JPH0254304B2 - - Google Patents
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- Publication number
- JPH0254304B2 JPH0254304B2 JP6624283A JP6624283A JPH0254304B2 JP H0254304 B2 JPH0254304 B2 JP H0254304B2 JP 6624283 A JP6624283 A JP 6624283A JP 6624283 A JP6624283 A JP 6624283A JP H0254304 B2 JPH0254304 B2 JP H0254304B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- parts
- ceramic
- group
- premix
- 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.)
- Expired
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- 239000000919 ceramic Substances 0.000 claims description 62
- 239000006260 foam Substances 0.000 claims description 27
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 claims description 25
- 239000002994 raw material Substances 0.000 claims description 23
- 229920005862 polyol Polymers 0.000 claims description 20
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 19
- 150000003077 polyols Chemical class 0.000 claims description 19
- -1 isocyanate compound Chemical class 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 17
- 239000003431 cross linking reagent Substances 0.000 claims description 15
- 239000012948 isocyanate Substances 0.000 claims description 14
- 239000002002 slurry Substances 0.000 claims description 14
- 229920001281 polyalkylene Polymers 0.000 claims description 13
- 238000001035 drying Methods 0.000 claims description 11
- 125000000524 functional group Chemical group 0.000 claims description 11
- 238000002156 mixing Methods 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 239000004094 surface-active agent Substances 0.000 claims description 8
- 238000010304 firing Methods 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 26
- 238000000034 method Methods 0.000 description 12
- 229920002635 polyurethane Polymers 0.000 description 11
- 239000004814 polyurethane Substances 0.000 description 11
- 239000003054 catalyst Substances 0.000 description 6
- UPMLOUAZCHDJJD-UHFFFAOYSA-N 4,4'-Diphenylmethane Diisocyanate Chemical compound C1=CC(N=C=O)=CC=C1CC1=CC=C(N=C=O)C=C1 UPMLOUAZCHDJJD-UHFFFAOYSA-N 0.000 description 5
- 239000005995 Aluminium silicate Substances 0.000 description 5
- 235000012211 aluminium silicate Nutrition 0.000 description 5
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 5
- 229920001451 polypropylene glycol Polymers 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 4
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 3
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 3
- 230000002159 abnormal effect Effects 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 239000004927 clay Substances 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- JXCHMDATRWUOAP-UHFFFAOYSA-N diisocyanatomethylbenzene Chemical compound O=C=NC(N=C=O)C1=CC=CC=C1 JXCHMDATRWUOAP-UHFFFAOYSA-N 0.000 description 3
- 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 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000002209 hydrophobic effect Effects 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 229910052863 mullite Inorganic materials 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- BFIAIMMAHAIVFT-UHFFFAOYSA-N 1-[bis(2-hydroxybutyl)amino]butan-2-ol Chemical compound CCC(O)CN(CC(O)CC)CC(O)CC BFIAIMMAHAIVFT-UHFFFAOYSA-N 0.000 description 2
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 229920005830 Polyurethane Foam Polymers 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- ZJCCRDAZUWHFQH-UHFFFAOYSA-N Trimethylolpropane Chemical compound CCC(CO)(CO)CO ZJCCRDAZUWHFQH-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 229910010293 ceramic material Inorganic materials 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000010433 feldspar Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229920001296 polysiloxane Polymers 0.000 description 2
- 239000011496 polyurethane foam Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- FQENQNTWSFEDLI-UHFFFAOYSA-J sodium diphosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])([O-])=O FQENQNTWSFEDLI-UHFFFAOYSA-J 0.000 description 2
- 235000019982 sodium hexametaphosphate Nutrition 0.000 description 2
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 description 2
- 229940048086 sodium pyrophosphate Drugs 0.000 description 2
- 239000000454 talc Substances 0.000 description 2
- 229910052623 talc Inorganic materials 0.000 description 2
- 235000019818 tetrasodium diphosphate Nutrition 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- XFNJVJPLKCPIBV-UHFFFAOYSA-N trimethylenediamine Chemical compound NCCCN XFNJVJPLKCPIBV-UHFFFAOYSA-N 0.000 description 2
- TUSDEZXZIZRFGC-UHFFFAOYSA-N 1-O-galloyl-3,6-(R)-HHDP-beta-D-glucose Natural products OC1C(O2)COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC1C(O)C2OC(=O)C1=CC(O)=C(O)C(O)=C1 TUSDEZXZIZRFGC-UHFFFAOYSA-N 0.000 description 1
- 239000004604 Blowing Agent Substances 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- 239000001263 FEMA 3042 Substances 0.000 description 1
- 239000005058 Isophorone diisocyanate Substances 0.000 description 1
- LRBQNJMCXXYXIU-PPKXGCFTSA-N Penta-digallate-beta-D-glucose Natural products OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-PPKXGCFTSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000012975 dibutyltin dilaurate Substances 0.000 description 1
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 1
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 1
- 239000004205 dimethyl polysiloxane Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- NIMLQBUJDJZYEJ-UHFFFAOYSA-N isophorone diisocyanate Chemical compound CC1(C)CC(N=C=O)CC(C)(CN=C=O)C1 NIMLQBUJDJZYEJ-UHFFFAOYSA-N 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000005056 polyisocyanate Substances 0.000 description 1
- 229920001228 polyisocyanate Polymers 0.000 description 1
- 229920005749 polyurethane resin Polymers 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 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
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- LRBQNJMCXXYXIU-NRMVVENXSA-N tannic acid Chemical compound OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-NRMVVENXSA-N 0.000 description 1
- 229920002258 tannic acid Polymers 0.000 description 1
- 229940033123 tannic acid Drugs 0.000 description 1
- 235000015523 tannic acid Nutrition 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
- DVKJHBMWWAPEIU-UHFFFAOYSA-N toluene 2,4-diisocyanate Chemical compound CC1=CC=C(N=C=O)C=C1N=C=O DVKJHBMWWAPEIU-UHFFFAOYSA-N 0.000 description 1
- 150000003673 urethanes Chemical class 0.000 description 1
- 229910052845 zircon Inorganic materials 0.000 description 1
- GFQYVLUOOAAOGM-UHFFFAOYSA-N zirconium(iv) silicate Chemical compound [Zr+4].[O-][Si]([O-])([O-])[O-] GFQYVLUOOAAOGM-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Filtering Materials (AREA)
- Polyurethanes Or Polyureas (AREA)
Description
【発明の詳細な説明】
この発明はセラミツク多孔体の製造法に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing porous ceramic bodies.
