JPH0153605B2 - - Google Patents
Info
- Publication number
- JPH0153605B2 JPH0153605B2 JP815384A JP815384A JPH0153605B2 JP H0153605 B2 JPH0153605 B2 JP H0153605B2 JP 815384 A JP815384 A JP 815384A JP 815384 A JP815384 A JP 815384A JP H0153605 B2 JPH0153605 B2 JP H0153605B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- phenolic resin
- curing
- water
- pvat
- 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
Links
- 239000005011 phenolic resin Substances 0.000 claims description 34
- 229920005989 resin Polymers 0.000 claims description 31
- 239000011347 resin Substances 0.000 claims description 31
- 239000011148 porous material Substances 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 8
- 239000012778 molding material Substances 0.000 claims description 4
- DHKHKXVYLBGOIT-UHFFFAOYSA-N 1,1-Diethoxyethane Chemical compound CCOC(C)OCC DHKHKXVYLBGOIT-UHFFFAOYSA-N 0.000 claims description 3
- 239000011354 acetal resin Substances 0.000 claims description 3
- 229920006324 polyoxymethylene Polymers 0.000 claims description 3
- 229920002554 vinyl polymer Polymers 0.000 claims description 3
- 229920001568 phenolic resin Polymers 0.000 description 31
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 29
- 239000000463 material Substances 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 239000004372 Polyvinyl alcohol Substances 0.000 description 10
- 239000003054 catalyst Substances 0.000 description 10
- 229920002451 polyvinyl alcohol Polymers 0.000 description 10
- 238000000034 method Methods 0.000 description 9
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 6
- -1 p-tert-aminophenol Chemical compound 0.000 description 6
- 150000002989 phenols Chemical class 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- 229920003987 resole Polymers 0.000 description 6
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 5
- 150000001299 aldehydes Chemical class 0.000 description 5
- 239000004640 Melamine resin Substances 0.000 description 4
- 229920000877 Melamine resin Polymers 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000010440 gypsum Substances 0.000 description 4
- 229910052602 gypsum Inorganic materials 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- 229920002472 Starch Polymers 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 238000005266 casting Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002243 precursor Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- QWBBPBRQALCEIZ-UHFFFAOYSA-N 2,3-dimethylphenol Chemical compound CC1=CC=CC(O)=C1C QWBBPBRQALCEIZ-UHFFFAOYSA-N 0.000 description 2
