WO2011064441A1 - Method for manufacturing nanofibrillated cellulose pulp and use of the pulp in paper manufacturing or in nanofibrillated cellulose composites - Google Patents
Method for manufacturing nanofibrillated cellulose pulp and use of the pulp in paper manufacturing or in nanofibrillated cellulose composites Download PDFInfo
- Publication number
- WO2011064441A1 WO2011064441A1 PCT/FI2010/050897 FI2010050897W WO2011064441A1 WO 2011064441 A1 WO2011064441 A1 WO 2011064441A1 FI 2010050897 W FI2010050897 W FI 2010050897W WO 2011064441 A1 WO2011064441 A1 WO 2011064441A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- pulp
- cellulose
- optical brightening
- brightening agent
- refining
- Prior art date
Links
Classifications
-
- 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
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/001—Modification of pulp properties
- D21C9/002—Modification of pulp properties by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives
- D21C9/005—Modification of pulp properties by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives organic compounds
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
- D21H11/16—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only modified by a particular after-treatment
- D21H11/18—Highly hydrated, swollen or fibrillatable fibres
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D1/00—Methods of beating or refining; Beaters of the Hollander type
- D21D1/20—Methods of refining
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
- D21H17/42—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups anionic
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/30—Luminescent or fluorescent substances, e.g. for optical bleaching
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/32—Bleaching agents
Definitions
- the invention relates to a method of manufacturing nanofibrillated cellulose pulp.
- the invention further relates to use of the pulp in paper manufacturing or in nanofibrillated cellulose composites.
- the new additive would preferably have features to reduce the inter-fiber bonding and, thus, increase a refining efficiency due to decreased energy consumption of the refining stage.
- the additive would preferably have features to reduce fiber-water and fiber-fiber bonding that occurs during drying and concentrating.
- the additive would preferably be some of those additives that are often added for another purpose on later process stages. Summary of the Invention
- the present invention solves at least some of the above mentioned problems by providing a method for pulp manufacturing wherein the produced pulp consist at least partly of nanofibrillated cellulose.
- the method comprises a step in which at least one type of optical brightening agent (OBA) is dosed before and/or during at least one pre- refining and/or fibrillation stage.
- OSA optical brightening agent
- the invention further discloses a use of the produced pulp in nanofibrillated cellulose composites or in paper or paperboard manufacturing including base paper manufacturing and finishing stages like, for example, the use in paper or paperboard coatings.
- optical brightening agents can increase the production efficiency of the nanofibrillated cellulose pulp if the additives are dosed before or during a pre-refining stage and/or a fibrillation stage.
- Optical brightening agents have been found to be able to create bonding with cellulose in such a way that the optical brightening agents can act as substituents in inter-fiber bonding and, thus, inhibiting hydrogen bonding of fibrils in cellulose.
- the increased production efficiency is mainly due to decreased energy consumption of the fibrillation stage because of the substituent effect.
- Optical brightening agents are also able to create bonding with water and, thus, to increase the efficiency of drying and concentrating processes.
- optical brightening agents are able to enable redispersing of nanofibrillated containing cellulose. Due to the dispersive effect, an optical brightening agent can be used as a dispersing agent in nanofibrillated concentrating and/or redispersing process and, therefore, help the process. In addition, due to the dispersive effect, the quality of the nanofibrillated cellulose pulp can be increased.
- At least one kind of optical brightening agent is added before a pulp pre-refining stage. According to another embodiment, at least one kind of optical brightening agent is added before a pulp fibrillation stage. According to another embodiment, at least one kind of optical brightening agent is dosed into the pulp at the pre-refining stage. According to another embodiment, at least one kind of optical brightening agent is dosed into the pulp at the fibrillation stage.
- the amount of the nanofibrillated cellulose in the produced pulp is more than 30 w-%, preferably more than 40 w-%, 50 w-%, 60 w-% or 70 w-%, and can be even up to 1 00 w-% measured from the dried pulp.
- the nanofibrillated cellulose pulp that can be produced according to the invention and, thus, contains one or more optical brightening agents, may be used in various end product applications.
- the cellulose pulp may be used, for example, in nanofibrillated cellulose composites, and/or in paper manufacturing, for example, in a base paper and/or in a finishing stage of produced paper.
- the finishing stages of produced paper includes, for example, coating stages.
- Fig. 5 shows some turbidity and centrifugation experimental test results of the fluidized samples.
- cellulose raw material refers to any cellulose raw material source that can be used in a production of cellulose pulp, refined pulp, or microfibrillar cellulose.
- the cellulose raw material can be based on any plant material that contains cellulose, for example wood material.
- the wood material can be from softwood trees, such as spruce, pine, fir, larch, douglas-fir or hemlock, or from hardwood trees, such as birch, aspen, poplar, alder, eucalyptus or acacia, or from a mixture of softwoods and hardwoods.
- Non-wood material can be from agricultural residues, grasses or other plant substances such as straw, leaves, bark, seeds, hulls, flowers, vegetables or fruits from cotton, corn, wheat, oat, rye, barley, rice, flax, hemp, manila hemp, sisal hemp, jute, ramie, kenaf, bagasse, bamboo or reed.
- agricultural residues, grasses or other plant substances such as straw, leaves, bark, seeds, hulls, flowers, vegetables or fruits from cotton, corn, wheat, oat, rye, barley, rice, flax, hemp, manila hemp, sisal hemp, jute, ramie, kenaf, bagasse, bamboo or reed.
- cellulose pulp refers in this application to cellulose fibers, which are isolated from any cellulose raw material using chemical, mechanical, thermomechanical, or chemithermo - mechanical pulping process(es). Typically the diameter of the fibers varies between 1 5-25 ⁇ and the length exceeds 500 ⁇ , but the present invention is not intended to be limited to these parameters.
- paper manufacturing refers to manufacturing process of any paper-like material, for example, paperboards, papers and/or paper composites.
- At least part of the lignin that has been included in cellulose raw material is advantageously removed from the cellulose raw material when it is processed into cellulose pulp to be used in the nanofibrillated cellulose production.
