside of the mould, or by applying pressure to the inside of the mould, or a combination of the two, and subsequently removed from the mould.
- the amount of water introduced into the mould is significantly reduced, and hence the dewatering time is reduced.
- the wet-forming time could be reduced to less than 20 seconds, compared to about 140 seconds using traditional furnish, and 60 seconds, using traditional furnish in an optimized process.
- the 3-dimensional article has lower water content after dewatering but before drying of the article than traditionally produced articles, preferably a water content of about 50 to about 75 % after dewatering, before demoulding.
- the demoulded article retains its form and can be handled safely without collapsing, for example transferred to a drying section of the
- Another aspect of the present disclosure relates to a 3-dimensional moulded fibre-based article, obtainable by a method according to any one of the above first aspect and embodiments thereof.
- the article is a container for liquids, preferably a fibre-based bottle.
- a barrier layer is applied to the inside of the fibre-based bottle, and the smooth finish achieved using foamed furnish constitutes a good basis onto which the barrier layer is applied.
- bottles for carbonated drinks must withstand a significant pressure, and the even fibre distribution and increased strength of the disclosed articles constitute advantageous properties.
- the inventors have performed extensive experimental work investigating the effect of different foaming agents and the feasibility of foaming in a mixing tank.
- the inventors have also produced paper fibre-based bottles in a series of
- Pre-mixer A pre-foaming mixer was constructed using a steel tank and a mixer mounted on a power drill. The tank volume was approximately 4 litres.
- Mixing tank A mixing tank was constructed from a closed tank with the possibility to adjust degree of mixing, residence time and pressure (for transport of foam to a wet-forming unit as described below)
- Moulding equipment one A modified pilot equipment for the production of paper bottles constructed basically as disclosed in WO 2016/055073 was used. However, no expandable pressure tool was used in the modified pilot equipment, thus the pulp was dewatered using only pressure inside the unit and vacuum outside the unit. Further, the drying was not performed in the wet-forming device itself but in a subsequent unit where an expandable pressing tool was used.
- Moulding equipment two moulding equipment one was upgraded to a bigger and faster pilot machine by ecoXpac (the applicant of WO 2016/055073).
- the new machine (“machine 2”) is following the same principle as the first moulding prototype, but most of the process steps are automatized.
- Pulp Bleached and refined softwood market pulp was used in the experiments. The pulp was refined in a conical low-consistency (LC) refiner using either a laboratory refiner or a slightly larger conventional refiner (Valmet JC-00 Conflo®). In both cases, the resulting pulp was identical with respect to Shopper- Riegler value, fibre properties and behavior in bottle production. 75% of the pulp was refined at 50 kWh/ton and 25% was refined at 300 kWh/ton. Tap water was used as process water.
- Foaming agents of commercial grade Different types of PVOH (polyvinyl alcohol) in the form of dry power, CMC (carboxymethyl cellulose), and different types of surfactants, e.g. SDS (sodium dodecyl sulphate) and non-ionic surfactants.
- Example 3 Before the actual bottle production described in Example 3 was performed, an investigation of the effect of different foaming agents was conducted by the inventors. A furnish with a concentration of 0.5% was foamed using different concentrations of foaming agents and the stability of the foam over time was recorded. The foaming agent was added to 4 liter of 0.5 % furnish, and then mixed for 60 s using a mixer attached to a power drill. A sample of about 2 liter of the foamed pulp was collected in a transparent and graded jar. The top level of the foam layer and the top level of the water phase were recorded at 30, 60 and 120 seconds after collection. The remaining foam volume was used as a measure of the stability of the foam.
- Example 3 Pilot-scale production of bottles based on traditional furnish and foamed furnish
- Paper bottles were produced in a batch-wise manner.
- the bottles were shaped similar to traditional bottles, i.e. they consisted of a bottle neck followed by a shoulder with increasing diameter, followed by a bottle body (with significantly large volume and diameter than the neck part), and a bottom part. All bottles produced had the same shape and volume, here 0.5 I.
- the wet-formed bottles generally contained about 72 ⁇ 2 % water. They were sufficiently form-stable to allow manual handling without deformation of the bottles. The outer surface of the bottles was smooth and uniform. Surprisingly, the bottles produced with 1.5 % foamed furnish had the same tactile and visual appearance as the bottles produced with un-foamed traditional 0.5 % furnish. The bottles were also comparable in terms of formation and floe distribution. [079] After this inspection, the wet bottles were transferred to the drying section. The drying section consisted of two mould halves of porous, heated metal. The temperature of the drying section was set to 200°C and the drying time was 120 seconds. An impermeable, flexible balloon was inserted through the bottle neck.