- NKTOLZVEWDHZMU-UHFFFAOYSA-N 2,5-xylenol Chemical compound CC1=CC=C(C)C(O)=C1 NKTOLZVEWDHZMU-UHFFFAOYSA-N 0.000 description 2
- NXXYKOUNUYWIHA-UHFFFAOYSA-N 2,6-Dimethylphenol Chemical compound CC1=CC=CC(C)=C1O NXXYKOUNUYWIHA-UHFFFAOYSA-N 0.000 description 2
- YCOXTKKNXUZSKD-UHFFFAOYSA-N 3,4-xylenol Chemical compound CC1=CC=C(O)C=C1C YCOXTKKNXUZSKD-UHFFFAOYSA-N 0.000 description 2
- TUAMRELNJMMDMT-UHFFFAOYSA-N 3,5-xylenol Chemical compound CC1=CC(C)=CC(O)=C1 TUAMRELNJMMDMT-UHFFFAOYSA-N 0.000 description 2
- HMNKTRSOROOSPP-UHFFFAOYSA-N 3-Ethylphenol Chemical compound CCC1=CC=CC(O)=C1 HMNKTRSOROOSPP-UHFFFAOYSA-N 0.000 description 2
- HXDOZKJGKXYMEW-UHFFFAOYSA-N 4-ethylphenol Chemical compound CCC1=CC=C(O)C=C1 HXDOZKJGKXYMEW-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-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
- HYBBIBNJHNGZAN-UHFFFAOYSA-N Furaldehyde Natural products O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 239000010425 asbestos Substances 0.000 description 2
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 239000003431 cross linking reagent Substances 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- LEQAOMBKQFMDFZ-UHFFFAOYSA-N glyoxal Chemical compound O=CC=O LEQAOMBKQFMDFZ-UHFFFAOYSA-N 0.000 description 2
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- RLSSMJSEOOYNOY-UHFFFAOYSA-N m-cresol Chemical compound CC1=CC=CC(O)=C1 RLSSMJSEOOYNOY-UHFFFAOYSA-N 0.000 description 2
- 238000003754 machining Methods 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229920003986 novolac Polymers 0.000 description 2
- QWVGKYWNOKOFNN-UHFFFAOYSA-N o-cresol Chemical compound CC1=CC=CC=C1O QWVGKYWNOKOFNN-UHFFFAOYSA-N 0.000 description 2
- IWDCLRJOBJJRNH-UHFFFAOYSA-N p-cresol Chemical compound CC1=CC=C(O)C=C1 IWDCLRJOBJJRNH-UHFFFAOYSA-N 0.000 description 2
- 238000006068 polycondensation reaction Methods 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 description 2
- 229910052895 riebeckite Inorganic materials 0.000 description 2
- 238000007127 saponification reaction Methods 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000011550 stock solution Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- KUFFULVDNCHOFZ-UHFFFAOYSA-N 2,4-xylenol Chemical compound CC1=CC=C(O)C(C)=C1 KUFFULVDNCHOFZ-UHFFFAOYSA-N 0.000 description 1
- IXQGCWUGDFDQMF-UHFFFAOYSA-N 2-Ethylphenol Chemical compound CCC1=CC=CC=C1O IXQGCWUGDFDQMF-UHFFFAOYSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- QHPQWRBYOIRBIT-UHFFFAOYSA-N 4-tert-butylphenol Chemical compound CC(C)(C)C1=CC=C(O)C=C1 QHPQWRBYOIRBIT-UHFFFAOYSA-N 0.000 description 1