- chemical pulp may be used more preferably for nanofibrillated cellulose production than mechanical pulp.
- the yield of the process wherein cellulose raw material is processed into cellulose pulp to be used in the nanofibrillated pulp production has been at least 50 %, at least 60 %, at least 70 % or at least 80 %.
- the cellulose pulp used in the nanofibrillated cellulose production may be preferably unbleached or bleached chemithermo or chemical pulp, more preferably unbleached or bleached chemical pulp, and the most preferably unbleached chemical pulp, because the method of the invention may be the most advantageous compared to other processes when the used cellulose pulp is chemically produced unbleached pulp.
- the term "refined pulp” refers to refined cellulose pulp. The refining of cellulose pulp is carried out with suitable equipment such as a refiner, grinder, homogenizer, colloider, friction grinder, fluidizer such as microfluidizer, macrofluidizer or fluidizer-type homogenizer or ultrasound sonicator.
- cellulose fibers typically have not been fully fibrillated; a large fraction of cellulose fibers with unchanged dimensions are still present in addition to refined cellulose material.
- the large fibers in the refined pulp may have fibrillated surface.
- the finest fraction of cellulose based material in the "refined pulp” consists of nanofibrillated cellulose, i.e. cellulose microfibrils and microfibril bundles with diameter less than 200 nm.
- nanofibrillated cellulose refers to a collection of isolated cellulose microfibrils or microfibril bundles derived from cellulose raw material.
- Microfibrils have typically high aspect ratio: the length might exceed one micrometer while the number-average diameter is typically below 200 nm.
- the diameter of microfibril bundles can also be larger but generally less than 1 ⁇ .
- the smallest microfibrils are similar to the so called elementary fibrils, which are typically 2-1 2 nm in diameter.
- the dimensions of the fibrils or fibril bundles are dependent on the raw material and disintegration method.
- the nanofibrillated cellulose may also contain some hemicelluloses; the amount may be dependent on the plant source.
- Nanofibrillated cellulose can also be any chemically or physically modified derivate of cellulose microfibrils or microfibril bundles.
- the chemical modification could be based for example on carboxymethylation, oxidation, esterification, or etherification reaction of cellulose molecules. Modification could also be realized by physical adsorption of anionic, cationic, or non-ionic substances or any combination of these on cellulose surface.
- nanofibrillated cellulose can be carried out before, after, or during the production of nanofibrillated cellulose.
- nanofibrillated cellulose There are several widely used synonyms for nanofibrillated cellulose.
- MFC microfibrillated cellulose
- Nanofibrillated cellulose described in this application is not the same material as the so called cellulose whiskers, which are also known as: cellulose nanowhiskers, cellulose nanocrystals, cellulose nanorods, rod-like cellulose microcrystals or cellulose nanowires.
- Nanofibrillated cellulose and normal cellulose are usually produced using different kind of refiners, because the refiners that are used conventionally in the pulp refiner production may not, at least efficiently, be used in nanofibrillated cellulose production. However, the refiners used in the conventional pulp production may be used as pre-refiners in nanofibrillated cellulose production.
- the term “fibrillation stage” means the stage that causes more fibrillar cellulose
- the term “pre-refiner stage” means the stage that may advantageously be used for pre-refining before a fibrillation stage in nanofibrillated cellulose production.
- Properties of nanofibrillated cellulose pulp differs hugely from conventional cellulose pulp due to many nano-sized particles of the nanofibrillated cellulose pulp and, thus, nanofibrillated cellulose cannot be though as a same material as conventional cellulose pulp.
- Nanofibrillated cellulose is, for example, gel-like material even in low consistency, and its water removal rate is usually slow.
- Paper sheets that contain a lot of nanofibrillated cellulose have special properties comparing to the sheets made from normal cellulose pulp, for example, they have usually high strength properties, their porosity is very low, and the sheets are usually (at least partly) transparent.
- FIGS. 1 a-1 d The differences between cellulose pulp, refined cellulose pulp and nanofibrillated cellulose pulp are illustrated in figures 1 a-1 d in optical microscopy pictures. Magnification is the same in the figures 1 a - 1 c.
- Figure 1 a shows an optical microscopy picture of typical cellulose pulp.
- Figure 1 b shows an microscopy picture of typical refined cellulose pulp.
- Figures 1 c and 1 d show microscopy pictures of typical nanofibrillated cellulose pulp.
- Figure 1 d shows the same situation as figure 1 c but with higher magnification wherein individual microfibrils and microfibril bundles with diameter less than 1 00 nm can be detected.
- the present invention provides a method for manufacturing nanofibrillated cellulose pulp by pre-refining and/or fibrillating the pulp with a presence of at least one kind of optical brightening agent.
- the present invention provides the use of the produced pulp in paper manufacturing or in nanofibrillated cellulose composites.
- optical brightening agents are dye-like compounds which absorb short-wave light in the ultraviolet and violet region of the electromagnetic spectrum not visible to the human eye and re-emit the light in the longer-wave blue region.
- optical brightening agents make the material, for example paper, to look less yellow to the human eyes and, thus, human eyes interpret the blue light as a higher degree of whiteness.
- the optical brightening agents are used to achieve better optical properties of the produced paper, for example, for a whitening effect of the produced paper.
- Optical brightening agent types that are typically used in the pulp and paper industry are, for example, di-, tetra-, and hexasulphonated stilbene compounds.
- the amount of sulphonated groups has an effect on the chemical properties of the optical brightening agent and, thus, the type of the used OBA may have an effect on the method according to an example embodiment of the invention.
- the more the optical brightening agent has sulphonated groups the bigger may be the effect of the used optical brightening agent on the method accordant with the invention.
- Some other most cornmercialiy available optical brightening agents in pulp and paper industries are based on coumarin and pyrazolone chemistries, Those mentioned optical brightening agent types are only some examples and also other types of optical brightening agents known in prior art can be used in this invention.
- those chemical types mentioned in the application, Le stilbene, coumarin and pyrazoline are preferred to use in the practice of this invention. From those chemicals, the anionic stilbene compounds may be the most preferably used in the invention.
