CN108570725A - A kind of melt spinning raw material of aluminium oxide continuous fiber, preparation method and aluminium oxide continuous fiber obtained - Google Patents
A kind of melt spinning raw material of aluminium oxide continuous fiber, preparation method and aluminium oxide continuous fiber obtained Download PDFInfo
- Publication number
- CN108570725A CN108570725A CN201710135875.6A CN201710135875A CN108570725A CN 108570725 A CN108570725 A CN 108570725A CN 201710135875 A CN201710135875 A CN 201710135875A CN 108570725 A CN108570725 A CN 108570725A
- Authority
- CN
- China
- Prior art keywords
- preparation
- melt spinning
- alumina
- fiber
- melt
- 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
- 239000000835 fiber Substances 0.000 title claims abstract description 165
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 title claims abstract description 121
- 238000002074 melt spinning Methods 0.000 title claims abstract description 88
- 238000002360 preparation method Methods 0.000 title claims abstract description 74
- 239000002994 raw material Substances 0.000 title claims abstract description 67
- 239000002243 precursor Substances 0.000 claims abstract description 79
- 239000000843 powder Substances 0.000 claims abstract description 47
- 238000000034 method Methods 0.000 claims abstract description 31
- 239000002270 dispersing agent Substances 0.000 claims abstract description 27
- 238000010438 heat treatment Methods 0.000 claims abstract description 25
- 239000002904 solvent Substances 0.000 claims abstract description 25
- 239000000203 mixture Substances 0.000 claims abstract description 21
- 238000006243 chemical reaction Methods 0.000 claims abstract description 13
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 8
- 239000007787 solid Substances 0.000 claims abstract description 8
- 238000000227 grinding Methods 0.000 claims abstract description 4
- 238000002156 mixing Methods 0.000 claims abstract description 4
- 238000009987 spinning Methods 0.000 claims description 57
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 50
- 238000002844 melting Methods 0.000 claims description 38
- 239000002202 Polyethylene glycol Substances 0.000 claims description 37
- 229920001223 polyethylene glycol Polymers 0.000 claims description 37
- 230000008018 melting Effects 0.000 claims description 36
- 229910052757 nitrogen Inorganic materials 0.000 claims description 26
- 238000005336 cracking Methods 0.000 claims description 25
- 238000010304 firing Methods 0.000 claims description 24
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 18
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical group CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 17
- 239000002245 particle Substances 0.000 claims description 11
- 238000003756 stirring Methods 0.000 claims description 11
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 9
- 239000004576 sand Substances 0.000 claims description 9
- XNWFRZJHXBZDAG-UHFFFAOYSA-N 2-METHOXYETHANOL Chemical compound COCCO XNWFRZJHXBZDAG-UHFFFAOYSA-N 0.000 claims description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 7
- ZNQVEEAIQZEUHB-UHFFFAOYSA-N 2-ethoxyethanol Chemical compound CCOCCO ZNQVEEAIQZEUHB-UHFFFAOYSA-N 0.000 claims description 4
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 229910052863 mullite Inorganic materials 0.000 claims description 3
- 230000006837 decompression Effects 0.000 claims description 2
- 238000005292 vacuum distillation Methods 0.000 claims description 2
- 239000004411 aluminium Substances 0.000 claims 3
- 238000010792 warming Methods 0.000 claims 3
- 229910052593 corundum Inorganic materials 0.000 claims 1
- 235000019441 ethanol Nutrition 0.000 claims 1
- 238000005070 sampling Methods 0.000 claims 1
- 229910052594 sapphire Inorganic materials 0.000 claims 1
- 229910001845 yogo sapphire Inorganic materials 0.000 claims 1
- 229910003158 γ-Al2O3 Inorganic materials 0.000 claims 1
- 239000002002 slurry Substances 0.000 abstract description 28
- 230000007547 defect Effects 0.000 abstract description 2
- 238000005245 sintering Methods 0.000 abstract description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 12
- 239000000919 ceramic Substances 0.000 description 12
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 11
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 9
- 239000000243 solution Substances 0.000 description 7
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 6
- 229910052786 argon Inorganic materials 0.000 description 6
- 230000009286 beneficial effect Effects 0.000 description 4
- 238000000197 pyrolysis Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 3
- 239000001307 helium Substances 0.000 description 3
- 229910052734 helium Inorganic materials 0.000 description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 3
- 238000009776 industrial production Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000001878 scanning electron micrograph Methods 0.000 description 3
- 238000003980 solgel method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000000578 dry spinning Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000003286 fusion draw glass process Methods 0.000 description 2
- 239000012784 inorganic fiber Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 2
- 229910001414 potassium ion Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910001415 sodium ion Inorganic materials 0.000 description 2
- 238000001308 synthesis method Methods 0.000 description 2
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- -1 ZrO 2 and SiO 2 Chemical class 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- SMZOGRDCAXLAAR-UHFFFAOYSA-N aluminium isopropoxide Chemical compound [Al+3].CC(C)[O-].CC(C)[O-].CC(C)[O-] SMZOGRDCAXLAAR-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000002468 ceramisation Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000000280 densification Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 229910052809 inorganic oxide Inorganic materials 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000003541 multi-stage reaction Methods 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000011224 oxide ceramic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000006254 rheological additive Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F9/00—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments
- D01F9/08—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments of inorganic material
- D01F9/10—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments of inorganic material by decomposition of organic substances
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
- C04B35/10—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on aluminium oxide
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/62227—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products obtaining fibres
- C04B35/62231—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products obtaining fibres based on oxide ceramics
- C04B35/62236—Fibres based on aluminium oxide
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Textile Engineering (AREA)
- Inorganic Chemistry (AREA)
- Inorganic Fibers (AREA)
Abstract
本发明涉及一种氧化铝连续纤维的熔融纺丝原料、其制备方法及制得的氧化铝连续纤维。包括:1)将聚铝氧烷置于反应釜中,加热至60~100℃,减压蒸馏,继续升温至110~140℃,保温,最后再升温至150~200℃,取样测软化点达到目标软化点时,停止加热,降至室温,得到固体氧化铝前驱体PAO‑P;2)将分散剂、含铝粉体和溶剂以质量比1:(1.5~4):(3~6)混合,研磨得到粉体浆料;3)将所得前驱体与所得粉体浆料混合,升温至150~200℃减压蒸馏得到熔融纺丝原料。本方法合成了可熔纺的氧化铝前驱体PAO‑P,并给出氧化铝纤维原丝熔融纺丝和烧结工艺,克服了氧化铝连续纤维无法通过熔融纺丝制备得到的缺陷。The invention relates to a raw material for melt spinning of alumina continuous fiber, its preparation method and the prepared alumina continuous fiber. Including: 1) Put the polyaluminoxane in the reaction kettle, heat to 60-100°C, distill under reduced pressure, continue to heat up to 110-140°C, keep warm, and finally heat up to 150-200°C, take samples to measure the softening point to reach When the target softening point is reached, stop heating and cool down to room temperature to obtain the solid alumina precursor PAO-P; 2) Mix the dispersant, aluminum-containing powder and solvent in a mass ratio of 1:(1.5~4):(3~6) Mixing and grinding to obtain a powder slurry; 3) mixing the obtained precursor with the obtained powder slurry, raising the temperature to 150-200° C. and distilling under reduced pressure to obtain a melt spinning raw material. The method synthesizes the melt-spinnable alumina precursor PAO-P, and provides the alumina fiber precursor melt spinning and sintering process, which overcomes the defect that the alumina continuous fiber cannot be prepared by melt spinning.
Description
技术领域technical field
本发明属于陶瓷纤维的制备领域,具体地说,涉及无机氧化物陶瓷纤维的制备,特别是涉及一种氧化铝连续纤维的熔融纺丝原料、其制备方法及制得的氧化铝连续纤维。The invention belongs to the field of preparation of ceramic fibers, in particular, relates to the preparation of inorganic oxide ceramic fibers, in particular to a melt spinning raw material of alumina continuous fibers, its preparation method and the prepared alumina continuous fibers.
背景技术Background technique
氧化铝纤维是一种高性能无机纤维。它以Al2O3为主要成分,有的还含有其它金属氧化物如ZrO2和SiO2等,具有长纤、短纤、晶须等多种形式。氧化铝纤维的突出优点是高强度、高模量,以及在1000~1200℃空气气氛下优异的力学性能,同时还具有热导率小,热膨胀系数低,抗热震性好等优点。此外,与其它高性能无机纤维如碳化硅纤维相比,氧化铝纤维原料成本低,且生产工艺简单,在航空航天和民用高端材料领域都有巨大的市场前景。Alumina fiber is a high-performance inorganic fiber. It is mainly composed of Al 2 O 3 , and some also contain other metal oxides such as ZrO 2 and SiO 2 , etc., and has various forms such as long fibers, short fibers, and whiskers. The outstanding advantages of alumina fiber are high strength, high modulus, and excellent mechanical properties in an air atmosphere of 1000-1200 ° C. At the same time, it also has the advantages of small thermal conductivity, low thermal expansion coefficient, and good thermal shock resistance. In addition, compared with other high-performance inorganic fibers such as silicon carbide fibers, the raw material cost of alumina fibers is low, and the production process is simple, so it has huge market prospects in the fields of aerospace and civil high-end materials.
