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JP4421815B2 - Kiln apparatus and method for producing fired product of tanned silver candy - Google Patents
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JP4421815B2 - Kiln apparatus and method for producing fired product of tanned silver candy - Google Patents

Kiln apparatus and method for producing fired product of tanned silver candy Download PDF

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JP4421815B2
JP4421815B2 JP2002327604A JP2002327604A JP4421815B2 JP 4421815 B2 JP4421815 B2 JP 4421815B2 JP 2002327604 A JP2002327604 A JP 2002327604A JP 2002327604 A JP2002327604 A JP 2002327604A JP 4421815 B2 JP4421815 B2 JP 4421815B2
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gas
kiln
mixed
exhaust gas
salt
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JP2004123503A (en
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実 坂本
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Description

【0001】
【発明の属する技術分野】
発明は、陶器、土器、瓦等を焼成する窯を造り、焼成窯外に混合ガスの発生窯を併設し、焼成窯と連結し、焼成窯に焼き物の素地を詰め加熱を行い、焼成物が適温に達すれば、加熱窯の乾留窯を加熱しておき、焼成窯の釉化準備が整えば、直ちに乾留窯内に塩、硼酸及び松脂を混合したガス材を投入し焚口を閉め、水タンクから水滴状に乾留窯内へ、水を落下させて加熱を続行し、水蒸気ガスを発生させ、炭化水素ガス、塩ガス、硼酸ガス、水蒸気ガスの4種類の混合したガスを発生させ、混合ガスを焼成窯内へ送り込み、素地の表面のシリカと接触させ、炭化水素ガスの混ざった塩ガスが釉化反応を起こし釉化し、ガラス状の燻し銀色の釉被膜を形成する燻し銀色釉の焼成物に関する。
【0002】
【従来の技術】
従来の燻し銀色釉を得る方法は、特願昭53−117154号出願 坂本 実(本件出願者と同じ)が有すれど、この出願は燻化窯で焼成物の燻化を行なう時に、薪や石炭等の燻化材を窯内に食塩と同時に投入して、食塩ガスと燻化ガスを発生させて、燻し銀の釉を形成する形成方法が記されている。
上記、記載の当時の使用していた燻し窯は、だるま窯と煙突を付けた倒焔窯である。だるま窯は、燃焼室の床にロストルを付け、薪や石炭を燃料として焼成し、燃焼中に薪や石炭の燃料が燃え切って炭化しない内に、次の燃料を早めに投入し、ロストルの上面におきの火床を15cm前後の厚さに造っておき、素地が適温に達すれば風道を閉め、窯の窓(煙り出し口)を小さくして焚口より、薪や石炭をおきの火床の上に投入し、投入が終われば焚口、風道を密封し、窓を煙の出る量に応じて小さくして吹かしを行い、投入された薪や石炭は、おきの火床の高熱により乾留され、炭化水素ガスを発生して素地に接触して、炭素被膜を形成させる。燻し終われば窓の吹かし穴を塞ぎ、窯内へ空気が進入しないように練り土を用いて密封して、焼成を行なう燻し製造の土窯である。更に同記載の倒焔窯は、煙突を付けて倒焔の焔で素地を焼成し、排煙は煙突を通って大気に排出して焼成を行なう窯である。燻化も燻化ガスを倒焔の焔で行い、排煙は煙突の根元に吹かし穴を設けて、吹かしの調整を行なって煙突に流し大気に排出して燻化を行なっていた。上記のだるま窯も倒焔窯も共に、広い燃焼室にロストルを設けた窯で、厚いおきの火床を造れる燻化窯である。このだるま窯、倒焔窯に、薪や石炭を投入時に食塩を同時に投入して、燻し銀色の釉を形成させる方法である。
【0003】
更に特願昭51−117154号に、近時ガス燻化の窯や石油燻化の燻し瓦窯が使用されるようになり、ガスや石油窯で銀色釉の瓦を作る場合は、食塩を別個な加熱装置で加熱し、食塩ガスにして、配管よりガスと同じように流せばよい。と記している。このガスや石油窯とは、ガス窯は、プロパンガスをガスバーナーで燃焼し、燻化は窯の天井部に20〜30個のガス噴出ノズルを付け、ノズルからプロパンガスを噴出させて燻化を行なう窯である。又、石油窯の燃焼は石油を石油バーナーで燃焼し、燻化は石油タンクからゴムホースを付け、ホースの先端に鉄パイプを付け、パイプの先端を窯底へ差し込み、石油を流して燻化ガスを発生させて、燻化を行なう窯である。上記の燻化窯に別個に加熱装置を設けて、食塩を加熱し食塩ガスにして配管より流し込み、燻し銀色の釉を得る方法が記されている。以上が従来の公知の燻し銀色の釉の形成方法である。
【0004】
【発明が解決しようとする為の課題】
従来の特願昭53−117154号の燻し銀色釉の焼成物を焼く窯は、燻し銀釉の焼成物だけ焼く専用窯ではなく、燻し瓦を焼くだるま窯で焼成を行なっていた。この窯は、燃焼室の床の広いロストルの付いた窯で、薪や石炭を燃料として焼く燻し窯である。この窯で、燻し銀釉の被膜の焼成物を得るには、薪や石炭を焚いて焚き残ったおきが灰化しない内に、次の燃料を投入し、おきの火床を造ることが必須条件である。火床の造れない窯では、釉化材を投入しても塩や薪、石炭の気化熱により、燃焼室の床の温度が急冷する。高温度の混合ガスが大量に発生しないと、低温度の混合ガスでは素地表面に混合ガスが接触しても、釉化も燻化の反応も起きない。
【0005】
更に上記の窯は、燃焼終えた高温の窯内へ焚口の蓋を取り除き、塩や薪、石炭を混合よく火床の上に撒き散らし、濃淡の無い混合ガスの発生の作業を行なうことは不可能であった。
【0006】
燃焼室の火床の上面に塩、薪、石炭を1回投入すると、燃焼室の温度が1100℃以上に達していても、500℃〜450℃位まで降下する。その為、1つの焚口に1度に大量の釉化材を投入せず、1つの焚口に投入する量を3分して、燃焼室が急冷やしないように投入していた。このような操作を行なっても、投入物の気化熱により温度が急冷していた。
【0007】
更にこの窯は、燃焼時に薪や石炭を焚き、煤煙や灰を大量に大気に撒き散らす。更に、燻化時は風道を塞ぎ、排煙口を小さくして薪や石炭を焚口よりおきの火床の上に投入し、火床の熱により乾留されてモクモクと煤煙を大気に排出していた。その後、公害問題が厳しくなり、又、大気汚染法の規制により有害ガスの排出が禁じられ、上記方法で焼く窯は使うことが出来なくなった。
【0008】
更に燃焼室内のロストルの上に、大量のおきの火床を造って、塩、薪、石炭を投入し、混合ガスを発生させる方法は、窯止め後の冷却時に、燃焼室に大量の投入した薪や石炭の炭化物の蓄熱により、窯の温度の降下に時間を要した。火床の無い窯と冷却時間を比較すると、同じ焼成温度でも、火床の無い窯は5時間〜6時間、窯の冷却が早い。
【0009】
又、冷却終わった窯内温度が300℃になれば、窯開けを行なうのであるが、火床の有る窯は、各々焚口に水を水桶に3杯か4杯を用意し、焚口を開けると素早く桶の水を炭に掛け、発火を防いで炭をかき出すのである。300℃の高い温度の炭に水を掛ければ、熱い水蒸気が焚口より噴出し、大量の炭をかき出すことは重労働である。
【0010】
