JPS644978B2 - - Google Patents
Info
- Publication number
- JPS644978B2 JPS644978B2 JP58081491A JP8149183A JPS644978B2 JP S644978 B2 JPS644978 B2 JP S644978B2 JP 58081491 A JP58081491 A JP 58081491A JP 8149183 A JP8149183 A JP 8149183A JP S644978 B2 JPS644978 B2 JP S644978B2
- Authority
- JP
- Japan
- Prior art keywords
- calcia
- magnesia
- refractory
- resin
- phenolic resin
- 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 24
- -1 alkylene carbonate Chemical compound 0.000 claims description 23
- 229920001568 phenolic resin Polymers 0.000 claims description 22
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 claims description 19
- 239000011822 basic refractory Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000000292 calcium oxide Substances 0.000 description 27
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 26
- 235000012255 calcium oxide Nutrition 0.000 description 26
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 22
- 239000011449 brick Substances 0.000 description 18
- 229910052799 carbon Inorganic materials 0.000 description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 17
- 229920005989 resin Polymers 0.000 description 13
- 239000011347 resin Substances 0.000 description 13
- 239000002904 solvent Substances 0.000 description 13
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 12
- 230000029087 digestion Effects 0.000 description 11
- 239000000395 magnesium oxide Substances 0.000 description 11
- 229910002804 graphite Inorganic materials 0.000 description 10
- 239000010439 graphite Substances 0.000 description 10
- 238000000034 method Methods 0.000 description 10
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 10
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 9
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 9
- 239000002994 raw material Substances 0.000 description 9
- 239000002893 slag Substances 0.000 description 9
- 239000011819 refractory material Substances 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000011230 binding agent Substances 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 6
- 238000005260 corrosion Methods 0.000 description 6
- 239000010459 dolomite Substances 0.000 description 6
- 229910000514 dolomite Inorganic materials 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 235000013980 iron oxide Nutrition 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 230000003628 erosive effect Effects 0.000 description 5
- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 description 5
- 229920003987 resole Polymers 0.000 description 5
- 238000004901 spalling Methods 0.000 description 4
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000001723 curing Methods 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 238000004898 kneading Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229920003986 novolac Polymers 0.000 description 3
- 150000002989 phenols Chemical class 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 150000004760 silicates Chemical class 0.000 description 3