氧化铝陶瓷熔点高且融化后粘度低,无法用传统的熔融拉丝工艺生产。为此各国研究者采用化学方法陆续开发出几条不同的生产路线,其中前驱体法是工业化制备氧化铝连续纤维的主要方法。根据前驱体原料种类差异,具体可分为有机纤维浸渍法、无机盐法、溶胶-凝胶法、有机聚合物前驱体法及泥浆溶液法等。3M公司采用溶胶-凝胶法,以结晶氯化铝、醋酸、铝粉、去离子水等为原料,经过多步反应形成主体为碱式氯化铝的粘性水溶胶。将制备的可拉丝胶体经连续干法纺丝干燥后形成前驱体原丝,通过连续热处理控制结晶方向和速度,转变成氧化物纤维(H.G.Sowman in'Sol-Gel Technology for Thin Films,Fibers,Preforms,Electronics,and Specialty Shapes'(edited by L.C.Klein),Noyes,Park Ridge,NJ,U.S.A,1988,p.140)。干法纺丝的缺点是溶液纺丝再烘干造成的溶剂挥发导致环境污染,以及溶剂挥发过程受环境温度、湿度影响大,原丝质量不易控制。而熔融纺丝工艺避免了溶剂的使用,根本解决了以上问题,因此成为化纤行业首选的纺丝工艺。Alumina ceramics have a high melting point and low viscosity after melting, so they cannot be produced by the traditional fusion drawing process. For this reason, researchers from various countries have successively developed several different production routes by using chemical methods, among which the precursor method is the main method for the industrial production of continuous alumina fibers. According to the different types of precursor raw materials, it can be divided into organic fiber impregnation method, inorganic salt method, sol-gel method, organic polymer precursor method and mud solution method. 3M Company adopts the sol-gel method, using crystalline aluminum chloride, acetic acid, aluminum powder, deionized water, etc. as raw materials, and undergoes multi-step reactions to form a viscous hydrosol whose main body is basic aluminum chloride. The prepared spinnable colloid is dried by continuous dry spinning to form a precursor precursor, and the crystallization direction and speed are controlled by continuous heat treatment, and converted into oxide fibers (H.G.Sowman in'Sol-Gel Technology for Thin Films, Fibers, Preforms , Electronics, and Specialty Shapes' (edited by L.C. Klein), Noyes, Park Ridge, NJ, U.S.A, 1988, p.140). The disadvantage of dry spinning is that the solvent volatilization caused by solution spinning and then drying leads to environmental pollution, and the solvent volatilization process is greatly affected by ambient temperature and humidity, and the quality of the raw silk is not easy to control. The melt spinning process avoids the use of solvents and fundamentally solves the above problems, so it has become the preferred spinning process in the chemical fiber industry.
E.I.Du Pont公司采用泥浆溶液法,以粒径<500nm的α-Al2O3粉体主原料,Al2(OH)5Cl·2H2O水溶液为流变助剂,经熔纺、老化、裂解、陶瓷化得到直径为20um,牌号为FP的氧化铝连续纤维,由于纤维较粗,力学性能不及3M公司水平(ALUMINA FIBER~US 3,808,015)。EIDu Pont Company adopts the slurry solution method, using α-Al 2 O 3 powder with a particle size of <500nm as the main raw material, and the Al 2 (OH) 5 Cl 2H 2 O aqueous solution as the rheological additive. After melt-spinning, aging, and cracking 1. The alumina continuous fiber with a diameter of 20um and a grade of FP is obtained through ceramicization. Because the fiber is relatively thick, the mechanical properties are not as good as the level of 3M Company (ALUMINA FIBER~US 3,808,015).
目前国内仅能实现氧化铝纤维棉的工业化生产,产品耐温等级仅有800℃,连续纤维研制仍处于实验室研究阶段,山东大学以氯化铝、硝酸铝及异丙醇铝为原料,采用溶胶-凝胶法制备了氧化铝连续纤维(CN2012140454976.7),产品性能接近国外中端产品水平,受合成方法局限,纤维中残存的钠钾离子,影响纤维的高温力学性能。At present, only the industrial production of alumina fiber cotton can be realized in China. The temperature resistance of the product is only 800°C. The development of continuous fiber is still in the laboratory research stage. Shandong University uses aluminum chloride, aluminum nitrate and aluminum isopropoxide as raw materials. Alumina continuous fiber (CN2012140454976.7) was prepared by sol-gel method. The performance of the product is close to the level of foreign mid-end products. Due to the limitation of the synthesis method, the residual sodium and potassium ions in the fiber affect the high temperature mechanical properties of the fiber.
熔融纺丝是将原料加热熔融,通过喷丝孔挤出,在空气中冷却固化形成纤维的纺丝方法。该方法的优点是对设备要求简单,无需溶剂,污染小,工作环境好。但是由于Al原子具有较强的金属性,难以制备出可以熔融的氧化铝前驱体,因此目前尚无采用前驱体熔融纺丝制备氧化铝纤维的报道,而氧化铝陶瓷熔点高且熔体的粘度低,因此无法像石英纤维那样采用传统的熔融拉丝法生产。Melt spinning is a spinning method in which raw materials are heated and melted, extruded through spinneret holes, cooled and solidified in air to form fibers. The method has the advantages of simple equipment requirements, no solvent, little pollution and good working environment. However, due to the strong metallicity of Al atoms, it is difficult to prepare alumina precursors that can be melted. Therefore, there is no report on the preparation of alumina fibers by melt spinning of precursors. However, alumina ceramics have a high melting point and a high melt viscosity. Low, so it cannot be produced by traditional fusion drawing method like quartz fiber.
鉴于以上原因,特提出本发明。In view of the above reasons, the present invention is proposed.
发明内容Contents of the invention
本发明要解决的技术问题在于克服现有技术的不足,提供一种氧化铝连续纤维的纺丝原料、其制备方法及制得的氧化铝连续纤维。The technical problem to be solved by the present invention is to overcome the deficiencies of the prior art, and provide a spinning raw material of alumina continuous fiber, its preparation method and the prepared alumina continuous fiber.
为实现本发明的目的,本发明采用如下技术方案:For realizing the purpose of the present invention, the present invention adopts following technical scheme:
一种氧化铝连续纤维的熔融纺丝原料的制备方法,其中,所述的制备方法包括如下步骤:A preparation method of melt spinning raw materials for alumina continuous fibers, wherein the preparation method comprises the steps of:
1)熔融纺丝型氧化铝前驱体的制备:将聚铝氧烷置于反应釜中,搅拌下加热至60~100℃,减压蒸馏30min~3h,继续升温至110~140℃,保温30min~3h,最后再升温至150~200℃,每10min取样测软化点,当达到目标软化点时,停止加热,氮气保护下降至室温,得到可熔纺的固体氧化铝前驱体PAO-P;1) Preparation of melt-spinning alumina precursor: put polyaluminoxane in a reaction kettle, heat to 60-100°C under stirring, distill under reduced pressure for 30min-3h, continue to heat up to 110-140°C, and keep warm for 30min ~3h, and finally increase the temperature to 150~200℃, take a sample every 10min to measure the softening point, when the target softening point is reached, stop heating, lower to room temperature under the protection of nitrogen, and obtain the melt-spinnable solid alumina precursor PAO-P;
2)粉体浆料的制备:将分散剂、含铝粉体和溶剂以质量比1:(1.5~4):(3~6)进行混合,研磨得到粉体浆料;2) Preparation of powder slurry: mixing dispersant, aluminum-containing powder and solvent at a mass ratio of 1:(1.5-4):(3-6), and grinding to obtain powder slurry;
3)熔融纺丝原料的制备:将步骤1)所得的前驱体与步骤2)所得的粉体浆料按质量比100:0~15:85均匀混合,优选80:20~30:70,然后升温至150~200℃减压蒸馏20min~2h得到熔融纺丝原料。3) Preparation of melt spinning raw materials: uniformly mix the precursor obtained in step 1) with the powder slurry obtained in step 2) at a mass ratio of 100:0 to 15:85, preferably 80:20 to 30:70, and then Raise the temperature to 150-200° C. and distill under reduced pressure for 20 minutes to 2 hours to obtain the raw material for melt spinning.
本发明所用的聚铝氧烷(PAO)购自苏州图纳材料有限公司,具体合成方式参见专利CN201610066594.5,通过减压蒸馏、高分子化等工艺进一步聚合聚铝氧烷分子链中的活性官能团,以提高其分子量和软化点,获得具有良好纺丝性能的固体氧化铝前驱体。The polyaluminoxane (PAO) used in the present invention is purchased from Suzhou Tuna Materials Co., Ltd., and the specific synthesis method can be found in patent CN201610066594.5. The activity in the molecular chain of polyaluminoxane is further polymerized by vacuum distillation, polymerization and other processes. functional groups to increase its molecular weight and softening point to obtain a solid alumina precursor with good spinning properties.
熔融纺丝是将原料加热熔融,通过喷丝孔挤出,在空气中冷却固化形成纤维的纺丝方法,具有对设备要求简单、无需溶剂、污染小和工作环境好的优点。而氧化铝陶瓷熔点高且熔体的粘度低,因此无法像石英纤维那样采用传统的熔融拉丝法生产。并且由于Al原子具有较强的金属性,使得难以制备出可以熔融的氧化铝前驱体,因此目前尚无采用前驱体熔融纺丝制备氧化铝纤维的报道。本发明获得了具有良好纺丝性能的固体氧化铝前驱体,克服了现有技术中氧化铝连续纤维难以通过熔融纺丝法制备得到的缺陷。Melt spinning is a spinning method in which raw materials are heated and melted, extruded through spinneret holes, and cooled and solidified in the air to form fibers. It has the advantages of simple equipment requirements, no solvent, less pollution and good working environment. Alumina ceramics have a high melting point and low melt viscosity, so they cannot be produced by traditional melting and drawing methods like quartz fibers. And because Al atoms have strong metallicity, it is difficult to prepare alumina precursors that can be melted, so there is no report on the preparation of alumina fibers by melt spinning precursors. The invention obtains a solid alumina precursor with good spinning performance, which overcomes the defect that the alumina continuous fiber is difficult to be prepared by a melt spinning method in the prior art.
其中,步骤1)中所述的目标软化点为80~130℃,优选90~125℃。Wherein, the target softening point described in step 1) is 80-130°C, preferably 90-125°C.
步骤2)中所述的研磨为放入砂磨机中以5Hz~46Hz频率研磨2~8h。The grinding described in step 2) is put into a sand mill and grind at a frequency of 5Hz-46Hz for 2-8h.
步骤2)中所述的分散剂采用如下方法制备得到:将聚铝氧烷与聚乙二醇于溶剂中回流反应1~3h,减压除溶剂得到分散剂(PAO-S)。The dispersant described in step 2) is prepared by the following method: polyaluminoxane and polyethylene glycol are refluxed in a solvent for 1-3 hours, and the solvent is removed under reduced pressure to obtain the dispersant (PAO-S).
所述的聚铝氧烷、聚乙二醇和溶剂的质量比为1:(0.2~1):(1~5);所述的聚乙二醇的分子量为200~6000;所述的溶剂为正丙醇、异丙醇、乙二醇甲醚、乙二醇乙醚中的一种或几种的混合物。The mass ratio of described polyaluminoxane, polyethylene glycol and solvent is 1:(0.2~1):(1~5); the molecular weight of described polyethylene glycol is 200~6000; Described solvent is One or a mixture of n-propanol, isopropanol, ethylene glycol methyl ether, and ethylene glycol ethyl ether.