更に昭和50年ごろより、ガス、石油の液化燃料を用いてバーナーで燃焼し、ガス、又は石油で燻す鉄板製の窯が使用されるようになった。燃焼時は、煤煙も出さず大気を汚染することも無く、公害問題も起きないが、燻し銀色釉の焼成物を得ることは不可能である。この窯は瓦1000枚入りの焼成窯でも、焚口が前後で14個から16個付いていて、焚口の直径も12cm前後で小さく、塩や薪、石炭を投入することが出来ない。又、投入しても燃焼室の床に均一に投げ込むことが不可能であり、又、投入してもガスや石油の燃焼では、おきの火床が出来ない。火床の無い燃焼室の床に石炭や塩を投入しても、気化熱により燃焼室の床が急冷して、高温の良好な混合ガスの発生は不可能である。
【0011】
更に燻し銀釉の焼成物の釉化に必要なことは、素地が均一に焼けて釉化温度が適温であることは申すまでもない。素地が充分焼成されていても、燃焼室内へ塩、薪、石炭等を投入し、投入物の投入の状態が悪く、一方の隅は塩の投入が多く、片方は薪、石炭が多いような投入をすると、薪や石炭の炭化水素ガスが先に素地と接触して炭素被膜を形成する。炭素被膜を形成した後に塩ガスが接触しようとしても、炭素被膜に覆われて、素地の表面のシリカに接触できず、炭化水素ガスだけが、炭素被膜を形成する。この付着した炭素被膜は、窯出し時に手で触るとベラベラと禿げる。禿げた素地は真黒な不良品となる。更に、塩ガスが先に接触すれば、釉化してガラス状にはなるが、炭化水素ガス分子がガラス状の釉の中に染入ることは出来ず、燻し銀の釉を得ることは望めない。上記のように、従来の窯の燃焼室に塩、薪、石炭を投入する方法は、投入することに濃淡の差があり、良好に混合したガスの発生は難しく、一等品は30%以下であった。
【0012】
更に従来の燻し焼きの焼成物は、1300年余りの伝統の歴史を有するが、大和の法隆寺の屋根瓦を見ても、又、江戸時代に建立されたお寺の屋根瓦を見ても変色して、窯出しの時の美しい燻し銀色を、保ち続けている瓦はない。良質の粘土を使って名人が焼いた瓦でも、50年も過ぎれば、風雨にさらされて灰黒色に変色し、窯出し時の美しい燻し銀色の光沢を無くしている。又、海岸近くの燻しの屋根瓦は、潮風に当たると塩分により黒茶色に変色する。海水の飛沫が風と共に掛かり、瓦の中に浸透して、瓦の中の鉄分と接触し、塩分により酸化して表面が変色する。又、置物や家庭用品等に使用すれば、長い間に燻しの被膜が禿げ光沢が無くなり黒色となる。更に従来の燻しの焼成物は、無釉のため吸水率が高い。又、屋根瓦、土管、植木鉢のように屋外で使用するものは、寒冷地の使用は凍害になり、破損率が高い。
【0013】
次に従来の塩焼き窯について申し述べる。昭和50年前後までは、公害問題も今日のように厳しくはなく、兵庫県明石方面では、大きな事業所が50以上塩焼き瓦や土管を焼成し、焼成時は石炭を焚き真黒な煤煙を出し、釉化時は有害な塩ガスを大気に放出していた。その後、公害問題は官民を問わず厳しくなり、現在では塩焼きの業者は皆無となっている。
【0014】
【問題を解決する為の手段】
上記目的を達成する為に本発明は、焼成窯とガス発生の乾留窯を、各々別個に造り、焼成窯と乾留窯をガス幹管で連結し、焼成と釉化は焼成窯で行い、混合ガスの発生は乾留窯で発生させて、ガス幹管を通して燃焼終わった焼成窯へ送入し、釉化を行う構造とした。
【0015】
更に大量の煤煙を大気に撒き散らすことのない石油、及びガスの流体燃料を使用し、バーナーで燃焼する焼成窯を造り、更に加熱窯もバーナーで燃焼して加熱を行い、混合ガスの発生を可能とした。
【0016】
更に金属板で箱型の窯を造り、窯の底部の煙道中央にガス幹管を設置し、ガス枝管を畔と畔の間に配置し、ガス幹管と連結し、ガス枝管のガス噴出穴から混合ガスを噴出可能とし、焼成窯の天井に排ガス穴を設けて、釉化終わった排ガスが抜けるようにしておき、焼成終わった焼成窯の窯底から混合ガスが、ガス噴出穴から一斉に噴出し、直上に上昇して素地の表面と接触して釉化する。釉化終われば更に上昇して排ガス穴に入る。混合ガスが窯底から上昇して釉化する窯を形成した。
【0017】
更に排ガス穴の上部に排ガス室を設け、排ガス室の上に排ガス焼却室を設置し、通気開閉弁を付けた排ガス通気管で連結し、排ガス焼却室には焚口を付け、バーナーを取り付け燃焼可能とし、更に排ガス焼却室の続きに立体の浄化タンクを設け、排ガス焼却室と連結し通気可能として、浄化タンク内の上部に噴霧ノズルを付ける。更に浄化タンク外の直下に溶液タンクを設けて、水酸化ナトリウムを10倍の水に溶かして溶液タンクに入れておき、動力ポンプを付けて溶液を噴霧ノズルに送入して、噴霧可能としておき、浄化タンク底部に開閉弁を付けて、浄化タンクの溶液が、溶液タンクに落下するように取り付けておく。焼成窯の内の釉化が始まると同時に、焼却室のバーナーに点火し、動力ポンプの始動を行なっておき、通気管開閉弁を開けて燃焼ガス、及び混合排ガスは排ガス穴に入り、排ガス室、排ガス通気管を抜けて排ガス焼却室に入り、混合排ガス中の炭化水素ガスは、バーナーにより燃焼して除去される。更に混合排ガスは浄化タンクに入って、噴霧ノズルより噴出した水酸化ナトリウム溶液の濃霧の中に入り、混合排ガスの中の塩ガスと接触して、還元反応により塩に還元して塩水の粒となり、浄化タンク底に落下し、更に溶液タンクに溜まり循環を続けて塩ガスは浄化され、無害なガスだけが煙突に入り大気に排出される、燻し銀色釉の焼成窯の排ガス処理の方法。
【0018】
更に焼成窯とは別個に焼成窯の煙突の反対側に、混合ガス発生の乾留窯を耐熱金属で造り、一方を混合ガス材を投入する投入口を付け、反対側を焼成窯のガス幹管と連結し、混合ガスを通気可能としておき、乾留窯を加熱可能にする為、乾留窯の周囲を金属板で包み、内部を断熱材で張り付け、下部に焚口を付ける。焚口にはバーナーを取り付け、更に窯天井部にジグザグの煙突を建て、一曲がり目の箇所の天井部から下向けに、耐熱金属で造った筒状の蒸気発生管を取り付け、筒の中に繊維状の金属繊維を詰め込んでおく。更に水蒸気発生管の上部に水タンクを設け、パイプで水蒸気発生管と水タンクを連結し中間に水調整弁を付け、水蒸気発生管内の金属繊維の上部に水を落下可能としておく。
【0019】
先ず焼成窯に素地を詰め燃焼を始め、素地の温度が1150℃に近づけば、加熱窯の加熱バーナーに点火し、乾留窯及び蒸気発生管に加熱を行いつつ燃焼を続けておく。更に焼成窯の温度が適温に達すれば、バーナーの燃焼を小さくして釉化準備を行い、準備が終われば、焼成窯のバーナーの火を止め、乾留窯内に塩、松脂、硼酸の混合ガス材を投入し、蓋を閉めて燃焼を続ける。加熱により混合ガス材は乾留分解し、塩ガス、炭化水素ガス、硼酸ガスとなり、混合された割合に応じた量のガスが混合して発生する。更に水調整弁を開き、水タンクの水を水滴状に蒸気発生管内の金属繊維の上に落下を続け、高温の金属繊維により水滴は熱分解され、水蒸気ガスとなって乾留窯内に入る。先に発生した3種類の混合ガスに、少量の水蒸気ガスが加わり、水蒸気ガスが加わることにより、素地表面に混合ガスの付着を増進する。乾留窯内で4種類のガスが混じりあって混合ガスとなり、焼成窯に送入させて素地と接触して、燻し銀色の釉を形成する混合ガスの発生を特長とする混合ガス窯の装置。
【0020】
更に良好な燻し銀色の釉を得る為、乾留窯に投入してガス化に用いる資材を、素地表面のシリカと接触して釉化する塩を選び、更に釉化した釉が、釉の中に混じり合って、燻し銀色の釉となる炭化水素ガスの発生材を松脂を選び、更に光沢をよくする硼酸を加える。松脂は、砕いて粒状として混ぜ合わせる。混合率は、塩57%、松脂40%、硼酸3%前後が良好である。又、混合したものを窯に入れて加熱を行い、粘状に溶けた後、箱状の形に流し込み冷えた後取り出し、固形のブロックとしておけば、運搬、投入時に好適である。乾留窯に投入する量は、瓦窯の場合は、1000枚入りの窯で15〜18kgを投入すればよい。
【0021】
【発明の実施形態】
本発明の実施形態を実施例に基づき図面を参照して説明する。
