• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The present invention relates to a method for producing a thermoset solid foam, comprising the following successive steps: (a) providing an expandable and thermosetting composition containing a sugar, an acid catalyst selected from strong acids, phosphoric acid and acidic mineral salts, (b) introduction of the expandable and thermosetting composition into a mold or application of the expandable composition on a support to a film having a thickness of at least 1 mm, (c) heating of the expandable and thermosetting composition at a temperature of at least 140 ° C to form a thermoset solid foam block.
    公开号:FR3035402A1
    申请号:FR1553771
    申请日:2015-04-27
    公开日:2016-10-28
    发明作者:Marie Savonnet；Pierre Salomon；Edouard Obert
    申请人:Saint Gobain Isover SA France；
    IPC主号:
    专利说明:

    [0001] The present invention relates to thermoset solid foams obtained by reaction and chemical foaming of an expansible composition containing sugars and an acid catalyst. The manufacture of insulating products based on mineral wool generally comprises a step of manufacturing the glass or rock fibers by a centrifugation process. On their path between the centrifuge device and the fiber collection belt, the still hot fibers are sprayed with an aqueous sizing composition, also known as a binder, which is then subjected to thermosetting reaction at temperatures of about 200 ° C. . Phenolic resins used for several decades as binders have been replaced more and more by products from renewable sources and emitting little or no formaldehyde, a compound considered to be harmful to human health . Thus, application WO 2007/014236 discloses sizing compositions, or binders, based on reducing sugars and amines or ammonium salts which, inter alia by Maillard reaction, harden and bind the glass fibers. on which they are applied. Applications WO 2009/019232 and WO 2009/019235 similarly disclose binders for glass fibers containing at least one reducing sugar and phosphate, sulfate, nitrate or ammonium carbonate, these reactants being capable of reacting by reaction. of Maillard after application to the glass fibers directly after formation of these. Application WO2012 / 028810 discloses sizing compositions based on non-reducing sugars and metal salts of mineral acids capable of hardening and binding the glass fibers to which they are applied.
    [0002] Finally, the application W02012 / 168621 discloses, in a similar manner, binders for glass fibers containing at least one non-reducing sugar, at least one non-reducing sugar dehydration catalyst, at least one amine and at least one ethylenic unsaturation. activated, these reagents being capable of reacting after application the glass fibers directly after formation thereof. The present invention is based on the surprising discovery that certain sugar-based sizing compositions, when heated in fairly concentrated form above a certain temperature (about 150 ° C), instead of spraying them. on hot glass fibers, are highly foaming. Gas evolution occurs at the same time as the curing reaction. The liquid starting composition, introduced into an open container and exposed to sufficient heat, increases in volume, thickens and eventually hardens, giving rise, after a few minutes, to a rigid, dark-colored foam. The Applicant has made numerous attempts to determine under which experimental conditions sugar-based compositions, reducing or non-reducing, formed thermoset foams. Without wishing to be bound by any particular theory, the Applicant believes that the reaction involved in the curing of the foaming compositions of the present application is based on an acid catalyzed dehydration reaction of the sugar, resulting in the formation of hydroxymethylfurfural. (HMF) capable of polymerizing. The present invention therefore relates to the use of a sugar-containing composition, and an acid catalyst selected from the group consisting of strong acids, phosphoric acid and acidic mineral salts, as an expandable and thermosetting composition for the manufacture of a foam-type insulating product. More particularly, the present invention relates to a method for producing a thermoset solid foam, usable as a thermal insulation product, comprising the following successive steps: (a) providing an expandable and thermosetting composition containing A sugar, an acid catalyst selected from strong acids, phosphoric acid and acidic mineral salts, (b) introducing the expandable and thermosetting composition into a mold or applying the expandable composition to a mold; supporting a film having a thickness of at least 1 mm, (c) heating the expandable and thermosetting composition to a temperature of at least 140 ° C to form a thermoset solid foam block.
    [0003] The sugar usable in the present invention may be a reducing sugar or a non-reducing sugar. By reducing sugars is meant carbohydrates of formula c (H2O) p having at least one aldehyde or ketone group (reducing group). Reducing sugars for use in the present invention include monosaccharides (monosaccharides) and osides (disaccharides, oligosaccharides, and polysaccharides). Hexoses, namely sugars comprising six carbon atoms, such as glucose, mannose, galactose and fructose, are preferably used.