步骤2)中,所述的含铝粉体为铝粉、玻璃态Al2O3、γ-Al2O3、α-Al2O3、莫来石中一种或几种的混合物,粉体粒径为30nm~500nm;步骤2)中,所述的溶剂为正丙醇、异丙醇、无水乙醇、乙二醇甲醚、乙二醇乙醚、甲苯中的一种或几种的混合物。In step 2), the aluminum-containing powder is a mixture of one or more of aluminum powder, glassy Al 2 O 3 , γ-Al 2 O 3 , α-Al 2 O 3 , and mullite. The particle size is 30nm~500nm; in step 2), the solvent is one or more of n-propanol, isopropanol, absolute ethanol, ethylene glycol methyl ether, ethylene glycol ethyl ether, toluene mixture.
本发明还提供所述的制备方法制备的氧化铝连续纤维的熔融纺丝原料。The invention also provides the raw material for melt spinning of alumina continuous fiber prepared by the preparation method.
本发明的目的还在于提供一种氧化铝连续纤维,所述的氧化铝连续纤维是采用本发明所述的熔融纺丝原料制备得到的。The object of the present invention is also to provide a continuous alumina fiber, which is prepared by using the melt spinning raw material described in the present invention.
本发明还进一步提供所述的氧化铝连续纤维的制备方法,该方法包括熔融纺丝、不熔化、裂解及烧成。The present invention further provides a method for preparing the alumina continuous fiber, which includes melt spinning, non-melting, cracking and firing.
进一步的,所述的熔融纺丝为:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至150~180℃,待其熔融为均匀的熔体并脱除残余气泡后,在110~155℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝。Further, the melt spinning is as follows: the spinning raw material is placed in the spinning cylinder of the melt spinning device, heated to 150-180°C under the protection of nitrogen, and melted into a uniform melt to remove residual air bubbles Afterwards, melt spinning is carried out at 110-155°C, and the continuous alumina fiber precursors are obtained through bundling and winding.
所述的不熔化为:将步骤1)所得的连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至30~40℃,在30~45%的相对湿度下保温20min~2h,再升温至60~95℃,在60~95%的湿度下保温10min~2h,冷却至室温得到不熔化纤维。The non-melting is as follows: the continuous alumina fiber precursor obtained in step 1) is placed in a constant temperature and humidity box, the temperature is first raised to 30-40°C, and the temperature is kept at 30-45% relative humidity for 20min-2h, and then Raise the temperature to 60-95°C, keep it warm for 10min-2h at a humidity of 60-95%, and cool to room temperature to obtain infusible fibers.
所述的裂解和烧成可按照本领域常用的方法进行,作为一种优选方案,所述的裂解和烧成按照下述方式进行:Described cracking and burning can be carried out according to the method commonly used in this field, and as a kind of preferred scheme, described cracking and burning are carried out in the following manner:
所述的裂解为:将步骤2)所得的不熔化纤维置于高温炉中以0.5~30℃/min升温至500~800℃,保温20min~3h,裂解气氛为氮气、氩气、氦气、空气中的一种或几种的混合气;The cracking is as follows: put the non-melting fiber obtained in step 2) in a high-temperature furnace to raise the temperature to 500-800°C at 0.5-30°C/min, keep it warm for 20min-3h, and the cracking atmosphere is nitrogen, argon, helium, One or several mixtures in the air;
所述的烧成为:将裂解后纤维以0.15~100℃/min的升温速率升温至1000~1800℃处理1min~10h,烧成气氛为空气。The firing process is as follows: the cracked fiber is heated to 1000-1800°C at a heating rate of 0.15-100°C/min for 1min-10h, and the firing atmosphere is air.
具体地说,所述的制备方法包括如下步骤:Specifically, the preparation method comprises the following steps:
1)熔融纺丝:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至150~180℃,待其熔融为均匀的熔体并脱除残余气泡后,在110~155℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝;1) Melt spinning: put the spinning raw material in the spinning cylinder of the melt spinning device, heat it up to 150-180°C under the protection of nitrogen, and after it is melted into a uniform melt and removes residual bubbles, it is heated at 110-180°C. Carry out melt spinning at 155°C, and obtain continuous alumina fiber precursors through bundling and collecting;
2)不熔化:将步骤1)所得的连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至30~40℃,在30~45%的相对湿度下保温20min~2h,再升温至60~95℃,在60~95%的湿度下保温10min~2h,冷却至室温得到不熔化纤维;2) No melting: Place the continuous alumina fiber precursor obtained in step 1) in a constant temperature and humidity box, first raise the temperature to 30-40°C, keep it warm for 20min-2h at a relative humidity of 30-45%, and then raise the temperature to 60-95°C, keep warm at 60-95% humidity for 10min-2h, cool to room temperature to obtain infusible fibers;
3)裂解:将步骤2)所得的不熔化纤维置于高温炉中以0.5~30℃/min升温至500~800℃,保温20min~3h,裂解气氛为氮气、氩气、氦气、空气中的一种或几种的混合气;3) Pyrolysis: put the non-melting fiber obtained in step 2) in a high-temperature furnace to raise the temperature to 500-800°C at 0.5-30°C/min, keep it warm for 20min-3h, and the cracking atmosphere is nitrogen, argon, helium, or air One or several mixtures of gases;
4)烧成:将裂解后纤维以0.15~100℃/min的升温速率升温至1000~1800℃处理1min~10h,烧成气氛为空气。4) Firing: heat up the cracked fibers to 1000-1800°C at a heating rate of 0.15-100°C/min for 1min-10h, and the firing atmosphere is air.
本方法的技术关键在于合成了可熔纺的固体氧化铝前驱体PAO-P,并给出氧化铝纤维原丝熔融纺丝和烧结工艺。为了进一步提高纤维强度,向纺丝原料中加入纳米含铝粉体,以及用于提高分散均匀性的接枝改性聚铝氧烷分散剂PAO-S。改性聚铝氧烷的另一有益效果是裂解后生成纳米微晶氧化铝,提高了纺丝原料的整体陶瓷产率和陶瓷纤维的致密化程度。本发明提供的氧化铝连续纤维制备方法绿色环保,质量稳定,高温力学性能优良,并可快速实现氧化铝连续纤维大规模工业化生产。The technical key of the method lies in the synthesis of the melt-spinnable solid alumina precursor PAO-P, and the melt-spinning and sintering process of alumina fiber precursors. In order to further improve the fiber strength, nano-aluminum powder and grafted modified polyaluminoxane dispersant PAO-S are added to the spinning raw material to improve the uniformity of dispersion. Another beneficial effect of the modified polyaluminoxane is to generate nano-microcrystalline alumina after cracking, which improves the overall ceramic yield of spinning raw materials and the densification degree of ceramic fibers. The preparation method of the alumina continuous fiber provided by the invention is green and environment-friendly, has stable quality, excellent high-temperature mechanical properties, and can rapidly realize large-scale industrial production of the alumina continuous fiber.
本发明所提供的氧化铝连续纤维的新型制备方法,通过合成可纺型固体氧化铝前驱体,实现熔融纺丝工艺,减少溶剂污染,提高生产效率和纤维质量一致性,同时本方法原料中不含钠钾离子,避免了高温下其对纤维的化学损伤。采用前驱体结合含铝粉体熔融纺丝,有效提高纤维原丝的铝含量,减少陶瓷化过程中的纤维体积收缩和力学性能损失。The new preparation method of alumina continuous fiber provided by the present invention realizes the melt spinning process by synthesizing the spinnable solid alumina precursor, reduces solvent pollution, improves production efficiency and fiber quality consistency, and at the same time does not contain any raw materials in the method. Containing sodium and potassium ions, it avoids chemical damage to fibers under high temperature. The use of precursors combined with aluminum-containing powders for melt spinning can effectively increase the aluminum content of fiber precursors and reduce fiber volume shrinkage and loss of mechanical properties during ceramization.
本发明的技术特点如下,以改性聚铝氧烷(PAO-S)作为分散剂与粉体均匀分散之后再与高分子化的氧化铝前驱体(PAO-P)混合制备纺丝原料,之后熔融纺丝制备氧化铝纤维原丝。改性聚铝氧烷作为分散剂的有益效果是提高前驱体PAO-P与粉体的相容性,且其在后续裂解过程中会生成氧化铝,有利于提高纺丝原料的整体陶瓷产率;该纺丝原料均相稳定,可在室温下密封存储2年以上。The technical characteristics of the present invention are as follows: use modified polyaluminoxane (PAO-S) as a dispersant to uniformly disperse the powder and then mix it with a high molecular weight alumina precursor (PAO-P) to prepare spinning raw materials, then Alumina fiber precursors were prepared by melt spinning. The beneficial effect of modified polyaluminoxane as a dispersant is to improve the compatibility between the precursor PAO-P and the powder, and it will generate alumina in the subsequent cracking process, which is conducive to improving the overall ceramic yield of spinning raw materials ; The spinning material is homogeneously stable and can be sealed and stored at room temperature for more than 2 years.
本发明的另一有益效果是,本发明采用熔融纺丝制备纤维原丝,设备简单,操作方便,成本低,无污染,适于快速实现放大规模生产。Another beneficial effect of the present invention is that the present invention adopts melt spinning to prepare fiber precursors, which has simple equipment, convenient operation, low cost, no pollution, and is suitable for rapid large-scale production.
附图说明Description of drawings
图1是实施例1所制备纤维的SEM图片;Fig. 1 is the SEM picture of the fiber prepared by embodiment 1;
图2是实施例1所制备纤维的XRD图片;Fig. 2 is the XRD picture of the fiber prepared in embodiment 1;
图3a是实施例3所制备纤维的SEM图片;Fig. 3 a is the SEM picture of the fiber prepared in embodiment 3;
图3b是实施例3所制备纤维的SEM放大图片;Fig. 3 b is the SEM enlarged picture of the fiber prepared in embodiment 3;
图4是实施例3所制备纤维的XRD图片;Fig. 4 is the XRD picture of the fiber prepared by embodiment 3;
图5是实施例3所制备纤维的照片;Fig. 5 is the photograph of the prepared fiber of embodiment 3;
图6是对比例1所制备纤维的照片;Fig. 6 is the photograph of the prepared fiber of comparative example 1;
图7a是实施例7所得纤维在1550℃处理20min后纤维的宏观照片;Fig. 7 a is the macrophotograph of the fiber after the fiber obtained in Example 7 was treated at 1550° C. for 20 min;
图7b是实施例7所得纤维在1550℃处理20min后纤维的微观照片;Figure 7b is a microscopic photo of the fiber obtained in Example 7 after being treated at 1550°C for 20min;
图8a是商品化的nextel-610纤维在1550℃处理20min后纤维的宏观照片;Figure 8a is a macroscopic photo of the commercial nextel-610 fiber treated at 1550°C for 20 minutes;
图8b是商品化的nextel-610纤维在1550℃处理20min后纤维的微观照片。Figure 8b is a microscopic photo of the commercial nextel-610 fiber treated at 1550°C for 20 minutes.