- UMHJEEQLYBKSAN-UHFFFAOYSA-N Adipaldehyde Chemical compound O=CCCCCC=O UMHJEEQLYBKSAN-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- SXRSQZLOMIGNAQ-UHFFFAOYSA-N Glutaraldehyde Chemical compound O=CCCCC=O SXRSQZLOMIGNAQ-UHFFFAOYSA-N 0.000 description 1
- 229930040373 Paraformaldehyde Natural products 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- RQPZNWPYLFFXCP-UHFFFAOYSA-L barium dihydroxide Chemical compound [OH-].[OH-].[Ba+2] RQPZNWPYLFFXCP-UHFFFAOYSA-L 0.000 description 1
- 229910001863 barium hydroxide Inorganic materials 0.000 description 1
- SRSXLGNVWSONIS-UHFFFAOYSA-N benzenesulfonic acid Chemical compound OS(=O)(=O)C1=CC=CC=C1 SRSXLGNVWSONIS-UHFFFAOYSA-N 0.000 description 1
- 229940092714 benzenesulfonic acid Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- YXVFYQXJAXKLAK-UHFFFAOYSA-N biphenyl-4-ol Chemical compound C1=CC(O)=CC=C1C1=CC=CC=C1 YXVFYQXJAXKLAK-UHFFFAOYSA-N 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 150000001896 cresols Chemical class 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229940015043 glyoxal Drugs 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004312 hexamethylene tetramine Substances 0.000 description 1
- 235000010299 hexamethylene tetramine Nutrition 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 239000010446 mirabilite Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920002866 paraformaldehyde Polymers 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000011164 primary particle Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 150000003856 quaternary ammonium compounds Chemical class 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 1
- 229940100445 wheat starch Drugs 0.000 description 1
Landscapes
- Producing Shaped Articles From Materials (AREA)
- Moulds, Cores, Or Mandrels (AREA)
Description
本発明は陶磁器、セラミツク成型体等、型を利
用して形を作る際に使用される成型々用素材に関
する。
陶磁器等の成型は通常原料粉体を水等に分散さ
せたスラリー状の泥漿を雌型の中に流し込み、型
に近接した部分が流動性を失つてから、余剰の流
動性をもつた泥漿を排出し、その半固化したもの
を型から取り出した後焼成等の工程を施すことに
より行われている。そしてこの雌型の素材として
は従来吸水性にすぐれた石こうが汎用されてい
た。石こうは吸水性にすぐれるため、スラリー状
の泥漿を半固化状態にする時間が短く鋳込型とし
て好適な素材であるが、表面のきめがやゝ粗く、
また泥漿中の塩基性成分に冒され易いため繰り返
し使用を行なうと表面が徐々に磨滅、損耗し、割
れたり、欠けたりすることから数十回程度の使用
で廃棄せねばならぬ欠点があつた。特に工業用と
して用いられるセラミツクスの場合、表面の平滑
度、平坦度及び寸法精度を高くする必要があり、
それに伴ない鋳込み型の表面精度も高度のものが
要求されている。
本発明者等は、石こう製鋳込み型に見られる上
記欠点に鑑み、成型々用素材について鋭意研究を
行い、本発明を完成したものであり、その目的と
するところは、強靭性を有し、泥漿に冒されず、
吸水性にすぐれ且つ一般の加工工具やNC加工等
の機械加工手段により容易に成型加工が可能な成
型々用素材を提供するにある。
上述の目的はポリビニールアセタール系樹脂A
とフエノール系樹脂Bとの混合物よりなる樹脂構
造体であつて、該構造体を構成する樹脂の比率が
重量比において、B/A=0.2〜5になるような
範囲で微細に混合分散され、連続気孔を有する多
孔質構造であることを特徴とする成型型用素材に
より達成される。
本発明に於て重要なことはポリビニールアセタ
ール系樹脂(PVAt系樹脂)にフエノール系樹脂
を微細に混合分散せしめ連続気孔を有する多孔質
体構造にした点にある。そしてPVAt系樹脂中に
混合分散せしめるフエノール系樹脂の量はPVAt