- the balloon After insertion, the balloon was expanded and exerted a pressure on the inside of the bottle. This presses the wet-formed bottle against the hot porous metal, a step referred to as restrained drying. Water escapes as vapour. After completion of the 120 s drying, the mould is opened and the bottle removed from the drying section.
- Reference bottles (“no. 1 & 13”): Traditional pulp without foaming agent was used as reference. This pulp had a concentration of 0.5 % (5 g dry pulp per kg solution). This is a typical concentration when using pulp to make paper bottles with the equipment described in this text, and with similar equipment. Higher
- the pulp was mixed in a mixing unit for 20 seconds and thereafter injected into the wet-forming section of the bottle production unit and treated as described in the method section above.
- the wet bottles were further treated in a drying section as described above.
- Bottles made with foamed pulp using SDS (“no. 2 & 14”): A hiqh- concentration pulp was prepared, having a concentration of 1.5 % (15 g dry pulp per kg solution). SDS -solution was added to the pulp at two different concentrations. In one batch, 1.2 ml of a 40 g/l SDS-solution was added to 1.5 I of 1.5 % pulp and mixed for 60 seconds with a stirrer mounted on a power drill, forming stable foam. In another batch (“no. 3”), termed“high SDS” 12 ml of a 40 g/l SDS-solution was added to 1.5 I of 1.5 % pulp and mixed for 60 seconds, forming stable foam.
- the pulp was then transferred into a mixing tank connected to the bottle forming machine, and further mixed for 60 seconds.
- the foamed pulp was thereafter immediately injected into the wet-forming section of the bottle production unit and treated as described in the method section above (18 s, 0.2 bar overpressure).
- the mixing tank was located in close proximity to the bottle forming unit, and it is estimated that the foamed furnish reached the mould within less than 3 seconds from formation of the foam.
- the resulting wet bottles were further treated in a drying section as described above.
- bottles made from pulp containing SDS were, thereafter, produced.
- additives a wet-strength agent, a retention polymer and a hydrophobic sizing agent
- Bottles made with foamed pulp using PVOH A high concentration pulp containing 1.5 % fibre was used. Different concentrations of polyvinyl alcohol were evaluated:
- Each sample was mixed for 60 s with a stirrer mounted on a power drill, forming a foam.
- the foamed pulp was then transferred into a mixing tank and further mixed for 60s.
- the foamed pulp was thereafter injected into the wet-forming section of the bottle production unit and treated as described in the method section above.
- the mixing tank was located in close proximity to the bottle forming unit, and it is estimated that the foamed furnish reached the mould within less than 3 s from formation of the foam.
- the produced wet bottles were further treated in a drying section as described above.
- Bottles made with foamed pulp using’’machine 2” with PVOH (“no. 10”): 7.5 ml of 50 g/l Poval 23-88 was added to 1.5 I of 1.5 % pulp and mixed for 60 seconds with a stirrer mounted on a power drill, forming stable foam.
- a stirrer mounted on a power drill By using ’’machine 2” equipment, bottles made from pulp containing PVOH were, thereafter, produced.
- Bottles made with foamed pulp using’’machine 2” with PVOH and furnish chemicals (“no. 11”): 7.5 ml of 50 g/l Poval 23-88 was added together with furnish chemicals (a wet-strength agent, a retention polymer and a hydrophobic sizing agent) to 1.5 I of 1.5 % pulp and mixed for 60 seconds with a stirrer mounted on a power drill, forming stable foam.
- furnish chemicals a wet-strength agent, a retention polymer and a hydrophobic sizing agent
- Bottles made with foamed pulp using CMC 8 ml of a 20 g/l CMC-solution was added to 1.5 I of 1.5 % pulp and mixed for 60 s with a beater mounted on a power drill. The pulp was then transferred into a mixing tank and further mixed for 60s. The pulp was thereafter injected to the wet-forming section of the bottle production unit and treated as described in the methods section above. The mixing tank was located in close proximity to the bottle forming unit, and it is estimated that the foamed furnish reached the mould within less than 3 seconds from formation of the foam. The produced wet bottles were further treated in a drying section as described above. Also here, a combination of CMC and traditional furnish additives (“no. 12”) was tested in order to find out if there would be any unwanted interactions between the traditional furnish additives and the CMC.
- the present inventors also cut samples from the paper bottles, both longitudinal- and circumferential stripes, and tested them according to ISO 1924-3. The theoretical pressure resistance at break was calculated. These values were compared to the PR values obtained in the explosion test. It was shown that the PR values were of the same magnitude as the theoretical values, which confirms the relevance of the explosion test developed by the inventors.
- a paper bottle must meet many requirements in order to be considered a realistic alternative to plastic bottles.
- One of the most important properties of a paper bottle is its ability to resist pressure, thus the importance of evaluating it. In this work the evaluation was done by measuring the Pressure Resistance Index (PRI) of the produced bottles.
- PRI Pressure Resistance Index
- Another advantage is that the efficiency of the wet-forming process can be significantly improved since part of the foamed pulp consists of air instead of water. Due to this, a higher pulp consistency can be used without increasing flocculation. It was surprisingly shown that for similar bottles, a furnish having three times higher pulp concentration than traditionally used could now be used without increasing the dewatering time or impairing bottle properties. It was also
- the fibre concentration of the furnish can be increased from about 0.5 % which is normally used, to above 1 %, preferably to about 1.5 % or more preferably to about 3 % or even higher while still maintaining desired formation and a high quality of the end product, or even improving the same. Without foaming, a fibre concentration above 1 % is difficult to use without
- the amount of water used in the moulding process can be significantly reduced. This will improve process economy and reduce environmental impact. It will be possible to use a higher fibre concentration, thus reducing the water consumption.
- Another advantage of using foamed furnishes is improved dryness profile due to improved uniformity or evenness of the bottle. It also makes it possible to use various lignocellulose and/or synthetic fibre types difficult or impossible to use without foam, such as long reinforcement fibre.
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Abstract
Description
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP18198384.2A EP3633105A1 (en) | 2018-10-03 | 2018-10-03 | Process for the manufacture of moulded fibre-based 3-dimensional articles and articles obtainable by said process |
| PCT/EP2019/076839 WO2020070255A1 (en) | 2018-10-03 | 2019-10-03 | Process for the manufacture of moulded fibre-based 3-dimensional articles and articles obtainable by said process |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP3861169A1 true EP3861169A1 (en) | 2021-08-11 |
| EP3861169C0 EP3861169C0 (en) | 2025-12-03 |
| EP3861169B1 EP3861169B1 (en) | 2025-12-03 |
Family
ID=63787741
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP18198384.2A Withdrawn EP3633105A1 (en) | 2018-10-03 | 2018-10-03 | Process for the manufacture of moulded fibre-based 3-dimensional articles and articles obtainable by said process |
| EP19778556.1A Active EP3861169B1 (en) | 2018-10-03 | 2019-10-03 | Process for the manufacture of moulded fibre-based 3-dimensional articles and articles obtainable by said process |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP18198384.2A Withdrawn EP3633105A1 (en) | 2018-10-03 | 2018-10-03 | Process for the manufacture of moulded fibre-based 3-dimensional articles and articles obtainable by said process |
Country Status (2)
| Country | Link |
|---|---|
| EP (2) | EP3633105A1 (en) |
| WO (1) | WO2020070255A1 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH719287A1 (en) | 2021-12-21 | 2023-06-30 | Alpla Werke Alwin Lehner Gmbh & Co Kg | Cutting device and method for assembling a container. |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2001032987A1 (en) * | 1999-11-01 | 2001-05-10 | Leopack B.V. | Moulded fibre products comprising modified starch and process for producing the same |
| WO2013192260A1 (en) * | 2012-06-19 | 2013-12-27 | Pepsico, Inc. | Method for making molded fiber bottles |
| FI126194B (en) * | 2013-09-13 | 2016-08-15 | Teknologian Tutkimuskeskus Vtt Oy | Ways to form fibrous product |
| WO2016055073A1 (en) | 2014-10-08 | 2016-04-14 | Ecoxpac A/S | A system and a method for producing a molded article, such as a bottle |
| WO2018021907A1 (en) * | 2016-07-25 | 2018-02-01 | Huhtamaki Molded Fiber Technology B.V. | Method for manufacturing a foamed packaging unit and a packaging unit from a foamed material |
| GB201612889D0 (en) | 2016-07-26 | 2016-09-07 | Natural Resources (2000) Ltd | Moulding of articles |
| EP3418446A1 (en) * | 2017-06-21 | 2018-12-26 | BillerudKorsnäs AB | Pulp mixture |
-
2018
- 2018-10-03 EP EP18198384.2A patent/EP3633105A1/en not_active Withdrawn
-
2019
- 2019-10-03 WO PCT/EP2019/076839 patent/WO2020070255A1/en not_active Ceased
- 2019-10-03 EP EP19778556.1A patent/EP3861169B1/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| EP3861169C0 (en) | 2025-12-03 |
| WO2020070255A1 (en) | 2020-04-09 |
| EP3861169B1 (en) | 2025-12-03 |
| EP3633105A1 (en) | 2020-04-08 |
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