EP3375934A1 - Process of making a flocks-based thermal and/or acoustic insulating material - Google Patents
Process of making a flocks-based thermal and/or acoustic insulating material Download PDFInfo
- Publication number
- EP3375934A1 EP3375934A1 EP18162261.4A EP18162261A EP3375934A1 EP 3375934 A1 EP3375934 A1 EP 3375934A1 EP 18162261 A EP18162261 A EP 18162261A EP 3375934 A1 EP3375934 A1 EP 3375934A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- mixture
- substance
- process according
- web
- property
- 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
- 238000000034 method Methods 0.000 title claims abstract description 65
- 244000144992 flock Species 0.000 title claims abstract description 42
- 239000011810 insulating material Substances 0.000 title claims abstract description 22
- 239000000203 mixture Substances 0.000 claims abstract description 76
- 239000000126 substance Substances 0.000 claims abstract description 68
- 239000001913 cellulose Substances 0.000 claims abstract description 29
- 229920002678 cellulose Polymers 0.000 claims abstract description 29
- 230000001046 anti-mould Effects 0.000 claims abstract description 22
- 239000002546 antimould Substances 0.000 claims abstract description 22
- 238000000227 grinding Methods 0.000 claims abstract description 20
- 238000001035 drying Methods 0.000 claims abstract description 5
- 150000003839 salts Chemical class 0.000 claims description 21
- 238000000576 coating method Methods 0.000 claims description 17
- 239000011248 coating agent Substances 0.000 claims description 16
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 13
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 12
- 239000000920 calcium hydroxide Substances 0.000 claims description 12
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 12
- 239000000347 magnesium hydroxide Substances 0.000 claims description 12
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 12
- 238000010410 dusting Methods 0.000 claims description 10
- 239000005871 repellent Substances 0.000 claims description 6
- 230000002209 hydrophobic effect Effects 0.000 claims description 5
- 238000004381 surface treatment Methods 0.000 claims description 4
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 3
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims description 3
- 239000005752 Copper oxychloride Substances 0.000 claims description 3
- WQZGKKKJIJFFOK-QTVWNMPRSA-N D-mannopyranose Chemical compound OC[C@H]1OC(O)[C@@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-QTVWNMPRSA-N 0.000 claims description 3
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 3
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 claims description 3
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 claims description 3
- 229930006000 Sucrose Natural products 0.000 claims description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 3
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims description 3
- ZRIUUUJAJJNDSS-UHFFFAOYSA-N ammonium phosphates Chemical class [NH4+].[NH4+].[NH4+].[O-]P([O-])([O-])=O ZRIUUUJAJJNDSS-UHFFFAOYSA-N 0.000 claims description 3
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 claims description 3
- 239000004202 carbamide Substances 0.000 claims description 3
- 239000001768 carboxy methyl cellulose Substances 0.000 claims description 3
- 235000010948 carboxy methyl cellulose Nutrition 0.000 claims description 3
- 239000008112 carboxymethyl-cellulose Substances 0.000 claims description 3
- HKMOPYJWSFRURD-UHFFFAOYSA-N chloro hypochlorite;copper Chemical compound [Cu].ClOCl HKMOPYJWSFRURD-UHFFFAOYSA-N 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 3
- 229910000365 copper sulfate Inorganic materials 0.000 claims description 3
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 claims description 3
- 235000013681 dietary sucrose Nutrition 0.000 claims description 3
- 239000008103 glucose Substances 0.000 claims description 3
- 239000000178 monomer Substances 0.000 claims description 3
- 229920000620 organic polymer Polymers 0.000 claims description 3
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 3
- 235000019422 polyvinyl alcohol Nutrition 0.000 claims description 3
- 229920005989 resin Polymers 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 3
- 239000002002 slurry Substances 0.000 claims description 3
- 238000003892 spreading Methods 0.000 claims description 3
- 229960004793 sucrose Drugs 0.000 claims description 3
- 235000000346 sugar Nutrition 0.000 claims description 3
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 claims description 3
- 229920002472 Starch Polymers 0.000 claims 2
- 239000008107 starch Substances 0.000 claims 2
- 235000019698 starch Nutrition 0.000 claims 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims 1
- 229910052802 copper Inorganic materials 0.000 claims 1
- 239000010949 copper Substances 0.000 claims 1
- 238000004804 winding Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 13
- 238000009736 wetting Methods 0.000 abstract 1
- 239000000123 paper Substances 0.000 description 31
- 239000000463 material Substances 0.000 description 13
- 239000000654 additive Substances 0.000 description 9
- 235000011116 calcium hydroxide Nutrition 0.000 description 7
- 235000012254 magnesium hydroxide Nutrition 0.000 description 7
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 5
- 235000010338 boric acid Nutrition 0.000 description 5
- 239000004327 boric acid Substances 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 239000010802 sludge Substances 0.000 description 5
- 239000002537 cosmetic Substances 0.000 description 4
- 231100000331 toxic Toxicity 0.000 description 4
- 230000002588 toxic effect Effects 0.000 description 4
- 239000010893 paper waste Substances 0.000 description 3
- 235000002639 sodium chloride Nutrition 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 150000001639 boron compounds Chemical class 0.000 description 2
- 150000001642 boronic acid derivatives Chemical class 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- GTYLWUZKRJYAJZ-UHFFFAOYSA-N dibutoxyborinic acid Chemical compound CCCCOB(O)OCCCC GTYLWUZKRJYAJZ-UHFFFAOYSA-N 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 230000001747 exhibiting effect Effects 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910021538 borax Inorganic materials 0.000 description 1
- 150000001638 boron Chemical class 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- RDMZIKMKSGCBKK-UHFFFAOYSA-N disodium;(9,11-dioxido-5-oxoboranyloxy-2,4,6,8,10,12,13-heptaoxa-1,3,5,7,9,11-hexaborabicyclo[5.5.1]tridecan-3-yl)oxy-oxoborane;tetrahydrate Chemical compound O.O.O.O.[Na+].[Na+].O1B(OB=O)OB(OB=O)OB2OB([O-])OB([O-])OB1O2 RDMZIKMKSGCBKK-UHFFFAOYSA-N 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- -1 for example Substances 0.000 description 1