需要说明的是,这些附图和文字描述并不旨在以任何方式限制本发明的构思范围,而是通过参考特定实施例为本领域技术人员说明本发明的概念。It should be noted that these drawings and text descriptions are not intended to limit the concept scope of the present invention in any way, but illustrate the concept of the present invention for those skilled in the art by referring to specific embodiments.
具体实施方式Detailed ways
为使本发明实施例的目的、技术方案和优点更加清楚,下面将结合本发明实施例中的附图,对实施例中的技术方案进行清楚、完整地描述,以下实施例用于说明本发明,但不用来限制本发明的范围。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention more clear, the technical solutions in the embodiments will be clearly and completely described below in conjunction with the drawings in the embodiments of the present invention. The following embodiments are used to illustrate the present invention , but not to limit the scope of the present invention.
实施例1Example 1
不加入粉体,PAO-P直接熔融纺丝制备氧化铝纤维Preparation of alumina fiber by direct melt spinning of PAO-P without adding powder
1.熔融纺丝原料的制备:1. Preparation of melt spinning raw materials:
熔融纺丝型氧化铝前驱体的制备:将500g聚铝氧烷置于反应釜中,搅拌下加热至80℃,减压蒸馏1h,继续升温至120℃,保温1h,最后再升温至160℃,每10min取样测软化点,当软化点达到90℃时,停止加热,氮气保护下降至室温得高分子化的氧化铝前驱体PAO-P;Preparation of melt-spinning alumina precursor: put 500g of polyaluminoxane in a reaction kettle, heat to 80°C under stirring, distill under reduced pressure for 1h, continue to heat up to 120°C, keep warm for 1h, and finally raise the temperature to 160°C , take a sample every 10 minutes to measure the softening point, when the softening point reaches 90 ° C, stop heating, nitrogen protection down to room temperature to obtain the polymerized alumina precursor PAO-P;
2.氧化铝纤维的制备2. Preparation of alumina fibers
(1)熔融纺丝:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至150℃,待其熔融为均匀的熔体并脱除残余气泡后,在120℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝;(1) Melt spinning: put the spinning raw material in the spinning cylinder of the melt spinning device, heat it up to 150°C under the protection of nitrogen, and wait for it to melt into a uniform melt and remove residual bubbles, then carry out at 120°C Melt spinning, bundled and collected to obtain continuous alumina fiber precursors;
(2)不熔化:将步骤(1)所得连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至40℃,在30%的相对湿度下保温30min,再升温至90℃,在80%的湿度下保温20min,冷却至室温得到不熔化纤维;(2) No melting: Place the continuous alumina fiber precursor obtained in step (1) in a constant temperature and humidity box, first raise the temperature to 40°C, keep it warm for 30min at a relative humidity of 30%, and then raise the temperature to 90°C. % humidity for 20 minutes, cooled to room temperature to obtain non-melting fibers;
(3)裂解:将步骤(3)所得不熔化纤维置于高温炉中以1℃/min升温至600℃,保温1h,裂解气氛为空气;(3) Cracking: place the non-melting fiber obtained in step (3) in a high-temperature furnace to raise the temperature to 600°C at 1°C/min, keep it warm for 1h, and the cracking atmosphere is air;
(4)烧成:将裂解后纤维以30℃/min的升温速率升温至1000℃处理20min,烧成气氛为空气。(4) Firing: heat up the pyrolyzed fibers to 1000° C. for 20 minutes at a heating rate of 30° C./min, and the firing atmosphere is air.
图1为所得纤维的SEM照片,由图可看出,纤维表面光滑,尺寸均匀,纤维直径为10~12μm。图2所示的XRD结果表明,纤维的晶相组成为γ-Al2O3。Fig. 1 is the SEM photo of the obtained fiber. It can be seen from the figure that the surface of the fiber is smooth, the size is uniform, and the fiber diameter is 10-12 μm. The XRD results shown in Figure 2 show that the crystal phase composition of the fiber is γ-Al 2 O 3 .
实施例2Example 2
不加入粉体,PAO-P直接熔融纺丝制备氧化铝纤维Preparation of alumina fiber by direct melt spinning of PAO-P without adding powder
1.熔融纺丝原料的制备:1. Preparation of melt spinning raw materials:
熔融纺丝型氧化铝前驱体的制备:将500g聚铝氧烷置于反应釜中,搅拌下加热至85℃,减压蒸馏2h,继续升温至140℃,保温1h,最后再升温至170℃,每10min取样测软化点,当软化点达到120℃时,停止加热,氮气保护下降至室温得高分子化的氧化铝前驱体PAO-P;Preparation of melt-spinning alumina precursor: put 500g of polyaluminoxane in a reaction kettle, heat to 85°C under stirring, distill under reduced pressure for 2h, continue to heat up to 140°C, keep warm for 1h, and finally raise the temperature to 170°C , take a sample every 10 minutes to measure the softening point, when the softening point reaches 120 ° C, stop heating, nitrogen protection down to room temperature to obtain the polymerized alumina precursor PAO-P;
2.氧化铝纤维的制备2. Preparation of alumina fibers
(1)熔融纺丝:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至180℃,待其熔融为均匀的熔体并脱除残余气泡后,在150℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝;(1) Melt spinning: put the spinning raw material in the spinning cylinder of the melt spinning device, heat it up to 180°C under the protection of nitrogen, and wait for it to melt into a uniform melt and remove residual bubbles, then carry out at 150°C Melt spinning, bundled and collected to obtain continuous alumina fiber precursors;
(2)不熔化:将步骤(1)所得连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至40℃,在40%的相对湿度下保温1h,再升温至85℃,在90%的湿度下保温30min,冷却至室温得到不熔化纤维;(2) No melting: Place the continuous alumina fiber precursor obtained in step (1) in a constant temperature and humidity box, first raise the temperature to 40°C, keep it warm at 40% relative humidity for 1h, then raise the temperature to 85°C, and heat it at 90°C % humidity for 30 minutes, cooled to room temperature to obtain non-melting fibers;
(3)裂解:将步骤(2)所得不熔化纤维置于高温炉中以5℃/min升温至700℃,保温2h,裂解气氛为氦气;(3) Pyrolysis: place the non-melting fiber obtained in step (2) in a high-temperature furnace to raise the temperature to 700°C at 5°C/min, keep it warm for 2h, and the cracking atmosphere is helium;
(4)烧成:将裂解后纤维以10℃/min的升温速率升温至1200℃处理10min,烧成气氛为空气。(4) Firing: heat up the pyrolyzed fibers to 1200° C. for 10 minutes at a heating rate of 10° C./min, and the firing atmosphere is air.
纤维表面光滑,尺寸均匀,纤维直径为10~12μm,纤维的晶相组成为γ-Al2O3。The surface of the fiber is smooth, the size is uniform, the diameter of the fiber is 10-12 μm, and the crystal phase composition of the fiber is γ-Al 2 O 3 .
实施例3Example 3
1.熔融纺丝原料的制备:1. Preparation of melt spinning raw materials:
(1)熔融纺丝型氧化铝前驱体的制备:将500g聚铝氧烷置于反应釜中,搅拌下加热至80℃,减压蒸馏1h,继续升温至120℃,保温1h,最后再升温至180℃,每10min取样测软化点,当软化点达到113℃时,停止加热,氮气保护下降至室温得高分子化的氧化铝前驱体PAO-P;(1) Preparation of melt-spinning alumina precursor: put 500g of polyaluminoxane in a reaction kettle, heat it to 80°C under stirring, distill under reduced pressure for 1h, continue to heat up to 120°C, keep it warm for 1h, and finally raise the temperature again To 180°C, take samples every 10 minutes to measure the softening point, when the softening point reaches 113°C, stop heating, nitrogen protection down to room temperature to obtain polymerized alumina precursor PAO-P;
(2)粉体浆料的制备:将聚铝氧烷(PAO)与聚乙二醇(PEG-200)于正丙醇中回流反应1h,聚铝氧烷(PAO)、聚乙二醇(PEG-200)与正丙醇的质量比为1:0.2:1,减压除溶剂得到分散剂(PAO-S);将分散剂、粒径为150nm的α-Al2O3粉体和正丙醇以质量比1:1.5:3放入砂磨机中以46Hz频率研磨5h得到粉体浆料;(2) Preparation of powder slurry: polyaluminoxane (PAO) and polyethylene glycol (PEG-200) were refluxed in n-propanol for 1 h, polyaluminoxane (PAO), polyethylene glycol ( The mass ratio of PEG-200) to n-propanol is 1:0.2:1, and the solvent is removed under reduced pressure to obtain a dispersant (PAO-S); Alcohol was put into a sand mill with a mass ratio of 1:1.5:3 and ground for 5 hours at a frequency of 46 Hz to obtain a powder slurry;
(3)纺丝原料的制备:将步骤(1)所得的前驱体与步骤(2)所得的粉体浆料按质量比70:30均匀混合,然后升温至170℃减压蒸馏30min得到纺丝原料;(3) Preparation of spinning raw materials: uniformly mix the precursor obtained in step (1) with the powder slurry obtained in step (2) at a mass ratio of 70:30, then heat up to 170°C and distill under reduced pressure for 30 minutes to obtain spinning raw material;
2.氧化铝纤维的制备2. Preparation of alumina fibers
(1)熔融纺丝:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至175℃,待其熔融为均匀的熔体并脱除残余气泡后,在145℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝;(1) Melt spinning: put the spinning raw material in the spinning cylinder of the melt spinning device, heat it up to 175°C under the protection of nitrogen, and wait for it to melt into a uniform melt and remove residual bubbles, then carry out at 145°C Melt spinning, bundled and collected to obtain continuous alumina fiber precursors;
(2)不熔化:将步骤(1)所得连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至30℃,在40%的相对湿度下保温50min,再升温至80℃,在90%的湿度下保温10min,冷却至室温得到不熔化纤维;(2) Non-melting: Place the continuous alumina fiber precursor obtained in step (1) in a constant temperature and humidity box, first raise the temperature to 30°C, keep it warm for 50min at a relative humidity of 40%, and then raise the temperature to 80°C. % humidity for 10 minutes, cooled to room temperature to obtain non-melting fibers;
(3)裂解:将步骤(3)所得不熔化纤维置于高温炉中以10℃/min升温至800℃,保温2h,裂解气氛为氮气;(3) Cracking: place the non-melting fiber obtained in step (3) in a high-temperature furnace to raise the temperature to 800°C at 10°C/min, keep it warm for 2h, and use nitrogen as the cracking atmosphere;
(4)烧成:将裂解后纤维以10℃/min的升温速率升温至1550℃处理20min,烧成气氛为空气。(4) Firing: heat up the pyrolyzed fibers to 1550° C. for 20 minutes at a heating rate of 10° C./min, and the firing atmosphere is air.