系樹脂に対して0.2〜5重量部の範囲である。
PVAt系樹脂に対するフエノール系樹脂の量が0.2
重量部未満であると脆くなり靭性及び加工性に欠
け吸水性も劣る。一方フエノール系樹脂の量が5
重量部を超えると強度、寸法安定性が不十分とな
る。
また、本発明に係る成型々素材の特長である吸
水性能は原材料の1つとして親水性樹脂である
PVAt系樹脂を用いた事、及び連続気孔の多孔質
体構造を備えたことによつてもたらされるもので
あり、かゝる連続気孔は後述する気孔形成方法に
よりはじめてなしうるものである。
そして気孔率が50%未満であると気孔の中で連
続気孔の占める割合が低くなり本素材の特徴であ
る吸水性能が阻害され80%を超えると構造体とし
ての強度が不十分となる。
更に平均気孔径が0.5ミクロン未満のものは製
造が困難であり、100ミクロンを越えるものはき
めが粗すぎて素材としては不適当である。
本発明に係る成型々用素材において、PVAt系
樹脂とフエノール系樹脂は共重合あるいは重縮合
という形で均一な高分子体を形成するのではな
く、各々が極めてミクロな状態で混合されている
ものであり、例えば以下に記載される方法にて製
造出来る。
第1の方法は、PVAt系樹脂、及びフエノール
系樹脂の前駆体又はプレポリマーを流動状態で混
合し、硬化反応を進める方法である。即ち、まず
所定量のポリビニールアルコール水溶液と、液状
フエノール樹脂プリポリマーを混合した液に、気
孔生成剤としての澱粉類あるいはその変性体等の
気孔生成剤の水分散液、及びアルデヒド類等の架
橋剤の酸類等の硬化触媒を各々必要量添加し、均
一に撹拌混合して反応原液となし、必要な型に注
入し、40〜80℃にて10〜20時間反応せしめ、多孔
質体を形成させるとともに予備硬化する。引き続
いて水洗、脱水、乾燥し、100〜200℃、好ましく
は120〜160℃にてキユアリングを行い、フエノー
ル系樹脂の硬化反応を完結させる事によつて製造
されるものであるが、そのキユアリングに要する
時間はその大きさと気孔率によつてかわるもので
あり、大型でしかも気孔率の低いものはキユアリ
ング時間が長くなる。即ちキユアリング時間は
各々のケースに応じて慎重に選定する事が必要で
ある。
上記本発明に用いるフエノール系樹脂としては
水溶性レゾール樹脂が好適である。
レゾール樹脂は、フエノール類をアルデヒド類
と塩基性触媒の存在下で反応させることにより製
造されるところの初期生成物であり、一般にフエ
ノール1モルに対し、1.5〜3.5モルのアルデヒド
類をやや過剰のアルカリ触媒の存在下で反応させ
た初期縮合物を安定な水溶性の状態に保たせるこ
とにより、水溶性レゾール樹脂が得られる。
レゾール樹脂の製造に用いられるフエノール類
としては、最も一般的には、フエノール及びクレ
ゾールが挙げられる。しかし、他のフエノール類
も使用することが出来、例えば該フエノール類と
しては、
フエノール、o−クレゾール、m−クレゾー
ル、p−クレゾール、2,3−キシレノール、
2,5−キシレノール,2,4―キシレノール,
2,6−キシレノール、3,4−キシレノール、
3,5−キシレノール、o−エチルフエノール、
m−エチルフエノール、p−エチルフエノール、
p−フエニルフエノール、p−tert−ブチルフエ
ノール、p−tert−アミノフエノール、ビスフエ
ノールA、レゾルシノール及びこれらフエノール
類の混合物が挙げられる。
このフエノール類と重縮合するために用いをア
ルデヒド類としては、ホルムアルデヒドが最も一
般的である。しかし、パラホルムアルデヒド、ヘ
キサメチレンテトラミン、フルフラール並びにグ
ルタルアルデヒド、アジポアルデヒド及びグリオ
キサール等のモノアルデヒド及びジアルデヒドも
使用し得る。
レゾール樹脂合成反応に用いる塩基性触媒とし
ては、カセイアルカリ、炭酸アルカリ、水酸化バ
リウム、水酸化カルシウム、アンモニア、第4級
アンモニウム化合物、アミン類等の公知のものを
使用すればよく、カセイソーダあるいはアンモニ
アが最も一般的に用いられる。
本発明に用いるポリビニルアルコールは一般に
酢酸ビニルをけん化して得られるものであつて、
その重合度、けん化度、分岐、他モノマーとの共
重合など特に制限はなく、また単独でも二種以上
混合しても使用しうるが、好ましくは重合度100
〜5000、けん化度70%以上のものがよい。
本発明に用いる硬化触媒としては、一般にフエ
ノール系樹脂の硬化に使用されている触媒を用い
ることが出来、塩酸、硫酸、蓚酸、乳酸、蟻酸、
酢酸、パラトルエンスルホン酸、ベンゼンスルホ
ン酸等が好適である。硬化触媒の添加量は、使用
する触媒の種類、原料配合組成、硬化温度等を考
慮し、適宜決定すればよい。
この際、フエノール系樹脂として反応性を有す
る粒状乃至粉末状のフエノール樹脂を使用すると
高強度のものが得られる。反応性を有する粒状な
いし粉末状フエノール樹脂とは、従来公知のレゾ
ール樹脂の硬化製品又はノボラツク樹脂の硬化製
品を粉砕したもの、或は従来公知の硬化ノボラツ
ク樹脂繊維を粉砕したものとは全く異なつてお
り、特開昭57−177011号公報に述べられた製造法
に従つて製造される球状一次粒子およびその二次
凝集物よりなるフエノール樹脂である。この反応
性を有する粒状ないし粉末状フエノール樹脂はそ
の形状が球形に近い粒子であることから、公知の
フエノール樹脂硬化物を粉砕して得られた粉末に
比べてポリビニルアルコールや液状フエノール樹
脂との混合性が良好であり、該樹脂を用いること
により多量のフエノール樹脂粉末を均一に混合し
た連続気孔を有する強度の高いPVAt系樹脂−フ
エノール系樹脂の混合系樹脂多孔質体を得る事が
可能となる。この反応性を有する粒状乃至粉末状
フエノール樹脂をフエノール系樹脂の一部として
使用する場合は、液状フエノール系樹脂プレポリ
マーあるいはポリビニルアルコール水溶液、又は
その混合液に添加し均一撹拌すれば良い。また、
フエノール系樹脂の全量を該粒状ないし粉末状フ
エノール樹脂とする場合はポリビニルアルコール