- 239000000417 fungicide Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 239000000976 ink Substances 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 231100000219 mutagenic Toxicity 0.000 description 1
- 239000003471 mutagenic agent Substances 0.000 description 1
- 231100000707 mutagenic chemical Toxicity 0.000 description 1
- 230000003505 mutagenic effect Effects 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000011087 paperboard Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000011012 sanitization Methods 0.000 description 1
- 229960001922 sodium perborate Drugs 0.000 description 1
- 235000010339 sodium tetraborate Nutrition 0.000 description 1
- 239000004328 sodium tetraborate Substances 0.000 description 1
- YKLJGMBLPUQQOI-UHFFFAOYSA-M sodium;oxidooxy(oxo)borane Chemical compound [Na+].[O-]OB=O YKLJGMBLPUQQOI-UHFFFAOYSA-M 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 230000002110 toxicologic effect Effects 0.000 description 1
- 231100000027 toxicology Toxicity 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 230000002087 whitening effect Effects 0.000 description 1
Images
Classifications
-
- 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
- D21H21/34—Ignifugeants
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/06—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by dry methods
- D21B1/066—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by dry methods the raw material being pulp sheets
-
- 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
- D21H21/36—Biocidal agents, e.g. fungicidal, bactericidal, insecticidal agents
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21J—FIBREBOARD; MANUFACTURE OF ARTICLES FROM CELLULOSIC FIBROUS SUSPENSIONS OR FROM PAPIER-MACHE
- D21J1/00—Fibreboard
- D21J1/16—Special fibreboard
- D21J1/20—Insulating board
Definitions
- the present invention refers to a process of making a flocks-based, cellulose-based thermal and/or acoustic insulating material.
- the majority of the known processes for manufacturing insulating flocks of the present type comprise using waste paper or paperboard as a raw material, and usually comprise a series of steps in which such material is firstly mechanically treated for being shredded and reduced in flocks, and then is treated by a series of additives for sanitizing the material, for example biologic inhibitors (boric acid, borax, etc.).
- biologic inhibitors for sanitizing the material, for example biologic inhibitors (boric acid, borax, etc.).
- the insulating materials obtained by such processes have the inconvenience of containing undesired substances (e. g. magazines, newspapers, etc.), optical whitening inks, coats, etc., and boron salts considered toxic by the latest European updates regarding in general the health protection.
- Some boron compounds were reclassified as mutagens and/or toxic for the reproduction system, according to what was established by the European Commission (No. 790/2009). The present limits for boric acid, borates, and tetraborates, were set by the SCCNFP in 1998.
- the CSSC were required to do an evaluation about the safety, based on the same scientific data by which the classification of the present compounds, listed in the CSSC original document, was modified.
- the CSSC is in the opinion of that all the substances listed in the tables attached to the document, apart from dibutyl hydrogen borate, are effectively regulated by number 1a of Annex III, while tetraborates are regulated both by number 1a and number 1b in the same Annex.
- dibutyl hydrogen borate no limit was set by the European Commission (No. 790/2009) and no evaluation was produced with reference to the risk thereof.
- the CSSC is in the opinion that the toxicity threshold of these substances is similar to the one of other boron compounds, and therefore they are considered safe if used under the conditions by which are used these latter.
- the CSSC observes that the octaborates are not classified as toxic for the reproduction system, and that does not exist a specific concentration limit set for them.
- Such process comprises introducing a group of additives, for example, fungicides, fire-retardant agents, dyes, etc., in the containing vat and/or in a pipe transporting the cellulose sludge pulp to a sludge press.
- a group of additives for example, fungicides, fire-retardant agents, dyes, etc.
- the Applicants have provided a new type of process of manufacturing a flocks-based, cellulose-based, insulating material, enabling to obtain a plurality of advantages, both with reference to the provision of the process and with reference to the quality of the manufactured product.
- the described process has the object of manufacturing a flocks-based, cellulose-based material.
- such process is characterized by the fact of providing the following steps:
- such process is characterized by the fact of providing the following steps:
- such process is characterized by the fact of providing the following steps:
- such process is characterized by the fact of providing the following steps:
- such process is characterized by the fact of providing the following steps:
- the step of applying a coating is made by a "size-press” station or a "film-press” station, or a coater, or a mill-finishing machine, or a spraying bar predisposed to apply, on both sides of said web, a mixture containing said first substance and said second substance.
- the mixture further contains a third substance having an anti-dusting property.
- the coating on the web with a determined density, preferably comprised between 5 and 30 gr/m 2 .
- the web exhibits a thickness comprised between 0.1 and 0.5 mm.
- the substance is selected between one or more in the group comprising rosin salts, water-repellent resins, and water-repellent paraffins.
- An independent aspect of the invention provides to use a paper making line for manufacturing a flocks-based insulating material, wherein said line comprises a "size-press” station, or a "film-press” station, or a coater, or a mill-finishing machine, or a spraying bar, such use comprising the steps of:
- said mixture comprises also a third substance having an anti-dusting property.
- the process of making the present cellulose-based thermal and/or acoustic insulating material comprises making an actual paper web, optionally, by adding to the cellulose-based pulp, from which it is desired to obtain such web, a mixture (A) and/or by subjecting such web to a specific treatment of the surface by a mixture (B) for providing the insulating material with determined properties.