焼成窯1の外形を金属板で箱型に造り、金属板の窯内部に断熱煉瓦を張り付け窯壁2を造り、窯底面に断熱煉瓦を張り、窯床3を造る。金属板で造った上下開閉の扉に、ウール状の断熱耐火物を張り付け、出入口扉4を組み立てる。更に金属板の天井部にウール状の耐火物を張り付け窯天井5を造る。両側下部に焚口6を複数設け、各々焚口6にバーナー7を設置し、燃焼可能となしておく。更に、煙道10を窯床3の中央に、窯壁2から一方を窯外の煙突11の基礎まで一文字に構築し、基礎の上に煙突11を建てる。煙突の基礎の上部に、煙道口12を設けて、密封可能な煙道蓋13を用意しておく。焼成窯1を焚き終わった時点で煙道口12に被せる。煙道口12の排煙の調節、及び開閉の作業を行なう扉14を煙突11の下部に設け、排煙の調節を可能となしておく。更に焼成室床15を支える畔16の耐火煉瓦を用意して造り、畔と畔の間に桁煉瓦を載せ焼成室床15を造る。床面には床下から焔や混合ガスが通る通焔穴22を設けておく。桁煉瓦の下が床下焔道17となり、床上が焼成室21となる。更に煙道10の中央に混合ガスが通るガス幹管18を通し、煙突11と反対側の窯壁2の外に、一部突出させて取り付ける。ガス噴出口20を設けた混合ガス枝管19を、畔16と畔16の中間に設置しておき、ガス幹管18と連結し、通気可能として、混合ガスが、ガス幹管18よりガス枝管19に入り、ガス噴出口20より噴出可能としておく。
【0022】
更に燃焼室24と焼成室21の奥側の境に、固定火扉風23を煉瓦で積み上げ、所々に火扉風の通焔穴22を設けて固定しておく。更に窯の出入口側の焼成室21と燃焼室24の境に窯出し時は取り外し、窯詰め終われば積み上げる、取り外し可能な煉瓦を用意しておき、窯詰め終わった後に固定火扉風23の高さと同じ高さまで積み上げ、通焔穴22を設けておく。
焼成時に強い焔が素地に当たらぬように火扉風を設置する。更に、焼成室床15中央部の煙道10の直上に、吸焔口26を設け、焼成中の焔が、吸炎口26に入り、煙道10に至るようにしておく。更に焼成室21の天井中央に、釉化時の排ガスが通気する排ガス穴27を設け、排ガス穴27の上部に長方形の排ガス室28を取り付ける。更に、排ガス室の上に焼成時は閉めておき、釉化時は開いて排気を行なう、通気管開閉弁30を取り付けた排ガス通気管29を取り付ける。
【0023】
更に排ガス室28の上部に排ガス焼却室31を設置し、排ガス通気管29で連結し通気可能とし、排ガス焚口32を付けた焚口に焼成室バーナー33を取り付け燃焼可能としておく。更に焼成窯1の側面に浄化タンク35を垂直に設置し、タンク内上部に噴霧ノズル36を設置し、更に浄化タンク35の外の下面に溶液タンク39を設置し、水酸化ナトリウムを10倍の水に溶かした溶液を入れておく。更に溶液を吸い上げる動力ポンプ38を取り付け、溶液タンク39の溶液を噴霧ノズル36により、噴出可能とするように、パイプ37で連結する。更に浄化タンク35の底部下面へ開閉弁40を付け、弁を開ければ、浄化タンク35内に溜まった溶液が、溶液タンクに落下可能としておく。更に浄化タンク35の下部から循環通気管41を煙道10と連結し、中間に循環開閉弁42を付けて、焼成窯1の冷却時に開け、通気可能としておく。更に排気ガス開閉弁44を付けた浄化ガス排気管43を、煙突11の煙道口12の上部から浄化タンク35の下部に連結し、通気可能としておく。
【0024】
次に加熱窯58を説明すると、焼成窯1の煙突11の反対側に、耐熱鋼で造った乾留窯45を長方形の箱形に造り、一方の側面にガス材の投入口47を設けて、窯蓋48を付けて開閉可能としておく。更に乾留窯45の投入口47の反対側を、焼成窯1の窯外壁に突出しているガス幹管18と連結する。更に乾留窯45の周囲を金属板で被い、内部を断熱耐火物を張り付けて、加熱室46を造る。加熱室46の下部に加熱室焚口49を設け、焚口には、加熱バーナー50を取り付け燃焼可能な状態としておく。加熱室46の天井の上部に、ジグザグのガス窯煙突51を建て、更に加熱室46の上に水タンク52を取り付け、水調整弁53を、水タンクの底部に下向けに取り付け、水調整弁53の下に透明のパイプで、U字型の水溜り59を取り付け、U字型の箇所に落下した水が溜まるようにし、水滴の落下が外見できるように取り付ける。水調整弁53を閉め忘れても、溜まっている水により閉め切られる。更に、ジグザグのガス窯煙突51の水平部から、蒸気発生管55を煙突の中に垂直に取り付け、蒸気発生管55の管の中に金属繊維56を詰めておく。更に蒸気発生管55上部と、水溜り59を水道パイプ54で連結し、水タンク52の水が蒸気発生管55内に落下可能としておく。次に蒸気発生管55と乾留窯45を蒸気パイプ57で連結しておく。以上が混合ガス発生装置である。
【0025】
更に本体装置の操作を記述すると、焼成窯1内に素地を詰めて、詰め終われば取り外し、火扉風25を積み上げて、固定火扉風23の高さと同等にしておく。更に出入口扉4を閉め、次に排ガス室28の上部にある通気管開閉弁30を閉め、煙突11の下部の煙道蓋13を取り外し、調節扉14を閉め、更に循環開閉弁42及び排ガス開閉弁44を閉める。次に乾留窯45の窯蓋48を閉めて点火用意をしておく。更に焼成窯1の両側の焚口6の、バーナー7に点火し焚き始める。焔は燃焼室24から上昇し天井部に至り、徐々に焼成室21の中央に入り、素地の間を抜けて吸焔口26に入り、更に煙道10を抜け煙突11に入り、煙突内を抜けて排出し燃焼を続ける。上部の素地が焼けると焔は、徐々に下部に入り吸焔口26に入る。下部が焼けると、床下焔道17からも通焔穴22を抜けて、下積みの素地の間を抜けて吸焔口26に入り、煙道10を通って煙突11に入り排気され焼成を続ける。更に素地が1150℃の温度に近づけば、加熱窯58の加熱バーナー50に点火し、乾留窯45及び蒸気発生管55を空焚き始めておく。
【0026】
焼成窯1の温度が1150℃前後の適温に達すれば、焼成窯1のバ−ナー7の火を小さくしておき、調節扉14を開いて煙道蓋13を煙道口12に被せ、煙道10を遮断し、更に排ガス通気管29の通気管開閉弁30を開き、次に排ガス開閉弁44を開け、溶液タンク39の溶液開閉弁40を開けて、釉化準備を整える。
【0027】
焼成窯1の釉化準備が整えば、バーナー7の燃焼を止めて、焚口蓋8で蓋をして、止金9で締め付けておき、加熱中の乾留窯45の窯蓋48を開き、混合ガス材を乾留窯45内へ素早く投入し、窯蓋48を閉めて加熱バーナー50を強火にして温度を上げ、混合ガスの発生を続け、水タンク52の水調整弁53を開き、水溜り59へ落下する水滴の量を見ながら調整を行なって、蒸気発生管55内に、点滴状に水滴の落下を始めておく。落下した水は、蒸気発生管55内の金属繊維56に接触して気化し水蒸気ガスとなり、蒸気パイプ57を通って乾留窯45内に入る。乾留窯が加熱を続けることにより混合ガス材が熱分解され、塩、松脂、硼酸は混合ガスとなり、更に水蒸気ガスが加わり、4種類のガスが同時に1つの窯内で発生し、否応なしに混ざり合い、濃淡のない混合ガスとして発生し、ガス幹管18に流入させて加熱を続けておき、通気管開閉弁30を開き、更に焼却室バーナー33に点火し、燃焼を始めておき、続いて動力ポンプ38のスイッチを入れて始動を始め、溶液タンク39内の水酸化ナトリウムの溶液を吸い上げ、噴霧ノズル36に送って噴出させ浄化タンク35内を濃霧状としておく。
【0028】
更に乾留窯45から発生した混合ガスは、ガス幹管18を通って、焼成室床15の床下全面に配管されたガス枝管19に入り、枝管に設けられたガス噴出口20により一斉に噴出し、焼成室床15の床全面にある通焔穴22を抜けて、焼成室21の底に充満する。次々に送り込まれる混合ガスは、燃焼ガスより温度が低く比重が重い。比重の重い混合ガスは素直に上昇して混合排ガス穴27に入り、更に排ガス室28に集められ、排ガス通気管29を抜けてガス焼却室31に入る。
【0029】
焼成された高温の素地は、燃焼ガスが追い出され混合ガスと徐々に入れ替わり、素地表面に接触付着し、素地表面のシリカと塩ガスが高い温度により釉化反応を起こし、炭化水素ガスが混ざったまま釉化する。混合ガスに混ざっている水蒸気ガスは、素地に混合ガスの付着を良くし、硼酸ガスは釉化を助け光沢をよくしながら50〜60分間吹かし作業を行なう。
【0030】