图3a和图3b为所得纤维的SEM照片和SEM放大照片,由图可看出,纤维表面光滑,尺寸均匀,颗粒尺寸小于500nm,纤维直径为10~12μm。图4所示的XRD结果表明,纤维的晶相组成为α-Al2O3。Figure 3a and Figure 3b are SEM photos and SEM enlarged photos of the obtained fibers. It can be seen from the figures that the fiber surface is smooth, the size is uniform, the particle size is less than 500nm, and the fiber diameter is 10-12 μm. The XRD results shown in Fig. 4 show that the crystal phase composition of the fiber is α-Al 2 O 3 .
实施例4Example 4
1.熔融纺丝原料的制备:1. Preparation of melt spinning raw materials:
(1)熔融纺丝型氧化铝前驱体的制备:将500g聚铝氧烷置于反应釜中,搅拌下加热至80℃,减压蒸馏1h,继续升温至110℃,保温3h,继续升温至180℃后,每10min取样测软化点,当软化点达到120℃时,停止加热,氮气保护下降至室温得高分子化的氧化铝前驱体PAO-P;(1) Preparation of melt-spinning alumina precursor: put 500g of polyaluminoxane in a reaction kettle, heat to 80°C under stirring, distill under reduced pressure for 1 hour, continue to heat up to 110°C, keep warm for 3 hours, and continue to heat up to After 180°C, samples were taken every 10 minutes to measure the softening point. When the softening point reached 120°C, the heating was stopped, and nitrogen protection dropped to room temperature to obtain the polymerized alumina precursor PAO-P;
(2)粉体浆料的制备:将聚铝氧烷(PAO)与聚乙二醇(PEG-2000)于异丙醇中回流反应2h,聚铝氧烷(PAO)、聚乙二醇(PEG-2000)和异丙醇的质量比为1:0.3:5,减压除溶剂得到分散剂(PAO-S);将分散剂、粒径为258nm的莫来石粉体和乙二醇乙醚以质量比1:2:4放入砂磨机中以30Hz频率研磨8h得到粉体浆料;(2) Preparation of powder slurry: polyaluminoxane (PAO) and polyethylene glycol (PEG-2000) were refluxed in isopropanol for 2 hours, polyaluminoxane (PAO), polyethylene glycol ( The mass ratio of PEG-2000) and isopropanol is 1:0.3:5, decompression solvent removal obtains dispersant (PAO-S); The dispersant, particle diameter are the mullite powder of 258nm and ethylene glycol ether Put it into a sand mill with a mass ratio of 1:2:4 and grind for 8 hours at a frequency of 30 Hz to obtain a powder slurry;
(3)纺丝原料的制备:将步骤(1)所得的前驱体与步骤(2)所得的粉体浆料按质量比50:50均匀混合,然后升温至180℃减压蒸馏20min得到纺丝原料;(3) Preparation of spinning raw materials: uniformly mix the precursor obtained in step (1) with the powder slurry obtained in step (2) at a mass ratio of 50:50, then heat up to 180°C and distill under reduced pressure for 20 minutes to obtain spinning raw material;
2.氧化铝纤维的制备2. Preparation of alumina fibers
(1)熔融纺丝:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至180℃,待其熔融为均匀的熔体并脱除残余气泡后,在155℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝;(1) Melt spinning: put the spinning raw material in the spinning cylinder of the melt spinning device, heat it up to 180°C under the protection of nitrogen, and wait for it to melt into a uniform melt and remove residual bubbles, then carry out at 155°C Melt spinning, bundled and collected to obtain continuous alumina fiber precursors;
(2)不熔化:将步骤(1)所得连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至35℃,在45%的相对湿度下保温60min,再升温至90℃,在60%的湿度下保温20min,冷却至室温得到不熔化纤维;(2) No melting: Place the continuous alumina fiber precursor obtained in step (1) in a constant temperature and humidity box, first raise the temperature to 35°C, keep it warm for 60min at a relative humidity of 45%, then raise the temperature to 90°C, and heat it at 60°C. % humidity for 20 minutes, cooled to room temperature to obtain non-melting fibers;
(3)裂解:将步骤(3)所得不熔化纤维置于高温炉中以20℃/min升温至650℃,保温3h,裂解气氛为空气;(3) Cracking: place the non-melting fiber obtained in step (3) in a high-temperature furnace to raise the temperature to 650°C at 20°C/min, keep it warm for 3h, and the cracking atmosphere is air;
(4)烧成:将裂解后纤维以0.5℃/min的升温速率升温至1400℃处理2h,烧成气氛为空气。(4) Firing: heat up the pyrolyzed fibers to 1400° C. for 2 hours at a heating rate of 0.5° C./min, and the firing atmosphere is air.
实施例5Example 5
1.熔融纺丝原料的制备:1. Preparation of melt spinning raw materials:
(1)熔融纺丝型氧化铝前驱体的制备:将500g聚铝氧烷置于反应釜中,搅拌下加热至60℃,减压蒸馏3h,继续升温至140℃,保温30min,继续升温至150℃后,每10min取样测软化点,当软化点达到110℃时,停止加热,氮气保护下降至室温得高分子化的氧化铝前驱体PAO-P;(1) Preparation of melt-spinning alumina precursor: put 500g of polyaluminoxane in a reaction kettle, heat to 60°C under stirring, distill under reduced pressure for 3 hours, continue to heat up to 140°C, keep warm for 30min, and continue to heat up to After 150°C, samples were taken every 10 minutes to measure the softening point. When the softening point reached 110°C, the heating was stopped, and nitrogen protection dropped to room temperature to obtain the polymerized alumina precursor PAO-P;
(2)粉体浆料的制备:将聚铝氧烷(PAO)与聚乙二醇(PEG-6000)于乙二醇乙醚中回流反应2.5h,聚铝氧烷(PAO)、聚乙二醇(PEG-6000)、乙二醇乙醚的质量比为1:0.8:4,减压除溶剂得到分散剂(PAO-S);将分散剂、粒径为50nm的γ-Al2O3粉体和乙二醇甲醚以质量比1:4:6放入砂磨机中以20Hz频率研磨2h得到粉体浆料;(2) Preparation of powder slurry: polyaluminoxane (PAO) and polyethylene glycol (PEG-6000) were refluxed in ethylene glycol ether for 2.5 hours, polyaluminoxane (PAO), polyethylene glycol The mass ratio of alcohol (PEG-6000) to ethylene glycol ether is 1:0.8:4, and the solvent is removed under reduced pressure to obtain a dispersant (PAO-S); the dispersant, γ-Al 2 O 3 powder with a particle size of 50nm The solid and ethylene glycol methyl ether are put into a sand mill with a mass ratio of 1:4:6 and ground for 2 hours at a frequency of 20 Hz to obtain a powder slurry;
(3)纺丝原料的制备:将步骤(1)所得的前驱体与步骤(2)所得的粉体浆料按质量比20:80均匀混合,然后升温至150℃减压蒸馏2h得到纺丝原料;(3) Preparation of spinning raw materials: uniformly mix the precursor obtained in step (1) with the powder slurry obtained in step (2) at a mass ratio of 20:80, then heat up to 150°C and distill under reduced pressure for 2 hours to obtain spinning raw material;
2.氧化铝纤维的制备2. Preparation of alumina fibers
(1)熔融纺丝:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至150℃,待其熔融为均匀的熔体并脱除残余气泡后,在110℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝;(1) Melt spinning: put the spinning raw material in the spinning cylinder of the melt spinning device, heat it up to 150°C under the protection of nitrogen, and wait for it to melt into a uniform melt and remove residual bubbles, then carry out at 110°C Melt spinning, bundled and collected to obtain continuous alumina fiber precursors;
(2)不熔化:将步骤(1)所得连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至30℃,在35%的相对湿度下保温40min,再升温至60℃,在85%的湿度下保温2h,冷却至室温得到不熔化纤维;(2) No melting: Place the continuous alumina fiber precursor obtained in step (1) in a constant temperature and humidity box, first raise the temperature to 30°C, keep it warm for 40min at a relative humidity of 35%, then raise the temperature to 60°C, and heat it at 85°C. % humidity for 2 hours, cooled to room temperature to obtain non-melting fibers;
(3)裂解:将步骤(3)所得不熔化纤维置于高温炉中以0.5℃/min升温至800℃,保温20min,裂解气氛为氩气;(3) Cracking: place the non-melting fiber obtained in step (3) in a high-temperature furnace to raise the temperature to 800°C at 0.5°C/min, keep it warm for 20min, and the cracking atmosphere is argon;
(4)烧成:将裂解后纤维以30℃/min的升温速率升温至1800℃处理1min,烧成气氛为空气。(4) Firing: heat up the pyrolyzed fibers to 1800° C. for 1 min at a heating rate of 30° C./min, and the firing atmosphere is air.