- GJYCVCVHRSWLNY-UHFFFAOYSA-N 2-butylphenol Chemical compound CCCCC1=CC=CC=C1O GJYCVCVHRSWLNY-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 239000012298 atmosphere 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
- 239000003054 catalyst Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 235000019441 ethanol Nutrition 0.000 description 2
- 238000013007 heat curing Methods 0.000 description 2
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 2
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000011823 monolithic refractory Substances 0.000 description 2
- 239000010680 novolac-type phenolic resin Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- KJFMBFZCATUALV-UHFFFAOYSA-N phenolphthalein Chemical compound C1=CC(O)=CC=C1C1(C=2C=CC(O)=CC=2)C2=CC=CC=C2C(=O)O1 KJFMBFZCATUALV-UHFFFAOYSA-N 0.000 description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 2
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- KJCVRFUGPWSIIH-UHFFFAOYSA-N 1-naphthol Chemical compound C1=CC=C2C(O)=CC=CC2=C1 KJCVRFUGPWSIIH-UHFFFAOYSA-N 0.000 description 1
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 1
- ZTMADXFOCUXMJE-UHFFFAOYSA-N 2-methylbenzene-1,3-diol Chemical compound CC1=C(O)C=CC=C1O ZTMADXFOCUXMJE-UHFFFAOYSA-N 0.000 description 1
- QTWJRLJHJPIABL-UHFFFAOYSA-N 2-methylphenol;3-methylphenol;4-methylphenol Chemical compound CC1=CC=C(O)C=C1.CC1=CC=CC(O)=C1.CC1=CC=CC=C1O QTWJRLJHJPIABL-UHFFFAOYSA-N 0.000 description 1
- WUQYBSRMWWRFQH-UHFFFAOYSA-N 2-prop-1-en-2-ylphenol Chemical compound CC(=C)C1=CC=CC=C1O WUQYBSRMWWRFQH-UHFFFAOYSA-N 0.000 description 1
- 229910052580 B4C Inorganic materials 0.000 description 1
- IGFHQQFPSIBGKE-UHFFFAOYSA-N Nonylphenol Natural products CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 description 1
- 229910052581 Si3N4 Inorganic materials 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- LLEMOWNGBBNAJR-UHFFFAOYSA-N biphenyl-2-ol Chemical compound OC1=CC=CC=C1C1=CC=CC=C1 LLEMOWNGBBNAJR-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- INAHAJYZKVIDIZ-UHFFFAOYSA-N boron carbide Chemical compound B12B3B4C32B41 INAHAJYZKVIDIZ-UHFFFAOYSA-N 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 229910052681 coesite Inorganic materials 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000007822 coupling agent Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 229930003836 cresol Natural products 0.000 description 1
- 229910052906 cristobalite Inorganic materials 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 235000019621 digestibility Nutrition 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 235000011187 glycerol Nutrition 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
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- ASHGTJPOSUFTGB-UHFFFAOYSA-N methyl resorcinol Natural products COC1=CC=CC(O)=C1 ASHGTJPOSUFTGB-UHFFFAOYSA-N 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical compound CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000011295 pitch Substances 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 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
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910052596 spinel Inorganic materials 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 229910052682 stishovite Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 229910052905 tridymite Inorganic materials 0.000 description 1