水溶液あるいはその他の添加剤を加えた混合液に
添加し、均一撹拌すれば良い。
第2の方法は、PVAt系樹脂多孔質体からあら
かじめ作成し、それに液状フエノール系樹脂、又
はその前駆体を所定量含浸させた後、熱処理硬化
反応を進める方法である。この場合はポリビニル
アルコール水溶液に澱粉類又はその変性体等の気
孔形成剤の水分散液、アルデヒド類等の架橋剤、
酸類等の触媒を各々必要量加え、均一撹拌した反
応原液を必要な型に注型し、40〜80℃にて反応さ
せる公知の方法によつてPVAt系樹脂多孔質体を
得た後、それを液状フエノール樹脂又はその前駆
体に浸漬し、所定圧を絞つた後100〜200℃の温度
にてキユアリングを行い、フエノール系樹脂の硬
化反応を完結する事によつて得られる。この方法
による場合は、多孔質体の基本はPVAt系樹脂に
よつて形成されるものであり、フエノール系樹脂
はそれに均一に含浸されるという組識をなし、第
1の方法とは若干組織を異にするものであり、フ
エノール系樹脂の比率が比較的低いものを製造す
るのに好適である。
そして本発明に於ては、例えばメラミン系樹
脂、フエノール系化合物、ヒンダードフエノール
系化合物、アミン系化合物、ヒドロキシルアミン
系化合物等就中メラミン系樹脂を配合すると、特
にキユアリング時の酸化、蓄熱現象、所謂パンキ
ング現象の抑制に有効である。メラミン系樹脂は
上記の効果に加えて多孔質体の硬度を向上する効
果をも有する。
この他増量あるいは強力の向上を目的として炭
酸カルシウム、芒硝、硫酸カルシウム等の塩類、
ガラス又はガラス繊維紛末、タルク、石綿、アス
ベスト、マイカ、金属及びその酸化物、炭化物の
紛末あるいはウイスカー、クレー等を適量加えて
もよい。
この様にして得られた本発明成型々用素材は通
常の手工具、NC加工等の機械加工の手段を用い
て所定の成型型に仕上げるが、この際加工々具に
よる「欠け」「割れ」「焼け」等の好ましからざる
現象が極めて少なく、その作業性が極めて良好で
ある。
更に型に加工後、加湿、洗浄、乾燥等の操作を
くり返しても「狂い」がほとんど生じない。特に
石こうに比し、磨滅、損耗が少なく、繰り返し使
用に耐える大きな特長を有する。
以下実施例を具げて本発明を具体的に説明す
る。
実施例 1
フエノール系樹脂として水溶性フエノール樹脂
水溶液(住友デユレス製PR−961A(純分64%))、
ポリビニールアルコーールとしてクラレ製PVA
―117粉体を使用した。
ポリビニールアルコールを水に溶解し水溶液と
しこれと前記PR−961Aを混合し均質粘調液を調
整した。混合比は各々の樹脂純分の重量換算で第
1表に示す割合になるようにした。更に、この液
に500gの小麦澱粉を水に分散し蒸煮したもの、
800gの37%ホルマリン及び700gの30%硫酸を添
加し、更に全量が10となるように水を加え十分
に撹拌した後塩化ビニール製の型枠に注型した。
なお、この場合の樹脂分の占める割合は10に
対し4Kgとなるようにした。
前記型枠を50℃に設定した温水中に入れ20時間
放置し反応を行なわしめた後型枠より内容物を取
り出した。然る後三日間シヤワーにかけ流水下で
洗浄し、引き続き乾燥を行なつた。乾燥したもの
を窒素気流下にて150℃でキユアリングを行なつ
た。
得られた製品の物性値を測定し、その結果を第
1表に示す。
The present invention relates to a molding material used to create shapes using molds, such as ceramics and ceramic molded bodies. When molding ceramics, etc., a slurry-like slurry made by dispersing raw material powder in water, etc. is poured into a female mold, and after the part close to the mold loses its fluidity, the surplus fluid slurry is poured out. This is done by discharging the material, taking out the semi-solidified material from the mold, and then subjecting it to a process such as firing. Gypsum, which has excellent water absorption, has been commonly used as the material for this female mold. Because gypsum has excellent water absorption, it takes less time to semi-solidify the slurry, making it a suitable material for casting molds, but it has a rather rough surface.
In addition, because it is easily affected by the basic components in the slurry, repeated use causes the surface to gradually wear out, wear out, crack, or chip, so it has to be discarded after being used a few dozen times. . Especially in the case of ceramics used for industrial purposes, it is necessary to have high surface smoothness, flatness, and dimensional accuracy.