セラミツク原料を混合したポリウレタン発泡体
を焼成して、ポリウレタンを除去するとともにセ
ラミツク原料を焼結させてセラミツク多孔体を製
造する方法が知られており、このセラミツク多孔
体は、耐食性、耐熱性、強度などの性質が優れて
いるので、材、イオン交換樹脂、隔膜、吸着
材、触媒担体、もしくは耐火煉瓦、耐熱材、建築
材などの多方面の用途に利用されている。 A method is known in which a ceramic porous body is manufactured by firing a polyurethane foam mixed with ceramic raw materials to remove the polyurethane and sintering the ceramic raw materials.This ceramic porous body has excellent corrosion resistance, heat resistance, and strength. Because of their excellent properties, they are used in a wide variety of applications, including materials, ion exchange resins, diaphragms, adsorbents, catalyst carriers, firebricks, heat-resistant materials, and construction materials.
従来のセラミツク多孔体の製造法の一例を説明
すると、セラミツク原料に水を加えた泥状セラミ
ツクに、エチレンオキシド・プロピレンオキシド
共重合体と末端に2個以上のイソシアネート基を
有するポリイソシアネート化合物とを反応させて
得られる親水性ウレタンプレポリマーを混合し、
この混合組成液を型に注入して反応発泡させたの
ち、該ウレタン発泡体を乾燥、焼成する多孔質セ
ラミツク成型品の製造法(特開昭56−145153号公
報参照)が知られており、この方法はプレポリマ
ー法といわれている。このプレポリマー法は、セ
ラミツク原料に多量の水が混合されて、型内で反
応発泡されたウレタン発泡体には多量の水が存在
する。従つてこの水を乾燥によつて除去する際
に、水の蒸発に伴つてウレタン発泡体が極度に収
縮し、ウレタン発泡体に歪や反りを生ずる。従つ
て焼成後のセラミツク多孔体の形状もよくない。 An example of a conventional method for manufacturing a ceramic porous body is to react an ethylene oxide/propylene oxide copolymer and a polyisocyanate compound having two or more isocyanate groups at the end with a ceramic mud made by adding water to a ceramic raw material. Mix the hydrophilic urethane prepolymer obtained by
A method for manufacturing a porous ceramic molded product is known (see Japanese Patent Laid-Open No. 145153/1983), in which this mixed composition liquid is injected into a mold, reacted and foamed, and then the urethane foam is dried and fired. This method is called the prepolymer method. In this prepolymer method, a large amount of water is mixed with the ceramic raw material, and a large amount of water is present in the urethane foam that is reacted and foamed in the mold. Therefore, when this water is removed by drying, the urethane foam shrinks extremely as the water evaporates, causing distortion and warpage in the urethane foam. Therefore, the shape of the ceramic porous body after firing is also not good.
またセラミツク多孔体の他の製造法として、セ
ラミツク原料と、分子中に活性水素原子を2個以
上有するポリオール化合物と、発泡剤と、水とを
混合撹拌した混合液に、有機イソシアネート化合
物を添加混合した組成液を型内で発泡させてウレ
タン発泡体を成型したのち、該ウレタン発泡体を
乾燥、焼成する製造法(特開昭55−71659号公報
参照)が知られており、この方法は一段法(ワン
シヨツト法)といわれている。この一段法は、上
記プレポリマー法に比べて乾燥時の収縮率は小さ
いが、ポリウレタン樹脂量が多く、そのため焼成
が困難であり、また比重の小さい軽量のものしか
生成されず、かつコストが高くなる。 In addition, as another method for manufacturing porous ceramic materials, an organic isocyanate compound is added to a mixed solution of a ceramic raw material, a polyol compound having two or more active hydrogen atoms in the molecule, a blowing agent, and water. A manufacturing method is known in which a composition liquid is foamed in a mold to form a urethane foam, and then the urethane foam is dried and fired (see JP-A-55-71659). It is called the one-shot method. This one-stage method has a smaller shrinkage rate during drying than the prepolymer method described above, but the amount of polyurethane resin is large, which makes firing difficult, and only lightweight products with low specific gravity are produced, and the cost is high. Become.