- optical brightening agents are quite expensive additives, thus, solutions provided in this invention are intended to be the most efficient if optical brightening agents are used in nanofibrillated pulp production wherein the optical brightening agent is otherwise added in a later stage to the pulp or to the end product.
- optical brightening agents are typically added at the wet end of the papermaking process, which include, for example, the fan pulp or the machine chest.
- optical brightening agent in accordance with some example embodiments of the invention does not necessarily increase additive costs but, quite the contrary, the retention of the optical brightening agent to the nanofibrillated pulp may be improved if the optical brightening agent is added before or during pre-refining stage or before or during a fibrillation step and, therefore, the overall costs of the used optical brightening agent may be decreased.
- the total amount of the needed optical brightening agent dosage according to an example embodiment of the invention can be smaller if the optical brightening agent is added accordant with some example embodiments of the invention due to several fiber - optical brightening agent bondings that may be formed during nanofibrillated cellulose pre-refining and/or fibrillation stages. Therefore, the efficiency of the nanofibrillated cellulose production can further be increased when the optical brightening agent is added to the produced pulp before or during the refining stage, not only because of the decreased energy consumption but also because of less additive costs.
- the optical brightening agent dosage to the nanofibrillated cellulose production may increase an ability of the nanofibrillated cellulose to carry the optical brightening agent and, therefore, a need for other optical brightening agent carriers e.g. Polyvinyl Alcohol (PVOH) may decrease.
- PVOH Polyvinyl Alcohol
- the method comprises a step wherein at least one type of the optical brightening agent (OBA) is dosed as a refining additive to the pulp which contains cellulose.
- OSA optical brightening agent
- the dosage is preferably done before a pre-refining and/or fibrillation stage.
- one type of the optical brightening agent can be added into the pulp at the pre-refining or the fibrillation stage.
- the pulp is fibrillated in at least one fibrillation stage after the additive addition, no matter in which stage the additive is added to the process.
- the anionic optical brightening agent is capable of inhibiting hydrogen bonding between the cellulose fibrils in cellulose and can therefore be used to create a dispersive effect, which dispersive effect can increase the quality of the produced nanofibrillated cellulose. Due to the dispersive effect, optical brightening agent can be used as a dispersing agent in the nanofibrillated concentrating/redispersing process and, therefore, may help the process.
- Nanofibrillated cellulose that contains optical brightening agent may improve not only the refining efficiency and the quality of the produced pulp but also both the strength and the optical properties of the end product to be produced from the pulp manufactured according to an example embodiment of the invention.
- the improvements in strength properties are mainly due to the features of nanofibrillated cellulose and the improvements in optical properties are mainly due to the features of the optical brightening agent.
- the novel invention can provide at least some of the following advantages:
- the amount of nanofibrillated cellulose in the pulp manufactured according to the invention may be 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95 or 1 00 w- %, including any and all ranges and subranges therein.
- the pulp manufacturing process according to invention has at least one fibrillation stage, possibly at least 2, 3 or 4 fibrillation stages. According to the invention at least one type of the optical brightening agent is added
- the pulp is fibrillated after at least one additive dosage in at least one fibrillation stage in order to form some nanofibrillated cellulose material.
- the addition of the optical brightening agent before or during the refining decreases the cellulose-cellulose bonding through hydroxyl groups by forming hydrogen bonds with the cellulose fibrils.
- the addition of the optical brightening agent creates a dispersive effect to the pulp suspension through the repulsive forces between the anionic groups.
- a bleached birch pulp made with conventional chemical pulping process was used as raw cellulose pulp.
- optical brightening agents Two different kinds of optical brightening agents were used as the refining additive: disulphonic type of the optical brightening agent and hexasulphonic type of the optical brightening agent. In addition, reference samples without addition of the optical brightening agent were performed.
- the pre-refining stage was performed with Voith refiner. Addition of the used optical brightening agent was always 2 w-%. The whole amount was dosed to the pulp before the pre-refiner stage, after which the samples were refined at energy of 200 kWh/t. The pre-refinings were performed in the consistency of 4%.
- the obtained pulps were diluted to 1 .6% for fluidizer and to 2% for Masuko.
- the optical brightening agents were dosed to the pre-refining process in order to improve their bonding to fiber surface. ple preparation
- the part of the samples was fluidized with the M-700 Microfluidics Processor. Those samples were dispersed with a mixer in 1 .6% consistency during 30 minutes. After dispersing, the samples were passed three times through fluidizer so that in the first pass there was only an APM chamber with diameter at 500 ⁇ . In the second pass, the fiber suspension was passed through two sequential chambers with diameters at 500 ⁇ and 200 ⁇ . The third pass was carried out so that the fiber suspension passed through sequential 500 ⁇ and 1 00 ⁇ diameter chambers. The condenser of the fluidizer was switched off during all these trials, as it was found to improve fibrillation in the first part of experiments.
- the grinded samples were dispersed in 2% consistency with a mixer during 1 5 minutes before the treatment with Masuko.
- the dispersed samples were passed four times through Masuko in such a way that in the first pass the gap between the grinding stones was looser than with the following three passes.
- the grinder was washed after the first and third pass. racterization
- the gel-like fiber suspensions obtained from Masuko and from fluidizer were characterized by measuring viscosity (Brookfield) and turbidity of the samples and by observing optical microscope and SEM images of the samples. In addition, with centrifugation measurements the dry matter content was measured from both the liquid and the solid phase in order to determine the amount of nano-sized material in the sample. paration of paper sheets
- Refining result can be estimated by measuring the viscosity level of the nanofibrillated cellulose sample, because the viscosity level of the pulp material goes along with the portion of nanofibrillated cellulose in the pulp.
- more refined, and thus, more fibrillated nanofibrillated cellulose is more gel-like material than less nanofibrillated cellulose. Therefore, more gellike material means more nanofibrillated cellulose in the sample and this bigger part of nanofibrillate cellulose can be seen in higher viscosity level in the sample.
- Samples with optical brightening agent - dosage were clearly more viscous than the reference samples. The amount of unfibrillated fibers can be estimated from optical microscopy pictures.
- FIGs 2a - 2c wherein viscosity results with some optical microscopy pictures of Masuko grinded samples are shown.
- the figure 2a presents the viscosity results of the reference sample 21 , the sample with disulphonic optical brightening agent dosage 22, and the sample with hexasulphonic optical brightening agent dosage 23.
- Figure 2b shows an optical microscopy picture of the reference sample 21
- figure 2c shows an optical microscopy picture of the sample 23 with hexasulphonic optical brightening agent dosage.
- Figures 3a and 3b show an optical microscopy images of fluidisator samples, wherein the reference sample (shown in figure 3a) and the sample 32 with hexasulphonic optical brightening agent (shown in figure 3b) are presented. The sample presented in figure 3b with the dosage of the optical brightening agent is clearly better fibrillated than the reference sample shown in figure 3a.
- Figures 4a and 4b show the same situation with SEM pictures (magnification : 1 0 000 x) in which the reference sample (in figure 4a) and the sample with hexasulphonated optical brightening agent addition (in figure 4b) are presented. As can be seen, the samples with hexasulphonated optical brightening agent looks clearly better compared to the reference sample, as many smaller fibrils can be seen in the image.
- Quality of the nanofibrillated cellulose can be analyzed using centrifugation of nano-sized material and measuring the turbidity of the samples. Centrifugation results are supposed to describe the degree of fibrillation so that the more the nano-sized material has more efficient fibrillation than less nano-sized material. When it comes to turbidity results, the smaller the value for turbidity is, the more there should be nano-sized material in the sample.
- Figure 5 shows turbidity and centrifugation results of the fluidized samples. In this figure the reference sample 51 , the sample 52 with disulphonic type of the optical brightening agent dosage, and the sample 53 with addition of hexasulphonic type of the optical brightening agent are presented.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Paper (AREA)
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/511,956 US20130000855A1 (en) | 2009-11-24 | 2010-11-05 | Method for manufacturing nanofibrillated cellulose pulp and use of the pulp in paper manufacturing or in nanofibrillated cellulose composites |
EP10832694.3A EP2504487B1 (de) | 2009-11-24 | 2010-11-05 | Verfahren zur herstellung einer nanofibrillierten zellulosepulpe und verwendung der pulpe bei der papierherstellung in nanofibrillierten zellulose-verbundstoffen |
CN2010800531975A CN102686799A (zh) | 2009-11-24 | 2010-11-05 | 用于生产纳米原纤化纤维素纸浆的方法及纸浆在造纸或纳米原纤化纤维素复合物中的用途 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI20096233A FI123289B (fi) | 2009-11-24 | 2009-11-24 | Menetelmä nanofibrilloidun selluloosamassan valmistamiseksi ja massan käyttö paperinvalmistuksessa tai nanofibrilloiduissa selluloosakomposiiteissa |
FI20096233 | 2009-11-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2011064441A1 true WO2011064441A1 (en) | 2011-06-03 |
Family
ID=41395280
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FI2010/050897 WO2011064441A1 (en) | 2009-11-24 | 2010-11-05 | Method for manufacturing nanofibrillated cellulose pulp and use of the pulp in paper manufacturing or in nanofibrillated cellulose composites |
Country Status (5)
Country | Link |
---|---|
US (1) | US20130000855A1 (de) |
EP (1) | EP2504487B1 (de) |
CN (1) | CN102686799A (de) |
FI (1) | FI123289B (de) |
WO (1) | WO2011064441A1 (de) |
Cited By (34)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012097446A1 (en) | 2011-01-21 | 2012-07-26 | Fpinnovations | High aspect ratio cellulose nanofilaments and method for their production |
US8231764B2 (en) | 2009-05-15 | 2012-07-31 | Imerys Minerals, Limited | Paper filler method |
WO2013117823A1 (en) * | 2012-02-10 | 2013-08-15 | Upm-Kymmene Corporation | Method for pretreating cellulose pulp |
WO2014068196A3 (en) * | 2012-11-03 | 2014-06-26 | Upm-Kymmene Corporation | Method for producing nanofibrillar cellulose |
WO2014147295A1 (en) * | 2013-03-20 | 2014-09-25 | Ahlstrom Corporation | Fibrous substrate containing fibers and nanofibrillar polysaccharide |
EP2799618A1 (de) | 2013-04-29 | 2014-11-05 | Blankophor GmbH & Co. KG | Verwendung von mikronisierter Cellulose und fluoreszierendes Weißmittel zur Oberflächenbehandlung von Cellulosematerialien |
WO2015011337A1 (en) * | 2013-07-26 | 2015-01-29 | Upm-Kymmene Coprporation | Method of modifying nanofibrillar cellulose composition |
US20150191036A1 (en) * | 2012-05-29 | 2015-07-09 | De La Rue International Limited | Substrate for security documents |
US20150218756A1 (en) * | 2012-08-21 | 2015-08-06 | Upm-Kymmene Corporation | Method for making paper product and paper product |
US9157189B2 (en) | 2011-09-12 | 2015-10-13 | Stora Enso Oyj | Method of controlling retention and an intermediate product used in the method |
EP2753738A4 (de) * | 2011-09-08 | 2016-01-06 | Spinnova Oy | Verfahren zur herstellung faserigem garn, faseriges garn und verwendung des faserigen garns |
EP2678474A4 (de) * | 2011-02-24 | 2016-03-23 | Innventia Ab | Einstufiges verfahren zur herstellung von nanozellstoff durch beschleunigung und zersetzung von rohmaterial |