Accordingly, a high level of surface precision is required for casting molds. In view of the above-mentioned drawbacks of gypsum casting molds, the present inventors conducted extensive research on materials for molding and completed the present invention.The purpose of this invention is to have toughness, Unaffected by mud,
It is an object of the present invention to provide a material for molding that has excellent water absorbency and can be easily molded using general processing tools or machining means such as NC processing. The above purpose is to use polyvinyl acetal resin A.
and a phenolic resin B, which are finely mixed and dispersed in such a range that the ratio of the resins constituting the structure is B/A = 0.2 to 5 in terms of weight ratio, This is achieved using a molding material that is characterized by a porous structure with continuous pores. What is important in the present invention is that a phenolic resin is finely mixed and dispersed in a polyvinyl acetal resin (PVAt resin) to form a porous structure having continuous pores. The amount of phenolic resin mixed and dispersed in the PVAt resin is PVAt.
The amount is in the range of 0.2 to 5 parts by weight based on the system resin.
The amount of phenolic resin to PVAt resin is 0.2
If it is less than 1 part by weight, it becomes brittle, has poor toughness and workability, and has poor water absorption. On the other hand, the amount of phenolic resin is 5
If the amount exceeds parts by weight, the strength and dimensional stability will be insufficient. In addition, the water absorption performance, which is a feature of the molded material according to the present invention, is achieved by using a hydrophilic resin as one of the raw materials.
This is achieved by using PVAt-based resin and having a porous structure with continuous pores, and such continuous pores can only be achieved by the pore formation method described below. If the porosity is less than 50%, the proportion of continuous pores among the pores will be low and the water absorption performance, which is a characteristic of this material, will be inhibited, and if it exceeds 80%, the strength of the structure will be insufficient. Furthermore, those with an average pore diameter of less than 0.5 microns are difficult to manufacture, and those with an average pore diameter of more than 100 microns are too coarse and unsuitable as materials. In the molding material according to the present invention, the PVAt resin and the phenolic resin do not form a uniform polymer through copolymerization or polycondensation, but are mixed in an extremely microscopic state. It can be produced, for example, by the method described below. The first method is to mix a PVAt-based resin and a phenolic resin precursor or prepolymer in a fluidized state and proceed with a curing reaction. That is, first, a predetermined amount of a polyvinyl alcohol aqueous solution and a liquid phenolic resin prepolymer are mixed, and an aqueous dispersion of a pore-forming agent such as starch or a modified product thereof as a pore-forming agent, and a crosslinking agent such as an aldehyde are added. Add the required amount of curing catalyst such as acid for each agent, stir and mix uniformly to make a reaction stock solution, pour it into the required mold, and react at 40 to 80℃ for 10 to 20 hours to form a porous body. and pre-cure. It is then manufactured by washing with water, dehydrating, drying, and curing at 100 to 200°C, preferably 120 to 160°C, to complete the curing reaction of the phenolic resin. The time required depends on the size and porosity of the material, with larger and lower porosity materials requiring longer curing times. That is, the curing time must be carefully selected depending on each case. A water-soluble resol resin is suitable as the phenolic resin used in the present invention. Resole resin is an initial product produced by reacting phenols with aldehydes in the presence of a basic catalyst, and generally 1.5 to 3.5 mol of aldehyde is added in slight excess to 1 mol of phenol. A water-soluble resol resin can be obtained by maintaining the initial condensate reacted in the presence of an alkali catalyst in a stable water-soluble state. Phenols used in the production of resol resins most commonly include phenols and cresols. However, other phenols can also be used, such as phenol, o-cresol, m-cresol, p-cresol, 2,3-xylenol,
2,5-xylenol, 2,4-xylenol,
2,6-xylenol, 3,4-xylenol,
3,5-xylenol, o-ethylphenol,
m-ethylphenol, p-ethylphenol,
Examples include p-phenylphenol, p-tert-butylphenol, p-tert-aminophenol, bisphenol A, resorcinol, and mixtures of these phenols. Formaldehyde is most commonly used as the aldehyde for polycondensation with the phenols. However, monoaldehydes and dialdehydes such as paraformaldehyde, hexamethylenetetramine, furfural and glutaraldehyde, adipaldehyde and glyoxal may also be used. As the basic catalyst used in the resol resin synthesis reaction, known catalysts such as caustic alkali, alkali carbonate, barium hydroxide, calcium hydroxide, ammonia, quaternary ammonium compounds, and amines may be used. is most commonly used. The polyvinyl alcohol used in the present invention is generally obtained by saponifying vinyl acetate, and
There are no particular restrictions on its degree of polymerization, degree of saponification, branching, copolymerization with other monomers, etc., and it can be used alone or in combination of two or more, but preferably has a degree of polymerization of 100.