实施例6Example 6
1.熔融纺丝原料的制备:1. Preparation of melt spinning raw materials:
(1)熔融纺丝型氧化铝前驱体的制备:将500g聚铝氧烷置于反应釜中,搅拌下加热至100℃,减压蒸馏30min,继续升温至125℃,保温2h,继续升温至200℃后,每10min取样测软化点,当软化点达到125℃时,停止加热,氮气保护下降至室温得高分子化的氧化铝前驱体PAO-P;(1) Preparation of melt-spinning alumina precursor: put 500g of polyaluminoxane in a reaction kettle, heat to 100°C under stirring, distill under reduced pressure for 30min, continue to heat up to 125°C, keep warm for 2h, and continue to heat up to After 200°C, take a sample every 10 minutes to measure the softening point. When the softening point reaches 125°C, stop heating, and lower it down to room temperature under nitrogen protection to obtain the polymerized alumina precursor PAO-P;
(2)粉体浆料的制备:将聚铝氧烷(PAO)与聚乙二醇(PEG-6000)于乙二醇甲醚中回流反应3h,聚铝氧烷(PAO)、聚乙二醇(PEG-6000)与乙二醇甲醚的质量比为1:0.4:2,减压除溶剂得到分散剂(PAO-S);将分散剂、粒径为30nm的γ-Al2O3粉体和乙二醇甲醚以质量比1:4:6放入砂磨机中以5Hz频率研磨4h得到粉体浆料;(2) Preparation of powder slurry: polyaluminoxane (PAO) and polyethylene glycol (PEG-6000) were refluxed in ethylene glycol methyl ether for 3 hours, polyaluminoxane (PAO), polyethylene glycol The mass ratio of alcohol (PEG-6000) to ethylene glycol methyl ether is 1:0.4:2, and the solvent is removed under reduced pressure to obtain a dispersant (PAO-S); the dispersant, γ-Al 2 O 3 with a particle size of 30nm Put the powder and ethylene glycol methyl ether in a sand mill at a mass ratio of 1:4:6 and grind for 4 hours at a frequency of 5 Hz to obtain a powder slurry;
(3)纺丝原料的制备:将步骤(1)所得的前驱体与步骤(2)所得的粉体浆料按质量比15:85均匀混合,然后升温至200℃减压蒸馏1.5h得到纺丝原料;(3) Preparation of spinning raw materials: uniformly mix the precursor obtained in step (1) with the powder slurry obtained in step (2) at a mass ratio of 15:85, then heat up to 200°C and distill under reduced pressure for 1.5h to obtain spinning silk raw material;
2.氧化铝纤维的制备2. Preparation of alumina fibers
(1)熔融纺丝:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至160℃,待其熔融为均匀的熔体并脱除残余气泡后,在130℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝;(1) Melt spinning: put the spinning raw material in the spinning cylinder of the melt spinning device, heat it up to 160°C under the protection of nitrogen, and wait for it to melt into a uniform melt and remove residual bubbles, then carry out at 130°C Melt spinning, bundled and collected to obtain continuous alumina fiber precursors;
(2)不熔化:将步骤(1)所得连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至30℃,在35%的相对湿度下保温20min,再升温至95℃,在95%的湿度下保温45min,冷却至室温得到不熔化纤维;(2) Non-melting: Place the continuous alumina fiber precursor obtained in step (1) in a constant temperature and humidity box, first raise the temperature to 30°C, keep it warm for 20min at a relative humidity of 35%, then raise the temperature to 95°C, and heat it at 95°C % humidity for 45 minutes, cooled to room temperature to obtain non-melting fibers;
(3)裂解:将步骤(3)所得不熔化纤维置于高温炉中以30℃/min升温至500℃,保温1h,裂解气氛为氩气;(3) Pyrolysis: place the non-melting fiber obtained in step (3) in a high-temperature furnace to raise the temperature to 500°C at 30°C/min, keep it warm for 1h, and the cracking atmosphere is argon;
(4)烧成:将裂解后纤维以0.15℃/min的升温速率升温至1000℃处理10h,烧成气氛为空气。(4) Firing: heat up the pyrolyzed fibers to 1000° C. for 10 h at a heating rate of 0.15° C./min, and the firing atmosphere is air.
实施例7Example 7
1.熔融纺丝原料的制备:1. Preparation of melt spinning raw materials:
(1)熔融纺丝型氧化铝前驱体的制备:将500g聚铝氧烷置于反应釜中,搅拌下加热至60℃,减压蒸馏3h,继续升温至140℃,保温30min,继续升温至200℃后,每10min取样测软化点,当软化点达到130℃时,停止加热,氮气保护下降至室温得高分子化的氧化铝前驱体PAO-P;(1) Preparation of melt-spinning alumina precursor: put 500g of polyaluminoxane in a reaction kettle, heat to 60°C under stirring, distill under reduced pressure for 3 hours, continue to heat up to 140°C, keep warm for 30min, and continue to heat up to After 200°C, take a sample every 10 minutes to measure the softening point. When the softening point reaches 130°C, stop heating, and lower it down to room temperature under nitrogen protection to obtain a polymerized alumina precursor PAO-P;
(2)粉体浆料的制备:将聚铝氧烷(PAO)与聚乙二醇(PEG-6000)于正丙醇中回流反应1.5h,聚铝氧烷(PAO)、聚乙二醇(PEG-6000)与正丙醇的质量比为1:0.5:3,减压除溶剂得到分散剂(PAO-S);将分散剂、粒径为500nm的γ-Al2O3粉体和甲苯以质量比1:3.5:5放入砂磨机中以15Hz频率研磨6h得到粉体浆料;(2) Preparation of powder slurry: polyaluminoxane (PAO) and polyethylene glycol (PEG-6000) were refluxed in n-propanol for 1.5h, polyaluminoxane (PAO), polyethylene glycol The mass ratio of (PEG-6000) to n-propanol is 1:0.5:3, and the solvent is removed under reduced pressure to obtain a dispersant (PAO-S); the dispersant, γ-Al 2 O 3 powder with a particle size of 500nm and Put toluene into a sand mill with a mass ratio of 1:3.5:5 and grind for 6 hours at a frequency of 15 Hz to obtain a powder slurry;
(3)纺丝原料的制备:将步骤(1)所得的前驱体与步骤(2)所得的粉体浆料按质量比25:75均匀混合,然后升温至160℃减压蒸馏45min得到纺丝原料;(3) Preparation of spinning raw materials: uniformly mix the precursor obtained in step (1) with the powder slurry obtained in step (2) at a mass ratio of 25:75, then heat up to 160°C and distill under reduced pressure for 45 minutes to obtain spinning raw material;
2.氧化铝纤维的制备2. Preparation of alumina fibers
(1)熔融纺丝:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至160℃,待其熔融为均匀的熔体并脱除残余气泡后,在115℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝;(1) Melt spinning: put the spinning raw material in the spinning cylinder of the melt spinning device, heat it up to 160°C under the protection of nitrogen, and wait for it to melt into a uniform melt and remove residual bubbles, then carry out at 115°C Melt spinning, bundled and collected to obtain continuous alumina fiber precursors;
(2)不熔化:将步骤(1)所得连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至30℃,在35%的相对湿度下保温2h,再升温至60℃,在85%的湿度下保温2h,冷却至室温得到不熔化纤维;(2) No melting: Place the continuous alumina fiber precursor obtained in step (1) in a constant temperature and humidity box, first raise the temperature to 30°C, keep it warm for 2 hours at a relative humidity of 35%, then raise the temperature to 60°C, and heat it at 85°C. % humidity for 2 hours, cooled to room temperature to obtain non-melting fibers;
(3)裂解:将步骤(3)所得不熔化纤维置于高温炉中以15℃/min升温至750℃,保温1.5h,裂解气氛为氩气;(3) Pyrolysis: place the non-melting fiber obtained in step (3) in a high-temperature furnace to raise the temperature to 750°C at 15°C/min, keep it warm for 1.5h, and the cracking atmosphere is argon;
(4)烧成:将裂解后纤维以100℃/min的升温速率升温至1300℃处理1min,烧成气氛为空气。(4) Firing: heat up the pyrolyzed fibers to 1300° C. for 1 min at a heating rate of 100° C./min, and the firing atmosphere is air.
实施例8Example 8
1.熔融纺丝原料的制备:1. Preparation of melt spinning raw materials:
(1)熔融纺丝型氧化铝前驱体的制备:将500g聚铝氧烷置于反应釜中,搅拌下加热至60℃,减压蒸馏3h,继续升温至140℃,保温30min,继续升温至150℃后,每10min取样测软化点,当软化点达到80℃时,停止加热,氮气保护下降至室温得高分子化的氧化铝前驱体PAO-P;(1) Preparation of melt-spinning alumina precursor: put 500g of polyaluminoxane in a reaction kettle, heat to 60°C under stirring, distill under reduced pressure for 3 hours, continue to heat up to 140°C, keep warm for 30min, and continue to heat up to After 150°C, take a sample every 10 minutes to measure the softening point. When the softening point reaches 80°C, stop heating, and lower it down to room temperature under nitrogen protection to obtain the polymerized alumina precursor PAO-P;
(2)粉体浆料的制备:将聚铝氧烷(PAO)与聚乙二醇(PEG-6000)于正丙醇中回流反应2.5h,聚铝氧烷(PAO)、聚乙二醇(PEG-6000)与正丙醇的质量比为1:1:5,减压除溶剂得到分散剂(PAO-S);将分散剂、粒径为50nm的铝粉和无水乙醇以质量比1:4:6放入砂磨机中以20Hz频率研磨2h得到粉体浆料;(2) Preparation of powder slurry: polyaluminoxane (PAO) and polyethylene glycol (PEG-6000) were refluxed in n-propanol for 2.5 hours, polyaluminoxane (PAO), polyethylene glycol The mass ratio of (PEG-6000) to n-propanol is 1:1:5, and the solvent is removed under reduced pressure to obtain a dispersant (PAO-S); the dispersant, aluminum powder with a particle size of 50nm and absolute ethanol are 1:4:6 was put into a sand mill and ground for 2 hours at a frequency of 20Hz to obtain a powder slurry;
(3)纺丝原料的制备:将步骤(1)所得的前驱体与步骤(2)所得的粉体浆料按质量比80:20均匀混合,然后升温至150℃减压蒸馏2h得到纺丝原料;(3) Preparation of spinning raw materials: uniformly mix the precursor obtained in step (1) with the powder slurry obtained in step (2) at a mass ratio of 80:20, then heat up to 150°C and distill under reduced pressure for 2 hours to obtain spinning raw material;
2.氧化铝纤维的制备2. Preparation of alumina fibers
(1)熔融纺丝:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至150℃,待其熔融为均匀的熔体并脱除残余气泡后,在110℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝;(1) Melt spinning: put the spinning raw material in the spinning cylinder of the melt spinning device, heat it up to 150°C under the protection of nitrogen, and wait for it to melt into a uniform melt and remove residual bubbles, then carry out at 110°C Melt spinning, bundled and collected to obtain continuous alumina fiber precursors;
(2)不熔化:将步骤(1)所得连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至30℃,在35%的相对湿度下保温40min,再升温至60℃,在85%的湿度下保温2h,冷却至室温得到不熔化纤维;(2) No melting: Place the continuous alumina fiber precursor obtained in step (1) in a constant temperature and humidity box, first raise the temperature to 30°C, keep it warm for 40min at a relative humidity of 35%, then raise the temperature to 60°C, and heat it at 85°C. % humidity for 2 hours, cooled to room temperature to obtain non-melting fibers;
(3)裂解:将步骤(3)所得不熔化纤维置于高温炉中以0.5℃/min升温至800℃,保温20min,裂解气氛为氩气;(3) Cracking: place the non-melting fiber obtained in step (3) in a high-temperature furnace to raise the temperature to 800°C at 0.5°C/min, keep it warm for 20min, and the cracking atmosphere is argon;
(4)烧成:将裂解后纤维以30℃/min的升温速率升温至1800℃处理1min,烧成气氛为空气。(4) Firing: heat up the pyrolyzed fibers to 1800° C. for 1 min at a heating rate of 30° C./min, and the firing atmosphere is air.