    [0004] Lactose or maltose are examples of disaccharides useful as reducing sugars. It is also possible advantageously to use starch hydrolysates obtained by enzymatic hydrolysis or acid hydrolysis of starch. The non-reducing sugars preferably used in the present invention are sucrose and trehalose. Throughout the application the term "sugar", even used in the singular, still includes mixtures of reducing sugars and / or non-reducing. The acid catalyzing the dehydration of the sugar may be a strong acid, i.e. an acid which dissociates completely when dissolved in water. The strong acids that can be used include hydrohalic acids, namely hydrochloric acid, hydroiodic acid and hydrobromic acid, sulfuric acid (H2SO4), nitric acid (HNO3), chloric acid and the like. (HCI03), perchloric acid (HCI04), manganic acid (H2MnO4), permanganic acid (HMnO4), trifluoroacetic acid, and superacids including fluoroantimonic acid (HF.SbF5), acid magical 5 (HSO3F.SbF5), trifluoromethanesulfonic acid (HSO3CF3), fluorosulfuric acid (HSO3F) and disulfuric acid (H2S207). In order to effectively catalyze the foaming and curing of the expandable compositions, the strong acid must be used in a concentration of at least 0.1 N (pH = 1), preferably at least 0.5 N.
    [0005] Although the phosphoric acid is not a strong acid (pKa1 of about 2), it can act as an acid dehydration catalyst provided it is used at a concentration of at least 0.1 mol / L. preferably at least 0.2 mol / L. Finally, the acid catalyst may be an acidic mineral salt. The term "acidic mineral salt" means a mineral salt which, when introduced into demineralised water, makes it possible to lower the pH to a value of less than 3. These acidic mineral salts do not include salts. minerals of alkali and alkaline earth metals, but include a large number of transition metal salts.
    [0006] Examples of acidic inorganic salts are sulphates, nitrates, chlorides and bromides of aluminum, gallium, copper, zinc, silver, nickel, iron and lead. The Applicant has obtained good results with aluminum sulphate, copper sulphate and copper nitrate which are particularly preferred. The acidic mineral salts will preferably be used in a concentration such that the pH of the composition is less than or equal to 3, preferably less than 2.5 and ideally less than 2. The expandable and thermosetting compositions used in the present invention for the formation of solid foams usually contain water. This water essentially acts as a solvent for sugar. Since the expandable composition used in the process of the present invention does not need to be finely dispersed in air, it is less critical than in the case of a binder for mineral fibers, ensure that its viscosity is sufficiently low. While an aqueous binder for mineral fibers has, at the time of spraying, at least 90% or even 95% water, the expandable compositions of the present invention are much more concentrated and viscous. They advantageously contain at most 60% by weight of water, in particular at most 35% by weight, preferably at most 25% by weight, more preferably at most 15% by weight and ideally at most 5% by weight of water. The solids content of the foamable composition before heating is therefore at least 40% by weight, in particular at least 65% by weight, preferably at least 75%, more preferably at least equal to at 85% by weight and ideally at least 95% by weight. The sugar is a total of at least 70%, preferably at least 80%, in particular at least 90% of the dry weight of the foamable composition.
    [0007] Although sugar and the acid catalyst are the major and essential components of the expandable composition, it may contain a number of other adjuvants and additives to improve the properties of the final thermoset foams or to reduce the cost of production. . The total amount of these additives and additives, however, preferably does not exceed 30% of the dry weight of the expandable composition. Thus, the expandable composition may contain, for example, one or more surfactants to reduce the average size and dispersion of the pore sizes of the final foam or to facilitate incorporation of a filler. The expandable composition preferably contains from 1 to 15% by weight, preferably from 2 to 10% by weight, based on the dry weight of the total foamable composition, of one or more surfactants. The expandable composition used in the present invention may further contain up to 20% by weight, preferably up to 10% by weight, based on the dry weight of the total foamable composition, of one or more fillers. mineral or organic.
    [0008] Finally, the expandable composition may contain one or more other additives conventionally used in the polymer processing and processing industry such as dyes, pigments, antibacterial or antifungal agents, flame retardants, UV absorbers, hydrophobic agents. . These additives represent in total preferably at most 10% of the dry weight of the composition. In the process of the present invention, reactive compositions, known as such in highly diluted form, are therefore used in a completely different manner from that described in the prior art documents mentioned in the introduction. They are not sprayed as fine droplets onto hot mineral fibers for the formation of a mat of fibers bonded together, but remain in compact, undispersed form. Their solids content is considerably higher than that of the compositions of the state of the art.