吹かし続行中の混合ガスは、排ガス焼却室31に入り、焼却バーナー33により焼却され、混合ガス中の炭化水素ガスは、燃焼して除去される。燃えない硼酸ガスと塩ガスは、浄化タンク35に入り、水酸化ナトリウム溶液の噴霧の中を降下し、塩ガスと接触して還元反応により、塩に還元して塩水の粒となって浄化タンク35の底に落下し、開閉弁40を通って、溶液タンク39に溜まる。再び動力ポンプ38に吸い上げられ、循環を繰り返し浄化を行なう。浄化タンク35内で塩ガスを除去された排ガスは、有害物質のない硼酸ガスだけの排ガスになって、浄化ガス排気管43に入り、更に煙突11に入り大気に排出される。乾留窯45からガスの発生は、50〜60分で乾留されてガス発生が終わる。
【0031】
乾留が終わりに近づけば、吹かしの混合排ガスの勢いがなくなり、真黒であった排ガスの色は、透明に近い色となる。その頃を見計らって窯止め作業を開始する。窯止めの操作は、加熱窯58の加熱バーナー50の燃焼を止め、次に水調整弁53を閉め、水の流れを止める。更に排ガスの通気管開閉弁30を閉め、次に焼却室バーナー33の燃焼を止め、焚口蓋34を用いて、排ガス焚口32に被せて密封する。更に動力ポンプ38の電源を切り、浄化タンク35の下部の開閉弁40を閉め、更に排ガス開閉弁44を閉めて、窯止めを終了する。窯止め後、1時間過ぎれば、次は冷却段階に入るのである。先ず、通気管開閉弁30、及び循環開閉弁42を1度に開放せず、20分間おきに3回に分けて少しずつ開け、3回目には全開して、窯開けまでそのままにして冷却を行なう。
【0032】
上記操作を行なうことにより窯内の高温ガスは上昇を始め、排ガス穴27を抜けて排ガス室28に入り、更に排ガス通気管29を抜け、排ガス焼却室31内に入り、ここで冷却され冷めたガスは、浄化タンク35の上部に入る。冷却されて比重が重くなったガスはタンク内を降下して、循環通気管41を通って煙道10に至り、焼成窯1内の煙道10を、横に流れ込む。次々と比重の重いガスが降下すると、煙道10内のガスは、煙道10の直上にある吸焔口26を抜けて、焼成窯1の窯底に流れ込み、窯底から比重の重いガスが比重の軽いガスを、下から押し上げる。押し上げられた軽いガスは次々と上昇して、再び排ガス穴27に入り、更に上昇して排ガス室28及び排ガス通気管29を抜けて、排ガス焼却室31に入って冷却され、更に浄化タンク35を降下して循環を繰り返す。対流作用による冷却方法で冷却を行ない、300℃以下になれば、出入口扉4を徐々に開けて窯出しを行なう。
【0033】
浄化終わった水酸化ナトリウム溶液の噴霧によって塩水となって浄化タンク39に溜まった廃液は、強アルカリ性のため希硫酸を加えて、PH7.0〜PH8.0に中和し、無害となして海に流し処置を行なう。
【0034】
【発明の効果】
本発明は、以上の説明のように構成されているので、以下に記載されるような効果を果たす。
【0035】
焼成窯外に混合ガス発生装置を設け、塩、松脂、硼酸の混合ガス材を、乾留窯に入れて加熱を行ない、水タンクから水滴を注入することにより、塩ガス、炭化水素ガス、硼酸ガス、水蒸気ガスの4種類のガスが、投入量に応じた釣合いのよい高温の混合ガスを得ることが可能となり、製品も、一等品が95%以上となった。
【0036】
釉化操作開始から終わるまで、焼成室の床底全面から同時に濃淡のない混合ガスを噴出することにより、炭化水素ガスだけが先に素地に接触して炭素被膜を形成し、塩ガスが接触しても釉化反応を起こさない。又、炭化水素ガス不足の塩ガスが接触しても、燻し銀色の釉の形成を行なわない等の不合理なことが起きないようになった。
【0037】
ガス発生の混合ガス発生装置を焼成室とは別個に設けて、乾留窯に加熱を続けて、高温の混合ガスを焼成窯に送ることにより、焼成窯内に、塩、石炭、薪を投入する時のような燃焼室が急冷することはない。窯が急冷すると窯壁や耐火煉瓦がひび割れを起こし損傷が激しい。又、製品も急冷により釉化不良の製品が出来ることがあるが、そのようなことが起こらなくなった。
【0038】
更に乾留窯で混合ガスを発生させることにより、大量の石炭や薪を焚いて、おきの火床を造ることが不要になり、窯開け時に、高温の大量の炭やコークスをかき出す作業が要らなくなった。更に炭やコークスの保有熱が無いため、窯出し作業が簡単に行なえるようになった。
【0039】
窯止め終了後、焼成窯内の高温ガスが窯外へ誘導して、排ガス焼却室、浄化タンクを通し対流作用により循環させて、既存の設備を併用して冷却を早めることが可能となった。
【0040】
本発明の素地の表面を釉化する方法は、従来の釉薬を掛けて高温で釉薬を溶かす方法ではなく、焼成物の素地の中に既存するシリカが、混合ガス中の塩ガスと接触して釉化反応を起こし、釉化を得ることにより、小さな細工に仕上げた素地もそのまま釉化する。如何なる小さな細工も、釉化によって埋まったり、角が丸くなることはない。
【0041】
焼成窯より排出される釉化終わった混合排ガスの処理を、混合排ガス中の炭化水素ガスが燃焼室で燃焼し、更に塩ガスは、浄化タンク内で水酸化ナトリウムの溶液の噴霧と接触して還元反応を起こし、塩に還元して塩水となり、塩ガスは除去され有害なガスは、浄化されて公害を及ぼすことがなくなった。
【図面の簡単な説明】
【図1】 装置全体の断面図である。
【図2】 B−Bの断面図である。図中の8は焚口蓋(8)を上から見た図である。
【図3】 C−Cの断面図である。
【図4】 A−Aの断面図である。一部焼成室(24)を上から見た図である。
【符号の説明】
1 焼成窯 31 排ガス焼却室
2 窯 壁 32 排ガス焚口
3 窯 床 33 焼却室バーナー
4 出入口扉 34 排ガス焚口蓋
5 ヘ 35 浄化タンク
6 焚 口 36 噴霧ノズル
7 バーナー 37 パイプ
8 焚口蓋 38 動力ポンプ
9 止 金 39 溶液タンク
10 煙 道 40 開閉弁
11 煙 突 41 循環通気管
12 煙道口 42 循環開閉弁
13 煙道蓋 43 浄化ガス排気管
14 調節扉 44 排ガス開閉弁
15 焼成室床 45 乾留窯
16 畔 46 加熱室
17 床下焔道 47 投入口
18 ガス幹管 48 窯 蓋
19 ガス枝管 49 加熱焚口
20 ガス噴出口 50 加熱バーナー
21 焼成室 51 加熱窯煙突
22 通焔穴 52 水タンク
23 固定火扉風 53 水調整弁
24 燃焼室 54 水道パイプ
25 取り外し火扉風 55 蒸気発生管
26 吸焔口 56 金属繊維
27 排ガス穴 57 蒸気パイプ
28 排ガス室 58 加熱窯
29 排ガス通気管 59 水溜り
30 通気管開閉弁
[0001]
BACKGROUND OF THE INVENTION
The invention creates a kiln for firing pottery, earthenware, tiles, etc., has a mixed gas generation kiln outside the firing kiln, is connected to the firing kiln, is filled with the base of the pottery and heated, and the fired product is If the temperature reaches an appropriate temperature, heat the dry distillation kiln of the heating kiln, and if the baking kiln is ready for hatching, immediately put a gas material mixed with salt, boric acid and pine resin into the dry distillation kiln, close the throat, and close the water tank Water is dropped into the carbonization furnace in the form of water droplets, and heating is continued to generate steam gas, and four types of mixed gas, hydrocarbon gas, salt gas, boric acid gas, and steam gas, are generated. The fired product of tanned silver-colored soot is brought into contact with silica on the surface of the substrate, and the salt gas mixed with hydrocarbon gas undergoes a hatching reaction and hatches to form a glassy glazed silver-colored soot film. About.
[0002]
[Prior art]
A conventional method for obtaining a tanned silver candy is Japanese Patent Application No. 53-117154 filed by Minoru Sakamoto (same as the applicant of the present application). A forming method is described in which a hatching material such as coal is introduced into a kiln simultaneously with salt to generate salt gas and hatching gas to form a glazed silver shell.
The sushi kiln used at the time described above is a daruma kiln and an overturned kiln with a chimney. The Daruma kiln attaches a rooster to the floor of the combustion chamber, burns firewood and coal as fuel, and throws in the next fuel as soon as possible while burning firewood and coal fuel without burning and burning, A firebed on the top surface is built to a thickness of about 15cm, and when the substrate reaches the proper temperature, the airway is closed, the kiln window (smoke outlet) is made smaller, and firewood and coal are fired from the mouth. Put it on the floor, and when it is done, seal the entrance and the airway, blow down the window according to the amount of smoke, and throw the firewood and coal Carbonized to generate hydrocarbon gas and contact the substrate to form a carbon coating. When it is finished, it is a clay kiln manufactured by sashimi, which closes the hole in the window and seals it with kneaded clay so that air does not enter the kiln. Further, the above-described inverted kiln is a kiln in which a chimney is attached and the substrate is fired with the chimney of an overturn, and the smoke is discharged to the atmosphere through the chimney and fired. Hatching was carried out with the use of hatching gas, and the flue gas was hatched by making a blow hole at the base of the chimney, adjusting the blowing, and flowing it into the chimney to discharge it into the atmosphere. Both the above-mentioned Daruma kiln and fallen kiln are kilns with a wide combustion chamber and a roasting kiln that can create a thick firebed. This is a method in which salt is added to the daruma kiln and the inverted kiln at the same time as pouring and coal are added to form a silvery cocoon.
[0003]
In addition, Japanese Patent Application No. 51-117154 has recently used gas hatching furnaces and oil hatching tile tile kilns, and when making silver tile tiles in gas and oil kilns, separate salt. It may be heated with a simple heating device to form a salt gas, and flow in the same manner as the gas from the pipe. It is written. With this gas or oil kiln, the gas kiln burns propane gas with a gas burner, and hatching is performed by attaching 20 to 30 gas ejection nozzles on the ceiling of the kiln and ejecting propane gas from the nozzles. It is a kiln that performs. Oil kilns burn oil with an oil burner, and hatching attaches a rubber hose from the oil tank, attaches an iron pipe to the tip of the hose, and inserts the tip of the pipe into the kiln bottom. It is a kiln that generates and generates hatching. A method is described in which a heating device is separately provided in the above-described hatching furnace, and salt is heated to form a salt gas, which is poured from a pipe to obtain a silver-colored soot. The above is a conventional method for forming a tanned silver cocoon.
[0004]
[Problems to be Solved by the Invention]
The conventional kiln for burning fired silver-colored potatoes disclosed in Japanese Patent Application No. 53-117154 is not a dedicated kiln for burning only fired silver-glazed fired products, but fired tiles are fired in a kiln furnace. This kiln is a kiln with a wide combustion chamber floor and a kiln that burns firewood and coal as fuel. In this kiln, in order to obtain a fired product of a glazed silver candy film, it is indispensable to smash firewood and coal into the remaining fuel so that it does not ash and the next fuel is added to create a firebed for every fire. It is a condition. In a kiln that does not have a firebed, the temperature of the combustion chamber floor is rapidly cooled by the heat of vaporization of salt, soot, and coal even when the hatching material is added. If a large amount of high-temperature mixed gas is not generated, even if the mixed gas contacts the substrate surface in the low-temperature mixed gas, neither hatching nor hatching reaction occurs.
[0005]
Furthermore, the above-mentioned kiln removes the lid of the spout into the high-temperature kiln that has been burned, and mixes salt, soot, and coal on the firebed with good mixing, so that it is not possible to generate a mixture gas without concentration. It was possible.
[0006]
When salt, soot, and coal are once injected into the upper surface of the combustion chamber fire bed, even if the temperature of the combustion chamber reaches 1100 ° C. or higher, the temperature drops to about 500 ° C. to 450 ° C. For this reason, a large amount of hatching material was not introduced into one well at a time, but the amount to be charged into one well was divided into 3 minutes so that the combustion chamber was not rapidly cooled. Even when such an operation was performed, the temperature was rapidly cooled by the heat of vaporization of the input.
[0007]
Furthermore, this kiln burns soot and coal during combustion, and disperses a large amount of smoke and ash into the atmosphere. In addition, during hatching, the wind passage is closed, the smoke vent is made smaller, soot and coal are put on the firebed every other than the mouth, and it is dry-distilled by the heat of the firebed and exhausts the smoke and smoke into the atmosphere. It was. After that, pollution problems became severe, and emission of toxic gases was prohibited by the regulations of the Air Pollution Law, making it impossible to use kilns baked by the above method.
[0008]
Furthermore, a method of creating a large amount of firebed on the rooster in the combustion chamber and adding salt, firewood, and coal to generate a mixed gas was introduced into the combustion chamber during cooling after kiln stoppage. It took time to lower the temperature of the kiln due to the heat storage of firewood and coal carbide. Comparing the cooling time with a kiln without a firebed, the kiln without a firebed cools the kiln quickly for 5 to 6 hours even at the same firing temperature.
[0009]
In addition, when the temperature in the kiln after cooling reaches 300 ° C., the kiln is opened. However, each kiln with a firebed is prepared with 3 or 4 cups of water in the culvert and when the groin is opened. Quickly sprinkle firewood water on charcoal to prevent ignition and scavenge charcoal. It is hard work to sprinkle a large amount of charcoal when hot water vapor spouts from the mouth if water is put on the high temperature charcoal at 300 ° C.
[0010]
Furthermore, from around 1975, iron-plate kilns burned with a burner using gas or petroleum liquefied fuel and then burned with gas or petroleum have been used. At the time of combustion, no smoke or smoke is produced, the air is not polluted, and no pollution problems occur. However, it is impossible to obtain a burned silver-colored fired product. This kiln is a firing kiln containing 1000 pieces of tiles, and has 14 to 16 sheds at the front and back, and the diameter of the shed is small at around 12 cm, and salt, firewood, and coal cannot be input. Moreover, even if it is thrown in, it cannot be thrown uniformly into the floor of the combustion chamber. Even if coal or salt is put into the floor of the combustion chamber without a fire bed, the combustion chamber floor is rapidly cooled by the heat of vaporization, and it is impossible to generate a good mixed gas at a high temperature.
[0011]
Further, it is needless to say that the hatching of the fired product of the glazed silver bran is that the substrate is uniformly burned and the hatching temperature is appropriate. Even if the substrate is sufficiently baked, salt, soot, coal, etc. are put into the combustion chamber, the state of the input of the input is bad, one corner has a lot of salt input, and one side has a lot of soot and coal When charged, soot and coal hydrocarbon gas first comes into contact with the substrate to form a carbon coating. Even if the salt gas tries to contact after forming the carbon coating, it is covered with the carbon coating and cannot contact the silica on the surface of the substrate, and only the hydrocarbon gas forms the carbon coating. This attached carbon coating will be bald when touched by hand when leaving the kiln. The bald base becomes a black defect. Further, if the salt gas comes into contact first, it is hatched to become glassy, but hydrocarbon gas molecules cannot penetrate into the glassy soot, and it is not possible to obtain tanned silver soot. As described above, the method of adding salt, soot, and coal into the combustion chamber of a conventional kiln has a difference in density in the input, it is difficult to generate a well-mixed gas, and the first-class product is 30% or less Met.
[0012]
Furthermore, the traditional fired baked goods have a history of more than 1300 years, but even if you look at the roof tiles of Horyu-ji Temple in Yamato or the roof tiles of temples built in the Edo period, the color changes. And there is no roof tile that keeps the beautiful tanned silver color when it leaves the kiln. Even a tile baked by a master using high-quality clay, after 50 years, it has been exposed to wind and rain and turned gray-black in color, losing the beautiful tanned silvery luster when leaving the kiln. In addition, the tile roof tiles near the coast turn black-brown due to salt when hit by the sea breeze. Sea water splashes with the wind, penetrates into the roof tile, comes into contact with iron in the roof tile, oxidizes by the salt, and discolors the surface. Moreover, if it is used for figurines and household goods, the tanned film will fade and become black for a long time. Furthermore, the conventional baked fired product has a high water absorption rate because it is free of wrinkles. In addition, those used outdoors such as roof tiles, clay pipes, and flower pots are frost-damaged in cold regions and have a high damage rate.
[0013]
Next, I will describe the conventional salt-baked kiln. Until around 1975, the pollution problem was not as severe as it is today, and in the Akashi area of Hyogo Prefecture, more than 50 large-scale salt fired tiles and clay pipes were fired. During hatching, harmful salt gases were released into the atmosphere. Since then, pollution problems have become severe, regardless of public or private sector, and there are now no salt-bakers.
[0014]
[Means for solving problems]
In order to achieve the above object, the present invention creates a firing kiln and a gas generating dry distillation kiln separately, connects the firing kiln and the dry distillation kiln with a gas trunk pipe, performs firing and hatching in the firing kiln, mixing The gas was generated in a dry distillation kiln, sent to a firing kiln that had been burned through a gas trunk, and hatched.
[0015]
In addition, using a fluid fuel of oil and gas that does not disperse a large amount of smoke into the atmosphere, create a firing kiln that burns with a burner, and also a heating kiln that burns and heats with a burner to generate mixed gas It was possible.
[0016]
In addition, a box-shaped kiln is made of metal plates, a gas trunk pipe is installed in the center of the flue at the bottom of the kiln, a gas branch pipe is placed between the banks, and connected to the gas trunk pipe. The mixed gas can be ejected from the gas ejection hole, and an exhaust gas hole is provided in the ceiling of the firing kiln so that exhausted exhaust gas can escape, and the mixed gas flows from the bottom of the firing kiln to the gas ejection hole. It erupts all at once, rises directly above and contacts the surface of the substrate and hatches. After hatching, it rises further and enters the exhaust hole. A kiln was formed in which the mixed gas rose from the kiln bottom and hatched.