- the web As soon as the web has taken a final configuration from the point of view of its composition and structure, it is mechanically processed for obtaining flocks forming the final product.
- making flocks by obtaining an intermediate product consisting in an actual paper web enables to be capable of precisely and repeatably controlling the thickness and density of the final flocks; further, it enables to always precisely and repeatably control the quantity of additives introduced to them.
- mixture (A) means a mixture which can be added by mass to the cellulose-based pulp before forming the paper web or sheet.
- mixture (B) means a mixture which can be used for treating the surface of a paper web or sheet obtained by the cellulose-based pulp.
- the substances with a fireproof property useable both in mixture (A) and in mixture (B) can be ammonium phosphate salts, urea, or aluminum salts.
- ammonium phosphate salts urea
- aluminum salts aluminum sulfate and/or aluminum polychloride both directly reacted during the manufacturing step can be used.
- the substances with an anti-mould property useable both in mixture (A) and in mixture (B) can be cupric salts, such as for example copper sulfate, copper oxychloride, Bordeaux slurry.
- mixture (A) and mixture (B) can have the same or a different composition from each other.
- the mixture (A) comprises at least one substance having an anti-mould property
- the mixture (A) comprises at least one substance having an anti-mould property
- the cupric salt such as calcium and/or magnesium hydroxides, can be in a powder state and liquid state.
- the weight percentage of said combination is comprised between 0.01% and 10% by the total weight of the final cellulose-based product (flocks) to be obtained.
- the percentage by weight of the cupric salt is comprised between 2% and 40%, by the total weight of said combination.
- the mixture (A) comprises the combination of cupric salt and calcium hydroxide, magnesium hydroxide or a mixture thereof (substances capable of making basic the product); the percentage by weight of calcium hydroxide, magnesium hydroxide, or a mixture thereof, is comprised between 60% and 98% by weight with respect to the total weight of said combination.
- such salt is present in a percentage comprised between 0.1% and 1% by weight with respect to the total weight of the final cellulose-based product to be obtained.
- the weight ratio of the cupric salt to the fireproof substance is comprised between 1:2 and 1:50 in the cellulose-based final product obtained by applying the process of the present invention.
- mixture (A) and/or mixture (B) can comprise at least one substance having an anti-dusting property.
- the substances capable of imparting an anti-dusting property can be amide-based organic polymers, carboxymethylcellulose; cold-soluble polyvinyl alcohols, and also monomers of mono-disaccharide sugars (glucose, mannose, saccharose, etc.); preferably, mixtures (A) and/or (B) comprise such elements as ligands and with an anti-dusting property.
- the anti-dusting property consists in more bonding cellulose fibrils and several fillers together, contained in the paper web, in order to reduce the dispersion thereof in air as an aerosol of fine particulate.
- Such property enables to avoid to form dust during the steps of flocking and blowing the insulating material, improving in this way from one side the safety of the working environment - due to the smaller amount of suspended dusts - and, on the other side, by making more uniform and time constant the average size of a cellulose flock.
- the herein described process can be directly executed in a standard line for manufacturing paper, as will be shown in the following, suitably adapted for being capable of reproducing the present process.
- the raw materials of the process can be unaltered raw materials, particularly wood, or can be secondary materials, for example waste paper, paper making sludge, or a combination thereof.
- the process comprises making a pulp for manufacturing the paper web, which generally speaking, can have the same characteristics as a standard pulp for producing paper (step 10 of the diagram in Fig. 1 ).
- a mixture (A) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property, can be added to the cellulose-based pulp (step 10 of the diagram in Fig. 1 - in which additives by mass are added).
- the mixture (A) further comprises also an additional substance having the anti-dusting property.
- the mixture (A) comprises at least one substance having an anti-mould property
- such mixture comprises also calcium hydroxide, magnesium hydroxide, or a mixture thereof.
- such pulp comprising said additives
- the headbox of the line which in turn, supplies the pulp on a forming wire, on which the pulp is evenly distributed and starts moving along the line until a sheet is formed.
- the water content in the pulp is gradually decreased by passing the pulp through a series of cylinders groups, particularly - as an example of the main cylinders groups of the line: drainer cylinders, press cylinders, and drying cylinders.
- the grammage and thickness of the sheet can be suitably adjusted as a function of particular applications to which the insulating material is destined.
- Preferred grammage values are comprised between 5 and 200 gr/m 2 .
- the sheet thickness is comprised between 0.1 and 0.5 mm.
- Such adjustment is performed by acting on the same parameters on which it is possible to act, for adjusting density and thickness, in the field of a standard process for making paper.
- the density is controlled at the headbox by adjusting the distribution of the pulp on the forming wire.
- the sheet thickness is controlled by the above-mentioned press cylinders, by adjusting the height development in the formed nip through such cylinders.
- the surface of the obtained web or sheet could be treated by a mixture (B) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property, downstream the drying cylinders, when the sheet has already a stable defined structure (step 30 in Fig. 1 ).
- the mixture (B) further comprises a substance having an anti-dusting property.
- such treatment provides to cover the sheet, preferably on both sides, with a group of substances adapted to impart it determined properties in view of the final use of the material as insulating material.
- a coating material a mixture (B) comprising at least one substance having a fireproof property, and at least one further substance having an anti-mould property.
- such surface treatment of the sheet is obtained by a so-called “size-press” station or by a “film-press” station, such stations are usually used for apply a coat to the paper.
- Fig. 2 which schematically illustrates a "size-press" station
- such station usually comprises two squeezing cylinders 101 through which the sheet moves and, above such cylinders, there is a kind of well 103 containing the mixture for coating the paper.
- the sheet is completely dipped in the mixture before arriving to the two cylinders, and in this way, the paper is completely deeply impregnated by the mixture.
- the mixture quantity which remains applied on the sheet depends on the pressure between the two cylinders.