实施例9Example 9
1.熔融纺丝原料的制备:1. Preparation of melt spinning raw materials:
(1)熔融纺丝型氧化铝前驱体的制备:将500g聚铝氧烷置于反应釜中,搅拌下加热至80℃,减压蒸馏1h,继续升温至110℃,保温3h,继续升温至180℃后,每10min取样测软化点,当软化点达到120℃时,停止加热,氮气保护下降至室温得高分子化的氧化铝前驱体PAO-P;(1) Preparation of melt-spinning alumina precursor: put 500g of polyaluminoxane in a reaction kettle, heat to 80°C under stirring, distill under reduced pressure for 1 hour, continue to heat up to 110°C, keep warm for 3 hours, and continue to heat up to After 180°C, samples were taken every 10 minutes to measure the softening point. When the softening point reached 120°C, the heating was stopped, and nitrogen protection dropped to room temperature to obtain the polymerized alumina precursor PAO-P;
(2)粉体浆料的制备:将聚铝氧烷(PAO)与聚乙二醇(PEG-2000)于异丙醇中回流反应2h,聚铝氧烷(PAO)、聚乙二醇(PEG-2000)与异丙醇的质量比为1:0.2:1,减压除溶剂得到分散剂(PAO-S);将分散剂、粒径为258nm的玻璃态Al2O3和异丙醇以质量比1:2:4放入砂磨机中以30Hz频率研磨8h得到粉体浆料;(2) Preparation of powder slurry: polyaluminoxane (PAO) and polyethylene glycol (PEG-2000) were refluxed in isopropanol for 2 hours, polyaluminoxane (PAO), polyethylene glycol ( The mass ratio of PEG-2000) and isopropanol is 1:0.2:1, and the desolventization under reduced pressure obtains dispersant (PAO-S); The dispersant, particle diameter are the glass state Al of 258nm O 3 and isopropanol Put it into a sand mill with a mass ratio of 1:2:4 and grind for 8 hours at a frequency of 30 Hz to obtain a powder slurry;
(3)纺丝原料的制备:将步骤(1)所得的前驱体与步骤(2)所得的粉体浆料按质量比50:50均匀混合,然后升温至180℃减压蒸馏20min得到纺丝原料;(3) Preparation of spinning raw materials: uniformly mix the precursor obtained in step (1) with the powder slurry obtained in step (2) at a mass ratio of 50:50, then heat up to 180°C and distill under reduced pressure for 20 minutes to obtain spinning raw material;
2.氧化铝纤维的制备2. Preparation of alumina fibers
(1)熔融纺丝:将纺丝原料置于熔融纺丝装置的纺丝筒中,氮气保护下升温加热至180℃,待其熔融为均匀的熔体并脱除残余气泡后,在155℃进行熔融纺丝,经集束、收丝,得连续氧化铝纤维原丝;(1) Melt spinning: put the spinning raw material in the spinning cylinder of the melt spinning device, heat it up to 180°C under the protection of nitrogen, and wait for it to melt into a uniform melt and remove residual bubbles, then carry out at 155°C Melt spinning, bundled and collected to obtain continuous alumina fiber precursors;
(2)不熔化:将步骤(1)所得连续氧化铝纤维原丝置于恒温恒湿箱中,先升温至35℃,在45%的相对湿度下保温60min,再升温至90℃,在60%的湿度下保温20min,冷却至室温得到不熔化纤维;(2) No melting: Place the continuous alumina fiber precursor obtained in step (1) in a constant temperature and humidity box, first raise the temperature to 35°C, keep it warm for 60min at a relative humidity of 45%, then raise the temperature to 90°C, and heat it at 60°C. % humidity for 20 minutes, cooled to room temperature to obtain non-melting fibers;
(3)裂解:将步骤(3)所得不熔化纤维置于高温炉中以20℃/min升温至650℃,保温3h,裂解气氛为空气;(3) Cracking: place the non-melting fiber obtained in step (3) in a high-temperature furnace to raise the temperature to 650°C at 20°C/min, keep it warm for 3h, and the cracking atmosphere is air;
(4)烧成:将裂解后纤维以0.5℃/min的升温速率升温至1400℃处理2h,烧成气氛为空气。(4) Firing: heat up the pyrolyzed fibers to 1400° C. for 2 hours at a heating rate of 0.5° C./min, and the firing atmosphere is air.
对比例1Comparative example 1
为了说明改性聚铝氧烷PAO-S作为分散剂的技术效果,本发明做了以下对比实验:将实施例3中的PAO-S换成常用的聚乙二醇(PEG-200)作为分散剂;其他条件不变。In order to illustrate the technical effect of the modified polyaluminoxane PAO-S as a dispersant, the present invention has done the following comparative experiments: the PAO-S in Example 3 is replaced with commonly used polyethylene glycol (PEG-200) as a dispersant agent; other conditions remain unchanged.
结果发现所制备的纺丝原料中粉体的分散很不均匀,纺丝过程中,团聚的粉体很容易堵塞喷丝孔造成断丝。It was found that the dispersion of the powder in the prepared spinning raw material was very uneven, and the agglomerated powder could easily block the spinneret holes and cause broken filaments during the spinning process.
实施例3和对比例1所得纤维原丝的扫描电镜图如图5和图6所示,由图可看出将分散剂由PAO-S换成PEG-200后,纤维原丝中出现了粉体聚集的区域。The scanning electron micrographs of the fiber precursors obtained in Example 3 and Comparative Example 1 are shown in Figure 5 and Figure 6. It can be seen from the figures that after the dispersant is changed from PAO-S to PEG-200, powdery particles appear in the fiber precursors. area of accumulation.
表1给出了实施例及对比例的纺丝原料的陶瓷产率,可看出粉体浆料的引入可大大提高纺丝原料的陶瓷产率,对比实施例3和对比例1可看出采用PAO-S作为分散剂对提高纺丝原料的陶瓷产率是有利的。Table 1 has provided the ceramic yield of the spinning raw material of embodiment and comparative example, it can be seen that the introduction of powder slurry can greatly improve the ceramic yield of spinning raw material, it can be seen from comparative example 3 and comparative example 1 The use of PAO-S as a dispersant is beneficial to increase the ceramic yield of spinning raw materials.
表1、实施例所制备的纺丝原料的陶瓷产率The ceramic yield of the spinning raw material prepared by table 1, embodiment
对比例2Comparative example 2
为了对比本方法所制备的纤维的耐高温性能,我们将本实施例7所得的纤维与商品化的nextel-610纤维共同置于马弗炉中升温至1550℃,保温20min,对比二者的宏观及微观形貌,结果如图7a、图7b、图8a和图8b所示,如图7a、图7b可看出,本方法制备的纤维经1550℃,20min的高温处理之后(左),纤维仍较为柔韧,束丝可以承受10g的塑料环的重量,SEM图(右)显示纤维由尺寸均一的百纳米级粉体紧密堆积组成;由图8a和图8b可看出,而商品化的nextel-610纤维经1550℃,20min高温处理之后(左),纤维之间发生粘黏并丝,纤维变得非常脆,完全丧失柔韧性,SEM图(右)显示纤维有尺寸不一的纳米至微米级粉体疏松的堆积而成。该实验表明本发明所制备的纤维在耐高温性能方面较以商品化的纤维是具有优势的。In order to compare the high temperature resistance of the fibers prepared by this method, we put the fibers obtained in Example 7 and the commercialized nextel-610 fibers together in a muffle furnace to raise the temperature to 1550°C and keep the temperature for 20 minutes to compare the macroscopic and microscopic morphology, the results are shown in Figure 7a, Figure 7b, Figure 8a and Figure 8b, as can be seen from Figure 7a and Figure 7b, after the fiber prepared by this method is treated at 1550 ° C for 20 minutes (left), the fiber It is still relatively flexible, and the bundle can bear the weight of a 10g plastic ring. The SEM image (right) shows that the fiber is composed of densely packed hundreds of nanometer powders with uniform size; it can be seen from Figure 8a and Figure 8b, while the commercial nextel After the -610 fiber was treated at 1550°C for 20 minutes (left), the fibers became sticky and silky, and the fiber became very brittle and completely lost flexibility. The SEM image (right) shows that the fiber has different sizes from nanometers to micrometers. Grade powder is loosely accumulated. This experiment shows that the fiber prepared by the present invention is superior to the commercialized fiber in terms of high temperature resistance.