    [0009] When the expandable composition is spread as a continuous film on a support, the thickness of the film before heating, i.e. before expansion and curing, is preferably at least 2 mm, in particular at least 5 mm, and more preferably at least 10 mm.
    [0010] The volume of the foam block formed can vary within very wide limits. When the expandable composition is used in a continuous process forming, for example, strips or profiles of insulating materials, it is potentially infinite. When the expandable composition is used to form discrete blocks, for example foams or foams, the amount thereof is preferably such that the volume of each block of thermoset solid foam is at least 500 cc, preferably at least equal to 0.001 m3, in particular at least 0.01 m3. The foam block is preferably in the form of a plate. To react the sugar it is necessary to heat the foamable composition to a temperature of at least 140 ° C. The reaction temperature will preferably be from 150 ° C to 180 ° C. This temperature is, of course, that measured at the heart of the reaction mixture. To heat the expandable composition in step (c), any conventional means known in the field of processing and processing of polymers, such as hot air, thermal radiation, microwaves or placing in contact with a hot support (mold). Of course, the temperature of the heating means (oven, support, mold) may be greater than the reaction temperature mentioned above, for example between 160 and 210 ° C. Another subject of the present invention is a solid foam that can be obtained by the method that is the subject of the present invention. The solid foams prepared by the process of the invention are of a dark brown to black color. Their density is between 30 and 60 kg / m3. They have a closed porosity with an average pore diameter, determined by X-ray tomography, between 100 and 800 nm.
    [0011] EXAMPLE 1 Mineral Salts Several thermosetting expansible compositions are prepared by adding an aqueous solution of the acidic catalyst (acidic mineral salt) to a glucose monohydrate powder. The mixture is stirred at room temperature to disperse the powder. The Table la indicates the respective amounts of sugar and acid mineral salt, expressed as solids, the mol / L concentration of the acid catalyst as well as the total solids content of the compositions prepared. Each of the compositions is introduced into a flat-bottomed aluminum dish (5 cm in diameter) into a film having a thickness of about 1 mm. The cups are introduced into an oven heated to 200 ° C. After 20 minutes, they are removed, allowed to cool to room temperature and the thickness of the foam formed is observed: Scale: -: less than 0.5 cm +: 0.5 to 1 cm ++: 1.1 to 2 cm +++: 2.1 to 3 cm 15 ++++: 3.1 to 4 cm more than 4 cm 3035402 - 9 - Table 1: Acidic mineral salts Sucre Catalyst Concentratio Extract Thickness of acidic foam n dry acid catalyst 85 parts of D-glucose monohydrate 15 parts 0.6 mol / L 60% +++++ Al2 (504) 3 92,5 parts of D-glucose monohydrate 7,5 parts Al2 (504) 3 0.3 mol / L 60% +++++ 98.5 parts of D-glucose monohydrate 1.5 parts Al2 (504) 3 0.06mo1 / L 60% +++++ 99.85 parts of D-glucose monohydrate 0.15 parts Al2 (504) 3 0.006 mol / L 60% +++++ 85 parts of D-glucose monohydrate 15 parts of 1.4 mol / L 60% +++++ Cu504 85 parts of D-glucose monohydrate 15 parts of 1.2 mol / L 60% +++++ Cu (NO3) 2 The foams formed are all brown to black.
    [0012] By way of comparison, similar compositions are prepared either by omitting the acid catalyst or by replacing the acidic mineral salts (Al 2 (504) 3 Cu 504 and Cu (NO 3) 2) with inorganic salts which do not allow the composition to be acidified until at a pH below 3.
    [0013] The results are shown in Table lb below. Table lb: Comparative Mineral Salts Sugar Catalyst Concentratio Extract Thickness of Acidic Moss Dry Acid Catalyst 100 parts of D-glucose monohydrate - - 60% - 85 parts of D-glucose monohydrate 15 parts of 1.9 moles / L 60% - Mg504 85 parts of D-glucose monohydrate 15 parts of 1.3 mol / L 60% - Ca504 85 parts of D-glucose monohydrate 15 parts of 1.8 mol / L 60% - AlPO4 85 parts of D Glucose monohydrate 15 parts of 3.9 mol / L 60% - NaCl These samples are yellow in caramel color after 20 minutes of cooking. No formation of foam is observed. Example 2 Strong acids and phosphoric acid Several thermosetting expansible compositions are prepared by adding an aqueous solution of the acid catalyst (strong acid or phosphoric acid) to a glucose monohydrate powder. The mixture is stirred at room temperature to disperse the powder. Table 2a shows the mol / L concentration of the acid catalyst used as well as the total solids content of the compositions prepared. Each of the compositions is introduced into a flat-bottomed aluminum dish (5 cm in diameter) in a film having a thickness of about 1 mm 3035402. The cups are introduced into an oven heated to 200 ° C. After 20 minutes, they are removed, allowed to cool to room temperature and the thickness of the formed foam is observed. The rating scale is identical to that of Example 1.
    [0014] Table 2a Strong acids and phosphoric acid Sugar Catalyst Concentratio Extract Thickness of the acidic foam n dry acid catalyst 100 parts of D-glucose monohydrate HCI 1 mol / L 60% +++++ 100 parts of D-glucose monohydrate H2504 0, 28 mol / L 60% +++++ 100 parts of D-glucose monohydrate H2504 0.1 mol / L 60% +++++ 100 parts of D-glucose monohydrate HNO3 1.2 mol / L 60% ++ 100 parts of D-glucose monohydrate H3PO4 0.20 mol / L 60% ++++ Hydrochloric acid, sulfuric acid and phosphoric acid used at a concentration greater than or equal to 0.1 mol / L give 10 bulky foams of brown to black color. Unexplainably nitric acid, even at a high concentration, foams relatively less than other acids. For comparison, the same acids are used at a concentration of 0.01 mol / L. The results are shown in Table 2b below. 3035402 - 12 - Table 2b Strong acids and phosphoric acid (comparative) Sugar Catalyst Concentratio Extract Thickness of the acidic foam n dry acid catalyst 100 parts of D-glucose monohydrate HCI 0.01 mol / L 60% - 100 parts of D-glucose monohydrate H2504 0.01 mol / L 60% - 100 parts of D-glucose monohydrate HNO3 0.01 mol / L 60% - 100 parts of D-glucose monohydrate H3PO4 0.01 mol / L 60% - No foam forms .
    [0015] The Applicant has also performed a series of tests by contacting D-glucose with increasing amounts of acetic acid (weak acid) and heating the mixture under the same conditions. Even at an acetic acid concentration greater than 15 mol / L, no foam formation is observed.
    权利要求:
    Claims (15)
    [0001]
    REVENDICATIONS1. A process for producing a thermoset solid foam, comprising the following successive steps: (a) providing an expandable and thermosetting composition containing a sugar, - an acid catalyst selected from strong acids, phosphoric acid and acidic mineral salts, (b) introduction of the expandable and thermosetting composition into a mold or application of the expandable composition on a support to a film having a thickness of at least 1 mm, (C) heating of the expandable and thermosetting composition at a temperature of at least 140 ° C to form a thermoset solid foam block.
    [0002]
    2. Process according to Claim 1, characterized in that the concentration of strong acids is at least 0.1 N, the concentration of phosphoric acid is at least 0.1 mol / L or the concentration in acidic mineral salts is such that the pH of the composition is less than or equal to
    [0003]
    3. 3. Method according to claim 1 or 2, characterized in that the thickness of the film is at least 2 mm, preferably at least 5 mm, in particular at least 10 mm.
    [0004]
    4. Method according to any one of the preceding claims, characterized in that the thermoset solid foam block is a plate.
    [0005]
    5. Method according to any one of the preceding claims, characterized in that the expandable composition contains at most 60% by weight, preferably at most 25% by weight, more preferably at most 15% by weight and in particular at most 5% by weight of water. 3035402 - 14 -
    [0006]
    6. Process according to any one of the preceding claims, characterized in that the sugar represents at least 70%, preferably at least 80%, in particular at least 90% of the dry weight of the foamable composition. 5
    [0007]
    7. Process according to any one of the preceding claims, characterized in that the sugar is chosen from reducing sugars and non-reducing sugars, preferably from reducing sugars.
    [0008]
    8. Process according to claim 7, characterized in that the sugar is a reducing sugar chosen from glucose and starch hydrolysates. 10
    [0009]
    9. Process according to any one of the preceding claims, characterized in that the acidic mineral salts are chosen from sulphates, nitrates, chlorides and bromides of aluminum, gallium, copper, zinc, silver, nickel, iron and lead.
    [0010]
    10. Process according to any one of the preceding claims, characterized in that the expandable composition further contains up to 20% by weight, preferably up to 10% by weight, based on the dry weight of the expandable composition. total, of one or more mineral or organic fillers.
    [0011]
    Solid foam obtainable by the process of any one of the preceding claims.
    [0012]
    12. Solid foam according to claim 11, characterized in that it has a density of between 30 and 60 kg / m3.
    [0013]
    13. Solid foam according to claim 11 or 12, characterized in that it has a closed porosity. 25
    [0014]
    14. Solid foam according to one of claims 11 to 13, characterized in that the average pore diameter determined by X-ray tomography is between 100 and 800 nm.
    [0015]
    15. Use of a sugar-containing composition, an acid catalyst selected from strong acids, phosphoric acid and acidic mineral salts, as an expandable and thermosetting composition for the manufacture of a insulating foam product.
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    同族专利:
    公开号 | 公开日
    WO2016174328A1|2016-11-03|
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    RU2716185C2|2020-03-06|
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    DK3289008T3|2019-05-06|
    RU2017134540A3|2019-08-02|
    US20180201747A1|2018-07-19|
    FR3035402B1|2019-04-05|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    WO2009019232A1|2007-08-03|2009-02-12|Knauf Insulation Limited|Mineral wool insulation|
    WO2012028810A2|2010-08-30|2012-03-08|Saint-Gobain Isover|Sizing composition for mineral wool comprising a non-reducing sugar and an inorganic acid metal salt, and insulating products obtained|
    WO2012168621A1|2011-05-25|2012-12-13|Saint-Gobain Isover|Formaldehyde-free sizing composition for fibres, in particular mineral fibres, and resulting products.|
    US2914494A|1955-10-25|1959-11-24|Armstrong Cork Co|Resinous products|
    RU2353633C2|2003-10-10|2009-04-27|Дау Глобал Текнолоджиз Инк.|Composite containing segregated clay in soot and its obtaining|
    EA019802B1|2005-07-26|2014-06-30|Кнауф Инзулацьон Гмбх|Formaldehyde-free uncured binder, composition comprising same and method for preparing fibers bound by a binder|FR3075208B1|2017-12-18|2019-12-20|Saint-Gobain Isover|PROCESS FOR PRODUCING THERMOSET POLYESTER FOAMS WITH PREOLIGOMERIZATION STEP|
    FR3080850A1|2018-05-04|2019-11-08|Saint-Gobain Isover|THERMAL INSULATION MATERIAL|
    FR3089984B1|2018-12-18|2021-01-01|Saint Gobain Isover|Use of linear diols for the manufacture of bio-based polyester foams|
    法律状态:
    2016-04-20| PLFP| Fee payment|Year of fee payment: 2 |
    2016-10-28| PLSC| Publication of the preliminary search report|Effective date: 20161028 |
    2017-04-21| PLFP| Fee payment|Year of fee payment: 3 |
    2018-04-25| PLFP| Fee payment|Year of fee payment: 4 |
    2019-04-26| PLFP| Fee payment|Year of fee payment: 5 |
    2020-04-29| PLFP| Fee payment|Year of fee payment: 6 |
    2021-04-30| PLFP| Fee payment|Year of fee payment: 7 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1553771|2015-04-27|
    FR1553771A|FR3035402B1|2015-04-27|2015-04-27|THERMODURCAL FOAMS AND METHOD OF MANUFACTURE|FR1553771A| FR3035402B1|2015-04-27|2015-04-27|THERMODURCAL FOAMS AND METHOD OF MANUFACTURE|
    EP16723422.8A| EP3289008B1|2015-04-27|2016-04-19|Thermoset foams and manufacutring process|
    JP2017555620A| JP6757331B2|2015-04-27|2016-04-19|Thermosetting foam and manufacturing method|
    US15/569,095| US20180201747A1|2015-04-27|2016-04-19|Thermoset foams and manufacturing process|
    RU2017134540A| RU2716185C2|2015-04-27|2016-04-19|Thermoset foams and manufacturing process thereof|
    DK16723422.8T| DK3289008T3|2015-04-27|2016-04-19|THERMO-HEARDED FOAM AND PROCEDURE FOR MANUFACTURING|
    PCT/FR2016/050906| WO2016174328A1|2015-04-27|2016-04-19|Thermoset foams and manufacutring process|
    KR1020177030603A| KR20170141206A|2015-04-27|2016-04-19|Heat cured foams and manufacturing methods|
    CA2981162A| CA2981162A1|2015-04-27|2016-04-19|Thermoset foams and manufacutring process|
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