- the sheet moves to an infrared oven for being dried.
- a film-press station is different from the above described size-press station or coater, or mill-finishing machine because the mixture is not directly applied on the sheet, but on one of the two squeezing cylinders, which then transfers it on the sheet.
- the present treatment enables to completely coat the surface of the paper web and, further, to accurately control the density and thickness of the coating. Also, in this case, the parameters used for performing such kind of adjustment can be the same as those used for adjusting the density and thickness of the coating made in the scope of a standard coating process.
- the values of the density of the deposited coating are comprised between 5 and 20 gr/m 2 .
- hydrophobic the paper web by treating the surface of the web itself by at least one or more particular substances adapted for this purpose.
- the surface treatment will be a spreading; the substance can be selected among one or more in a group comprising rosin salts, water-repellent resins, and water-repellent paraffins.
- the so-formed paper web can be subjected to a directly in-line step for grinding it into flocks, so that downstream the web manufacturing line, it is possible to provide a grinding station adapted to perform such step.
- the web after being possibly cut-to-size along the opposite longitudinal edges, can be also wound in a reel and then can be stored in such format.
- This option clearly enables to substantially reduce the occupied space in a warehouse and enables to make easier to transport the material.
- the web instead of being wound in a reel, can be cut in single sheets which are stored as packs.
- it also foreseeable to transform the paper web in flocks only when the insulating material is installed, so that the web is directly subjected to the grinding step on the field.
- grinding and making the flocks can be done in a factory and the produced flocks are in this case packaged inside bags for being transported.
- the grinding step is performed by a hammer mill.
- FIG. 3 illustrates an example of a movable machine adapted to perform such step. As illustrated, this machine is preferably provided with wheels.
- Such machine is adapted to directly house the reel, and is also capable, according to a continuous process, to blow the formed flocks on the field.
- such machine comprises a chamber 201 containing one or more grinding tools (a micro mill), in which the sheet unwound from the reel, is shredded for reducing it to the desired dimensions.
- a chamber 201 containing one or more grinding tools (a micro mill), in which the sheet unwound from the reel, is shredded for reducing it to the desired dimensions.
- Such chamber communicates with a second chamber 206 in which the formed flocks are gathered.
- the machine comprises a fan 208 for suctioning the formed flocks and supplying them, through a tube 212, directly on the field.
- a partitioning membrane provided with openings (for example a mesh - not illustrated), such openings have predetermined dimensions for only enabling the passage of flocks having dimensions less than a given threshold value.
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Pest Control & Pesticides (AREA)
- Wood Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Paper (AREA)
- Adhesives Or Adhesive Processes (AREA)
Abstract
Description
- The present invention refers to a process of making a flocks-based, cellulose-based thermal and/or acoustic insulating material.
- The majority of the known processes for manufacturing insulating flocks of the present type comprise using waste paper or paperboard as a raw material, and usually comprise a series of steps in which such material is firstly mechanically treated for being shredded and reduced in flocks, and then is treated by a series of additives for sanitizing the material, for example biologic inhibitors (boric acid, borax, etc.).
- The insulating materials obtained by such processes have the inconvenience of containing undesired substances (e. g. magazines, newspapers, etc.), optical whitening inks, coats, etc., and boron salts considered toxic by the latest European updates regarding in general the health protection.
- Some boron compounds were reclassified as mutagens and/or toxic for the reproduction system, according to what was established by the European Commission (No. 790/2009). The present limits for boric acid, borates, and tetraborates, were set by the SCCNFP in 1998.
- Using cosmetic products made of substances classified as carcinogenic, mutagenic or toxic for the reproduction system (CMR), categorized in classes 1, 2 and 3 and in the Annex I of the directive 67/548/EEC, should be banned: only the substances falling into the class 3 can be used, provided that they are evaluated and approved by competent agencies.
- In light of the new classification of some compounds, the CSSC were required to do an evaluation about the safety, based on the same scientific data by which the classification of the present compounds, listed in the CSSC original document, was modified.
- Octaborates, and particularly disodium octaborate tetrahydrate, cited in the suggestion of the SCCNFP in 1998 as the substances used in tests, are not explicitly listed in the Annex III of the Cosmetic Directive. Therefore, it was requested to specify if this class of substances is comprised in numbers 1a and 1b of the Annex III. On the contrary, the boric acid and sodium perborate were treated in a distinct document.
- Based on the present chemical, biological and toxicologic knowledges, the CSSC is in the opinion of that all the substances listed in the tables attached to the document, apart from dibutyl hydrogen borate, are effectively regulated by number 1a of Annex III, while tetraborates are regulated both by number 1a and number 1b in the same Annex. With reference to dibutyl hydrogen borate, no limit was set by the European Commission (No. 790/2009) and no evaluation was produced with reference to the risk thereof.
- Regarding to the maximum limits of the concentration set by the European Commission (No. 790/2009) which are less than the ones present in the Cosmetic Directive, CSSC is in the opinion that using boric acid, borates, and tetraborates is safe for consumers under the conditions listed in number 1a of Annex III of the Cosmetic Directive. However, the maximum concentration of tetraborates should be reduced to values less than 5.5% (calculated by the mass of boric acid).
- With reference to the octaborates, the CSSC is in the opinion that the toxicity threshold of these substances is similar to the one of other boron compounds, and therefore they are considered safe if used under the conditions by which are used these latter. However, the CSSC observes that the octaborates are not classified as toxic for the reproduction system, and that does not exist a specific concentration limit set for them.