- 239000011452 unfired brick Substances 0.000 description 1
Landscapes
- Compositions Of Oxide Ceramics (AREA)
Description
〔産業上の利用分野〕
本発明はフリーのCaOを含有するドロマイトク
リンカー、マグドロクリンカー又は電融カルシ
ア、電融マグネシアーカルシア、焼結カルシアク
リンカー等を一部又は全部に使用した不焼成耐火
物及び不定形耐火物或いはこれらを非酸化性雰囲
気下で焼成した焼成耐火物の製造法に関するもの
である。
〔従来技術〕
近年転炉を始めとする製鋼炉においてマグネシ
ア−カーボンれんがの普及が急速に進んでいるこ
とは周知の所である。マグネシア−カーボンれん
がはマグネシア源として電融或いは焼結のマグネ
シアクリンカー、カーボン源として天然のりん状
黒鉛を使用し、バインダとしてフエノール類樹脂
を用いた不焼成耐火物であるが、マグネシアの高
耐食性に加えて黒鉛の高耐食性、高耐熱衝撃性の
特徴を相乗した耐食性、耐スポーリング性に優れ
た耐火物である。
かかるマグネシア−カーボンれんがの実炉での
損耗状況はスポーリングによる剥離は全くと言つ
ていい程なく、稼動表面から滑らかに溶損され
る。この溶損速度に影響を及ぼす因子としては、
スラグのCaO/SiO2比、鉄酸化物の量等の化学
反応に依存するものの他に溶鋼、溶融スラグの流
動に伴なう物理的な摩耗が考えられている。
耐火物中の黒鉛はシリケートに対して濡れ難い
性質を有している反面、スラブ中のFeO等の鉄酸
化物に対しては容易に酸化され、消失してしまう
欠点がある。
また、マグネシアは鉄酸化物には比較的安定で
あるがシリケート、特にC/Sの低いシリケート
に対してはCMS、C3MS2等を生成し溶流する。
以上のように鉄酸化物を含む溶融スラグに対して
は黒鉛の酸化、マグネシアの侵食が平行して起こ
り、溶損が進行するものと考えられている。
一方、上記のマグネシア−カーボンれんがと特
性が異なる材質としてマグネシア−カルシア−カ
ーボンれんががある。そしてカルシア含有原料例
えばマグドロクリンカー、ドロマイトクリンカー
は従来から焼成マグドロれんがに使用されてお
り、耐スラグ浸透性に優れ構造的スポーリングに
対する抵抗性は良好な反面、転炉等の含酸化鉄ス
ラグを生成する炉においては耐食性に劣り操業条
件の苛酷化と共の高マグネシア、低カルシアの耐
火物へと変遷してきたことは周知の所である。
これらのマグネシア−カルシア−カーボンれん
がとして従来から製造されているものにタール、
ピツチ類を結合剤としたタールドロマイトれんが
がある。通常この耐火物はマグネシア、ドロマイ
トに少量の黒鉛を使用して成るが、黒鉛の使用量
が少ない為に含酸化鉄のスラグを還元するに充分
でなく、また黒鉛の使用量を増大せしめた場合に
は、ピツチ類が熱可塑性であるがゆえに、熱処理
時に黒鉛配向方向と垂直な方向に大きな膨張を生
じ、良好な組織が得られないという欠点がある。
また、マグネシア−カーボンれんがとが様なフ
エノール樹脂を用いた場合には、レゾール型では
硬化時に結合水が発生する為に含カルシア原料の
消化を生じ、れんが崩壊をもたらすので不適であ
り、一方、ヘキサメチレンテトラミンを硬化剤と
したノボラツク型フエノール樹脂を用いた場合
は、レゾール型のように著しい消化現象はみられ
ないが、加熱硬化時或いは耐火物を炉に内張りし
昇温する過程でやはり消化による亀裂或いは組織
劣化を生じるので好ましくない。
かかる理由によるフエノール樹脂を結合剤とし
たマグネシア−カルシア−カーボン系耐火物は実
用化されていない。
〔発明の目的〕
上述の種々の欠陥を除去する目的で、本発明者
等はフリーのCaOを含有する耐火物において、黒
鉛などのカーボン源を多量に含む場合、カルシア
がマグネシアに比較して必ずしも耐食性が劣ると
は言えない。即ちスラグ成分の中でカルシアに対
して最も悪影響を及ぼす酸化鉄は耐火物中に含ま
れるカーボンとの酸化−還元反応によつて活性が
著しく低下し、カルシアに対する弊害を生じ難
い。以上のようにカーボンによつて還元されたス
ラグ、特にその組成が転炉の吹錬初期のように低
CaO/SiO2比のものでは、カルシアはスラグと
反応することによつて反応層の融点を一時的に高
める特性を有しており、稼動表面に高融点反応層
を形成してマグネシア−カーボンれんがにみられ
る連続的な溶損を抑制する効果が期待できる。ま
たカルシアは熱力学的な見地からカーボン共存下
における安定性に優れており、マグネシアとカー
ボンの直接反応が懸念される使用条件下ではカル
シアの優位性があることを見い出し、カルシアを
含有する耐火物において、結合剤としてフエノー
ル類樹脂を使用し、上記の欠陥を除く方法につい
て研究した。
本発明者はフエノール樹脂が消化現象をもたら
す原因を追求し、特殊な溶剤とフエノール樹脂を
併用することによりフリーのCaOを含有する原料
の使用を可能ならしめた。ノボラツク型フエノー
ル樹脂の使用に伴う消化の要因としてフエノール
樹脂水酸基分解と親水性溶剤の使用が考えられ
る。フエノール樹脂の溶剤としては一般にメチル
アルコール、エチルアルコール、プロピルアルコ
ールのような1価アルコール、エチレングリコー
ル、プロピレングリコール、グリセリン等の多価
アルコールが用いられるが、これらは全て親水性
溶剤であり、カルシアを含む原料に対して最も弊
害となる吸湿性を有する。
またフエノール樹脂化学の研究によると300℃
付近で多量の水を発生することが報告されてい
る。これはフエノール性水酸基の分解であると推
察されている。
本発明は消化要因となる上記フエノール樹脂の
欠点をアルキレンカーボネートを溶媒として使用
することにより一挙に解決したものである。
〔発明の効果〕
本発明はフリーのCaOを含有する塩基性耐火物
の製造において、結合剤としてフエノール樹脂と
アルキレンカーボネートを用いることによつて優
れた耐食性、スポーリング抵抗性を有し、かつ、
フエノール樹脂消化性のない耐火物を製造する方
法である。
本発明に用いるアルキレンカーボネートはエチ
レンカーボネート、プロピレンカーボネート等の
無色、透明、無臭の非吸湿性、非腐食性の安定な
液状のアルキレンカーボネートが好適である。
本発明に使用するフエノール樹脂は一般のフエ
ノール又はフエノール類とホルムアルデヒド源を
触媒下で反応せしめたものである。ここでフエノ
ール類とは1分子中に1個以上のフエノール性水
酸基を有し、かつフエノール性水酸基に対してオ
ルト位、またはパラ位が2個以上空位であるよう
な化合物であればよい。より具体的にはフエノー
ル、クレゾール、クロロフエノール、ノニルフエ
ノール、ブチルフエノール、フエニルフエノー
ル、ビスフエノールA、フエノールフタレイン、
レゾルシノール、メチルレゾルシノール、ハイド