~5000, preferably with a saponification degree of 70% or more. As the curing catalyst used in the present invention, catalysts generally used for curing phenolic resins can be used, such as hydrochloric acid, sulfuric acid, oxalic acid, lactic acid, formic acid,
Acetic acid, para-toluenesulfonic acid, benzenesulfonic acid, etc. are suitable. The amount of the curing catalyst to be added may be appropriately determined in consideration of the type of catalyst used, the composition of raw materials, the curing temperature, etc. At this time, if a reactive granular or powdery phenolic resin is used as the phenolic resin, high strength can be obtained. Reactive granular or powdered phenolic resin is completely different from pulverized cured products of conventionally known resol resins or cured novolak resins, or pulverized cured novolak resin fibers. This is a phenolic resin made of spherical primary particles and secondary aggregates thereof, which is manufactured according to the manufacturing method described in JP-A-57-177011. Since this reactive granular or powdered phenolic resin has a nearly spherical shape, it is easier to mix with polyvinyl alcohol or liquid phenolic resin than powder obtained by pulverizing known cured phenolic resins. By using this resin, it is possible to obtain a high-strength PVAt resin-phenol resin mixed resin porous body with continuous pores in which a large amount of phenolic resin powder is uniformly mixed. . When using this reactive granular or powdered phenolic resin as part of the phenolic resin, it may be added to a liquid phenolic resin prepolymer, an aqueous polyvinyl alcohol solution, or a mixture thereof and stirred uniformly. Also,
When the entire amount of the phenolic resin is to be made into the granular or powdered phenolic resin, it may be added to an aqueous polyvinyl alcohol solution or a mixed solution containing other additives and stirred uniformly. The second method is to prepare a porous PVAt-based resin in advance, impregnate it with a predetermined amount of liquid phenol-based resin or its precursor, and then proceed with a heat treatment curing reaction. In this case, in an aqueous polyvinyl alcohol solution, an aqueous dispersion of a pore forming agent such as starch or its modified product, a crosslinking agent such as an aldehyde, etc.
After adding the required amount of each catalyst such as acids and stirring uniformly, the reaction stock solution is cast into the required mold and reacted at 40 to 80°C to obtain a porous PVAt-based resin by a known method. It is obtained by immersing the resin in a liquid phenolic resin or its precursor, and curing at a temperature of 100 to 200° C. after reducing a predetermined pressure to complete the curing reaction of the phenolic resin. In this method, the porous body is basically formed of PVAt resin, and the phenol resin is uniformly impregnated into it, so the structure is slightly different from that in the first method. It is suitable for producing products with a relatively low proportion of phenolic resin. In the present invention, when a melamine resin, for example, a melamine resin, a phenol compound, a hindered phenol compound, an amine compound, a hydroxylamine compound, etc. is blended, oxidation and heat accumulation phenomena, especially during curing, can be avoided. This is effective in suppressing the so-called punking phenomenon. In addition to the above effects, the melamine resin also has the effect of improving the hardness of the porous body. In addition, salts such as calcium carbonate, mirabilite, calcium sulfate, etc., for the purpose of increasing volume or improving strength,
Appropriate amounts of glass or glass fiber powder, talc, asbestos, asbestos, mica, metals and their oxides, carbide powders, whiskers, clay, etc. may be added. The material for molding of the present invention obtained in this way is finished into a predetermined mold using ordinary hand tools and machining methods such as NC processing. There are extremely few undesirable phenomena such as "burning" and the workability is extremely good. Moreover, even after repeated operations such as humidification, washing, and drying after being processed into molds, "misalignment" hardly occurs. In particular, compared to gypsum, it has the great advantage of being less prone to wear and tear and being able to withstand repeated use. The present invention will be specifically described below with reference to Examples. Example 1 As a phenolic resin, a water-soluble phenolic resin aqueous solution (PR-961A (purity 64%) manufactured by Sumitomo Duress),
Kuraray PVA as polyvinyl alcohol
-117 powder was used. Polyvinyl alcohol was dissolved in water to make an aqueous solution, and the above PR-961A was mixed to prepare a homogeneous viscous liquid. The mixing ratio was adjusted to the proportions shown in Table 1 in terms of the weight of each pure resin. Furthermore, 500g of wheat starch was dispersed in water and steamed in this liquid,
800 g of 37% formalin and 700 g of 30% sulfuric acid were added, and water was further added so that the total amount was 10%. After stirring thoroughly, the mixture was cast into a mold made of vinyl chloride. In this case, the ratio of the resin content was 10 to 4 kg. The mold was placed in warm water set at 50° C. and left to react for 20 hours, after which the contents were taken out from the mold. Thereafter, it was washed under running water under a shower for three days, and then dried. The dried material was cured at 150°C under a nitrogen stream. The physical properties of the obtained product were measured and the results are shown in Table 1.