[0017]
In addition, an exhaust gas chamber is provided above the exhaust gas hole, an exhaust gas incineration chamber is installed above the exhaust gas chamber, connected by an exhaust gas vent pipe with a vent on / off valve, a flare is attached to the exhaust gas incineration chamber, and a burner can be attached for combustion In addition, a three-dimensional purification tank is provided after the exhaust gas incineration chamber, and connected to the exhaust gas incineration chamber so as to allow ventilation, and a spray nozzle is attached to the upper portion of the purification tank. In addition, a solution tank is provided directly under the purification tank. Sodium hydroxide is dissolved in 10 times water and placed in the solution tank, and the solution is sent to the spray nozzle with a power pump to enable spraying. Then, an opening / closing valve is attached to the bottom of the purification tank so that the solution in the purification tank is dropped to the solution tank. At the same time the hatching of the firing furnace begins, the burner in the incineration chamber is ignited, the power pump is started, the vent pipe on / off valve is opened, the combustion gas and mixed exhaust gas enter the exhaust gas hole, and the exhaust gas chamber The hydrocarbon gas in the mixed exhaust gas is burned and removed by the burner through the exhaust gas vent pipe and entering the exhaust gas incineration chamber. Further, the mixed exhaust gas enters the purification tank, enters the concentrated mist of the sodium hydroxide solution ejected from the spray nozzle, contacts the salt gas in the mixed exhaust gas, and is reduced to salt by a reduction reaction to form salt water particles. A method of exhaust gas treatment for a tanned silver-colored fired kiln that falls to the bottom of the purification tank and further accumulates in the solution tank and continues to circulate to purify the salt gas, and only harmless gas enters the chimney and is discharged to the atmosphere.
[0018]
In addition to the firing kiln, on the other side of the chimney of the firing kiln, a dry distillation kiln that generates mixed gas is made of heat-resistant metal, and one side is provided with an inlet for introducing mixed gas material, and the other side is the gas trunk of the firing kiln. In order to allow the mixed gas to be ventilated and to heat the dry distillation kiln, the periphery of the dry distillation kiln is wrapped with a metal plate, the inside is attached with a heat insulating material, and a throat is attached to the lower part. A burner is attached to the shed, a zigzag chimney is built on the ceiling of the kiln, a cylindrical steam generation pipe made of heat-resistant metal is attached downward from the ceiling at the first bend, and fibers are placed in the cylinder. Stuffed metal fibers. Further, a water tank is provided at the upper part of the water vapor generating pipe, the water vapor generating pipe and the water tank are connected by a pipe, a water regulating valve is provided in the middle, and water can be dropped onto the upper part of the metal fiber in the water vapor generating pipe.
[0019]
First, the substrate is filled in the firing kiln and starts burning. When the temperature of the substrate approaches 1150 ° C., the heating burner of the heating kiln is ignited, and combustion is continued while heating the dry distillation kiln and the steam generating tube. Furthermore, if the temperature of the firing furnace reaches an appropriate temperature, the combustion of the burner is reduced to prepare for hatching. When the preparation is completed, the firing of the firing furnace is stopped, and a mixed gas of salt, pine resin and boric acid in the dry distillation furnace Add material, close the lid and continue burning. The mixed gas material is subjected to dry distillation cracking by heating to become a salt gas, a hydrocarbon gas, and a boric acid gas, and an amount of gas corresponding to the mixed ratio is generated. Further, the water regulating valve is opened, and the water in the water tank continues to drop onto the metal fibers in the steam generation pipe, and the water drops are thermally decomposed by the high-temperature metal fibers to enter the dry distillation kiln as steam gas. A small amount of water vapor gas is added to the three types of mixed gas generated earlier, and the water vapor gas is added to promote the adhesion of the mixed gas to the substrate surface. A mixed gas kiln apparatus characterized by the generation of a mixed gas that mixes four types of gas in a dry distillation kiln to form a mixed gas, which is sent to the firing kiln and contacts the substrate to form a tanned silver-colored soot.
[0020]
In order to obtain a better tanned silver cocoon, the material used for gasification by putting it in a dry distillation kiln is selected as a salt that hatches in contact with the silica on the surface of the substrate. Select rosin as the hydrocarbon gas generating material that mixes and turns into a silver-colored soot, and then adds boric acid to improve gloss. The pine resin is crushed and mixed in a granular form. As for the mixing rate, 57% salt, 40% pine resin, and 3% boric acid are good. Moreover, after mixing and putting into a kiln and heating and melt | dissolving in a viscous form, it is suitable for the time of conveyance and injection | throwing-in if it takes out after pouring into a box shape and taking out as a solid block. In the case of a tile kiln, the amount put into the dry distillation kiln may be 15-18 kg in a 1000-sheet kiln.
[0021]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described based on examples with reference to the drawings.
The outer shape of the firing kiln 1 is made in a box shape with a metal plate, a heat insulating brick is attached to the inside of the metal plate kiln to make a kiln wall 2, a heat insulating brick is attached to the bottom of the kiln, and a kiln floor 3 is made. Wool-like heat-insulating refractories are attached to the upper and lower doors made of metal plates, and the door 4 is assembled. Further, a kiln ceiling 5 is constructed by attaching a wool-like refractory to the ceiling of the metal plate. A plurality of sheds 6 are provided at the lower portions of both sides, and burners 7 are installed in the sheds 6 respectively so that combustion is possible. Furthermore, the chimney 10 is constructed in the center of the kiln floor 3, one side from the kiln wall 2 to the foundation of the chimney 11 outside the kiln, and the chimney 11 is built on the foundation. At the upper part of the chimney foundation, a flue port 12 is provided to prepare a sealable flue lid 13. When the firing kiln 1 is finished, it is placed over the flue 12. A door 14 for adjusting the flue gas at the flue port 12 and performing the opening and closing operation is provided at the lower part of the chimney 11 so that the flue gas can be adjusted. Further, a refractory brick of the shore 16 that supports the firing chamber floor 15 is prepared, and the firing chamber floor 15 is constructed by placing a girder brick between the shore and the shore. A through hole 22 through which the soot and mixed gas pass from below the floor is provided on the floor surface. Below the girder brick is an underfloor tunnel 17 and above the floor is a firing chamber 21. Further, a gas trunk pipe 18 through which the mixed gas passes through the center of the flue 10 is passed, and a part of the gas trunk pipe 18 is attached to the outside of the kiln wall 2 opposite to the chimney 11. A mixed gas branch pipe 19 provided with a gas outlet 20 is installed in the middle between the shore 16 and the shore 16 and is connected to the gas trunk pipe 18 so that the gas can be vented. It enters into the pipe | tube 19 and it enables it to eject from the gas ejection port 20. FIG.
[0022]
Further, on the boundary between the combustion chamber 24 and the firing chamber 21, a fixed fire door wind 23 is piled up with bricks, and fire door wind through holes 22 are provided and fixed in places. Furthermore, a removable brick is prepared at the boundary between the firing chamber 21 and the combustion chamber 24 on the entrance / exit side of the kiln, which is removed when leaving the kiln and stacked when the kiln is packed. They are stacked up to the same height as that, and a through hole 22 is provided.