セラミツク多孔体は、その用途によつては高度
の寸法安定性が要求される。セラミツク多孔体の
寸法安定性を阻害するのは、ウレタン発泡体の乾
燥時の収縮性と、乾燥したウレタン発泡体の焼成
時の収縮性とに因るものであるが、両者の収縮性
には相関性があるとみられるので、乾燥時の収縮
抑制することによつて焼成時の収縮性も相当抑制
されると考えられている。 Porous ceramic bodies are required to have a high degree of dimensional stability depending on their use. The dimensional stability of porous ceramics is inhibited by the shrinkage of the urethane foam during drying and the shrinkage of the dried urethane foam during firing. Since there appears to be a correlation, it is thought that by suppressing shrinkage during drying, shrinkage during firing will also be considerably suppressed.
乾燥時の熱収縮性は、セラミツク原料に混合す
る水の量が多いほど大きくなるので、熱収縮を小
さくするには水の添加量を抑制することにある
が、水の添加量を余り小さくすると組成物の混合
反応が均一とならず、また型による成型も円滑に
進まないという欠点がある。 Heat shrinkage during drying increases as the amount of water mixed into the ceramic raw material increases, so the best way to reduce heat shrinkage is to suppress the amount of water added, but if the amount of water added is too small, There are disadvantages in that the mixing reaction of the composition is not uniform and the molding with a mold does not proceed smoothly.
この発明は、上記の問題を解決するために、各
原料成分の配合順序と配合割合を変更したもので
ある。 In order to solve the above-mentioned problems, this invention changes the blending order and blending ratio of each raw material component.
すなわちこの発明は、(a)2個以上のOH基をも
つ平均分子量3000〜10000のポリアルキレンポリ
オールと、(b)2個以上のNCO基をもつ有機イソ
シアネート化合物とをOH基/NCO基のモル比が
0.01〜0.5の割合で混合したプレミツクスを製造
し、一方、(c)2個以上の官能基をもつ架橋剤と、
水系セラミツクスラリーとを、上記(b)有機イソシ
アネート化合物のNCO基に対する(c)架橋剤の官
能基のモル比が0.29〜7.5の割合で混合して泥状
セラミツクを製造し、上記プレミツクスと泥状セ
ラミツクとを、上記(a)、(b)、(c)成分の総重量がセ
ラミツク原料100重量部に対して10〜35重量部の
割合になるように配合し、この配合組成液を型に
注入して反応発泡させたのち、該ウレタン発泡体
を乾燥、焼成することを特徴とするセラミツク多
孔体の製造法である。 In other words, this invention combines (a) a polyalkylene polyol with an average molecular weight of 3,000 to 10,000 having two or more OH groups, and (b) an organic isocyanate compound having two or more NCO groups, in a molar ratio of OH groups/NCO groups. The ratio is
(c) a crosslinking agent having two or more functional groups;
Aqueous ceramic slurry is mixed with the above premix at a molar ratio of the functional group of the crosslinking agent (c) to the NCO group of the organic isocyanate compound of (b) from 0.29 to 7.5, and the premix and the slurry are mixed together. Ceramic is blended so that the total weight of the above components (a), (b), and (c) is 10 to 35 parts by weight based on 100 parts by weight of the ceramic raw material, and this blended composition liquid is molded. This is a method for producing a porous ceramic body, which is characterized in that the urethane foam is injected, reacted and foamed, and then dried and fired.
この発明に使用される(a)成分のポリアルキレン
ポリオールは、グリセリン、トリメチロールプロ
パン、ペンタエリスリトールなどを開始剤とし
て、プロピレンオキシドを付加させ、好ましくは
更に一部にエチレンオキシドを付加した官能基数
2以上で、平均分子量が3000〜10000、好ましく
は5000〜7000の通常の疎水性ポリオールである。
ポリアルキレンポリオールの平均分子量が3000未
満では成形されたウレタン発泡体の強度が弱く、
型からの離型が困難となり、平均分子量が10000
を越えると粘度が高く、またOH当量が低いので
離型が困難である。 The polyalkylene polyol as component (a) used in this invention is prepared by adding propylene oxide using glycerin, trimethylolpropane, pentaerythritol, etc. as an initiator, and preferably having 2 or more functional groups to which ethylene oxide is added to a part of the polyalkylene polyol. It is a conventional hydrophobic polyol having an average molecular weight of 3,000 to 10,000, preferably 5,000 to 7,000.
If the average molecular weight of the polyalkylene polyol is less than 3000, the strength of the molded urethane foam will be low;
It becomes difficult to release from the mold, and the average molecular weight is 10,000.
If it exceeds 50%, the viscosity is high and the OH equivalent is low, making it difficult to release from the mold.
上記(a)ポリアルキレンポリオールに混合される
(b)成分の有機イソシアネート化合物は2個以上の
NCO基を有し、常温で液状のものであり、トル
イレンジイソシアネート(TDI)、ジフエニルメ
タンジイソシアネート(MDI)、イソホロンジイ
ソシアネートなどの芳香族基を有するものが好ま
しい。 Mixed with the above (a) polyalkylene polyol
The organic isocyanate compound of component (b) contains two or more
Those having an NCO group, being liquid at room temperature, and having an aromatic group such as toluylene diisocyanate (TDI), diphenylmethane diisocyanate (MDI), and isophorone diisocyanate are preferred.
水系セラミツクスラリーに混合される(c)架橋剤
は、末端に2個以上のOH基、NH2基などの官能
基を有し、水溶性あるいは水に分散性可能なもの
であり、ジエタノールアミン、トリエタノールア
ミン、トリブタノールアミン、トリメチロールプ
ロパン、グリセリン、トリメチレンジアミン、エ
チレングリコール、ジエチレングリコールなどが
例示される。 The crosslinking agent (c) mixed into the aqueous ceramic slurry has two or more functional groups such as OH groups and NH 2 groups at its terminals, is water-soluble or water-dispersible, and has diethanolamine, triethanolamine, etc. Examples include ethanolamine, tributanolamine, trimethylolpropane, glycerin, trimethylenediamine, ethylene glycol, diethylene glycol, and the like.
セラミツク原料は、高温に加熱することによつ
て一般に焼結体となり得るものであつて、カオリ
ン、粘土類、シリカ、アルミナ、長石、陶石、ム
ライト、ジルコン、ジルコニア、チタニア、炭化
珪素、コージライトなどが例示され、またこれら
各種の原料を混合したものである。 Ceramic raw materials can generally be turned into sintered bodies by heating to high temperatures, and include kaolin, clays, silica, alumina, feldspar, pottery stone, mullite, zircon, zirconia, titania, silicon carbide, and cordierite. For example, it is a mixture of these various raw materials.
セラミツク原料に添加される水の量は、セラミ
ツク100重量部に対して10〜100重量部、好ましく
は30〜60重量部であつて、水系セラミツクスラリ
ーがプレミツクスと混合できる程度に少ない方が
好ましい。水量が10重量部未満では粘度が高くな
つて成型が困難となり、100重量部を越えると、
ポリウレタンの量がセラミツク原料と水との総量
に比べて少なくなり、ポリウレタンが希釈され過
ぎて成型されたウレタン発泡体の強度が低下し、
離型が困難となると共に、ウレタン発泡体の乾燥
時の熱収縮性が大きくなる。なおこの水系セラミ
ツクスラリーには、一般窯業関係で利用されるピ
ロリン酸ソーダ、炭酸ソーダなどの解こう剤や、
タンニン酸、リグニンなどの保護コロイドを添加
する場合があり、これらの添加量はそれぞれ0.01
〜0.1重量部が好ましい。 The amount of water added to the ceramic raw material is 10 to 100 parts by weight, preferably 30 to 60 parts by weight, based on 100 parts by weight of the ceramic, and is preferably as small as possible to mix the aqueous ceramic slurry with the premix. If the amount of water is less than 10 parts by weight, the viscosity becomes high and molding becomes difficult, and if it exceeds 100 parts by weight,
The amount of polyurethane becomes smaller than the total amount of ceramic raw materials and water, and the polyurethane becomes too diluted, reducing the strength of the molded urethane foam.
It becomes difficult to release the mold and the heat shrinkage of the urethane foam increases when drying. This aqueous ceramic slurry contains peptizers such as sodium pyrophosphate and soda carbonate, which are used in the general ceramics industry.
Protective colloids such as tannic acid and lignin may be added, and the amount of each added is 0.01
~0.1 part by weight is preferred.
この発明の特徴とすることは、上記原料の配合
順序とその配合割合である。 The characteristics of this invention are the mixing order of the above-mentioned raw materials and their mixing ratios.
上記(a)ポリアルキレンポリオールと(b)有機イソ
シアネート化合物とを混合してプレミツクスを製
造する時の配合割合は、(b)有機イソシアネートの
NCO基に対する(a)ポリアルキレンポリオールの
OH基のモル比、OH基/NCO基=0.01〜0.5、好
ましくは0.02〜0.1である。このOH基/NCO基モ
ル比が0.01未満であると、ポリオール含有量が小
さいためにプレミツクスと水との分散が悪くなつ
て円滑に反応が進行し難く、また過剰量のNCO
基は2個以上の官能基を有する架橋剤や水とさき
に反応するために生成した発泡体はもろく、発泡
体として必要な強度、弾性を有する高分子化反応
は起こらない。OH基/NCO基モル比が0.5を越
えると、ポリオール含有量が多くなり過ぎるため
にポリオール成分とイソシアネート成分との反応
が緩慢になり、またポリオール成分が多い分だけ
架橋剤の添加量が少なくなり高分子化反応が不十
分で固化しない。 When producing a premix by mixing the above (a) polyalkylene polyol and (b) organic isocyanate compound, the blending ratio is as follows:
(a) Polyalkylene polyol to NCO group
The molar ratio of OH groups, OH groups/NCO groups, is 0.01 to 0.5, preferably 0.02 to 0.1. If the OH group/NCO group molar ratio is less than 0.01, the polyol content will be small and the dispersion between the premix and water will be poor, making it difficult for the reaction to proceed smoothly, and an excessive amount of NCO
Since the group reacts with a crosslinking agent having two or more functional groups or with water, the resulting foam is brittle and does not undergo a polymerization reaction to have the strength and elasticity required for a foam. When the OH group/NCO group molar ratio exceeds 0.5, the polyol content becomes too large and the reaction between the polyol component and the isocyanate component becomes slow, and the amount of crosslinking agent added decreases as the polyol component increases. Polymerization reaction is insufficient and solidification does not occur.
次に、セラミツク原料に水を混合したセラミツ
クスラリーに混合される(c)架橋剤の添加量は、(b)
有機イソシアネート化合物との量比によつて左右
され、(b)有機イソシアネート化合物のNCO基に
対する(c)架橋剤の官能基(OH基で代表させる)
のモル比、OH基/NCO基=0.29〜7.5、好ましく
は0.5〜4.0である。このOH基/NCO基モル比が
0.29未満の場合は、架橋剤が少ないために高分子
化が不十分で固化性が劣る。なおこの場合、水が
架橋剤として作用する筈であるが、実際的には固
化が悪く、この理由はつまびらかでないが、発泡
とゲル化とのバランスの問題ではないかと考えら
れる。またOH基/NCO基モル比が7.5を越える
場合は、ポリオールが少ないために、生成したポ
リウレタンのハードセグメントが中心となるた
め、固まりにくくなるかまたはボロボロしたもの
しかできなくなる。 Next, the amount of crosslinking agent (c) added to the ceramic slurry, which is a mixture of ceramic raw materials and water, is (b)
It depends on the amount ratio of (b) the NCO group of the organic isocyanate compound to the (c) functional group of the crosslinking agent (represented by the OH group).
The molar ratio of OH group/NCO group is 0.29 to 7.5, preferably 0.5 to 4.0. This OH group/NCO group molar ratio is
If it is less than 0.29, the amount of crosslinking agent is small, resulting in insufficient polymerization and poor solidification. In this case, water is supposed to act as a crosslinking agent, but in reality solidification is poor, and although the reason for this is not clear, it is thought to be a problem in the balance between foaming and gelation. If the molar ratio of OH group/NCO group exceeds 7.5, the hard segments of the produced polyurethane will be the main focus due to the small amount of polyol, making it difficult to solidify or only crumbly products will be produced.
次いで上記のプレミツクスと、架橋剤を含有し
た泥状セラミツクとを混合した組成液を型内で反
応硬化させるのであるが、この組成液中の(a)ポリ
アルキレンポリオール、(b)有機イソシアネート化
合物および(c)架橋剤からなるポリウレタン成分の
総重量は、セラミツク原料100重量部に対して5
〜40重量部である。ポリウレタン成分量が5重量
部未満であるとポリウレタン成分が少な過ぎて硬
化せず、また40重量部を越えるとポリウレタン量
が多くなり過ぎるため、焼結されたセラミツク多
孔体の比重が小さくなり過ぎ、強度が低くなり、
かつコスト高となる。 Next, a composition solution in which the above premix and mud-like ceramic containing a crosslinking agent are mixed is reacted and cured in a mold, and (a) polyalkylene polyol, (b) organic isocyanate compound and (c) The total weight of the polyurethane component consisting of the crosslinking agent is 5 parts by weight based on 100 parts by weight of the ceramic raw material.
~40 parts by weight. If the amount of polyurethane component is less than 5 parts by weight, there will be too little polyurethane component and it will not harden, and if it exceeds 40 parts by weight, the amount of polyurethane will be too large, and the specific gravity of the sintered ceramic porous body will become too small. The strength decreases,
Moreover, the cost is high.
上記プレミツクス製造に際して界面活性剤を添
加することが好ましい。界面活性剤としては、ポ
リジメチルシロキサン・ポリオキシアルキレン共
重合体が好適であり、界面活性剤の添加量は(a)ポ
リアルキレンポリオールと(b)有機イソシアネート
化合物との総量に対して1〜20重量部が好まし
い。1重量部未満では、プレミツクスの水に対す
る分散性が悪く、見掛け上はポリウレタン量を多
くしないと泥状セラミツクが硬化しなくなる。ま
た20重量部以上ではコスト高となる。 It is preferable to add a surfactant during the production of the above premix. As the surfactant, polydimethylsiloxane/polyoxyalkylene copolymer is suitable, and the amount of surfactant added is 1 to 20% based on the total amount of (a) polyalkylene polyol and (b) organic isocyanate compound. Parts by weight are preferred. If the amount is less than 1 part by weight, the premix has poor dispersibility in water, and it appears that the ceramic slurry will not harden unless the amount of polyurethane is increased. Moreover, if it exceeds 20 parts by weight, the cost will be high.
架橋剤とセラミツクスラリーとを混合した泥状
セラミツクには、触媒を添加することができ、ア
ミン系触媒として、N−アルキルモルホリン、
1,8ジアゾシクロ〔5,4,0〕ウンデカセン
(DBU)、トリメチルアミン、エチレンジアミン
等があげられ、すず系触媒としては、ジブチルチ
ンジラウレート等があげられ、これらの触媒は併
用してもよい。 A catalyst can be added to the ceramic mud prepared by mixing the crosslinking agent and the ceramic slurry, and N-alkylmorpholine, N-alkylmorpholine,
Examples include 1,8 diazocyclo[5,4,0]undecacene (DBU), trimethylamine, ethylenediamine, etc. Examples of the tin-based catalyst include dibutyltin dilaurate, and these catalysts may be used in combination.
上記に説明したプレミツクスと泥状セラミツク
とを混合して十分に撹拌した混合組成液は、型に
注入され、型内で反応、発泡させてウレタン発泡
体を得る。型内での反応は常温〜50℃、3〜5分
で行なわれる。 A mixed composition liquid obtained by mixing the premix and mud ceramic described above and thoroughly stirring the mixture is poured into a mold, and is reacted and foamed in the mold to obtain a urethane foam. The reaction in the mold is carried out at room temperature to 50°C for 3 to 5 minutes.
型内で成型されたウレタン発泡体は、型から取
り出したのち、80〜100℃、15〜24時間乾燥して
ウレタン発泡体に含有する水分を除去する。次い
で、乾燥されたウレタン発泡体は、高温の加熱炉
中で加熱される。この加熱は、ポリウレタンの熱
分解とセラミツク原料の焼結を行なうものであ
り、前者の工程は常温から400℃の範囲に上昇さ
れて行なわれ、その間にポリウレタンが除々に酸
化分解するか、もしくは酸素が不十分な雰囲気で
の熱分解が生じ、また後者の工程はセラミツク原
料によつて異なるが通常1100℃以上の温度にて行
なわれる。焼結後は、除々に放冷したのち加熱炉
から取り出す。 The urethane foam molded in the mold is removed from the mold and then dried at 80 to 100°C for 15 to 24 hours to remove moisture contained in the urethane foam. The dried urethane foam is then heated in a high temperature furnace. This heating is to thermally decompose the polyurethane and sinter the ceramic raw material. The former process is carried out at a temperature in the range of 400°C from room temperature, during which time the polyurethane gradually oxidizes and decomposes or is exposed to oxygen. Thermal decomposition occurs in an insufficient atmosphere, and the latter step is usually carried out at temperatures above 1100°C, although this varies depending on the ceramic raw material. After sintering, it is allowed to cool down gradually and then taken out from the heating furnace.
以下にこの発明の実施例を説明する。 Examples of the present invention will be described below.
実施例 1
合成ムライト50重量部、木節粘土10重量部、カ
オリン20重量部、タルク20重量部のセラミツク原
料に、水40重量部、トリブタノールアミン4部
(架橋剤)、ヘキサメタリン酸ナトリウム0.1重量
部、触媒(商品名U−cat2600、サンアボツト社
製)0.5重量部を加えて泥状セラミツクとする。
一方、クルードMDI5重量部、ポリプロピレング
リコール(平均分子量6000、官能基数3個)3重
量部、界面活性剤(商品名Y−6827、日本ユニカ
社製)1重量部を混合し、この混合物を上記泥状
セラミツクに混合撹拌し、型内へ注入する。型内
で固化し、脱型後のウレタン発泡体は、熱風循環
乾燥機にて80℃、12時間乾燥後の収縮率が2〜3
%であつて寸法安定性が優れたものであつた。こ
の乾燥体を焼成用ガス炉で12時間、1350℃に昇温
し、更に1時間保持したのち冷却して取り出し
た。得られたセラミツク多孔体はひび割れもな
く、大きな強度を有している。Example 1 Ceramic raw materials of 50 parts by weight of synthetic mullite, 10 parts by weight of Kibushi clay, 20 parts by weight of kaolin, and 20 parts by weight of talc, 40 parts by weight of water, 4 parts of tributanolamine (crosslinking agent), and 0.1 parts by weight of sodium hexametaphosphate. and 0.5 parts by weight of a catalyst (trade name: U-cat2600, manufactured by Sunabott Co., Ltd.) to form a mud-like ceramic.
On the other hand, 5 parts by weight of crude MDI, 3 parts by weight of polypropylene glycol (average molecular weight 6000, number of functional groups 3), and 1 part by weight of a surfactant (trade name Y-6827, manufactured by Nippon Unica Co., Ltd.) were mixed, and this mixture was added to the above slurry. Mix and stir the ceramic material and pour it into the mold. The urethane foam solidified in the mold and removed from the mold has a shrinkage rate of 2 to 3 after drying at 80℃ for 12 hours in a hot air circulation dryer.
% and had excellent dimensional stability. This dried body was heated to 1350° C. for 12 hours in a firing gas furnace, held for an additional hour, cooled, and taken out. The obtained ceramic porous body has no cracks and has high strength.
なお、プレミツクス中の(a)成分OH基/(b)成分
NCO基は0.07、(c)成分OH基/(b)成分NCO基は
2.43、セラミツク原料100部に対する(a)+(b)+(c)
量は12部である。 In addition, the (a) component OH group/(b) component in the premix
NCO group is 0.07, (c) component OH group/(b) component NCO group is
2.43, (a) + (b) + (c) for 100 parts of ceramic raw material
The quantity is 12 parts.
実施例 2
アルミナ(平均粒径5ミクロン)66重量部、ア
ルミナ(平均粒径0.5ミクロン)28重量部、カオ
リン30重量部、炭酸マグネシウム0.5重量部、炭
酸カルシウム2.5重量部に、水45重量部、トリエ
タノールアミン5重量部を加えて泥状セラミツク
とする。あらかじめ、TDI13.6重量部、ポリプロ
ピレングリコール(平均分子量5000、官能基数3
個)5重量部、界面活性剤(商品名SF−8428、
東レシリコーン社製)0.5重量部を混合したプレ
ミツクスに、上記泥状セラミツクを混合撹拌して
モールド内に注入した。上記実施例1と同様に型
から取り出し、乾燥したのちの収縮率は4%であ
つて異常なソリは見られなかつた。この乾燥物を
ガス炉で20時間で1700℃にまで昇温し、2時間保
持したのち冷却した。焼結されたセラミツク多孔
体は、ヒビ割れやソリは見られなかつた。Example 2 66 parts by weight of alumina (average particle size: 5 microns), 28 parts by weight of alumina (average particle size: 0.5 microns), 30 parts by weight of kaolin, 0.5 parts by weight of magnesium carbonate, 2.5 parts by weight of calcium carbonate, 45 parts by weight of water, Add 5 parts by weight of triethanolamine to form a ceramic slurry. In advance, 13.6 parts by weight of TDI, polypropylene glycol (average molecular weight 5000, number of functional groups 3)
) 5 parts by weight, surfactant (trade name SF-8428,
The slurry ceramic was mixed and stirred into a premix containing 0.5 parts by weight of Toray Silicone Co., Ltd.) and poured into a mold. After being removed from the mold and dried in the same manner as in Example 1, the shrinkage rate was 4% and no abnormal warpage was observed. The temperature of this dried product was raised to 1700° C. over 20 hours in a gas furnace, maintained for 2 hours, and then cooled. No cracks or warpage were observed in the sintered ceramic porous body.
なお、プレミツクス中の(a)成分OH基/(b)成分
NCO基は0.02、(c)成分OH基/(b)成分NCO基は
0.7、セラミツク原料100部に対する(a)+(b)+(c)量
は23.6部であつた。 In addition, the (a) component OH group/(b) component in the premix
NCO group is 0.02, (c) component OH group / (b) component NCO group is
0.7, and the amount of (a) + (b) + (c) was 23.6 parts with respect to 100 parts of ceramic raw material.
実施例 3
カオリン20重量部、長石40重量部、抗火石30重
量部、木節粘土10重量部の混合セラミツクに、水
50重量部、ピロリン酸ナトリウム0.05重量部、ト
リエタノールアミン5重量部を加えて泥状セラミ
ツクとする。一方、クルードMDI6重量部、ポリ
プロピレングリコール(平均分子量7000、官能基
数平均2.5個)2.8重量部、界面活性剤(商品名
PRX−607、東レシリコーン社製)1.5重量部を
混合したプレミツクスに、上記泥状セラミツクを
混合撹拌して実施例1と同様にしてポリウレタン
発泡体の乾燥物を得た。この乾燥物の収縮率は3
%であり、異常なソリの発生は見られなかつた。Example 3 Water was added to a ceramic mixture of 20 parts by weight of kaolin, 40 parts by weight of feldspar, 30 parts by weight of anti-firestone, and 10 parts by weight of Kibushi clay.
Add 50 parts by weight, 0.05 parts by weight of sodium pyrophosphate, and 5 parts by weight of triethanolamine to form a mud-like ceramic. On the other hand, 6 parts by weight of crude MDI, 2.8 parts by weight of polypropylene glycol (average molecular weight 7000, average number of functional groups 2.5), surfactant (trade name
A dried polyurethane foam was obtained in the same manner as in Example 1 by mixing and stirring the slurry ceramic into a premix containing 1.5 parts by weight of PRX-607 (manufactured by Toray Silicone Co., Ltd.). The shrinkage rate of this dry product is 3
%, and no abnormal warpage was observed.
なお、プレミツクス中の(a)成分OH基/(b)成分
NCO基は0.04、(c)成分OH基/(b)成分NCO基は
4、セラミツク原料100部に対する(a)+(b)+(c)量
は13.8部であつた。 In addition, the (a) component OH group/(b) component in the premix
The NCO group was 0.04, the component (c) OH group/(b) component NCO group was 4, and the amount of (a)+(b)+(c) was 13.8 parts based on 100 parts of the ceramic raw material.
比較例 1
上記実施例1において、クルードMDI、ポリ
プロピレングリコール、界面活性剤、触媒などを
あらかじめ混合しないで、別々にかつ同時に泥状
セラミツクに混合、撹拌したが、全く硬化しなか
つた。Comparative Example 1 In Example 1, the crude MDI, polypropylene glycol, surfactant, catalyst, etc. were mixed separately and simultaneously into the ceramic mud and stirred without being mixed in advance, but the mixture did not harden at all.
比較例 2
合成ムライト50重量部、木節粘土10重量部、カ
オリン20重量部、タルク20重量部のセラミツク原
料に、水40重量部、ヘキサメタリン酸ナトリウム
0.1重量部、親水性ウレタンプレポリマー(トリ
レンジイソシアネート2.5モルと、エチレンオキ
シドを90%含む平均分子量5000のポリエチレン・
ポリプロピレングリコール1モルとの反応生成
物)15重量部を混合反応させ、型内に注入成形し
た。このウレタン発泡体の実施例1と同様の乾燥
収縮率は13%であり、四隅には異常な収縮がみら
れた。Comparative Example 2 Ceramic raw materials of 50 parts by weight of synthetic mullite, 10 parts by weight of Kibushi clay, 20 parts by weight of kaolin, and 20 parts by weight of talc, 40 parts by weight of water, and sodium hexametaphosphate.
0.1 part by weight, hydrophilic urethane prepolymer (polyethylene with an average molecular weight of 5000 containing 2.5 mol of tolylene diisocyanate and 90% ethylene oxide).
15 parts by weight of the reaction product with 1 mol of polypropylene glycol were mixed and reacted, and injection molded into a mold. The drying shrinkage rate of this urethane foam, similar to that of Example 1, was 13%, and abnormal shrinkage was observed at the four corners.
この発明の方法によれば、ポリアルキレンポリ
オールと有機イソシアネート化合物とは疎水性で
あるために、泥状セラミツクとプレミツクスとを
混合したときに、プレミツクスは泥状セラミツク
中の水と反応しないために粘度上昇が少ないので
泥状セラミツク中の水の添加量を少なくすること
ができる。なお従来の親水性プレポリマー法では
プレミツクスが親水性であり、かつ組成物の粘度
上昇が著しいので水の添加量を多くする必要があ
る。またこの発明ではポリアルキレンポリオール
と有機イソシアネート化合物とは、プレミツクス
中で分子的単位で接触しているので反応し易く、
反応によつて直ちに高分子化して樹脂が生成する
のでウレタン発泡体成型に要するウレタン樹脂量
が少なくてすむ。さらにこの発明では、疎水性の
ウレタン発泡体を利用するものであるため、ウレ
タン発泡体の水による膨潤がなく、そのためウレ
タン発泡体の乾燥時の収縮率が小さく、ソリなど
の発生がない。さらにまたこの発明は、水系セラ
ミツクスラリーに使用する水の添加量が少なくて
よいので、ウレタン発泡体の乾燥に要するエネル
ギーと時間が節減できて経済的となる。 According to the method of this invention, since the polyalkylene polyol and the organic isocyanate compound are hydrophobic, when the mud-like ceramic and the premix are mixed, the premix does not react with the water in the mud-like ceramic, so that the viscosity increases. Since the rise is small, the amount of water added to the muddy ceramic can be reduced. In the conventional hydrophilic prepolymer method, the premix is hydrophilic and the viscosity of the composition increases significantly, so it is necessary to add a large amount of water. In addition, in this invention, the polyalkylene polyol and the organic isocyanate compound are in contact with each other in molecular units in the premix, so they easily react.
Since the resin is immediately polymerized by the reaction, the amount of urethane resin required for molding the urethane foam can be small. Furthermore, since the present invention uses a hydrophobic urethane foam, the urethane foam does not swell with water, so the shrinkage rate of the urethane foam when drying is small, and warpage does not occur. Furthermore, since the present invention requires only a small amount of water to be added to the aqueous ceramic slurry, the energy and time required for drying the urethane foam can be saved, making it economical.
Claims (1)
10000のポリアルキレンポリオールと、(b)2個以
上のNCO基をもつ有機イソシアネート化合物と
をOH基/NCO基モル比が0.01〜0.5の割合で混合
したプレミツクスを製造し、一方、(c)2個以上の
官能基をもつ架橋剤と、水系セラミツクスラリー
とを、上記(b)有機イソシアネート化合物のNCO
基に対する(c)架橋剤の官能基のモル比が0.29〜
7.5の割合で混合して泥状セラミツクを製造し、
上記プレミツクスと泥状セラミツクとを、上記
(a)、(b)、(c)成分の総重量がセラミツク原料100重
量部に対して10〜35重量部の割合になるように配
合し、この配合組成液を型に注入して反応発泡さ
せたのち、該ウレタン発泡体を乾燥、焼成するこ
とを特徴とするセラミツク多孔体の製造法。 2 (a)ポリアルキレンポリオールと(b)有機イソシ
アネート化合物とを混合してプレミツクスを製造
するに際し、界面活性剤を添加する特許請求の範
囲第1項記載のセラミツク多孔体の製造法。[Scope of Claims] 1 (a) Average molecular weight of 3,000 or more with two or more OH groups
10,000 polyalkylene polyol and (b) an organic isocyanate compound having two or more NCO groups at a molar ratio of OH group/NCO group of 0.01 to 0.5. A crosslinking agent having more than 100 functional groups and an aqueous ceramic slurry are combined with the above (b) organic isocyanate compound NCO
The molar ratio of the functional group of the crosslinking agent (c) to the group is from 0.29 to
Mix in a ratio of 7.5 to produce mud ceramic,
The above premix and the mud ceramic
Components (a), (b), and (c) are mixed so that the total weight is 10 to 35 parts by weight based on 100 parts by weight of the ceramic raw material, and this mixed composition liquid is poured into a mold to form a reaction foam. 1. A method for producing a porous ceramic body, which comprises drying and firing the urethane foam. 2. The method for producing a porous ceramic body according to claim 1, wherein a surfactant is added when producing a premix by mixing (a) a polyalkylene polyol and (b) an organic isocyanate compound.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6624283A JPS59190250A (en) | 1983-04-13 | 1983-04-13 | Manufacture of ceramic porous body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6624283A JPS59190250A (en) | 1983-04-13 | 1983-04-13 | Manufacture of ceramic porous body |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59190250A JPS59190250A (en) | 1984-10-29 |
| JPH0254304B2 true JPH0254304B2 (en) | 1990-11-21 |
Family
ID=13310194
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6624283A Granted JPS59190250A (en) | 1983-04-13 | 1983-04-13 | Manufacture of ceramic porous body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59190250A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6479418B2 (en) | 1999-12-16 | 2002-11-12 | Isotis N.V. | Porous ceramic body |
| EP1108698B8 (en) * | 1999-12-16 | 2006-10-04 | IsoTis N.V. | Porous ceramic body |
| JP6039820B2 (en) * | 2012-11-21 | 2016-12-07 | 韓国生産技術研究院Korea Institute Of Industrial Technology | Manufacturing method of ceramic filter |
| US9796632B2 (en) | 2012-11-21 | 2017-10-24 | Korea Institute Of Industrial Technology | Method for manufacturing ceramic filter |
-
1983
- 1983-04-13 JP JP6624283A patent/JPS59190250A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59190250A (en) | 1984-10-29 |
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