以上所述仅是本发明的较佳实施例而已,并非对本发明作任何形式上的限制,虽然本发明已以较佳实施例揭露如上,然而并非用以限定本发明,任何熟悉本发明的技术人员在不脱离本发明技术方案范围内,当可利用上述提示的技术内容作出些许变动或修饰为等同变化的等效实施例,但凡是未脱离本发明技术方案的内容,依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本发明方案的范围内。The above descriptions are only preferred embodiments of the present invention, and do not limit the present invention in any form. Although the present invention has been disclosed as above with preferred embodiments, it is not intended to limit the present invention. Anyone familiar with the technology of the present invention Without departing from the scope of the technical solution of the present invention, personnel can use the technical content suggested above to make some changes or modify them into equivalent embodiments with equivalent changes. Any simple modifications, equivalent changes and modifications made to the above embodiments still fall within the scope of the solutions of the present invention.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710135875.6A CN108570725B (en) | 2017-03-08 | 2017-03-08 | A kind of melt-spinning raw material of alumina continuous fiber, its preparation method and prepared alumina continuous fiber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710135875.6A CN108570725B (en) | 2017-03-08 | 2017-03-08 | A kind of melt-spinning raw material of alumina continuous fiber, its preparation method and prepared alumina continuous fiber |
Publications (2)
Publication Number | Publication Date |
---|---|
CN108570725A true CN108570725A (en) | 2018-09-25 |
CN108570725B CN108570725B (en) | 2019-08-20 |
Family
ID=63576876
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710135875.6A Active CN108570725B (en) | 2017-03-08 | 2017-03-08 | A kind of melt-spinning raw material of alumina continuous fiber, its preparation method and prepared alumina continuous fiber |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108570725B (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107904697A (en) * | 2017-11-20 | 2018-04-13 | 苏州图纳新材料科技有限公司 | The poly- aikyiaiurnirsoxan beta of solid-state, the preparation method of the poly- aikyiaiurnirsoxan beta of solid-state, alumina fibre cotton and preparation method thereof |
CN110467439A (en) * | 2019-08-02 | 2019-11-19 | 中国航发北京航空材料研究院 | The preparation method of alumina fibre enhancing porous alumina ceramic based composites |
CN110592724A (en) * | 2019-09-04 | 2019-12-20 | 中国科学院化学研究所 | A kind of Hf-Al-Si composite oxide ceramic fiber and its preparation method |
CN111733484A (en) * | 2020-07-22 | 2020-10-02 | 中国科学院化学研究所 | A kind of Al-Si complex oxide continuous ceramic fiber and preparation method thereof |
CN112409004A (en) * | 2020-11-12 | 2021-02-26 | 上海榕融新材料科技有限公司 | Preparation method of slurry for alumina continuous fiber reinforced ceramic composite material |
CN113620693A (en) * | 2021-09-09 | 2021-11-09 | 成都海鑫高科技有限公司 | Preparation method of Gamma alumina fiber |
CN113968725A (en) * | 2020-07-22 | 2022-01-25 | 中国科学院化学研究所 | Al-Zr complex phase oxide continuous ceramic fiber and preparation method thereof |
CN113968743A (en) * | 2020-07-22 | 2022-01-25 | 中国科学院化学研究所 | Al-Si co-polymerized oxide ceramic precursor and preparation method thereof |
CN115448340A (en) * | 2022-08-10 | 2022-12-09 | 杭州智华杰科技有限公司 | Method for improving thermal conductivity of aluminum oxide |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4101615A (en) * | 1973-02-20 | 1978-07-18 | Sumitomo Chemical Company, Limited | Process for producing alumina fiber or alumina-silica fiber |
JPS61225318A (en) * | 1985-03-29 | 1986-10-07 | Toyo Sutoufuaa Chem:Kk | Production of alumina fiber |
US5002750A (en) * | 1987-03-05 | 1991-03-26 | Sumitomo Chemical Company, Limited | Process for producing alumina-based fiber |
US5575964A (en) * | 1993-08-19 | 1996-11-19 | Sumitomo Chemical Company, Limited | Method for producing silica-alumina fiber |
CN101634056A (en) * | 2009-08-25 | 2010-01-27 | 西安交通大学 | Method for preparing alumina-based continuous fiber |
CN102965764A (en) * | 2012-11-13 | 2013-03-13 | 山东大学 | Preparation method of aluminum oxide ceramic continuous fiber |
CN104736494A (en) * | 2012-10-25 | 2015-06-24 | 日本电气硝子株式会社 | Glass composition for glass fibers, glass fibers, and method for producing glass fibers |
CN105754106A (en) * | 2016-01-31 | 2016-07-13 | 苏州图纳新材料科技有限公司 | Aluminum oxide ceramic precursor polymer and preparation method of aluminum oxide ceramic precursor polymer |
-
2017
- 2017-03-08 CN CN201710135875.6A patent/CN108570725B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4101615A (en) * | 1973-02-20 | 1978-07-18 | Sumitomo Chemical Company, Limited | Process for producing alumina fiber or alumina-silica fiber |
JPS61225318A (en) * | 1985-03-29 | 1986-10-07 | Toyo Sutoufuaa Chem:Kk | Production of alumina fiber |
US5002750A (en) * | 1987-03-05 | 1991-03-26 | Sumitomo Chemical Company, Limited | Process for producing alumina-based fiber |
US5575964A (en) * | 1993-08-19 | 1996-11-19 | Sumitomo Chemical Company, Limited | Method for producing silica-alumina fiber |
CN101634056A (en) * | 2009-08-25 | 2010-01-27 | 西安交通大学 | Method for preparing alumina-based continuous fiber |
CN104736494A (en) * | 2012-10-25 | 2015-06-24 | 日本电气硝子株式会社 | Glass composition for glass fibers, glass fibers, and method for producing glass fibers |
CN102965764A (en) * | 2012-11-13 | 2013-03-13 | 山东大学 | Preparation method of aluminum oxide ceramic continuous fiber |
CN105754106A (en) * | 2016-01-31 | 2016-07-13 | 苏州图纳新材料科技有限公司 | Aluminum oxide ceramic precursor polymer and preparation method of aluminum oxide ceramic precursor polymer |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107904697A (en) * | 2017-11-20 | 2018-04-13 | 苏州图纳新材料科技有限公司 | The poly- aikyiaiurnirsoxan beta of solid-state, the preparation method of the poly- aikyiaiurnirsoxan beta of solid-state, alumina fibre cotton and preparation method thereof |
CN110467439A (en) * | 2019-08-02 | 2019-11-19 | 中国航发北京航空材料研究院 | The preparation method of alumina fibre enhancing porous alumina ceramic based composites |
CN110592724A (en) * | 2019-09-04 | 2019-12-20 | 中国科学院化学研究所 | A kind of Hf-Al-Si composite oxide ceramic fiber and its preparation method |
CN113968725A (en) * | 2020-07-22 | 2022-01-25 | 中国科学院化学研究所 | Al-Zr complex phase oxide continuous ceramic fiber and preparation method thereof |
CN111733484A (en) * | 2020-07-22 | 2020-10-02 | 中国科学院化学研究所 | A kind of Al-Si complex oxide continuous ceramic fiber and preparation method thereof |
CN113968743A (en) * | 2020-07-22 | 2022-01-25 | 中国科学院化学研究所 | Al-Si co-polymerized oxide ceramic precursor and preparation method thereof |
CN113968743B (en) * | 2020-07-22 | 2022-07-12 | 中国科学院化学研究所 | A kind of Al-Si copolymerized oxide ceramic precursor and preparation method thereof |
CN113968725B (en) * | 2020-07-22 | 2022-09-16 | 中国科学院化学研究所 | Al-Zr complex phase oxide continuous ceramic fiber and preparation method thereof |
CN112409004A (en) * | 2020-11-12 | 2021-02-26 | 上海榕融新材料科技有限公司 | Preparation method of slurry for alumina continuous fiber reinforced ceramic composite material |
CN113620693A (en) * | 2021-09-09 | 2021-11-09 | 成都海鑫高科技有限公司 | Preparation method of Gamma alumina fiber |
CN113620693B (en) * | 2021-09-09 | 2022-08-23 | 成都海鑫高科技有限公司 | Preparation method of Gamma alumina fiber |
CN115448340A (en) * | 2022-08-10 | 2022-12-09 | 杭州智华杰科技有限公司 | Method for improving thermal conductivity of aluminum oxide |
CN115448340B (en) * | 2022-08-10 | 2024-06-21 | 杭州智华杰科技有限公司 | Method for improving heat conduction performance of alumina |
Also Published As
Publication number | Publication date |
---|---|
CN108570725B (en) | 2019-08-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN108570725B (en) | A kind of melt-spinning raw material of alumina continuous fiber, its preparation method and prepared alumina continuous fiber | |
CN104005115B (en) | A kind of preparation method of ceramic alumina fiber | |
CN104141181B (en) | A kind of containing SiO2the ZrO of doping2the preparation method of fiber | |
CN113502599B (en) | Flexible Y 2 Mo 3 O12/Al 2 O 3 High-temperature heat-insulation nanofiber membrane and preparation method thereof | |
CN102557628A (en) | Flexible yttrium stable zirconium oxide ceramic fiber and preparation method thereof | |
CN113502597B (en) | Flexible high-infrared-reflectivity yttrium manganate nanofiber membrane and preparation method thereof | |
CN108315838B (en) | A kind of method for preparing yttrium oxide nanofiber from yttrium polymer precursor | |
CN111995393B (en) | Method for preparing aluminum titanate ceramic fiber from titanium-aluminum polymer precursor | |
CN106048780B (en) | A kind of preparation method of alumina-based continuous fiber | |
CN113663611A (en) | A kind of high temperature resistant composite nanofiber aerogel material and preparation method thereof | |
CN106868632A (en) | A kind of method that coaxial electrostatic spinning prepares porous mullite fiber | |
CN113831581A (en) | High-elasticity anti-radiation nanofiber aerogel material and preparation method thereof | |
Wang et al. | Preparation of ultrafine flexible alumina fiber for heat insulation by the electrospinning method | |
CN110592724A (en) | A kind of Hf-Al-Si composite oxide ceramic fiber and its preparation method | |
CN115368119B (en) | Flexible aerogel of sub-crystalline alumina nanofiber and preparation method thereof | |
CN103643402B (en) | A kind of preparation method of lanthanum zirconate ceramic fiber blanket | |
CN113648940B (en) | Ultra-light high-elasticity anti-radiation nanofiber aerogel material and preparation method thereof | |
CN103757750A (en) | Preparation method of alumina-based continuous fibers | |
CN105712716A (en) | Zirconium oxide fiber ceramic plate and preparing method thereof | |
CN114702319A (en) | Super-gravity air spinning method for alumina fiber membrane and application | |
CN103757751B (en) | A kind of preparation method of super high temperature zirconia ceramic fiber | |
CN102584244A (en) | Method for preparing hexagonal phase aluminum nitride nanofiber by using electrostatic spinning and ammonia nitridation | |
CN108085786A (en) | Mullite Ceramic Fibres cotton and preparation method thereof | |
CN113968743B (en) | A kind of Al-Si copolymerized oxide ceramic precursor and preparation method thereof | |
CN117888234A (en) | Method for preparing silicon carbide ceramic fiber by combining sol-gel and dry spinning |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |