CN113977841B - A kind of polyimide composite foam containing honeycomb core structure and preparation method thereof - Google Patents
A kind of polyimide composite foam containing honeycomb core structure and preparation method thereof Download PDFInfo
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- 239000006260 foam Substances 0.000 title claims abstract description 170
- 239000004642 Polyimide Substances 0.000 title claims abstract description 126
- 229920001721 polyimide Polymers 0.000 title claims abstract description 126
- 239000002131 composite material Substances 0.000 title claims abstract description 56
- 238000002360 preparation method Methods 0.000 title claims abstract description 29
- 239000002002 slurry Substances 0.000 claims abstract description 83
- 238000005187 foaming Methods 0.000 claims abstract description 74
- 238000004519 manufacturing process Methods 0.000 claims abstract description 17
- 238000011049 filling Methods 0.000 claims abstract description 12
- 239000011162 core material Substances 0.000 claims description 77
- 229910000831 Steel Inorganic materials 0.000 claims description 30
- 239000000463 material Substances 0.000 claims description 30
- 239000010959 steel Substances 0.000 claims description 30
- 239000003795 chemical substances by application Substances 0.000 claims description 22
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 15
- GTDPSWPPOUPBNX-UHFFFAOYSA-N ac1mqpva Chemical compound CC12C(=O)OC(=O)C1(C)C1(C)C2(C)C(=O)OC1=O GTDPSWPPOUPBNX-UHFFFAOYSA-N 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 13
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- 229910021641 deionized water Inorganic materials 0.000 claims description 5
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- 229920001228 polyisocyanate Polymers 0.000 claims description 5
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
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- VLDPXPPHXDGHEW-UHFFFAOYSA-N 1-chloro-2-dichlorophosphoryloxybenzene Chemical compound ClC1=CC=CC=C1OP(Cl)(Cl)=O VLDPXPPHXDGHEW-UHFFFAOYSA-N 0.000 claims description 2
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 claims description 2
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 claims description 2
- 239000012975 dibutyltin dilaurate Substances 0.000 claims description 2
- -1 polymethylene Polymers 0.000 claims description 2
- 229920006389 polyphenyl polymer Polymers 0.000 claims description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 2
- KSBAEPSJVUENNK-UHFFFAOYSA-L tin(ii) 2-ethylhexanoate Chemical compound [Sn+2].CCCCC(CC)C([O-])=O.CCCCC(CC)C([O-])=O KSBAEPSJVUENNK-UHFFFAOYSA-L 0.000 claims description 2
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 claims 1
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical compound C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 claims 1
- 238000009827 uniform distribution Methods 0.000 claims 1
- 238000005303 weighing Methods 0.000 claims 1
- 239000003063 flame retardant Substances 0.000 abstract description 18
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 abstract description 13
- 230000000694 effects Effects 0.000 abstract description 6
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- 239000000779 smoke Substances 0.000 description 9
- 239000000126 substance Substances 0.000 description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 8
- 239000002585 base Substances 0.000 description 6
- 239000004620 low density foam Substances 0.000 description 5
- 150000008064 anhydrides Chemical class 0.000 description 4
- 239000004619 high density foam Substances 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- 238000009413 insulation Methods 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 150000008065 acid anhydrides Chemical class 0.000 description 3
- 239000004760 aramid Substances 0.000 description 3
- 229920003235 aromatic polyamide Polymers 0.000 description 3
- 150000007942 carboxylates Chemical class 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000012965 benzophenone Substances 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 238000010097 foam moulding Methods 0.000 description 2
- 150000003949 imides Chemical group 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000010907 mechanical stirring Methods 0.000 description 2
- OLAPPGSPBNVTRF-UHFFFAOYSA-N naphthalene-1,4,5,8-tetracarboxylic acid Chemical compound C1=CC(C(O)=O)=C2C(C(=O)O)=CC=C(C(O)=O)C2=C1C(O)=O OLAPPGSPBNVTRF-UHFFFAOYSA-N 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- VQVIHDPBMFABCQ-UHFFFAOYSA-N 5-(1,3-dioxo-2-benzofuran-5-carbonyl)-2-benzofuran-1,3-dione Chemical compound C1=C2C(=O)OC(=O)C2=CC(C(C=2C=C3C(=O)OC(=O)C3=CC=2)=O)=C1 VQVIHDPBMFABCQ-UHFFFAOYSA-N 0.000 description 1
- QQGYZOYWNCKGEK-UHFFFAOYSA-N 5-[(1,3-dioxo-2-benzofuran-5-yl)oxy]-2-benzofuran-1,3-dione Chemical compound C1=C2C(=O)OC(=O)C2=CC(OC=2C=C3C(=O)OC(C3=CC=2)=O)=C1 QQGYZOYWNCKGEK-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- GDVKFRBCXAPAQJ-UHFFFAOYSA-A dialuminum;hexamagnesium;carbonate;hexadecahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Al+3].[Al+3].[O-]C([O-])=O GDVKFRBCXAPAQJ-UHFFFAOYSA-A 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 229910021389 graphene Inorganic materials 0.000 description 1
- 239000007770 graphite material Substances 0.000 description 1
- 238000000875 high-speed ball milling Methods 0.000 description 1
- 229960001545 hydrotalcite Drugs 0.000 description 1
- 229910001701 hydrotalcite Inorganic materials 0.000 description 1
- 150000002466 imines Chemical class 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000004377 microelectronic Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 229940057847 polyethylene glycol 600 Drugs 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000002937 thermal insulation foam Substances 0.000 description 1
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/02—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
- B29C44/08—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles using several expanding or moulding steps
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G73/00—Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
- C08G73/06—Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
- C08G73/10—Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
- C08G73/1003—Preparatory processes
- C08G73/1035—Preparatory processes from tetracarboxylic acids or derivatives and diisocyanates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/02—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by the reacting monomers or modifying agents during the preparation or modification of macromolecules
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/36—After-treatment
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2379/00—Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen, or carbon only, not provided for in groups C08J2361/00 - C08J2377/00
- C08J2379/04—Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
- C08J2379/08—Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Laminated Bodies (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
技术领域technical field
本发明涉及阻燃材料技术领域,特别涉及一种含蜂窝芯格结构的聚酰亚胺复合泡沫及其制备方法。The invention relates to the technical field of flame-retardant materials, in particular to a polyimide composite foam with a honeycomb core structure and a preparation method thereof.
背景技术Background technique
一步法聚酰亚胺泡沫是一种以酸酐及异氰酸酯为原材料制备的聚酰亚胺泡沫。由于其酰亚胺环结构和多孔结构,一步法聚酰亚胺泡沫具有吸声、隔热、耐辐射、耐高低温、耐酸碱性等多种突出的理化性能,同时与其他类型聚酰亚胺泡沫相比,其生产工艺相对简单、成品率更高且价格更为低廉,因此被广泛应用于航空航天、汽车、高速列车、微电子等高端领域。One-step polyimide foam is a kind of polyimide foam prepared from acid anhydride and isocyanate as raw materials. Due to its imide ring structure and porous structure, the one-step polyimide foam has various outstanding physical and chemical properties such as sound absorption, heat insulation, radiation resistance, high and low temperature resistance, acid and alkali resistance, and is compatible with other types of polyimide foam. Compared with imine foam, its production process is relatively simple, the yield is higher and the price is lower, so it is widely used in high-end fields such as aerospace, automobiles, high-speed trains, and microelectronics.
进一步地,在对隔热吸声泡沫材料阻燃性及使用安全性要求并不严苛,而完全酰亚胺化的一步法聚酰亚胺泡沫价格过高无法大量应用于建筑、储藏等普通技术领域,一步法聚酰亚胺泡沫由于其配方可调节性及可设计性极强,表现出独特的技术优势。其核心在于,一步法聚酰亚胺泡沫配方及发泡成型制备技术可以通过减少占原材料成本比重较高的酸酐或其衍生物用量的方式,实现酸酐或其衍生物与异氰酸酯用量比例的降低、材料酰亚胺化程度的降低,最终在保证材料生产成本、阻燃性及使用安全性线性下降的同时,仍然能够保证泡沫体的发泡成型,得到隔热吸声效果良好的泡沫体。因此,一步法聚酰亚胺泡沫的该项制备技术优势,有利于不同领域用特定防火等级的一步法聚酰亚胺泡沫制备及生产,在保证材料防火等级不严重过剩的同时,最终产品价格相比于完全亚胺化的一步法聚酰亚胺泡沫得到有效降低,实现了一步法聚酰亚胺泡沫材料产能及应用领域的大幅度提升。Furthermore, when the flame retardancy and use safety requirements of heat-insulating and sound-absorbing foam materials are not strict, the price of fully imidized one-step polyimide foam is too high to be widely used in construction, storage, etc. In the field of technology, one-step polyimide foam shows unique technical advantages due to its strong formula adjustability and designability. The core is that the one-step polyimide foam formulation and foam molding preparation technology can reduce the proportion of acid anhydride or its derivatives to isocyanate by reducing the amount of acid anhydride or its derivatives that account for a high proportion of raw material costs. The reduction of the degree of imidization of the material can ultimately ensure the linear decrease of the material production cost, flame retardancy and safety of use, while still ensuring the foam molding of the foam, and obtaining a foam with good heat insulation and sound absorption effect. Therefore, the advantage of this preparation technology of one-step polyimide foam is conducive to the preparation and production of one-step polyimide foam with specific fire protection grade in different fields. While ensuring that the fire protection grade of the material is not seriously excessive, the price of the final product Compared with the fully imidized one-step polyimide foam, it has been effectively reduced, and the production capacity and application field of one-step polyimide foam have been greatly improved.
为进一步提高系列化一步法聚酰亚胺泡沫材料与其他聚合物基隔热吸声泡沫材料的市场竞争能力,探索在不改变系列化一步法聚酰亚胺泡沫材料制备配方中酸酐或其衍生物用量、酰亚胺化程度条件下,进一步提高其阻燃性及使用安全性乃至机械性能的新路径,已成为系列化一步法聚酰亚胺泡沫材料发展的主要方向。基于这些新路径的探索发现,可反推进行已满足特定防火等级要求的一步法聚酰亚胺泡沫材料制备配方的进一步调节即酸酐或其衍生物用量的进一步降低,以实现材料成本的进一步降低。In order to further improve the market competitiveness of serialized one-step polyimide foam materials and other polymer-based heat-insulating and sound-absorbing foam materials, it is necessary to explore the method of anhydride or its derivatives without changing the preparation formula of serialized one-step polyimide foam materials. Under the conditions of the amount of material used and the degree of imidization, a new path to further improve its flame retardancy, safety in use and even mechanical properties has become the main direction for the development of serialized one-step polyimide foam materials. Based on the discovery of these new paths, the further adjustment of the one-step polyimide foam preparation formula that has met the requirements of a specific fire rating can be reversed, that is, the further reduction of the amount of anhydride or its derivatives, so as to further reduce the material cost. .
与此同时,一步法聚酰亚胺泡沫作为轻质功能材料,其在较低密度下表现出易撕裂、易断裂、强度不高等问题,而目前针对一步法聚酰亚胺泡沫机械性能的提升往往采用模压提升密度等方式来解决,但是却会造成原材料用量及制造成本的急剧增加。At the same time, one-step polyimide foam, as a lightweight functional material, exhibits problems such as easy tearing, easy fracture, and low strength at lower densities, and the current research on the mechanical properties of one-step polyimide foam The improvement is often solved by molding to increase the density, but it will cause a sharp increase in the amount of raw materials and manufacturing costs.
目前,国内外科研工作者及相关单位主要通过添加各种阻燃剂的方式来进一步提高一步法聚酰亚胺泡沫的阻燃性及使用安全性。At present, domestic and foreign scientific research workers and related units mainly add various flame retardants to further improve the flame retardancy and safety of one-step polyimide foam.
在中国专利文献CN107286343A公开的“一种无卤复合阻燃聚酰亚胺泡沫材料及其制备方法”中,发明人通过添加石墨类材料和磷系阻燃剂在密封球磨钢罐中高速球磨而制备出石墨烯磷酸或磷酸化石墨阻燃材料来提高一步法聚酰亚胺泡沫的阻燃性。In "A Halogen-Free Composite Flame-Retardant Polyimide Foam Material and Its Preparation Method" disclosed in the Chinese patent document CN107286343A, the inventor added graphite materials and phosphorus-based flame retardants to high-speed ball milling in a sealed ball mill steel tank. Graphene phosphoric acid or phosphorylated graphite flame retardant materials were prepared to improve the flame retardancy of one-step polyimide foam.
在中国专利文献CN104497255A公开的“一步法制备高阻燃性低密度聚酰亚胺泡沫的方法”中,发明人通过同时添加水滑石和液体阻燃剂,显著提高了一步法聚酰亚胺泡沫的阻燃性。In the "one-step method for preparing high flame-retardant low-density polyimide foam" disclosed in Chinese patent document CN104497255A, the inventor significantly improved the one-step method of polyimide foam by adding hydrotalcite and liquid flame retardant at the same time. flame retardancy.
在中国专利文献CN110922627A公开的“一种低成本阻燃聚酰亚胺绝热泡沫及其制备方法和用途”中,发明人通过添加自主合成的反应型磷系阻燃剂提升了材料的阻燃性。In "A Low-Cost Flame-Retardant Polyimide Thermal Insulation Foam and Its Preparation Method and Application" disclosed in Chinese patent document CN110922627A, the inventor improved the flame retardancy of the material by adding a self-synthesized reactive phosphorus-based flame retardant .
上述添加阻燃剂的方式均能够有效提升一步法聚酰亚胺泡沫材料的阻燃性及使用安全性,然而目前大部分高效阻燃剂的成本远高于均苯四甲酸酐等价格低廉的酸酐原材料,成为一项新的核心成本要素。与此同时,大部分高效阻燃剂为液体,在一步法聚酰亚胺泡沫高温固化过程中容易挥发,既降低了其本身的阻燃效果,也不利于环境保护,而且添加量过高还会引起内部团聚现象,严重影响材料的力学性能。The above methods of adding flame retardants can effectively improve the flame retardancy and safety of one-step polyimide foam materials. However, the cost of most high-efficiency flame retardants is much higher than that of cheap pyromellitic anhydrides. Anhydride raw materials have become a new core cost element. At the same time, most high-efficiency flame retardants are liquids, which are easy to volatilize during the high-temperature curing process of one-step polyimide foam, which not only reduces its own flame retardant effect, but also is not conducive to environmental protection. It will cause internal agglomeration and seriously affect the mechanical properties of the material.
在《Effects of aramid honeycomb core on the flame retardance andmechanical property for isocyanate-based polyimide foams》中,作者通过以芳纶蜂窝芯格对一步法聚酰亚胺泡沫整体进行空间分隔的方式,实现了其阻燃性的有效提升以及材料力学性能的大幅度提升。但是,芳纶蜂窝芯格本身成本相比于低酰亚胺化程度的一步法聚酰亚胺泡沫成本还要高,因此不适于在工业化生产方面应用。进一步地,相关研究人员开展了以铝蜂窝对一步法聚酰亚胺泡沫整体进行空间分隔的研究,虽然提升了其阻燃性及使用安全性,但是由于铝蜂窝的热桥作用,大大损失了其隔热性能,使一步法聚酰亚胺泡沫的导热系数由0.04W/(m·K)左右上升至0.5W/(m·K)左右,隔热或保温功能降低到原来的10%左右,对材料的应用极为不利。In "Effects of aramid honeycomb core on the flame retardance and mechanical property for isocyanate-based polyimide foams", the author realizes its flame retardancy by separating the space of the whole one-step polyimide foam with aramid honeycomb core lattice The effective improvement of the performance and the substantial improvement of the mechanical properties of the material. However, the cost of the aramid honeycomb core itself is higher than that of the one-step polyimide foam with a low degree of imidization, so it is not suitable for industrial production. Further, relevant researchers carried out research on the space separation of the whole one-step polyimide foam with aluminum honeycomb. Although its flame retardancy and safety in use have been improved, due to the thermal bridge effect of aluminum honeycomb, it has greatly lost Its heat insulation performance makes the thermal conductivity of one-step polyimide foam rise from about 0.04W/(m K) to about 0.5W/(m K), and the heat insulation or heat preservation function is reduced to about 10% of the original , which is extremely unfavorable to the application of the material.
发明内容Contents of the invention
有鉴于此,为解决上述技术问题,本发明的目的在于提出一种含蜂窝芯格结构的聚酰亚胺复合泡沫及其制备方法,其能够解决现有技术中阻燃材料的阻燃性能和力学性能不足、且生产工艺复杂和生产成本高的技术问题。In view of this, in order to solve the above-mentioned technical problems, the object of the present invention is to propose a polyimide composite foam containing a honeycomb core structure and a preparation method thereof, which can solve the problems of the flame-retardant properties of flame-retardant materials in the prior art and The technical problems of insufficient mechanical properties, complex production process and high production cost.
所采用的技术方案为:The technical solutions adopted are:
本发明的一种含蜂窝芯格结构的聚酰亚胺复合泡沫的制备方法,包括以下步骤:A kind of preparation method of the polyimide composite foam containing honeycomb core lattice structure of the present invention, comprises the following steps:
S1.发泡料浆的用量计算:按照含蜂窝芯格结构的聚酰亚胺复合泡沫整体表观密度及制备聚酰亚胺泡沫蜂窝芯格的模具规格,设计聚酰亚胺泡沫蜂窝芯格的密度较高,含蜂窝芯格结构的聚酰亚胺复合泡沫整体表观密度较低,计算发泡料浆总用量以及用于制备聚酰亚胺泡沫蜂窝芯格的发泡料浆用量,二者之差为用于填充蜂窝芯格芯格的发泡料浆用量;S1. Calculation of the amount of foaming slurry: According to the overall apparent density of the polyimide composite foam with the honeycomb core structure and the mold specifications for preparing the polyimide foam honeycomb core, design the polyimide foam honeycomb core The density is higher, and the overall apparent density of the polyimide composite foam containing the honeycomb core structure is low. To calculate the total amount of foaming slurry and the amount of foaming slurry used to prepare the polyimide foam honeycomb core, The difference between the two is the amount of foaming slurry used to fill the honeycomb cell;
S2.发泡料浆的配制:先后称取极性溶剂、芳香二酐,加入接有回流冷凝器的反应装置中,搅拌并使体系升温至40-80℃后停止加热,随后加入脂肪醇与芳香二酐进行酯化反应至反应结束;冷却至室温后依次加入泡沫稳定剂、表面活性剂、催化剂、去离子水,搅拌均匀后得到发泡底料;将发泡底料自反应装置中倒入发泡料浆混合容器中后,立刻向发泡底料中加入多异氰酸酯,经机械搅拌均匀后,即为发泡料浆;S2. Preparation of foaming slurry: Weigh the polar solvent and aromatic dianhydride successively, add them to the reaction device connected to the reflux condenser, stir and raise the temperature of the system to 40-80°C, stop heating, then add fatty alcohol and Carry out esterification reaction of aromatic dianhydride to the end of the reaction; after cooling to room temperature, add foam stabilizer, surfactant, catalyst, and deionized water in sequence, and stir evenly to obtain a foaming base material; pour the foaming base material from the reaction device After entering the foaming slurry mixing container, immediately add polyisocyanate to the foaming base material, and after mechanical stirring, it is the foaming slurry;
S3.聚酰亚胺泡沫蜂窝芯格的制备:按照步骤S1计算的聚酰亚胺泡沫蜂窝芯格的发泡料浆用量及步骤S2配制的总的发泡料浆,从步骤S2配制的总的发泡料浆中取得计算量的用于制备聚酰亚胺泡沫蜂窝芯格的发泡料浆后,将该发泡料浆迅速均匀倒入上开口并涂有脱模剂的钢质模具底部,以带有环形均匀分布钢质六棱柱结构并涂有脱模剂的钢板为上盖,快速闭模、拧紧螺丝,静置10-15min,随后将模具放入160-240℃温度的烘箱内,高温固化2-3h,降温脱模后得到聚酰亚胺泡沫蜂窝芯格;S3. The preparation of polyimide foam honeycomb core grid: according to the foaming slurry consumption of the polyimide foam honeycomb core grid calculated in step S1 and the total foaming slurry prepared in step S2, the total foaming slurry prepared from step S2 After obtaining the calculated amount of foaming slurry used to prepare the polyimide foam honeycomb cell from the foaming slurry, pour the foaming slurry quickly and evenly into a steel mold with an upper opening and coated with a release agent At the bottom, use a steel plate with a circular evenly distributed steel hexagonal prism structure and coated with a release agent as the upper cover, quickly close the mold, tighten the screws, let it stand for 10-15 minutes, and then put the mold into an oven at a temperature of 160-240°C Inside, high-temperature curing for 2-3 hours, and polyimide foam honeycomb cells obtained after cooling and demoulding;
S4.含蜂窝芯格结构的聚酰亚胺复合泡沫的制备:继续使用步骤S3中所用上开口并涂有脱模剂的钢质模具,根据步骤S1计算的填充蜂窝芯格芯格的发泡料浆用量;从步骤S2配制的总的发泡料浆中取得计算量的用于填充芯材芯格的发泡料浆后,将该发泡料浆迅速均匀倒入其底部,随后快速将步骤S3所制备的聚酰亚胺泡沫蜂窝芯格插入模具中,以涂有脱模剂的平板型钢板为上盖,快速闭模、拧紧螺丝,静置10-15min,随后将模具放入160-240℃温度的烘箱内,高温固化2-3h,降温脱模后,得到含蜂窝芯格结构的聚酰亚胺复合泡沫。S4. the preparation of the polyimide composite foam that contains honeycomb core lattice structure: continue to use the steel mold that upper opening is used in step S3 and be coated with release agent, the foaming of filling honeycomb core lattice core lattice according to step S1 calculation Slurry consumption; After obtaining the calculated foaming slurry for filling the core material grid from the total foaming slurry prepared in step S2, the foaming slurry is quickly and evenly poured into its bottom, and then quickly Insert the polyimide foam honeycomb core grid prepared in step S3 into the mold, use the flat steel plate coated with the release agent as the upper cover, quickly close the mold, tighten the screws, let stand for 10-15min, and then put the mold into 160 In an oven at a temperature of -240°C, cure at a high temperature for 2-3 hours, and after cooling down and demolding, a polyimide composite foam with a honeycomb core structure is obtained.
进一步地,步骤S2中,按重量份计,芳香二酐20-200份,脂肪醇5-80份,异氰酸酯100-195份,极性溶剂50-70份,泡沫稳定剂10-15份,表面活性剂10-15份,催化剂5-10份和去离子水10-15份。Further, in step S2, by weight, 20-200 parts of aromatic dianhydride, 5-80 parts of fatty alcohol, 100-195 parts of isocyanate, 50-70 parts of polar solvent, 10-15 parts of foam stabilizer, the surface 10-15 parts of active agent, 5-10 parts of catalyst and 10-15 parts of deionized water.
进一步地,步骤S2中,所述芳香二酐包括3,3',4,4'-二苯酮四酸二酐、4,4'-氧双邻苯二甲酸酐、3,3',4,4'-联苯四酸二酐、均苯四甲酸二酐中的一种或多种的混合物。Further, in step S2, the aromatic dianhydride includes 3,3',4,4'-benzophenonetetracarboxylic dianhydride, 4,4'-oxydiphthalic anhydride, 3,3',4 , A mixture of one or more of 4'-biphenyltetracarboxylic dianhydride and pyromellitic dianhydride.
进一步地,步骤S2中,所述脂肪醇包括甲醇、乙醇、丙醇、异丙醇中的一种或多种的混合物。Further, in step S2, the fatty alcohol includes a mixture of one or more of methanol, ethanol, propanol, and isopropanol.
进一步地,步骤S2中,所述催化剂包括三乙醇胺、辛酸亚锡、二月桂酸二丁基锡、Dabco33-LV中的一种或多种的混合物。Further, in step S2, the catalyst includes a mixture of one or more of triethanolamine, stannous octoate, dibutyltin dilaurate, and Dabco33-LV.
进一步地,步骤S2中,所述异氰酸酯为NCO重量百分数为30%-40%的多苯基多亚甲基多异氰酸酯。Further, in step S2, the isocyanate is polyphenylpolymethylene polyisocyanate with an NCO weight percentage of 30%-40%.
本发明的一种含蜂窝芯格结构的聚酰亚胺复合泡沫,其是由上述任一方案所述的制备方法制得的。A polyimide composite foam containing a honeycomb core structure of the present invention is prepared by the preparation method described in any of the above schemes.
进一步地,所述聚酰亚胺泡沫蜂窝芯格的壁厚为2-4mm。Further, the polyimide foam honeycomb cell has a wall thickness of 2-4mm.
进一步地,所述聚酰亚胺泡沫蜂窝芯格的外接圆直径为7.2-20.0mm。Further, the diameter of the circumscribed circle of the polyimide foam honeycomb cell is 7.2-20.0 mm.
与现有技术相比,本发明的有益效果在于:Compared with prior art, the beneficial effect of the present invention is:
本发明制备的含蜂窝芯格结构的聚酰亚胺复合泡沫,在不改变系列化一步法聚酰亚胺泡沫材料整体的基体树脂成分及密度、不添加阻燃剂的前提下,仅通过具有相同成分的高密度蜂窝芯格结构的引入,实现局部密度的宏观不均匀化及分隔,依靠高密度蜂窝芯格结构在燃烧过程中形成的致密、自支撑防火隔热炭层以及对蜂窝芯格中所填充低密度泡沫燃烧时火焰的分割,实现了火焰聚集程度的降低,阻止了空气对流,最终降低了复合泡沫整体的燃烧程度、热量释放行为、燃烧烟气释放行为,实现了其使用安全性的进一步提升,为特定防火等级一步法聚酰亚胺泡沫生产成本的进一步降低奠定技术基础,提升了一步法聚酰亚胺泡沫材料市场竞争力。The polyimide composite foam containing the honeycomb core structure prepared by the present invention can only be obtained by having The introduction of the high-density honeycomb core structure with the same composition can realize the macroscopic inhomogeneity and separation of local density, relying on the dense, self-supporting fire-proof and heat-insulating carbon layer formed by the high-density honeycomb core structure during the combustion process and the effect on the honeycomb core structure. The division of the flame when the low-density foam filled in the middle reduces the degree of flame aggregation, prevents air convection, and finally reduces the overall combustion degree, heat release behavior, and combustion smoke release behavior of the composite foam, and realizes its safe use. The further improvement of the property lays a technical foundation for the further reduction of the production cost of one-step polyimide foam with a specific fire protection grade, and improves the market competitiveness of one-step polyimide foam materials.
与此同时,依靠蜂窝结构特殊的力学特性实现泡沫力学性能的进一步提升。而且本发明操作简便,制备要求低,其产品便于工业化生产和广泛应用。At the same time, relying on the special mechanical properties of the honeycomb structure to further improve the mechanical properties of the foam. Moreover, the invention has simple and convenient operation, low preparation requirements, and its products are convenient for industrialized production and wide application.
综上,本发明解决了现有技术中阻燃材料的阻燃性能和力学性能不足、且生产工艺复杂和生产成本高的问题,在通过具有相同成分的高密度蜂窝结构的引入实现局部密度的宏观不均匀化及分隔下,实现了提高阻燃性能、安全性、力学性能、简化生产工艺和降低生产成本的有益效果。In summary, the present invention solves the problems of insufficient flame retardant and mechanical properties of flame retardant materials in the prior art, complicated production process and high production cost, and achieves local density by introducing a high-density honeycomb structure with the same composition. Under the macroscopic inhomogeneity and separation, the beneficial effects of improving flame retardancy, safety, mechanical properties, simplifying the production process and reducing the production cost are realized.
附图说明Description of drawings
图1为本发明实施例1中所用的带有环形分布六棱柱的钢质模具上盖的结构示意图。FIG. 1 is a schematic structural view of a steel mold upper cover with annularly distributed hexagonal prisms used in Example 1 of the present invention.
具体实施方式Detailed ways
下面结合本实施例的附图,以及通过对比例和实施例来对本发明进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明部分的实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The present invention will be clearly and completely described below in conjunction with the accompanying drawings of the present embodiment, as well as comparative examples and examples. Apparently, the described examples are only some, not all, examples of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts fall within the protection scope of the present invention.
对比例1Comparative example 1
称取17.3克N,N-二甲基甲酰胺溶液、11.76克3,3',4,4'-二苯酮四酸二酐加入接有回流冷凝器的反应装置中,搅拌并使体系升温至50℃后停止加热,随后加入2.44克甲醇与3,3',4,4'-二苯酮四酸二酐进行酯化反应,反应结束后得到透明的羧酸酯溶液,待上述溶液冷却至室温后依次加入3.75克聚乙二醇600、3.75克AK8805表面活性剂、2.4克催化剂、3.6克去离子水,搅拌均匀后得到发泡底料,将发泡底料自反应装置中倒入发泡料浆混合容器中后,立刻向发泡底料中加入45克NCO重量份数为31.5%的多亚甲基多苯基多异氰酸酯,高速机械搅拌得到发泡料浆,将发泡料浆迅速均匀倒入上开口并涂有脱模剂的内腔尺寸为10cm*10cm*5cm的钢质模具底部,以涂有脱模剂长方体钢板为上盖,快速拧紧螺丝,闭合实验模具的上口,封闭实验模具,静置12分钟后,将其放入180℃的烘箱内,高温固化2小时,降温脱模得到密度为94±2kg/m3的一步法聚酰亚胺泡沫。Weigh 17.3 grams of N,N-dimethylformamide solution and 11.76 grams of 3,3',4,4'-benzophenone tetraacid dianhydride into the reaction device connected to the reflux condenser, stir and raise the temperature of the system After reaching 50°C, stop heating, then add 2.44 grams of methanol and 3,3',4,4'-benzophenonetetraacid dianhydride for esterification reaction, and obtain a transparent carboxylate solution after the reaction, wait for the above solution to cool After reaching room temperature, add 3.75 grams of polyethylene glycol 600, 3.75 grams of AK8805 surfactant, 2.4 grams of catalyst, 3.6 grams of deionized water, and stir evenly to obtain a foaming base material, which is poured into the foaming base material from the reaction device. After foaming slurry mixing container, add 45 grams of NCO weight fractions to be the polymethylene polyphenyl polyisocyanate of 31.5% at once in foaming base material, high-speed mechanical stirring obtains foaming slurry, foaming material The slurry is quickly and evenly poured into the bottom of the steel mold with a cavity size of 10cm*10cm*5cm on the upper opening and coated with a release agent. With a rectangular steel plate coated with a release agent as the upper cover, quickly tighten the screws to close the upper part of the experimental mold. mouth, closed the experimental mold, put it into an oven at 180°C after standing for 12 minutes, cured it at high temperature for 2 hours, cooled and demolded to obtain a one-step polyimide foam with a density of 94±2kg/ m3 .
所制备的一步法聚酰亚胺泡沫极限氧指数值为22.5%;压缩强度为364kPa;导热系数为0.051W/(m·K);燃烧热量释放峰值183kW/m2;燃烧烟气释放总量6.79m2/m2。The limiting oxygen index of the prepared one-step polyimide foam is 22.5%; the compressive strength is 364kPa; the thermal conductivity is 0.051W/(m·K); the peak value of combustion heat release is 183kW/m 2 ; the total amount of combustion smoke is released 6.79m 2 /m 2 .
对比例2Comparative example 2
本对比例与对比例1不同的是所有试剂或药品用量为对比例中相应试剂或药品用量重量的20%,其余操作与实施例1相同,得到密度为75±2kg/m3的一步法聚酰亚胺泡沫。The difference between this comparative example and comparative example 1 is that the amount of all reagents or medicines is 20% of the weight of the corresponding reagents or medicines in the comparative example. imide foam.
所制备的一步法聚酰亚胺泡沫极限氧指数值为24.9%;压缩强度为290kPa;导热系数为0.053W/(m·K);燃烧热量释放峰值214kW/m2;燃烧烟气释放总量7.17m2/m2。The limiting oxygen index of the prepared one-step polyimide foam is 24.9%; the compressive strength is 290kPa; the thermal conductivity is 0.053W/(m·K); the peak value of combustion heat release is 214kW/m 2 ; the total amount of combustion smoke is released 7.17m 2 /m 2 .
对比例3Comparative example 3
本对比例与对比例1不同的是“3,3',4,4'-二苯酮四酸二酐的用量为34.27克,甲醇的加入量为7.11克,反应结束后得到的是半透明的粘稠状羧酸酯溶液”,其余操作与实施例1相同,得到密度为125±2kg/m3的一步法聚酰亚胺泡沫。The difference between this comparative example and comparative example 1 is that the amount of 3,3',4,4'-benzophenonetetraacid dianhydride is 34.27 grams, and the amount of methanol added is 7.11 grams. After the reaction, the result is translucent Viscous carboxylate solution", all the other operations are the same as in Example 1 to obtain a density of 125 ± 2kg/m The one -step polyimide foam.
所制备的一步法聚酰亚胺泡沫极限氧指数值为22.2%;压缩强度为372kPa;导热系数为0.049W/(m·K);燃烧热量释放峰值159kW/m2;燃烧烟气释放总量5.41m2/m2。The limiting oxygen index of the prepared one-step polyimide foam is 22.2%; the compressive strength is 372kPa; the thermal conductivity is 0.049W/(m·K); the peak value of combustion heat release is 159kW/m 2 ; the total amount of combustion smoke is released 5.41m 2 /m 2 .
对比例4Comparative example 4
本对比例与对比例1不同的是“3,3',4,4'-二苯酮四酸二酐的用量为56.78克,甲醇的加入量为11.38克,反应结束后得到的是近乎白色的膏状羧酸酯溶液”,其余操作与实施例1相同,得到密度约为147±2kg/m3的一步法聚酰亚胺泡沫。The difference between this comparative example and comparative example 1 is that the amount of 3,3',4,4'-benzophenone tetraacid dianhydride is 56.78 grams, and the amount of methanol added is 11.38 grams. After the reaction, the obtained product is almost white The pasty carboxylate solution of ", all the other operations are identical with embodiment 1, obtain density about 147 ± 2kg/m The one-step polyimide foam of density.
所制备的一步法聚酰亚胺泡沫极限氧指数值为30.7%;压缩强度为387kPa;导热系数为0.047W/(m·K);燃烧热量释放峰值143kW/m2;燃烧烟气释放总量4.08m2/m2。The prepared one-step polyimide foam has a limiting oxygen index value of 30.7%; a compressive strength of 387kPa; a thermal conductivity of 0.047W/(m·K); a peak value of combustion heat release of 143kW/m 2 ; a total combustion smoke emission 4.08m 2 /m 2 .
实施例1Example 1
参照图1中所示的示意图,制作高密度聚酰亚胺泡沫蜂窝芯格用带有环形分布六棱柱的模具钢质上盖,模具内腔尺寸为20cm*20cm*5cm。模具钢质上盖所镶嵌六棱柱长度同样为5cm、边长为9.6mm(即外接圆直径为19.2mm)。按照设计图纸,先在钢板正中心镶嵌第一个六棱柱,然后再按照图纸均匀环形镶嵌其他六棱柱,两相邻六棱柱之间间隔(缝隙)为2mm,即保证最终所制备出的蜂窝芯格壁厚为2mm。按照图纸,待镶嵌完毕所有完整的六棱柱后,最后按照图纸及边界实际情况,镶嵌非完整的六棱柱。Referring to the schematic diagram shown in Figure 1, the steel upper cover of the mold with annular distribution of hexagonal prisms is used to make the high-density polyimide foam honeycomb cell. The cavity size of the mold is 20cm*20cm*5cm. The length of the hexagonal prism inlaid on the steel upper cover of the mold is also 5cm, and the side length is 9.6mm (that is, the diameter of the circumscribed circle is 19.2mm). According to the design drawings, first inlay the first hexagonal prism in the center of the steel plate, and then inlay other hexagonal prisms in a uniform ring according to the drawing. The interval (gap) between two adjacent hexagonal prisms is 2mm, which is to ensure the final prepared honeycomb core. The grid wall thickness is 2mm. According to the drawings, after all the complete hexagonal prisms are inlaid, finally inlay the incomplete hexagonal prisms according to the drawings and the actual situation of the boundary.
本实施例中该带六棱柱的上盖放入模具后,六棱柱体积与模具中剩余空间体积比39.9:10.2,即最终所制备的复合泡沫中芯格中填充的低密度泡沫体积与蜂窝芯格高密度泡沫体积之比。In this embodiment, after the upper cover with the hexagonal prism is put into the mold, the ratio of the volume of the hexagonal prism to the remaining space in the mold is 39.9:10.2, that is, the volume of the low-density foam filled in the core lattice of the final composite foam and the honeycomb core Ratio of high-density foam volume.
本实施例制备与对比例1密度相同的含蜂窝芯格结构的复合泡沫,即复合泡沫整体表观密度为94±2kg/m3。鉴于本实施例所用模具内腔体积即复合泡沫整体表观体积为对比例1的4倍,因此配置分别制备蜂窝芯格及填充芯格的泡沫发泡料浆的各试剂及化学药品总用量为对比例1中相对应试剂及化学药品的4倍。本实施例设定制备泡沫密度为280kg/m3的高密度聚酰亚胺泡沫蜂窝芯格,则填充蜂窝芯格芯格的低密度聚酰亚胺泡沫密度为46.4kg/m3。依据上述数据,进一步地计算出用于制备高密度聚酰亚胺泡沫蜂窝芯格的发泡料浆质量应该是对比例1中发泡料浆质量的2.43倍,用于填充蜂窝芯格的发泡料浆质量应该是对比例1中发泡料浆质量的1.57倍。In this example, a composite foam containing a honeycomb cell structure with the same density as Comparative Example 1 was prepared, that is, the overall apparent density of the composite foam was 94±2kg/m 3 . In view of the cavity volume of the mold used in this embodiment, that is, the overall apparent volume of the composite foam is 4 times that of Comparative Example 1, the total amount of reagents and chemicals used to prepare the foam foaming slurry of the honeycomb core grid and the core grid respectively is 4 times that of the corresponding reagents and chemicals in Comparative Example 1. In this embodiment, a high-density polyimide foam honeycomb cell with a foam density of 280 kg/m 3 is prepared, and the density of the low-density polyimide foam filled with the honeycomb cell is 46.4 kg/m 3 . According to above-mentioned data, further calculate the foaming slurry quality that is used to prepare high-density polyimide foam honeycomb lattice should be 2.43 times of the foaming slurry quality in comparative example 1, be used for filling the foaming slurry quality of honeycomb lattice The foam slurry quality should be 1.57 times of the foam slurry quality in Comparative Example 1.
按照对比例1中的料浆制备过程,及上述所计算出的各种物料用量,配制用于制备高密度聚酰亚胺泡沫蜂窝芯格的发泡料浆,将发泡料浆迅速均匀倒入上开口并涂有脱模剂的内腔尺寸为20cm*20cm*5cm的钢质模具底部,然后迅速将本实施例设计及制作的带有环形均匀分布钢质六棱柱结构并涂有脱模剂的上盖盖上进行快速闭模、拧紧螺丝,静置15分钟,随后将模具放入180℃温度的烘箱内,高温固化2小时,降温脱模后得到实际泡沫密度为277kg/m3的聚酰亚胺泡沫蜂窝芯格,室温下放置1-2天备用。待蜂窝芯格可用后,按照对比例1中的料浆制备过程,及上述所计算出的各种物料用量,配制用于填充蜂窝芯格的发泡料浆,迅速均匀倒入内腔尺寸为20cm*20cm*5cm的钢质模具底部,随后快速将上述制备聚酰亚胺泡沫蜂窝芯格插入模具中,以涂有脱模剂的平板型钢板为上盖,快速闭模、拧紧螺丝,静置15分钟,随后将模具放入180℃温度的烘箱内,高温固化2小时,降温脱模后得到实际整体表观密度为92.5kg/m3的含蜂窝芯格结构的聚酰亚胺复合泡沫。According to the slurry preparation process in Comparative Example 1, and the above-mentioned calculated various material consumptions, the preparation is used to prepare the foaming slurry of high-density polyimide foam honeycomb core grid, and the foaming slurry is quickly and evenly poured Insert the bottom of the steel mold with an inner cavity size of 20cm*20cm*5cm with the upper opening and coated with a release agent, and then quickly apply the circular uniformly distributed steel hexagonal prism structure designed and manufactured in this embodiment and coated with a release agent. Quickly close the mold on the upper cover of the agent, tighten the screws, and let it stand for 15 minutes, then put the mold in an oven at a temperature of 180°C, and cure it at a high temperature for 2 hours. After cooling down and demoulding, the actual foam density is 277kg/ m3 Polyimide foam honeycomb grid, placed at room temperature for 1-2 days for later use. After the honeycomb cell is available, according to the slurry preparation process in Comparative Example 1, and the amount of various materials calculated above, the foaming slurry used to fill the honeycomb cell is prepared, and quickly and evenly poured into the inner cavity with a size of The bottom of the 20cm*20cm*5cm steel mold, and then quickly insert the polyimide foam honeycomb core prepared above into the mold, use the flat steel plate coated with the release agent as the upper cover, quickly close the mold, tighten the screws, and statically Set it aside for 15 minutes, then put the mold into an oven at 180°C, and cure it at high temperature for 2 hours. After cooling down and demoulding, a polyimide composite foam with a honeycomb core structure with an actual overall apparent density of 92.5kg/ m3 was obtained. .
所制备的含蜂窝芯格结构的聚酰亚胺复合泡沫的极限氧指数值为28.4%;压缩强度为421kPa;导热系数为0.040W/(m·K);燃烧热量释放峰值67kW/m2;燃烧烟气释放总量1.02m2/m2。The limiting oxygen index value of the prepared polyimide composite foam containing the honeycomb core structure is 28.4%; the compressive strength is 421kPa; the thermal conductivity is 0.040W/(m·K); the combustion heat release peak value is 67kW/m 2 ; The total amount of combustion smoke released is 1.02m 2 /m 2 .
实施例2Example 2
本实施例采用实施例1中所设计及制作的模具,该带六棱柱的上盖放入模具后,六棱柱体积与模具中剩余空间体积比仍为39.9:10.2,即最终所制备的复合泡沫中芯格中填充的低密度泡沫体积与蜂窝芯格高密度泡沫体积之比。This embodiment adopts the mold designed and made in Example 1. After the upper cover with hexagonal prism is put into the mold, the ratio of the volume of the hexagonal prism to the remaining space in the mold is still 39.9:10.2, that is, the final prepared composite foam The ratio of the volume of low density foam filled in the center cell to the volume of high density foam in the honeycomb cell.
本实施例制备与对比例3密度相同的含蜂窝芯格结构的复合泡沫,即复合泡沫整体表观密度为125±1kg/m3。鉴于本实施例所用模具内腔体积即复合泡沫整体表观体积为对比例3的4倍,因此配置分别制备蜂窝芯格及填充芯格的泡沫发泡料浆的各试剂及化学药品总用量为对比例3中相对应试剂及化学药品的4倍。本实施例设定制备泡沫密度为400kg/m3的高密度聚酰亚胺泡沫蜂窝芯格,则填充蜂窝芯格芯格的低密度聚酰亚胺泡沫密度为54.7kg/m3。依据上述数据,进一步地计算出用于制备高密度聚酰亚胺泡沫蜂窝芯格的发泡料浆质量应该是对比例3中发泡料浆质量的2.61倍,用于填充蜂窝芯格的发泡料浆质量应该是对比例3中发泡料浆质量的1.39倍。In this example, a composite foam containing a honeycomb cell structure with the same density as Comparative Example 3 was prepared, that is, the overall apparent density of the composite foam was 125±1 kg/m 3 . In view of the cavity volume of the mold used in this embodiment, that is, the overall apparent volume of the composite foam is 4 times that of Comparative Example 3, the total amount of each reagent and chemicals used for preparing the foam foam slurry of the honeycomb core grid and the filled core grid respectively is 4 times that of the corresponding reagents and chemicals in Comparative Example 3. In this embodiment, a high-density polyimide foam honeycomb cell with a foam density of 400 kg/m 3 is prepared, and the density of the low-density polyimide foam filled with the honeycomb cell is 54.7 kg/m 3 . According to above-mentioned data, further calculate the foaming slurry quality that is used to prepare high-density polyimide foam honeycomb lattice should be 2.61 times of the foaming slurry quality in comparative example 3, be used for filling the foaming slurry quality of honeycomb lattice The foam slurry quality should be 1.39 times of the foam slurry quality in Comparative Example 3.
按照对比例3中的料浆制备过程,及上述所计算出的各种物料用量,配制用于制备高密度聚酰亚胺泡沫蜂窝芯格的发泡料浆,将发泡料浆迅速均匀倒入上开口并涂有脱模剂的内腔尺寸为20cm*20cm*5cm的钢质模具底部,然后迅速将本实施例设计及制作的带有环形均匀分布钢质六棱柱结构并涂有脱模剂的上盖盖上进行快速闭模、拧紧螺丝,静置15分钟,随后将模具放入180℃温度的烘箱内,高温固化2小时,降温脱模后得到实际泡沫密度为394kg/m3的聚酰亚胺泡沫蜂窝芯格,室温下放置1-2天备用。待蜂窝芯格可用后,按照对比例3中的料浆制备过程,及上述所计算出的各种物料用量,配制用于填充蜂窝芯格的发泡料浆,迅速均匀倒入内腔尺寸为20cm*20cm*5cm的钢质模具底部,随后快速将上述制备聚酰亚胺泡沫蜂窝芯格插入模具中,以涂有脱模剂的平板型钢板为上盖,快速闭模、拧紧螺丝,静置15分钟,随后将模具放入180℃温度的烘箱内,高温固化2小时,降温脱模后得到实际整体表观密度为123.8kg/m3的含蜂窝芯格结构的聚酰亚胺复合泡沫。According to the slurry preparation process in Comparative Example 3, and the above-mentioned calculated various material consumptions, the preparation is used to prepare the foaming slurry of high-density polyimide foam honeycomb core lattice, pour the foaming slurry rapidly and evenly Insert the bottom of the steel mold with an inner cavity size of 20cm*20cm*5cm with the upper opening and coated with a release agent, and then quickly apply the circular uniformly distributed steel hexagonal prism structure designed and manufactured in this embodiment and coated with a release agent. Quickly close the mold on the upper cover of the agent, tighten the screws, and let it stand for 15 minutes, then put the mold in an oven at a temperature of 180°C, and cure it at a high temperature for 2 hours. After cooling down and demolding, the actual foam density is 394kg/ m3 Polyimide foam honeycomb grid, placed at room temperature for 1-2 days for later use. After the honeycomb cell is available, according to the slurry preparation process in Comparative Example 3, and the amount of various materials calculated above, the foaming slurry for filling the honeycomb cell is prepared, and poured quickly and evenly into the inner cavity with a size of The bottom of the 20cm*20cm*5cm steel mold, and then quickly insert the polyimide foam honeycomb core prepared above into the mold, use the flat steel plate coated with the release agent as the upper cover, quickly close the mold, tighten the screws, and statically Set it aside for 15 minutes, then put the mold into an oven at 180°C, and cure it at high temperature for 2 hours. After cooling down and demoulding, a polyimide composite foam with a honeycomb core structure with an actual overall apparent density of 123.8kg/ m3 was obtained. .
所制备的含蜂窝芯格结构的聚酰亚胺复合泡沫的极限氧指数值为29.1%;压缩强度为464kPa;导热系数为0.042W/(m·K);燃烧热量释放峰值55kW/m2;燃烧烟气释放总量0.93m2/m2。The limiting oxygen index value of the prepared polyimide composite foam containing the honeycomb core structure is 29.1%; the compressive strength is 464kPa; the thermal conductivity is 0.042W/(m·K); the combustion heat release peak value is 55kW/m 2 ; The total combustion smoke emission is 0.93m 2 /m 2 .
实施例3Example 3
本实施例采用实施例1中所设计及制作的模具,该带六棱柱的上盖放入模具后,六棱柱体积与模具中剩余空间体积比仍为39.9:10.2,即最终所制备的复合泡沫中芯格中填充的低密度泡沫体积与蜂窝芯格高密度泡沫体积之比。This embodiment adopts the mold designed and made in Example 1. After the upper cover with hexagonal prism is put into the mold, the ratio of the volume of the hexagonal prism to the remaining space in the mold is still 39.9:10.2, that is, the final prepared composite foam The ratio of the volume of low density foam filled in the center cell to the volume of high density foam in the honeycomb cell.
本实施例制备与对比例4密度相同的含蜂窝芯格结构的复合泡沫,即复合泡沫整体表观密度为157±3kg/m3。鉴于本实施例所用模具内腔体积即复合泡沫整体表观体积为对比例4的4倍,因此配置分别制备蜂窝芯格及填充芯格的泡沫发泡料浆的各试剂及化学药品总用量为对比例4中相对应试剂及化学药品的4倍。本实施例设定制备泡沫密度为450kg/m3的高密度聚酰亚胺泡沫蜂窝芯格,则填充蜂窝芯格芯格的低密度聚酰亚胺泡沫密度为82.1kg/m3。依据上述数据,进一步地计算出用于制备高密度聚酰亚胺泡沫蜂窝芯格的发泡料浆质量应该是对比例4中发泡料浆质量的2.34倍,用于填充蜂窝芯格的发泡料浆质量应该是对比例4中发泡料浆质量的1.66倍。In this example, a composite foam with a honeycomb core structure having the same density as Comparative Example 4 was prepared, that is, the overall apparent density of the composite foam was 157±3kg/m 3 . In view of the cavity volume of the mold used in this embodiment, that is, the overall apparent volume of the composite foam is 4 times that of Comparative Example 4, the total amount of each reagent and chemicals used for preparing the foam foam slurry of the honeycomb core grid and the filled core grid respectively is 4 times of corresponding reagents and chemicals in comparative example 4. In this embodiment, a high-density polyimide foam honeycomb cell with a foam density of 450 kg/m 3 is prepared, and the density of the low-density polyimide foam filled with the honeycomb cell is 82.1 kg/m 3 . According to above-mentioned data, further calculate the foaming slurry quality that is used to prepare high-density polyimide foam honeycomb lattice should be 2.34 times of the foaming slurry quality in comparative example 4, be used for filling the foaming slurry quality of honeycomb lattice The foam slurry quality should be 1.66 times of the foam slurry quality in Comparative Example 4.
按照对比例4中的料浆制备过程,及上述所计算出的各种物料用量,配制用于制备高密度聚酰亚胺泡沫蜂窝芯格的发泡料浆,将发泡料浆迅速均匀倒入上开口并涂有脱模剂的内腔尺寸为20cm*20cm*5cm的钢质模具底部,然后迅速将本实施例设计及制作的带有环形均匀分布钢质六棱柱结构并涂有脱模剂的上盖盖上进行快速闭模、拧紧螺丝,静置15分钟,随后将模具放入180℃温度的烘箱内,高温固化2小时,降温脱模后得到实际泡沫密度为441kg/m3的聚酰亚胺泡沫蜂窝芯格,室温下放置1-2天备用。待蜂窝芯格可用后,按照对比例4中的料浆制备过程,及上述所计算出的各种物料用量,配制用于填充蜂窝芯格的发泡料浆,迅速均匀倒入内腔尺寸为20cm*20cm*5cm的钢质模具底部,随后快速将上述制备聚酰亚胺泡沫蜂窝芯格插入模具中,以涂有脱模剂的平板型钢板为上盖,快速闭模、拧紧螺丝,静置15分钟,随后将模具放入180℃温度的烘箱内,高温固化2小时,降温脱模后得到实际整体表观密度为153.6kg/m3的含蜂窝芯格结构的聚酰亚胺复合泡沫。According to the slurry preparation process in Comparative Example 4, and the above-mentioned calculated various material consumptions, the preparation is used to prepare the foaming slurry of high-density polyimide foam honeycomb core lattice, pour the foaming slurry rapidly and evenly Insert the bottom of the steel mold with an inner cavity size of 20cm*20cm*5cm with the upper opening and coated with a release agent, and then quickly apply the circular uniformly distributed steel hexagonal prism structure designed and manufactured in this embodiment and coated with a release agent. Quickly close the mold on the upper cover of the agent, tighten the screws, and let it stand for 15 minutes, then put the mold in an oven at a temperature of 180°C, and cure it at a high temperature for 2 hours. After cooling down and demolding, the actual foam density is 441kg/ m3 Polyimide foam honeycomb grid, placed at room temperature for 1-2 days for later use. After the honeycomb cell is available, according to the preparation process of the slurry in Comparative Example 4 and the amount of various materials calculated above, the foaming slurry for filling the honeycomb cell is prepared, and quickly and evenly poured into the inner cavity with a size of The bottom of the 20cm*20cm*5cm steel mold, and then quickly insert the polyimide foam honeycomb core prepared above into the mold, use the flat steel plate coated with the release agent as the upper cover, quickly close the mold, tighten the screws, and statically Set it aside for 15 minutes, then put the mold into an oven at 180°C, and cure it at high temperature for 2 hours. After cooling down and demolding, a polyimide composite foam with a honeycomb core structure with an actual overall apparent density of 153.6kg/ m3 was obtained. .
所制备的含蜂窝芯格结构的聚酰亚胺复合泡沫的极限氧指数值为31.1%;压缩强度为452kPa;导热系数为0.039W/(m·K);燃烧热量释放峰值51kW/m2;燃烧烟气释放总量0.81m2/m2。The limiting oxygen index value of the prepared polyimide composite foam containing the honeycomb core structure is 31.1%; the compressive strength is 452kPa; the thermal conductivity is 0.039W/(m·K); the combustion heat release peak value is 51kW/m 2 ; The total amount of combustion smoke released is 0.81m 2 /m 2 .
实施例4Example 4
本实施例与实施例1-3所用模具外观尺寸及内腔尺寸一致,即模具内腔尺寸为20cm*20cm*5cm,制备高密度聚酰亚胺泡沫蜂窝芯格用带有环形分布六棱柱的模具钢质上盖所镶嵌六棱柱长度同样为5cm,但是不同之处在于六棱柱边长变为4.8mm(即外接圆直径为9.6mm)。两相邻六棱柱之间间隔(缝隙)为2mm,即保证最终所制备出的蜂窝芯格壁厚为2mm。模具其他制作过程及所参照图纸与实施例1-3所用模具一致。This embodiment is consistent with the mold appearance size and inner cavity size used in Examples 1-3, that is, the mold inner cavity size is 20cm*20cm*5cm, which is used to prepare high-density polyimide foam honeycomb cells with annular distribution of hexagonal prisms. The length of the hexagonal prism inlaid on the mold steel upper cover is also 5cm, but the difference is that the side length of the hexagonal prism becomes 4.8mm (that is, the diameter of the circumscribed circle is 9.6mm). The interval (gap) between two adjacent hexagonal prisms is 2 mm, which means that the final prepared honeycomb cell has a wall thickness of 2 mm. Other manufacturing processes of the mold and the drawings referred to are consistent with the molds used in Examples 1-3.
本实施例中该带六棱柱的上盖放入模具后,六棱柱体积与模具中剩余空间体积比10.0:5.4,即最终所制备的复合泡沫中芯格中填充的低密度泡沫体积与蜂窝芯格高密度泡沫体积之比。In this embodiment, after the upper cover with the hexagonal prism is put into the mold, the ratio of the volume of the hexagonal prism to the remaining space in the mold is 10.0:5.4, that is, the volume of the low-density foam filled in the core cell of the final composite foam and the honeycomb core Ratio of high-density foam volume.
本实施例用于制备泡沫材料的发泡料浆配制过程及配方与实施例3相同。The preparation process and formula of the foam slurry used to prepare the foam material in this embodiment are the same as those in Embodiment 3.
本实施例制备与对比例4密度相同的含蜂窝芯格结构的复合泡沫,即复合泡沫整体表观密度为157±3kg/m3。鉴于本实施例所用模具内腔体积即复合泡沫整体表观体积为对比例4的4倍,因此配置分别制备蜂窝芯格及填充芯格的泡沫发泡料浆的各试剂及化学药品总用量为对比例4中相对应试剂及化学药品的4倍。本实施例设定制备泡沫密度为400kg/m3的高密度聚酰亚胺泡沫蜂窝芯格,则填充蜂窝芯格芯格的低密度聚酰亚胺泡沫密度为25.8kg/m3。依据上述数据,进一步地计算出用于制备高密度聚酰亚胺泡沫蜂窝芯格的发泡料浆质量应该是对比例4中发泡料浆质量的3.57倍,用于填充蜂窝芯格的发泡料浆质量应该是对比例4中发泡料浆质量的0.43倍。In this example, a composite foam with a honeycomb core structure having the same density as Comparative Example 4 was prepared, that is, the overall apparent density of the composite foam was 157±3kg/m 3 . In view of the cavity volume of the mold used in this embodiment, that is, the overall apparent volume of the composite foam is 4 times that of Comparative Example 4, the total amount of each reagent and chemicals used for preparing the foam foam slurry of the honeycomb core grid and the filled core grid respectively is 4 times of corresponding reagents and chemicals in comparative example 4. In this embodiment, a high-density polyimide foam honeycomb cell with a foam density of 400 kg/m 3 is prepared, and the density of the low-density polyimide foam filled with the honeycomb cell is 25.8 kg/m 3 . According to above-mentioned data, further calculate the foaming slurry quality that is used to prepare high-density polyimide foam honeycomb lattice should be 3.57 times of the foaming slurry quality in comparative example 4, be used for filling the foaming slurry quality of honeycomb lattice The foam slurry quality should be 0.43 times of the foam slurry quality in Comparative Example 4.
按照实施例3所示过程制备高密度聚酰亚胺泡沫蜂窝芯格,降温脱模后得到实际泡沫密度为395kg/m3的聚酰亚胺泡沫蜂窝芯格,室温下放置1-2天备用。待蜂窝芯格可用后,按照实施例3过程制备复合泡沫。最终得到实际整体表观密度为154.2kg/m3的含蜂窝芯格结构的聚酰亚胺复合泡沫。Prepare high-density polyimide foam honeycomb core grid according to the process shown in embodiment 3, obtain actual foam density after the demoulding that is 395kg/m The polyimide foam honeycomb core grid of 395kg/ m3 , place 1-2 days standby under room temperature . After the honeycomb cell is available, the composite foam is prepared according to the process of Example 3. Finally, the polyimide composite foam containing the honeycomb core structure with an actual overall apparent density of 154.2kg/ m3 was obtained.
所制备的含蜂窝芯格结构的聚酰亚胺复合泡沫的极限氧指数值为31.5%;压缩强度为437kPa;导热系数为0.038W/(m·K);燃烧热量释放峰值48kW/m2;燃烧烟气释放总量0.77m2/m2。The limiting oxygen index value of the prepared polyimide composite foam containing the honeycomb core structure is 31.5%; the compressive strength is 437kPa; the thermal conductivity is 0.038W/(m·K); the combustion heat release peak value is 48kW/m 2 ; The total combustion smoke emission is 0.77m 2 /m 2 .
上文所列出的一系列的详细说明仅仅是针对本发明的可行性实施例的具体说明,它们并非用以限制本发明的保护范围,凡未脱离本发明技艺精神所作的等效实施例或变更均应包含在本发明的保护范围之内。The series of detailed descriptions listed above are only specific descriptions for feasible embodiments of the present invention, and they are not intended to limit the protection scope of the present invention. Any equivalent embodiment or All changes should be included within the protection scope of the present invention.
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US5188879A (en) * | 1991-07-15 | 1993-02-23 | Sorrento Engineering Corporation | Polyimide foam filled structures |
CN104804190A (en) * | 2015-04-30 | 2015-07-29 | 哈尔滨工程大学 | Flame-retardant polyimide foam material comprising honeycomb core space structure, and preparation method |
CN104910380A (en) * | 2015-06-02 | 2015-09-16 | 哈尔滨工程大学 | Preparation method of honeycomb-reinforced polyimide foam composite material |
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US5188879A (en) * | 1991-07-15 | 1993-02-23 | Sorrento Engineering Corporation | Polyimide foam filled structures |
CN104804190A (en) * | 2015-04-30 | 2015-07-29 | 哈尔滨工程大学 | Flame-retardant polyimide foam material comprising honeycomb core space structure, and preparation method |
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