- Moreover, in the art it is known a type of process for manufacturing a flocks-based, cellulose-based insulating material, comprising using papermaking sludge as raw material. This process is described, for example, in document
WO 2010/067338 . The industrial process described in such document comprises, with reference to the basic steps thereof, mixing the waste papermaking sludge with waste paper and, possibly, with first extraction cellulose directly obtained from wood, grinding the material mixed in this way in order to obtain the desired size, treating the material in a pulper for separating and insulating the single cellulose fibers, further mechanically treating them inside a mill, and lastly a step of drying the material. Such process comprises introducing a group of additives, for example, fungicides, fire-retardant agents, dyes, etc., in the containing vat and/or in a pipe transporting the cellulose sludge pulp to a sludge press. - In such context, the Applicants have provided a new type of process of manufacturing a flocks-based, cellulose-based, insulating material, enabling to obtain a plurality of advantages, both with reference to the provision of the process and with reference to the quality of the manufactured product.
- Such process is characterized by the fact of exhibiting the steps disclosed in claim 1.
- The characteristics indicated in claims are integrally comprised in the herein given technical teachings.
- Further characteristics and advantages of the present invention will be better understood from the following description made with reference to the attached drawings given only in an exemplifying non-restrictive way, wherein:
-
Fig. 1 schematically shows an embodiment of the herein described process; -
Fig. 2 represents an embodiment example of a specific step of the herein described process; -
Fig. 3 represents an example of a machine for performing the grinding operation provided in the herein described process. - The following description illustrates several specific details for the purpose of providing a thorough comprehension of the embodiments. The embodiments can be provided without one or more of the specific details, or with other methods, components, or materials, etc.. In other cases, known structures, materials or operations are not specifically shown or described for avoiding to make obscure the different aspects of the embodiment.
- The herein used references are only given for convenience and do not therefore define the scope and range of the embodiments.
- As hereinbefore discussed, the described process has the object of manufacturing a flocks-based, cellulose-based material.
- Such process is characterized by the fact of providing the following steps:
- preparing a cellulose-based pulp;
- optionally adding to said pulp a mixture (A) by mass comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property;
- making a paper web having a determined thickness and grammage, from said pulp;
- optionally, as an alternative or in combination with the step of adding by mass, applying on said web a coating consisting of a mixture (B) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property;
- subjecting said (optionally coated) web to a grinding operation for obtaining flocks forming said flocks-based insulating material.
- In a preferred aspect, such process is characterized by the fact of providing the following steps:
- preparing a cellulose-based pulp;
- adding to said pulp a mixture (A) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property;
- making a paper web having a determined thickness and grammage, from said pulp;
- subjecting said web to a grinding operation for obtaining flocks forming said flocks-based insulating material.
- In a more preferred aspect, such process is characterized by the fact of providing the following steps:
- preparing a cellulose-based pulp;
- adding to said pulp a mixture (A) comprising at least one substance having a fireproof property and at least one substance having an anti-mould property;
- making a paper web having a determined thickness and grammage, from said pulp;
- subjecting said web to a grinding operation for obtaining flocks forming said flocks-based insulating material.
- In another preferred aspect, such process is characterized by the fact of providing the following steps:
- preparing a cellulose-based pulp;
- adding to said pulp a mixture (A) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property;
- making a paper web having a determined thickness and grammage, from said pulp;
- applying on said web a coating consisting of a mixture (B) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property;
- subjecting said coated web to a grinding operation for obtaining flocks forming said flocks-based insulating material.
- In another further preferred aspect, such process is characterized by the fact of providing the following steps:
- preparing a cellulose-based pulp;
- making a paper web having a determined thickness and grammage, from said pulp;
- applying on said web a coating consisting of a mixture (B) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property;
- subjecting said coated web to a grinding operation for obtaining flocks forming said flocks-based insulating material.
- In a more preferred aspect, such process is characterized by the fact of providing the following steps:
- preparing a cellulose-based pulp;
- making a paper web having a determined thickness and grammage, from said pulp;
- applying on said web a coating consisting of a mixture (B) comprising a first substance having a fireproof property and a second substance having an anti-mould property;
- subjecting said coated web to a grinding operation for obtaining flocks forming said flocks-based insulating material.
- In an additional aspect according to anyone of the preceding aspects, the step of applying a coating is made by a "size-press" station or a "film-press" station, or a coater, or a mill-finishing machine, or a spraying bar predisposed to apply, on both sides of said web, a mixture containing said first substance and said second substance.
- In an additional aspect, according to anyone of the preceding aspects, the mixture further contains a third substance having an anti-dusting property.
- In an additional aspect, according to anyone of the preceding aspects, it is provided to apply the coating on the web, with a determined density, preferably comprised between 5 and 30 gr/m2.
- In an additional aspect, according to anyone of the preceding aspects, the web exhibits a thickness comprised between 0.1 and 0.5 mm.
- In an additional aspect, according to anyone of the preceding aspects, it is provided to make said web with a grammage comprised between 50 and 400 gr/m2 (in an exemplifying non-restrictive way, between 50 and 300 gr/m2).
- In an additional aspect, according to anyone of the preceding aspects, it is provided to wind said web of coated paper, in a reel, and then to unwind the web from said reel and to subject it to said grinding operation.
- In an additional aspect, according to anyone of the preceding aspects, it is provided to make hydrophobic the paper web by treating the surface of the web by at least one substance adapted to make it hydrophobic, said surface treatment particularly consisting in spreading.
- In a further aspect, according to the preceding aspect, the substance is selected between one or more in the group comprising rosin salts, water-repellent resins, and water-repellent paraffins.
- An independent aspect of the invention provides to use a paper making line for manufacturing a flocks-based insulating material, wherein said line comprises a "size-press" station, or a "film-press" station, or a coater, or a mill-finishing machine, or a spraying bar, such use comprising the steps of:
- supplying to said station, a mixture containing a first substance having a fireproof property, and a second substance having an anti-mould property,
- making, by said line, a paper web exhibiting a determined grammage and thickness, and by said "size-press" station, or "film-press" station, or a coater, or a mill-finishing machine, or a spraying bar, applying on both sides of said web, a coating consisting of said mixture.
- In an additional aspect, according to the preceding aspect, said mixture comprises also a third substance having an anti-dusting property.
- The process of making the present cellulose-based thermal and/or acoustic insulating material comprises making an actual paper web, optionally, by adding to the cellulose-based pulp, from which it is desired to obtain such web, a mixture (A) and/or by subjecting such web to a specific treatment of the surface by a mixture (B) for providing the insulating material with determined properties.
- As soon as the web has taken a final configuration from the point of view of its composition and structure, it is mechanically processed for obtaining flocks forming the final product.
- In view of what is hereinbefore described, the completely novel approach of such process is therefore clear with respect to the known processes discussed at the beginning.
- Moreover, as said, all such processes provide to obtain simple water-based mixtures or a dry material, and to introduce in such mixtures, possible additives. Then, such mixtures are directly mechanically processed.
- In such known processes, necessarily there are intrinsic limits with reference to the control level which can be performed on the structure and consistency of the single flocks and on the additive quantity applied to these, due to the methods used both for forming the flocks and for introducing the different additives.
- On the contrary, such inconveniences are completely overcome by the herein described process.
- Indeed, as specifically described in the following, making flocks by obtaining an intermediate product consisting in an actual paper web, enables to be capable of precisely and repeatably controlling the thickness and density of the final flocks; further, it enables to always precisely and repeatably control the quantity of additives introduced to them.
- In the scope of the present description, the term "mixture (A)" means a mixture which can be added by mass to the cellulose-based pulp before forming the paper web or sheet.
- In the scope of the present description, the term "mixture (B)" means a mixture which can be used for treating the surface of a paper web or sheet obtained by the cellulose-based pulp.
- The substances with a fireproof property useable both in mixture (A) and in mixture (B) can be ammonium phosphate salts, urea, or aluminum salts. With reference to this matter, aluminum sulfate and/or aluminum polychloride both directly reacted during the manufacturing step can be used.
- The substances with an anti-mould property useable both in mixture (A) and in mixture (B) can be cupric salts, such as for example copper sulfate, copper oxychloride, Bordeaux slurry.
- In the scope of the present description, the mixture (A) and mixture (B) can have the same or a different composition from each other.
- In the embodiments according to the process of the present invention, wherein the mixture (A) comprises at least one substance having an anti-mould property, is also present calcium hydroxide, magnesium hydroxide, or a mixture thereof.
- The cupric salt, such as calcium and/or magnesium hydroxides, can be in a powder state and liquid state.
- In the embodiments according to the process of the present invention, wherein the mixture (A) comprises the combination of cupric salt and calcium hydroxide, magnesium hydroxide or a mixture thereof, the weight percentage of said combination is comprised between 0.01% and 10% by the total weight of the final cellulose-based product (flocks) to be obtained.
- Preferably, in the embodiments according to the process of the present invention, wherein the mixture (A) comprises the combination of cupric salt and calcium hydroxide, magnesium hydroxide, or a mixture thereof, the percentage by weight of the cupric salt is comprised between 2% and 40%, by the total weight of said combination.
- Still more particularly, in the embodiments according to the process of the present invention wherein the mixture (A) comprises the combination of cupric salt and calcium hydroxide, magnesium hydroxide or a mixture thereof (substances capable of making basic the product); the percentage by weight of calcium hydroxide, magnesium hydroxide, or a mixture thereof, is comprised between 60% and 98% by weight with respect to the total weight of said combination.
- Preferably, in the embodiments according to the process of the present invention wherein the mixture (B) comprises cupric salt, such salt is present in a percentage comprised between 0.1% and 1% by weight with respect to the total weight of the final cellulose-based product to be obtained.
- Preferably, the weight ratio of the cupric salt to the fireproof substance is comprised between 1:2 and 1:50 in the cellulose-based final product obtained by applying the process of the present invention.
- In the embodiments according to the process of the present invention, moreover the mixture (A) and/or mixture (B) can comprise at least one substance having an anti-dusting property.
- The substances capable of imparting an anti-dusting property can be amide-based organic polymers, carboxymethylcellulose; cold-soluble polyvinyl alcohols, and also monomers of mono-disaccharide sugars (glucose, mannose, saccharose, etc.); preferably, mixtures (A) and/or (B) comprise such elements as ligands and with an anti-dusting property.
- With reference to this matter, it is observed that the anti-dusting property consists in more bonding cellulose fibrils and several fillers together, contained in the paper web, in order to reduce the dispersion thereof in air as an aerosol of fine particulate. Such property enables to avoid to form dust during the steps of flocking and blowing the insulating material, improving in this way from one side the safety of the working environment - due to the smaller amount of suspended dusts - and, on the other side, by making more uniform and time constant the average size of a cellulose flock.
- The herein described process can be directly executed in a standard line for manufacturing paper, as will be shown in the following, suitably adapted for being capable of reproducing the present process.
- The raw materials of the process can be unaltered raw materials, particularly wood, or can be secondary materials, for example waste paper, paper making sludge, or a combination thereof.
- From such raw materials, the process comprises making a pulp for manufacturing the paper web, which generally speaking, can have the same characteristics as a standard pulp for producing paper (step 10 of the diagram in
Fig. 1 ). - According to the process of the present invention, a mixture (A) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property, can be added to the cellulose-based pulp (
step 10 of the diagram inFig. 1 - in which additives by mass are added). Preferably, according to the process according to the invention, the mixture (A) further comprises also an additional substance having the anti-dusting property. - In an embodiment according to the process of the present invention, wherein the mixture (A) comprises at least one substance having an anti-mould property, such mixture comprises also calcium hydroxide, magnesium hydroxide, or a mixture thereof.
- In the preferred embodiment, wherein the process is made in a conventional line for manufacturing paper, such pulp, comprising said additives, is stored inside the headbox of the line, which in turn, supplies the pulp on a forming wire, on which the pulp is evenly distributed and starts moving along the line until a sheet is formed.
- Specifically, in a per se known way, the water content in the pulp is gradually decreased by passing the pulp through a series of cylinders groups, particularly - as an example of the main cylinders groups of the line: drainer cylinders, press cylinders, and drying cylinders.
- Downstream these cylinders, there is the already formed paper web having a moisture content equal to about 5%. Making the paper web is shown in
Fig. 1 bystep 20. - The grammage and thickness of the sheet can be suitably adjusted as a function of particular applications to which the insulating material is destined. Preferred grammage values are comprised between 5 and 200 gr/m2. Preferably, the sheet thickness is comprised between 0.1 and 0.5 mm.
- Such adjustment is performed by acting on the same parameters on which it is possible to act, for adjusting density and thickness, in the field of a standard process for making paper. Particularly, the density is controlled at the headbox by adjusting the distribution of the pulp on the forming wire. On the contrary, the sheet thickness is controlled by the above-mentioned press cylinders, by adjusting the height development in the formed nip through such cylinders.
- If, as an alternative to what was beforehand described (being not excluded the possibility of combining the processes) the paper web were made from cellulose-based pulp to which the cited additives are not added, then, the surface of the obtained web or sheet could be treated by a mixture (B) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property, downstream the drying cylinders, when the sheet has already a stable defined structure (
step 30 inFig. 1 ). Preferably, according to the process of the invention, the mixture (B) further comprises a substance having an anti-dusting property. - In an embodiment according to the process of the present invention, such treatment provides to cover the sheet, preferably on both sides, with a group of substances adapted to impart it determined properties in view of the final use of the material as insulating material. Specifically, such treatment provides to use as a coating material a mixture (B) comprising at least one substance having a fireproof property, and at least one further substance having an anti-mould property.
- In different preferred embodiments, as in the illustrated one, such surface treatment of the sheet is obtained by a so-called "size-press" station or by a "film-press" station, such stations are usually used for apply a coat to the paper.
- With reference to
Fig. 2 , which schematically illustrates a "size-press" station, such station usually comprises two squeezingcylinders 101 through which the sheet moves and, above such cylinders, there is a kind of well 103 containing the mixture for coating the paper. - The sheet is completely dipped in the mixture before arriving to the two cylinders, and in this way, the paper is completely deeply impregnated by the mixture. The mixture quantity which remains applied on the sheet depends on the pressure between the two cylinders.
- Usually, downstream the two cylinders, the sheet moves to an infrared oven for being dried.
- A film-press station is different from the above described size-press station or coater, or mill-finishing machine because the mixture is not directly applied on the sheet, but on one of the two squeezing cylinders, which then transfers it on the sheet.
- The present treatment enables to completely coat the surface of the paper web and, further, to accurately control the density and thickness of the coating. Also, in this case, the parameters used for performing such kind of adjustment can be the same as those used for adjusting the density and thickness of the coating made in the scope of a standard coating process.
- Preferably, the values of the density of the deposited coating are comprised between 5 and 20 gr/m2.
- In an optional but advantageous embodiment, it is possible to make hydrophobic the paper web by treating the surface of the web itself by at least one or more particular substances adapted for this purpose. Particularly, the surface treatment will be a spreading; the substance can be selected among one or more in a group comprising rosin salts, water-repellent resins, and water-repellent paraffins.
- The so-formed paper web can be subjected to a directly in-line step for grinding it into flocks, so that downstream the web manufacturing line, it is possible to provide a grinding station adapted to perform such step.
- Alternatively, the web, after being possibly cut-to-size along the opposite longitudinal edges, can be also wound in a reel and then can be stored in such format. This option clearly enables to substantially reduce the occupied space in a warehouse and enables to make easier to transport the material. Possibly, the web instead of being wound in a reel, can be cut in single sheets which are stored as packs. In view of the above given advantages, it also foreseeable to transform the paper web in flocks only when the insulating material is installed, so that the web is directly subjected to the grinding step on the field. Alternatively, grinding and making the flocks can be done in a factory and the produced flocks are in this case packaged inside bags for being transported. Preferably, the grinding step is performed by a hammer mill.
- In
Fig. 1 , the grinding process is anyway generally indicated by thestep 40. - With reference to the step of grinding the web on the field,
Fig. 3 illustrates an example of a movable machine adapted to perform such step. As illustrated, this machine is preferably provided with wheels. - Such machine is adapted to directly house the reel, and is also capable, according to a continuous process, to blow the formed flocks on the field.
- Particularly, as it is visible in
Fig. 3 , in the several embodiments, and also in the illustrated one, such machine comprises achamber 201 containing one or more grinding tools (a micro mill), in which the sheet unwound from the reel, is shredded for reducing it to the desired dimensions. Such chamber communicates with asecond chamber 206 in which the formed flocks are gathered. Moreover, the machine comprises afan 208 for suctioning the formed flocks and supplying them, through atube 212, directly on the field. Between the first and second chambers, it is provided a partitioning membrane provided with openings (for example a mesh - not illustrated), such openings have predetermined dimensions for only enabling the passage of flocks having dimensions less than a given threshold value. - Obviously, being understood that the principles of the invention are true, the manufacturing details and the embodiments can be changed, also substantially, from what was herein illustrated in an exemplifying non-restrictive way, without, however, falling out of the scope of the invention, as it is defined in the attached claims.
Claims (15)
- Process of making a flocks-based, cellulose-based thermal and/or acoustic insulating materials, characterized by the fact it comprises the following steps:- preparing a cellulose-based pulp;- adding to said pulp a mixture (A) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property;- making a paper web having determined thickness and grammage, from said pulp to which said mixture is added;- subjecting said web to a grinding operation in order to obtain flocks forming said flocks-based insulating material.
- Process according to claim 1, wherein the mixture (A) comprises at least one substance having a fireproof property and at least one substance having the anti-mould property.
- Process according to claim 1 or 2, wherein the substance having a fireproof property is selected among ammonium phosphate salts, urea and aluminum salts and/or the substance having the anti-mould property is selected among cupric salts, preferably is selected among copper sulfate, copper oxychloride, and Bordeaux slurry.
- Process according to claim 1, or 2, or 3, wherein the mixture (A) comprises the substance having an anti-mould property including a copper-based compound, such as a cupric salt, and particularly also calcium hydroxide, magnesium hydroxide, or a mixture of calcium hydroxide and magnesium hydroxide.
- Process according to claim 4, wherein the weight percentage of the combination of cupric salt and calcium hydroxide, magnesium hydroxide or a mixture thereof, is comprised between 0.01% and 10% with respect to the total weight of the final flocks-based, cellulose-based product.
- Process according to claim 4 or 5, wherein the weight percentage of the cupric salt is comprised between 2% and 40% with respect to the total weight of the combination of cupric salt and calcium hydroxide, magnesium hydroxide and a mixture thereof.
- Process according to claim 4 or 5 or 6, wherein the weight percentage of calcium hydroxide, magnesium hydroxide and a mixture thereof is comprised between 60% and 98% with respect to the total weight of the combination of cupric salt and calcium hydroxide, magnesium hydroxide and a mixture thereof.
- Process according to anyone of the preceding claims, wherein the mixture (A) further comprises at least one substance having an anti-dusting property, preferably selected among starch-based organic polymers; carboxymethylcellulose; cold-soluble polyvinyl alcohols; monomers of mono-disaccharide sugars, preferably glucose, mannose, saccharose.
- Process according to anyone of the preceding claims adjusted in order to obtain a web, the thickness thereof being comprised between 0.1 and 0.5 mm and having a grammage comprised between 50 and 200 gr/m2.
- Process according to anyone of the preceding claims, comprising the steps of:- making hydrophobic the paper web by treating the surface of the web by at least one substance adapted to make it hydrophobic, said surface treatment particularly consisting in spreading, optionally the substance being selected among one or more in the group comprising rosin salts, water-repellent resins, and water-repellent paraffins;- optionally, winding said paper web in a reel, and, then, unwinding the web from said reel and subjecting it to said grinding operation.
- Process according to anyone of the preceding claims, comprising the step of applying on said web a coating consisting of a mixture (B) comprising at least one substance having a fireproof property and/or at least one substance having an anti-mould property, wherein the substance having the fireproof property is selected among ammonium phosphate salts, urea and aluminum salts, and/or the substance having the anti-mould property is selected among cupric salts, preferably is selected among copper sulfate, copper oxychloride, and Bordeaux slurry.
- Process according to the preceding claim, wherein the mixture (B) comprises cupric salt, such salt being present in a percentage comprised between 0,1% and 1% by weight with respect to the total weight of the final cellulose-based product to be obtained.
- Process according to anyone of the preceding claims 11 or 12, wherein the mixture (B) further comprises at least one substance having an anti-dusting property, preferably selected among starch-based organic polymers; carboxymethylcellulose; cold-soluble polyvinyl alcohols; monomers of mono-disaccharide sugars, preferably glucose, mannose, saccharose.
- Process according to anyone of the preceding claims 11 or 12, wherein the step of applying on said web a coating consisting in a mixture (B) comprises coating the sheet preferably on both sides:- by a "size-press" station, wherein the sheet is dipped in the mixture (B) before reaching two cylinders, and the paper is impregnated by the mixture (B); downstream the two cylinders, the sheet passes through a drying station, such as an infrared oven; or- by a film-press station, wherein the mixture (B) is applied on at least one of two squeezing cylinders, from which is transferred on the sheet.
- Process according to the preceding claim, wherein the density of the coating obtained from the mixture (B) has values comprised between 5 and 20 gr/m2.
Priority Applications (1)
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SI201830881T SI3375934T1 (en) | 2017-03-16 | 2018-03-16 | Process of making a flocks-based thermal and/or acoustic insulating material |
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IT102017000029362A IT201700029362A1 (en) | 2017-03-16 | 2017-03-16 | PROCEDURE FOR REALIZING A THERMAL AND / OR ACOUSTIC INSULATING MATERIAL IN FLAKES |
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EP3375934A1 true EP3375934A1 (en) | 2018-09-19 |
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EP (1) | EP3375934B1 (en) |
ES (1) | ES2941487T3 (en) |
HU (1) | HUE061712T2 (en) |
IT (1) | IT201700029362A1 (en) |
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WO2024100087A1 (en) | 2022-11-09 | 2024-05-16 | Circusol Holding B.V. | Method and system for manufacturing cellulose-based insulation |
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US20120199303A1 (en) * | 2011-02-08 | 2012-08-09 | International Paper Company | Partially Fire Resistant Insulation Material Comprising Unrefined Virgin Pulp Fibers and Wood Ash Fire Retardant Component |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2024100087A1 (en) | 2022-11-09 | 2024-05-16 | Circusol Holding B.V. | Method and system for manufacturing cellulose-based insulation |
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SI3375934T1 (en) | 2023-06-30 |
EP3375934B1 (en) | 2023-01-11 |
ES2941487T3 (en) | 2023-05-23 |
IT201700029362A1 (en) | 2018-09-16 |
HUE061712T2 (en) | 2023-08-28 |
PL3375934T3 (en) | 2023-05-22 |
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