【表】
実施例 2
第3成分として、反応性を有する粒状フエノー
ル樹脂(鐘紡(株)製商品名ベルパールS、平均粒度
50μm)またはメラミン系樹脂(昭和高分子(株)製
商品名ミルベンレジン純分50%)を添加する事と
し、実施例1の示す組成の水溶性フエノール樹脂
及びポリビニールアルコールを減じてその分これ
らの成分を添加した。
添加物、組成等は実施例1に準じ、樹脂混合比
は第2表に併記した。さらに、反応条件も実施例
1に準じた。結果を第2表に示す。[Table] Example 2 As the third component, reactive granular phenolic resin (trade name: Bell Pearl S, manufactured by Kanebo Co., Ltd., average particle size
50 μm) or melamine resin (product name: Milben Resin, manufactured by Showa Kobunshi Co., Ltd. purity 50%), and the water-soluble phenolic resin and polyvinyl alcohol having the composition shown in Example 1 were reduced, and the amount of these resins was reduced accordingly. Added ingredients. The additives, composition, etc. were the same as in Example 1, and the resin mixing ratio was also listed in Table 2. Furthermore, the reaction conditions were also the same as in Example 1. The results are shown in Table 2.
【表】【table】
Claims (1)
ル系樹脂Bとの混合物よりなる樹脂構造体であつ
て、該構造体を構成する樹脂の比率が重量比にお
いて、B/A=0.2〜5になるような範囲で微細
に混合分散され、連続気孔を有する多孔質体構造
であることを特徴とする成型型用素材。 2 連続気孔を有する多孔質体構造が気孔率50〜
80容量%、平均気孔径0.5〜100μのものである特
許請求の範囲第1項に記載の成型型用素材。[Scope of Claims] 1. A resin structure made of a mixture of polyvinyl acetal resin A and phenol resin B, wherein the ratio of the resins constituting the structure is B/A=0.2 to 0.2 by weight. 5. A molding material characterized by having a porous structure having continuous pores and being finely mixed and dispersed within a range of 5. 2 Porous body structure with continuous pores has a porosity of 50~
80% by volume and an average pore diameter of 0.5 to 100μ.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP815384A JPS60151002A (en) | 1984-01-19 | 1984-01-19 | Blank for molding die |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP815384A JPS60151002A (en) | 1984-01-19 | 1984-01-19 | Blank for molding die |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60151002A JPS60151002A (en) | 1985-08-08 |
| JPH0153605B2 true JPH0153605B2 (en) | 1989-11-15 |
Family
ID=11685372
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP815384A Granted JPS60151002A (en) | 1984-01-19 | 1984-01-19 | Blank for molding die |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60151002A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4836917A (en) * | 1986-10-06 | 1989-06-06 | Kanebo, Ltd. | Apparatus for performing separation of a solid-liquid mixture |
| JP5426224B2 (en) * | 2009-04-20 | 2014-02-26 | タテホ化学工業株式会社 | Ceramic sintered body with excellent dimensional accuracy and manufacturing method thereof |
-
1984
- 1984-01-19 JP JP815384A patent/JPS60151002A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60151002A (en) | 1985-08-08 |
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