EP2997191A4 (de) * | 2013-05-15 | 2016-12-21 | Upm Kymmene Corp | Verfahren zur herstellung nanofibrillärer cellulose und zur herstellung eines papierprodukts |
US9739011B2 (en) | 2011-11-14 | 2017-08-22 | Upm-Kymmene Corporation | Method for producing nanofibrillar cellulose |
US20180066073A1 (en) * | 2016-09-01 | 2018-03-08 | Hs Manufacturing Group Llc | Methods for biobased derivatization of cellulosic surfaces |
US10053817B2 (en) | 2010-04-27 | 2018-08-21 | Fiberlean Technologies Limited | Process for the manufacture of structured materials using nano-fibrillar cellulose gels |
US10119919B2 (en) | 2014-06-30 | 2018-11-06 | Upm-Kymmene Corporation | Method and device for monitoring the quality of nanofibrillar cellulose |
US10214859B2 (en) | 2016-04-05 | 2019-02-26 | Fiberlean Technologies Limited | Paper and paperboard products |
US10253457B2 (en) | 2010-11-15 | 2019-04-09 | Fiberlean Technologies Limited | Compositions |
US10294371B2 (en) | 2009-03-30 | 2019-05-21 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose gels |
US10301774B2 (en) | 2009-03-30 | 2019-05-28 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose suspensions |
US10463205B2 (en) | 2016-07-01 | 2019-11-05 | Mercer International Inc. | Process for making tissue or towel products comprising nanofilaments |
US10570261B2 (en) | 2016-07-01 | 2020-02-25 | Mercer International Inc. | Process for making tissue or towel products comprising nanofilaments |
US10577469B2 (en) | 2015-10-14 | 2020-03-03 | Fiberlean Technologies Limited | 3D-formable sheet material |
US10640927B2 (en) | 2016-09-19 | 2020-05-05 | Mercer International, Inc. | Absorbent paper products having unique physical strength properties |
US10724173B2 (en) | 2016-07-01 | 2020-07-28 | Mercer International, Inc. | Multi-density tissue towel products comprising high-aspect-ratio cellulose filaments |
US10731298B2 (en) | 2012-06-15 | 2020-08-04 | University Of Maine System Board Of Trustees | Release paper and method of manufacture |
CN111684130A (zh) * | 2017-12-04 | 2020-09-18 | 芬欧汇川集团 | 由化学纸浆制造用于复合应用的纸浆前体材料的方法及其产品 |
US10794006B2 (en) | 2016-04-22 | 2020-10-06 | Fiberlean Technologies Limited | Compositions comprising microfibrilated cellulose and polymers and methods of manufacturing fibres and nonwoven materials therefrom |
EP3733959A1 (de) * | 2019-05-03 | 2020-11-04 | Valmet Technologies, Inc. | Überwachung und steuerung der raffinierung von faserzellstoff |
US11155697B2 (en) | 2010-04-27 | 2021-10-26 | Fiberlean Technologies Limited | Process for the production of gel-based composite materials |
US11352747B2 (en) | 2018-04-12 | 2022-06-07 | Mercer International Inc. | Processes for improving high aspect ratio cellulose filament blends |
US11724941B2 (en) | 2018-02-15 | 2023-08-15 | North Carolina State University | Synthesis of micron and nanoscale carbon spheres and structures using hydrothemal carbonization |
US11846072B2 (en) | 2016-04-05 | 2023-12-19 | Fiberlean Technologies Limited | Process of making paper and paperboard products |
Families Citing this family (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9284474B2 (en) | 2007-12-20 | 2016-03-15 | University Of Tennessee Research Foundation | Wood adhesives containing reinforced additives for structural engineering products |
FI124724B (fi) * | 2009-02-13 | 2014-12-31 | Upm Kymmene Oyj | Menetelmä muokatun selluloosan valmistamiseksi |
US8835141B2 (en) * | 2011-06-09 | 2014-09-16 | The United States Of America As Represented By The Secretary Of Agriculture | Methods for integrated conversion of lignocellulosic material to sugars or biofuels and nano-cellulose |
FI126013B (en) * | 2012-02-13 | 2016-05-31 | Upm Kymmene Corp | A method and system for treating fibril cellulose, as well as a fibril cellulose material |
SE537517C2 (sv) * | 2012-12-14 | 2015-05-26 | Stora Enso Oyj | Våtlagt arkmaterial innefattande mikrofibrillerad cellulosasamt förfarande för tillverkning därav |
US9656914B2 (en) | 2013-05-01 | 2017-05-23 | Ecolab Usa Inc. | Rheology modifying agents for slurries |
US10695947B2 (en) | 2013-07-31 | 2020-06-30 | University Of Maine System Board Of Trustees | Composite building products bound with cellulose nanofibers |
US9303360B2 (en) * | 2013-08-08 | 2016-04-05 | Ecolab Usa Inc. | Use of nanocrystaline cellulose and polymer grafted nanocrystaline cellulose for increasing retention in papermaking process |
US9410288B2 (en) | 2013-08-08 | 2016-08-09 | Ecolab Usa Inc. | Use of nanocrystaline cellulose and polymer grafted nanocrystaline cellulose for increasing retention in papermaking process |
AU2013399666B2 (en) * | 2013-09-04 | 2017-05-25 | Halliburton Energy Services, Inc. | Nano-carbohydrate composites as a lost circulation materials - LCM origami and other drilling fluid applications |
FI126042B (en) * | 2014-03-31 | 2016-06-15 | Upm Kymmene Corp | Method for producing nanofibril cellulose and nanofibril cellulose product |
GB201409047D0 (en) * | 2014-05-21 | 2014-07-02 | Cellucomp Ltd | Cellulose microfibrils |
US9970159B2 (en) * | 2014-12-31 | 2018-05-15 | Innovatech Engineering, LLC | Manufacture of hydrated nanocellulose sheets for use as a dermatological treatment |
CA2983185C (en) | 2015-05-01 | 2019-06-04 | Fpinnovations | A dry mixed re-dispersible cellulose filament/carrier product and the method of making the same |
US10240290B2 (en) * | 2015-06-04 | 2019-03-26 | Gl&V Usa, Inc. | Method of producing cellulose nanofibrils |
CA3001717A1 (en) | 2015-10-15 | 2017-04-20 | Ecolab Usa Inc. | Nanocrystalline cellulose and polymer-grafted nanocrystalline cellulose as rheology modifying agents for magnesium oxide and lime slurries |
FI130254B (en) * | 2016-02-03 | 2023-05-11 | Kemira Oyj | METHOD FOR PREPARATION OF MICROFIBRILLATED CELLULOSE AND PRODUCT |
SE539833C2 (en) * | 2016-04-01 | 2017-12-12 | Stora Enso Oyj | Process for production of film comprising microfibrillated cellulose |
AU2017247688B2 (en) * | 2016-04-04 | 2020-11-05 | Fiberlean Technologies Limited | Compositions and methods for providing increased strength in ceiling, flooring, and building products |
SE539950C2 (en) * | 2016-05-20 | 2018-02-06 | Stora Enso Oyj | An uv blocking film comprising microfibrillated cellulose, a method for producing said film and use of a composition having uv blocking properties |
SE541755C2 (en) * | 2017-03-01 | 2019-12-10 | Stora Enso Oyj | Process for production of film comprising microfibrillated cellulose |
WO2019018150A1 (en) | 2017-07-17 | 2019-01-24 | Ecolab USA, Inc. | RHEOLOGY MODIFICATION AGENTS FOR SLURRY |
US10865317B2 (en) | 2017-08-31 | 2020-12-15 | Kimberly-Clark Worldwide, Inc. | Low-fluorine compositions with cellulose for generating superhydrophobic surfaces |
CA3106586A1 (en) * | 2018-07-19 | 2020-01-23 | Kemira Oyj | Cellulose composition |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060185808A1 (en) * | 2005-02-19 | 2006-08-24 | Nguyen Xuan T | Fixation of optical brightening agents onto papermaking fiber |
US20090205795A1 (en) * | 2008-02-07 | 2009-08-20 | Yonghao Ni | Combined process of peroxide bleaching of wood pulps and addition of optical brightening agents |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3534912A (en) * | 1967-01-11 | 1970-10-20 | Beloit Corp | Low speed refining of a papermaking pulp solution |
US3591451A (en) * | 1969-02-06 | 1971-07-06 | Ethyl Corp | Pretreatment of vegetable matter and delignification of the refined matter with chloring dioxide |
SK3499A3 (en) * | 1996-07-15 | 1999-07-12 | Rhodia Chimie Sa | Additivation of essentially amorphous cellulose nanofibrils with carboxyl cellulose with a high degree of substitution |
US7638016B2 (en) * | 2005-02-19 | 2009-12-29 | International Paper Company | Method for treating kraft pulp with optical brighteners after chlorine bleaching to increase brightness |
US7914646B2 (en) * | 2006-07-21 | 2011-03-29 | Nalco Company | Compositions and processes for paper production |
PL1984561T3 (pl) * | 2006-02-08 | 2016-07-29 | Innventia Ab | Sposób wytwarzania mikrofibrylowanej celulozy |
US20090025895A1 (en) * | 2006-02-20 | 2009-01-29 | John Stuart Cowman | Process for the Manufacture of Paper and Board |
JP4831570B2 (ja) | 2006-03-27 | 2011-12-07 | 木村化工機株式会社 | 機能性粒子含有率の高い機能性セルロース材料及びその製造方法 |
JP4958097B2 (ja) * | 2006-07-19 | 2012-06-20 | 国立大学法人京都大学 | ナノファイバーシート及びその製造方法並びに繊維強化複合材料 |
BRPI0809172A2 (pt) * | 2007-04-05 | 2014-09-16 | Akzo Nobel Nv | "método de fabricação de papel a partir de polpa refinada" |
JP5398180B2 (ja) * | 2007-06-11 | 2014-01-29 | 国立大学法人京都大学 | リグニン含有ミクロフィブリル化植物繊維及びその製造方法 |
WO2009069641A1 (ja) * | 2007-11-26 | 2009-06-04 | The University Of Tokyo | セルロースナノファイバーとその製造方法、セルロースナノファイバー分散液 |
SE0800807L (sv) | 2008-04-10 | 2009-10-11 | Stfi Packforsk Ab | Nytt förfarande |
-
2009
- 2009-11-24 FI FI20096233A patent/FI123289B/fi active IP Right Review Request
-
2010
- 2010-11-05 US US13/511,956 patent/US20130000855A1/en not_active Abandoned
- 2010-11-05 EP EP10832694.3A patent/EP2504487B1/de active Active
- 2010-11-05 WO PCT/FI2010/050897 patent/WO2011064441A1/en active Application Filing
- 2010-11-05 CN CN2010800531975A patent/CN102686799A/zh active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060185808A1 (en) * | 2005-02-19 | 2006-08-24 | Nguyen Xuan T | Fixation of optical brightening agents onto papermaking fiber |
US20090205795A1 (en) * | 2008-02-07 | 2009-08-20 | Yonghao Ni | Combined process of peroxide bleaching of wood pulps and addition of optical brightening agents |
Non-Patent Citations (1)
Title |
---|
See also references of EP2504487A4 * |
Cited By (70)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10982387B2 (en) | 2009-03-30 | 2021-04-20 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose suspensions |
US10294371B2 (en) | 2009-03-30 | 2019-05-21 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose gels |
US10301774B2 (en) | 2009-03-30 | 2019-05-28 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose suspensions |
US10975242B2 (en) | 2009-03-30 | 2021-04-13 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose gels |
US10100464B2 (en) | 2009-05-15 | 2018-10-16 | Fiberlean Technologies Limited | Paper filler composition |
US11970817B2 (en) | 2009-05-15 | 2024-04-30 | Fiberlean Technologies Limited | Paper filler composition |
US11162219B2 (en) | 2009-05-15 | 2021-11-02 | Fiberlean Technologies Limited | Paper filler composition |
US11732411B2 (en) | 2009-05-15 | 2023-08-22 | Fiberlean Technologies Limited | Paper filler composition |
US11377791B2 (en) | 2009-05-15 | 2022-07-05 | Fiberlean Technologies Limited | Paper filler composition |
US9127405B2 (en) | 2009-05-15 | 2015-09-08 | Imerys Minerals, Limited | Paper filler composition |
US8231764B2 (en) | 2009-05-15 | 2012-07-31 | Imerys Minerals, Limited | Paper filler method |
US10100467B2 (en) | 2010-04-27 | 2018-10-16 | Fiberlean Technologies Limited | Process for the manufacture of structured materials using nano-fibrillar cellulose gels |
US11155697B2 (en) | 2010-04-27 | 2021-10-26 | Fiberlean Technologies Limited | Process for the production of gel-based composite materials |
US10633796B2 (en) | 2010-04-27 | 2020-04-28 | Fiberlean Technologies Limited | Process for the manufacture of structured materials using nano-fibrillar cellulose gels |
US10053817B2 (en) | 2010-04-27 | 2018-08-21 | Fiberlean Technologies Limited | Process for the manufacture of structured materials using nano-fibrillar cellulose gels |
US10253457B2 (en) | 2010-11-15 | 2019-04-09 | Fiberlean Technologies Limited | Compositions |
US11136721B2 (en) | 2010-11-15 | 2021-10-05 | Fiberlean Technologies Limited | Compositions |
US11655594B2 (en) | 2010-11-15 | 2023-05-23 | Fiberlean Technologies Limited | Compositions |
US9051684B2 (en) | 2011-01-21 | 2015-06-09 | Fpinnovations | High aspect ratio cellulose nanofilaments and method for their production |
WO2012097446A1 (en) | 2011-01-21 | 2012-07-26 | Fpinnovations | High aspect ratio cellulose nanofilaments and method for their production |
EP2678474A4 (de) * | 2011-02-24 | 2016-03-23 | Innventia Ab | Einstufiges verfahren zur herstellung von nanozellstoff durch beschleunigung und zersetzung von rohmaterial |
US9388529B2 (en) | 2011-02-24 | 2016-07-12 | Innventia Ab | Single-step method for production of nano pulp by acceleration and disintegration of raw material |
EP2753738A4 (de) * | 2011-09-08 | 2016-01-06 | Spinnova Oy | Verfahren zur herstellung faserigem garn, faseriges garn und verwendung des faserigen garns |
US9157189B2 (en) | 2011-09-12 | 2015-10-13 | Stora Enso Oyj | Method of controlling retention and an intermediate product used in the method |
US9739011B2 (en) | 2011-11-14 | 2017-08-22 | Upm-Kymmene Corporation | Method for producing nanofibrillar cellulose |
US9725849B2 (en) | 2012-02-10 | 2017-08-08 | Upm-Kymmene Corporation | Method for pretreating cellulose pulp |
CN104105827A (zh) * | 2012-02-10 | 2014-10-15 | 芬欧汇川集团 | 预处理纤维素浆料的方法 |
US9315942B2 (en) | 2012-02-10 | 2016-04-19 | Upm-Kymmene Corporation | Method for pretreating cellulose pulp |
WO2013117823A1 (en) * | 2012-02-10 | 2013-08-15 | Upm-Kymmene Corporation | Method for pretreating cellulose pulp |
US20150191036A1 (en) * | 2012-05-29 | 2015-07-09 | De La Rue International Limited | Substrate for security documents |
US10731298B2 (en) | 2012-06-15 | 2020-08-04 | University Of Maine System Board Of Trustees | Release paper and method of manufacture |
US9702085B2 (en) * | 2012-08-21 | 2017-07-11 | Upm-Kymmene Corporation | Method for making paper product and paper product |
US20150218756A1 (en) * | 2012-08-21 | 2015-08-06 | Upm-Kymmene Corporation | Method for making paper product and paper product |
WO2014068196A3 (en) * | 2012-11-03 | 2014-06-26 | Upm-Kymmene Corporation | Method for producing nanofibrillar cellulose |
US9797093B2 (en) | 2012-11-03 | 2017-10-24 | Upm-Kymmene Corporation | Method for producing nanofibrillar cellulose |
JP2016501926A (ja) * | 2012-11-03 | 2016-01-21 | ウーペーエム−キュンメネ コーポレイションUPM−Kymmene Corporation | ナノフィブリル化セルロースの製造方法 |
US10781025B2 (en) | 2013-03-20 | 2020-09-22 | Ahlstrom-Munksjö Oyj | Fibrous substrate containing fibers and nanofibrillar polysaccharide |
WO2014147295A1 (en) * | 2013-03-20 | 2014-09-25 | Ahlstrom Corporation | Fibrous substrate containing fibers and nanofibrillar polysaccharide |
FR3003581A1 (fr) * | 2013-03-20 | 2014-09-26 | Ahlstroem Oy | Support fibreux a base de fibres et de nanofibrilles de polysaccharide |
EP2799618A1 (de) | 2013-04-29 | 2014-11-05 | Blankophor GmbH & Co. KG | Verwendung von mikronisierter Cellulose und fluoreszierendes Weißmittel zur Oberflächenbehandlung von Cellulosematerialien |
WO2014177504A1 (en) * | 2013-04-29 | 2014-11-06 | Blankophor Gmbh & Co. Kg | Use of micronized cellulose and fluorescent whitening agent for surface treatment of cellulosic materials |
US20160060814A1 (en) * | 2013-04-29 | 2016-03-03 | Blankophor Gmbh & Co., Kg | Use of Micronized Cellulose and Fluorescent Whitening Agent for Surface Treatment of Cellulosic Materials |
JP2016522862A (ja) * | 2013-04-29 | 2016-08-04 | ブランコファー ゲーエムベーハー ウント コー.カーゲー | セルロース系材料の表面処理用の微粉化セルロース及び蛍光増白剤の使用 |
US9976256B2 (en) | 2013-05-15 | 2018-05-22 | Upm-Kymmene Corporation | Method for making nanofibrillar cellulose and for making a paper product |
EP2997191A4 (de) * | 2013-05-15 | 2016-12-21 | Upm Kymmene Corp | Verfahren zur herstellung nanofibrillärer cellulose und zur herstellung eines papierprodukts |
WO2015011337A1 (en) * | 2013-07-26 | 2015-01-29 | Upm-Kymmene Coprporation | Method of modifying nanofibrillar cellulose composition |
US9809655B2 (en) | 2013-07-26 | 2017-11-07 | Upm-Kymmene Corporation | Method of modifying nanofibrillar cellulose composition |
US10119919B2 (en) | 2014-06-30 | 2018-11-06 | Upm-Kymmene Corporation | Method and device for monitoring the quality of nanofibrillar cellulose |
US11932740B2 (en) | 2015-10-14 | 2024-03-19 | Fiberlean Technologies Limited | 3D-formable sheet material |
US11384210B2 (en) | 2015-10-14 | 2022-07-12 | Fiberlean Technologies Limited | 3-D formable sheet material |