ロキノン、ナフトール、イソプロペニルフエノー
ル等が挙げられる。もちろん、これらフエノール
類を2種以上混合使用することも可能である。フ
エノール樹脂の形態については縮合水発生量の少
ないノボラツク型が好ましいがレゾール型でも樹
脂製造の際に反応を進め高分子化したタイプ例え
ば固型レゾールでは硬化時の縮合水発生量が比較
的少なく、本発明による溶剤との併用であれば致
命的な消化をもたらすまでには至らず使用するこ
とができ、この際レゾールのメチロール基をブタ
ノールなどとブトキシ化すれば更に良い。無論ノ
ボラツク型とレゾール型の併用も可能である。
フエノール樹脂と併用するアルキレンカーボネ
ートとしてはエチレンカーボネート、プロピレン
カーボネート等が挙げられるが、必ずしもこれら
に限定される訳ではなく、フエノール性水酸基と
反応性を有するアルキレンカーボネートは如何な
るものでも使用することができる。
樹脂と溶剤の使用方法に関しては種々の方法が
ある。フエノール樹脂を製造する際の反応完了或
いは冷却過程で適量のアルキレンカーボネートを
添加し、適度な粘度に調整したバインダを用いる
方法、或いは耐火物混練時にフエノール樹脂とア
ルキレンカーボネートを同時に添加し、混練過程
で樹脂を溶解せしめる方法等があるが、本発明は
フエノール樹脂とアルキレンカーボネートが共存
するという前提を満足すればその製造方法にとら
れない。
フエノール樹脂とアルキレンカーボネートの使
用比率に制限はないが、耐火物の混練性、耐火物
性能面からはフエノール樹脂:アルキレンカーボ
ネートの重量比で40:60〜90:10の範囲が好まし
い。アルキレンカーボネートの使用比率が少ない
場合にはヒドロキシアキルエーテル化されないフ
エノール性水酸基が多くなりカルシア含有原料の
消化を抑制するに充分でなく、また逆にアルキレ
ンカーボネートの使用比率が高くなつた場合には
結合に寄与しない溶剤の比率が増大する為に耐火
物の強度組織が劣化して好ましくない。
また本発明に使用するアルキレンカーボネート
の特徴的な反応として樹脂の加熱硬化時にフエノ
ール性水酸基を定量的にヒドロキシアルキルエー
テル化させる。このとき耐火物中のフリーのCaO
はこの反応の触媒と成るので溶剤として使用した
アルキレンカーボネートは効率良く反応に寄与す
る。フエノール性水酸基がヒドロキシアルキルエ
ーテル化したフエノール樹脂硬化体をN2雰囲気
中、種々の温度で熱分解せしめガスクロマトグラ
フイーで発生する水の量を測定した。プロピレン
カーボネートを溶剤として使用した本発明による
樹脂硬化体はエチレングリコールを溶剤として使
用した通常の樹脂硬化体に比較して発生する水の
量が300℃では約1/7、400℃では約1/6と大幅に減
少しており、著しい消化性を有するカルシア含有
原料に対しては極めて好ましい性状を有すことが
確認された。
本発明に使用される必須の耐火物原料としては
マグドロ、ドロマイト、電融又は焼結のカルシ
ア、電融マグネシア−カルシア等のカルシア含有
原料の一種又は二種以上があり、必要に応じてマ
グネシア、スピネル等の酸化物、黒鉛、カーボン
ブラツク、コークス、無煙炭、炭化珪素、窒化珪
素、炭化ホウ素等の非酸化物を使用することもで
きる。
またAl、Cr、Ni、Fe、Si等の金属又はこれら
の炭化物、窒化物を添加することや、骨材と樹脂
の親和性、接着性を向上させる為に界面活性剤、
カツプリング剤を添加することもできる。
本発明による耐火物は低温で乾燥した不焼成塩
基性耐火物、或いは非酸化性雰囲気で焼成した焼
成塩基性耐火物として供することが可能であり、
また不定形耐火物を製造することもできる。以下
に実施例をあげて本発明をさらに詳しく説明す
る。
〔実施例及び効果〕
実施例 1
ノボラツク型フエノール樹脂を製造し、冷却す
る過程で該樹脂65重量部に対してエチレンカーボ
ネート15重量部、プロピレンカーボネート20重量
部を添加して105poise/25℃の液状樹脂を得た。
[Industrial Application Field] The present invention is directed to unsintered refractories partially or entirely using dolomite clinker, magnesia clinker, fused calcia, fused magnesia calcia, sintered calcia clinker, etc. containing free CaO. and a method for producing a monolithic refractory or a fired refractory produced by firing these in a non-oxidizing atmosphere. [Prior Art] It is well known that magnesia-carbon bricks have been rapidly becoming popular in steelmaking furnaces such as converters in recent years. Magnesia-carbon brick is an unfired refractory that uses electrofused or sintered magnesia clinker as the magnesia source, natural phosphorous graphite as the carbon source, and phenolic resin as the binder. In addition, it is a refractory with excellent corrosion resistance and spalling resistance, combining the characteristics of graphite with high corrosion resistance and high thermal shock resistance. The wear condition of such magnesia-carbon bricks in an actual furnace is that there is almost no peeling due to spalling, and the bricks are smoothly melted away from the working surface. Factors that affect this erosion rate include:
In addition to factors that depend on chemical reactions such as the CaO/SiO 2 ratio of the slag and the amount of iron oxide, physical wear associated with the flow of molten steel and molten slag is considered. Graphite in refractories has the property of not being easily wetted by silicates, but has the disadvantage that iron oxides such as FeO in slabs are easily oxidized and disappear. Furthermore, although magnesia is relatively stable against iron oxides, it forms CMS, C 3 MS 2 and the like and dissolves against silicates, especially silicates with low C/S.
As described above, it is thought that in molten slag containing iron oxide, oxidation of graphite and erosion of magnesia occur in parallel, leading to progress of erosion. On the other hand, there is a magnesia-calcia-carbon brick as a material having different characteristics from the above-mentioned magnesia-carbon brick. Calcia-containing raw materials, such as magdro clinker and dolomite clinker, have traditionally been used for fired magdro bricks, and have excellent slag penetration resistance and good resistance to structural spalling. It is well known that the furnaces that produce refractories have poor corrosion resistance, and as operating conditions have become more severe, there has been a shift to high magnesia and low calcia refractories. These magnesia-calcia-carbon bricks conventionally manufactured include tar,
There are tar dolomite bricks that use pittuce as a binder. Normally, this refractory is made of magnesia, dolomite, and a small amount of graphite, but because the amount of graphite used is small, it is not sufficient to reduce the iron oxide slag, and if the amount of graphite used is increased. Since the pitches are thermoplastic, they undergo large expansion in the direction perpendicular to the graphite orientation direction during heat treatment, making it difficult to obtain a good structure. Furthermore, when using a phenolic resin such as magnesia-carbon bricks, the resol type is unsuitable because bound water is generated during curing, which causes digestion of the calcia-containing raw material and causes the brick to collapse. When using a novolac type phenolic resin with hexamethylenetetramine as a curing agent, there is no noticeable digestion phenomenon as with the resol type, but digestion still occurs during heat curing or during the process of lining a furnace with refractory material and raising the temperature. This is not preferable because it may cause cracks or structural deterioration. For this reason, magnesia-calcia-carbon refractories using phenolic resin as a binder have not been put into practical use. [Purpose of the Invention] In order to eliminate the various defects described above, the present inventors have discovered that when a refractory containing free CaO contains a large amount of carbon source such as graphite, calcia is not necessarily as large as magnesia. It cannot be said that the corrosion resistance is inferior. That is, among the slag components, iron oxide, which has the most adverse effect on calcia, has a significantly reduced activity due to an oxidation-reduction reaction with carbon contained in the refractory, and is unlikely to cause any adverse effects on calcia. As mentioned above, the slag reduced by carbon, especially its composition, is as low as in the early stage of converter blowing.
With the CaO/ SiO2 ratio, calcia has the property of temporarily increasing the melting point of the reaction layer by reacting with slag, forming a high melting point reaction layer on the working surface and increasing the magnesia-carbon brick. It can be expected to have the effect of suppressing the continuous erosion seen in Furthermore, from a thermodynamic point of view, calcia has excellent stability in the coexistence of carbon, and we have found that calcia has an advantage under usage conditions where direct reaction between magnesia and carbon is a concern. In this paper, we researched a method to eliminate the above defects using a phenolic resin as a binder. The present inventor investigated the cause of the digestion phenomenon caused by phenolic resin, and made it possible to use raw materials containing free CaO by using a special solvent and phenolic resin together. The decomposition of phenolic resin's hydroxyl group and the use of hydrophilic solvents are thought to be the causes of digestion associated with the use of novolak-type phenolic resins. Generally, monohydric alcohols such as methyl alcohol, ethyl alcohol, and propyl alcohol, and polyhydric alcohols such as ethylene glycol, propylene glycol, and glycerin are used as solvents for phenolic resins, but these are all hydrophilic solvents and do not cause calcia. It has hygroscopic properties that are most detrimental to the raw materials it contains. According to research on phenolic resin chemistry, 300℃
It has been reported that a large amount of water is generated in the vicinity. This is presumed to be due to decomposition of phenolic hydroxyl groups. The present invention solves the above-mentioned drawbacks of phenolic resins, which are factors for digestion, at once by using alkylene carbonate as a solvent. [Effects of the Invention] The present invention has excellent corrosion resistance and spalling resistance by using phenolic resin and alkylene carbonate as binders in the production of basic refractories containing free CaO, and
This is a method for producing refractories that are not digestible with phenolic resin. The alkylene carbonate used in the present invention is preferably a colorless, transparent, odorless, non-hygroscopic, non-corrosive, stable liquid alkylene carbonate such as ethylene carbonate or propylene carbonate. The phenolic resin used in the present invention is obtained by reacting common phenol or phenols with a formaldehyde source under a catalyst. Here, the phenols may be compounds having one or more phenolic hydroxyl groups in one molecule and having two or more vacant positions ortho or para to the phenolic hydroxyl groups. More specifically, phenol, cresol, chlorophenol, nonylphenol, butylphenol, phenylphenol, bisphenol A, phenolphthalein,
Examples include resorcinol, methylresorcinol, hydroquinone, naphthol, isopropenylphenol, and the like. Of course, it is also possible to use a mixture of two or more of these phenols. Regarding the form of the phenolic resin, a novolak type is preferable because it generates less condensed water, but even resol types are polymerized through a reaction during resin production.For example, solid resols generate relatively less condensed water during curing. If used in combination with the solvent according to the present invention, it can be used without causing fatal digestion, and in this case, it is even better if the methylol group of the resol is butoxylated with butanol or the like. Of course, it is also possible to use the novolak type and the resol type in combination. Examples of the alkylene carbonate used in combination with the phenolic resin include ethylene carbonate, propylene carbonate, etc., but are not necessarily limited to these, and any alkylene carbonate that is reactive with a phenolic hydroxyl group can be used. There are various methods for using resins and solvents. A suitable amount of alkylene carbonate is added during the reaction completion or cooling process when producing phenolic resin, and a binder adjusted to an appropriate viscosity is used.Alternatively, phenolic resin and alkylene carbonate are added simultaneously during refractory kneading and the alkylene carbonate is added during the kneading process. Although there are methods such as dissolving the resin, the present invention is not limited to this method as long as the premise that the phenol resin and alkylene carbonate coexist is satisfied. There is no limit to the ratio of phenolic resin to alkylene carbonate used, but from the viewpoint of kneading properties of the refractory and performance of the refractory, the weight ratio of phenol resin to alkylene carbonate is preferably in the range of 40:60 to 90:10. If the ratio of alkylene carbonate used is low, there will be a large number of phenolic hydroxyl groups that are not converted into hydroxyalkyl ethers, which is not sufficient to suppress the digestion of calcia-containing raw materials, and conversely, if the ratio of alkylene carbonate used is high, the amount of phenolic hydroxyl groups that will not be converted into hydroxyalkyl ethers will be insufficient to suppress the digestion of calcia-containing raw materials. Since the proportion of the solvent that does not contribute to the refractory increases, the strength structure of the refractory deteriorates, which is undesirable. Further, as a characteristic reaction of the alkylene carbonate used in the present invention, phenolic hydroxyl groups are quantitatively converted into hydroxyalkyl ether during heat curing of the resin. At this time, free CaO in the refractory
serves as a catalyst for this reaction, so the alkylene carbonate used as a solvent efficiently contributes to the reaction. A cured phenolic resin in which phenolic hydroxyl groups were converted to hydroxyalkyl ethers was thermally decomposed at various temperatures in an N 2 atmosphere, and the amount of water generated was measured by gas chromatography. The cured resin according to the present invention using propylene carbonate as a solvent generates about 1/7 the amount of water at 300°C and about 1/7 at 400°C compared to a normal cured resin using ethylene glycol as a solvent. 6, which was confirmed to have extremely favorable properties for calcia-containing raw materials that have remarkable digestibility. The essential refractory raw materials used in the present invention include one or more calcia-containing raw materials such as magdromite, dolomite, fused or sintered calcia, and fused magnesia-calcia. Oxides such as spinel, and non-oxides such as graphite, carbon black, coke, anthracite, silicon carbide, silicon nitride, and boron carbide can also be used. In addition, metals such as Al, Cr, Ni, Fe, and Si, or their carbides and nitrides may be added, and surfactants, surfactants, etc. may be added to improve the affinity and adhesion between aggregate and resin.
Coupling agents may also be added. The refractory according to the present invention can be provided as an unfired basic refractory dried at a low temperature, or a fired basic refractory fired in a non-oxidizing atmosphere,
It is also possible to produce monolithic refractories. The present invention will be explained in more detail with reference to Examples below. [Examples and Effects] Example 1 A novolac type phenolic resin was produced, and during the cooling process, 15 parts by weight of ethylene carbonate and 20 parts by weight of propylene carbonate were added to 65 parts by weight of the resin to form a liquid at 105 poise/25°C. Resin was obtained.
【表】
第1表の化学組成を有するマグドロクリンカー
を使用して第2表実施例1による不焼成マグドロ
−カーボンれんがを得た。エチレングリコールを
溶剤とした通常の樹脂(比較例1)では乾燥時に
消化による大きな膨張、亀裂を生じたのに対し、
本発明によるれんがは良好な物性を得た。
このれんがを150トン転炉トラニオン部に使用
した。従来のマグネシア−カーボンれんがの溶損
速度が0.35mm/chであつたのに対し、該れんがは
0.30mm/ch溶損速度であり約15%の耐用性向上が
みられた。[Table] Unfired Magdro carbon bricks according to Example 1 in Table 2 were obtained using Magdro clinkers having the chemical compositions in Table 1. In contrast to the conventional resin using ethylene glycol as a solvent (Comparative Example 1), which caused large expansion and cracking due to digestion during drying,
The bricks according to the invention obtained good physical properties. These bricks were used for the trunnion part of a 150-ton converter. While the erosion rate of conventional magnesia-carbon bricks was 0.35 mm/ch, this brick
The corrosion rate was 0.30mm/ch, and an approximately 15% improvement in durability was observed.
【表】【table】
【表】
実施例 2〜4
ノボラツク型フエノール樹脂を製造し、冷却す
る過程で、該樹脂75重量部に対してプロピレンカ
ーボネート25重量部を添加して122poise/25℃の
液状樹脂を得た。
第3表のドロマイトクリンカー、電融カルシア
クリンカーを用いて第4表の不焼成れんがを製造
した。ジエチレングリコール及びメチルアルコー
ルを溶剤とした通常の樹脂では消化による亀裂が
発生し品質測定不能な状態であつたのに対し本発
明による実施例2〜4では良好な物性を得た。
実施例3の不焼成耐火物を120トンLF法取鍋ス
ラグラインに使用した。従来のマグネシア−カー
ボンれんが(比較例3)の平均ライフが57chで
あつたのに対し64chの耐用回数を記録し、優位
性が認められた。[Table] Examples 2 to 4 A novolak type phenolic resin was manufactured and during the cooling process, 25 parts by weight of propylene carbonate was added to 75 parts by weight of the resin to obtain a liquid resin at 122 poise/25°C. Unfired bricks shown in Table 4 were manufactured using the dolomite clinker and fused calcia clinker shown in Table 3. In the case of ordinary resins using diethylene glycol and methyl alcohol as solvents, cracks occurred due to digestion and the quality could not be measured, whereas in Examples 2 to 4 according to the present invention, good physical properties were obtained. The unfired refractory of Example 3 was used in a 120 ton LF method ladle slag line. Compared to the average life of conventional magnesia-carbon bricks (Comparative Example 3), which was 57 channels, the durability was recorded at 64 channels, and superiority was recognized.
【表】【table】
【表】
実施例 5
第1表のマグドロクリンカーと海水マグネシア
クリンカーを用いてマグドロ質スタンプ材を得
た。200×200×200mmの枠にスタンプ施工し、各
温度を処理した結果、第5表のように本発明によ
るスタンプ材は良好な物性が得られた。[Table] Example 5 A maguro-based stamp material was obtained using the maguro clinker and seawater magnesia clinker shown in Table 1. As a result of applying a stamp to a frame of 200 x 200 x 200 mm and treating it at various temperatures, the stamp material according to the present invention had good physical properties as shown in Table 5.
【表】【table】
【表】【table】
Claims (1)
において、フエノール樹脂とアルキレンカーボネ
ートを使用することを特徴とする塩基性耐火物の
製造法。1. A method for producing a basic refractory comprising using a phenolic resin and an alkylene carbonate in producing a basic refractory containing free CaO.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58081491A JPS59207869A (en) | 1983-05-09 | 1983-05-09 | Manufacture of basic refractories |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58081491A JPS59207869A (en) | 1983-05-09 | 1983-05-09 | Manufacture of basic refractories |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59207869A JPS59207869A (en) | 1984-11-26 |
| JPS644978B2 true JPS644978B2 (en) | 1989-01-27 |
Family
ID=13747865
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58081491A Granted JPS59207869A (en) | 1983-05-09 | 1983-05-09 | Manufacture of basic refractories |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59207869A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63100053A (en) * | 1986-10-15 | 1988-05-02 | ハリマセラミック株式会社 | Manufacture of basic refractories |
| US5897703A (en) * | 1993-10-29 | 1999-04-27 | Tokyo Chemical Co., Ltd | Hardening composition, hardened product, and method of producing hardened product |
| JPH07126048A (en) * | 1993-10-29 | 1995-05-16 | Toyo Chem Co Ltd | Inorganic cured composition |
| US5686506A (en) * | 1995-04-04 | 1997-11-11 | Borden Chemical, Inc. | Mixtures of phenolic novolaks for use with refractory aggregate and methods for making same |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6026065B2 (en) * | 1978-06-13 | 1985-06-21 | 黒崎窯業株式会社 | Manufacturing method for basic refractories |
-
1983
- 1983-05-09 JP JP58081491A patent/JPS59207869A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59207869A (en) | 1984-11-26 |
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