US10577469B2 (en) | 2015-10-14 | 2020-03-03 | Fiberlean Technologies Limited | 3D-formable sheet material |
US11274399B2 (en) | 2016-04-05 | 2022-03-15 | Fiberlean Technologies Limited | Paper and paperboard products |
US10801162B2 (en) | 2016-04-05 | 2020-10-13 | Fiberlean Technologies Limited | Paper and paperboard products |
US11846072B2 (en) | 2016-04-05 | 2023-12-19 | Fiberlean Technologies Limited | Process of making paper and paperboard products |
US11732421B2 (en) | 2016-04-05 | 2023-08-22 | Fiberlean Technologies Limited | Method of making paper or board products |
US10214859B2 (en) | 2016-04-05 | 2019-02-26 | Fiberlean Technologies Limited | Paper and paperboard products |
US10794006B2 (en) | 2016-04-22 | 2020-10-06 | Fiberlean Technologies Limited | Compositions comprising microfibrilated cellulose and polymers and methods of manufacturing fibres and nonwoven materials therefrom |
US11572659B2 (en) | 2016-04-22 | 2023-02-07 | Fiberlean Technologies Limited | Compositions comprising microfibrillated cellulose and polymers and methods of manufacturing fibres and nonwoven materials therefrom |
US10724173B2 (en) | 2016-07-01 | 2020-07-28 | Mercer International, Inc. | Multi-density tissue towel products comprising high-aspect-ratio cellulose filaments |
US10570261B2 (en) | 2016-07-01 | 2020-02-25 | Mercer International Inc. | Process for making tissue or towel products comprising nanofilaments |
US10463205B2 (en) | 2016-07-01 | 2019-11-05 | Mercer International Inc. | Process for making tissue or towel products comprising nanofilaments |
US11098134B2 (en) | 2016-09-01 | 2021-08-24 | Hs Manufacturing Group, Llc | Methods for biobased derivatization of cellulosic surfaces |
US10730959B2 (en) * | 2016-09-01 | 2020-08-04 | Hs Manufacturing Group, Llc | Methods for biobased derivatization of cellulosic surfaces |
US20180066073A1 (en) * | 2016-09-01 | 2018-03-08 | Hs Manufacturing Group Llc | Methods for biobased derivatization of cellulosic surfaces |
US10640927B2 (en) | 2016-09-19 | 2020-05-05 | Mercer International, Inc. | Absorbent paper products having unique physical strength properties |
US10640928B2 (en) | 2016-09-19 | 2020-05-05 | Mercer International Inc. | Absorbent paper products having unique physical strength properties |
CN111684130A (zh) * | 2017-12-04 | 2020-09-18 | 芬欧汇川集团 | 由化学纸浆制造用于复合应用的纸浆前体材料的方法及其产品 |
US11724941B2 (en) | 2018-02-15 | 2023-08-15 | North Carolina State University | Synthesis of micron and nanoscale carbon spheres and structures using hydrothemal carbonization |
US11352747B2 (en) | 2018-04-12 | 2022-06-07 | Mercer International Inc. | Processes for improving high aspect ratio cellulose filament blends |
EP3733959A1 (de) * | 2019-05-03 | 2020-11-04 | Valmet Technologies, Inc. | Überwachung und steuerung der raffinierung von faserzellstoff |
Also Published As
Publication number | Publication date |
---|---|
EP2504487A4 (de) | 2014-01-22 |
EP2504487B1 (de) | 2016-07-20 |
FI20096233A0 (fi) | 2009-11-24 |
CN102686799A (zh) | 2012-09-19 |
EP2504487A1 (de) | 2012-10-03 |
US20130000855A1 (en) | 2013-01-03 |
FI20096233A (fi) | 2011-05-25 |
FI123289B (fi) | 2013-01-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2504487B1 (de) | Verfahren zur herstellung einer nanofibrillierten zellulosepulpe und verwendung der pulpe bei der papierherstellung in nanofibrillierten zellulose-verbundstoffen | |
US9458571B2 (en) | Method for producing furnish, furnish and paper | |
CA2824191C (en) | High aspect ratio cellulose nanofilaments and method for their production | |
EP2236545B1 (de) | Verfahren zur Herstellung von nano-fibrillären Zellulosegels | |
RU2535688C2 (ru) | Способ получения модифицированной целлюлозы | |
Oliaei et al. | Microfibrillated lignocellulose (MFLC) and nanopaper films from unbleached kraft softwood pulp | |
CA2641607A1 (en) | Method for the manufacturing of microfibrillated cellulose | |
US11814794B2 (en) | Cellulose fiber molded product and method for manufacturing the same | |
SE543552C2 (en) | Refined cellulose fiber composition | |
Fathi et al. | Prospects for the preparation of paper money from cotton fibers and bleached softwood kraft pulp fibers with nanofibrillated cellulose | |
Park et al. | Utilization of cellulose micro/nanofibrils as paper additive for the manufacturing of security paper | |
AU2017327762A1 (en) | Method for producing cellulose filaments with less refining energy | |
JP7346018B2 (ja) | セルロース繊維スラリーの製造方法 | |
Tirronen | Applicability of fibrous and size index to characterize microfibrillated cellulose, fiber blends, and paper properties | |
WO2023209622A1 (en) | Dried modified pulp with a certain content of microfibrils and pre-fibrillated fibers | |
WO2015052380A1 (en) | Method for manufacturing a paper, a paper and its use, a furnish and a wood based composition |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 201080053197.5 Country of ref document: CN |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 10832694 Country of ref document: EP Kind code of ref document: A1 |
|
REEP | Request for entry into the european phase |
Ref document number: 2010832694 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2010832694 Country of ref document: EP |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 13511956 Country of ref document: US |