Install a fire door to prevent strong firewood from hitting the substrate during firing. Further, a suction port 26 is provided immediately above the flue 10 in the center of the firing chamber floor 15 so that the fired soot enters the flame suction port 26 and reaches the flue 10. Further, an exhaust gas hole 27 through which exhaust gas during hatching passes is provided in the center of the ceiling of the firing chamber 21, and a rectangular exhaust gas chamber 28 is attached to the upper part of the exhaust gas hole 27. Further, an exhaust gas vent pipe 29 having a vent pipe opening / closing valve 30 attached to the exhaust gas chamber, which is closed during firing and opened and exhausted during hatching, is attached.
[0023]
Further, an exhaust gas incineration chamber 31 is installed in the upper part of the exhaust gas chamber 28 and connected with an exhaust gas ventilation pipe 29 so as to allow ventilation, and a combustion chamber burner 33 is attached to the outlet having the exhaust gas outlet 32 to allow combustion. Further, a purification tank 35 is installed vertically on the side of the firing kiln 1, a spray nozzle 36 is installed in the upper part of the tank, a solution tank 39 is installed on the lower surface outside the purification tank 35, and sodium hydroxide is increased 10 times. Put a solution in water. Further, a power pump 38 for sucking up the solution is attached, and the solution in the solution tank 39 is connected by a pipe 37 so that the solution can be ejected by the spray nozzle 36. Furthermore, if the opening / closing valve 40 is attached to the bottom lower surface of the purification tank 35 and the valve is opened, the solution accumulated in the purification tank 35 can be dropped into the solution tank. Further, a circulation vent pipe 41 is connected to the flue 10 from the lower part of the purification tank 35, and a circulation opening / closing valve 42 is provided in the middle, which is opened when the firing kiln 1 is cooled to allow ventilation. Further, a purified gas exhaust pipe 43 with an exhaust gas opening / closing valve 44 is connected from the upper part of the chimney 11 of the chimney 11 to the lower part of the purification tank 35 so as to allow ventilation.
[0024]
Next, the heating kiln 58 will be described. On the opposite side of the chimney 11 of the firing kiln 1, a dry distillation kiln 45 made of heat-resistant steel is made in a rectangular box shape, and a gas material inlet 47 is provided on one side surface. A kiln lid 48 is attached so that it can be opened and closed. Further, the opposite side of the inlet 47 of the dry distillation furnace 45 is connected to the gas trunk pipe 18 protruding from the outer wall of the firing furnace 1. Furthermore, the periphery of the dry distillation kiln 45 is covered with a metal plate, and a heat-insulating refractory is attached to the inside to make a heating chamber 46. A heating chamber port 49 is provided at the lower part of the heating chamber 46, and a heating burner 50 is attached to the port to make it combustible. A zigzag gas kiln chimney 51 is built above the ceiling of the heating chamber 46, a water tank 52 is mounted on the heating chamber 46, a water adjustment valve 53 is attached downward to the bottom of the water tank, and the water adjustment valve A U-shaped water reservoir 59 is attached with a transparent pipe under 53 so that the dropped water can be collected in the U-shaped portion so that the drop of water can be seen. Even if the water adjustment valve 53 is forgotten to be closed, it is closed by the accumulated water. Further, a steam generation pipe 55 is vertically installed in the chimney from the horizontal portion of the zigzag gas furnace chimney 51, and the metal fibers 56 are packed in the steam generation pipe 55. Further, the upper part of the steam generation pipe 55 and the water reservoir 59 are connected by a water pipe 54 so that the water in the water tank 52 can fall into the steam generation pipe 55. Next, the steam generation pipe 55 and the dry distillation furnace 45 are connected by a steam pipe 57. The above is the mixed gas generator.
[0025]
Further, the operation of the main body apparatus will be described. The base material is packed in the firing kiln 1 and removed when the packing is finished, and the fire door wind 25 is piled up to be equal to the height of the fixed fire door wind 23. Further, the inlet / outlet door 4 is closed, then the vent pipe opening / closing valve 30 at the upper part of the exhaust gas chamber 28 is closed, the flue lid 13 at the lower part of the chimney 11 is removed, the adjustment door 14 is closed, and the circulation opening / closing valve 42 and the exhaust gas opening / closing are further closed. The valve 44 is closed. Next, the kiln lid 48 of the dry distillation kiln 45 is closed to prepare for ignition. Further, the burner 7 at both sides of the firing kiln 1 is ignited and started to burn. The soot rises from the combustion chamber 24 and reaches the ceiling, gradually enters the center of the firing chamber 21, passes through the base, enters the suction port 26, passes through the flue 10 and enters the chimney 11, and enters the chimney. Escape and continue to burn. When the upper substrate is baked, the soot gradually enters the lower part and enters the suction port 26. When the lower part is baked, it also passes through the through hole 22 from the underfloor tunnel 17, passes through the underlying material, enters the suction port 26, enters the chimney 11 through the flue 10 and continues to be baked. When the substrate further approaches a temperature of 1150 ° C., the heating burner 50 of the heating kiln 58 is ignited, and the dry distillation kiln 45 and the steam generating pipe 55 are started to air.
[0026]
When the temperature of the firing kiln 1 reaches an appropriate temperature of about 1150 ° C., the fire of the burner 7 of the firing kiln 1 is reduced, the adjustment door 14 is opened, and the flue lid 13 is put on the flue mouth 12 to place the flue 10 is further opened, the vent pipe on / off valve 30 of the exhaust gas vent pipe 29 is opened, then the exhaust gas on / off valve 44 is opened, and the solution on / off valve 40 of the solution tank 39 is opened to prepare for hatching.
[0027]
When preparation for hatching of the firing kiln 1 is complete, the combustion of the burner 7 is stopped, the lid is closed with the lid 8 and fastened with the clasp 9, and the kiln 48 of the dry distillation furnace 45 is opened and mixed. The gas material is quickly put into the dry distillation furnace 45, the furnace lid 48 is closed, the heating burner 50 is ignited to raise the temperature, the mixed gas is continuously generated, the water adjustment valve 53 of the water tank 52 is opened, and the water reservoir 59 is opened. The adjustment is made while observing the amount of water droplets falling to the inside of the steam generation pipe 55, so that the water droplets start dropping in the form of drops. The dropped water comes into contact with the metal fibers 56 in the steam generation pipe 55 and vaporizes to become steam gas, and enters the dry distillation furnace 45 through the steam pipe 57. As the dry distillation kiln continues to heat, the mixed gas material is pyrolyzed, salt, pine resin, and boric acid become mixed gas, and further, water vapor gas is added, and four types of gas are generated in one kiln at the same time and mixed unavoidably. The mixture gas is generated as a gas mixture without concentration, and flows into the gas main pipe 18 to keep heating, the vent pipe opening / closing valve 30 is opened, the incinerator burner 33 is ignited, combustion is started, and the power is continued. The pump 38 is turned on to start the operation, and the sodium hydroxide solution in the solution tank 39 is sucked up and sent to the spray nozzle 36 to be blown out so that the inside of the purification tank 35 is made into a thick mist.
[0028]
Further, the mixed gas generated from the dry distillation furnace 45 passes through the gas trunk pipe 18, enters the gas branch pipe 19 piped on the entire bottom surface of the firing chamber floor 15, and is simultaneously formed by the gas outlet 20 provided in the branch pipe. It blows out and passes through the through hole 22 on the entire floor of the baking chamber floor 15 to fill the bottom of the baking chamber 21. The mixed gas fed in one after another has a lower temperature and a higher specific gravity than the combustion gas. The mixed gas having a high specific gravity rises straightly and enters the mixed exhaust gas hole 27, is further collected in the exhaust gas chamber 28, passes through the exhaust gas vent pipe 29, and enters the gas incineration chamber 31.
[0029]
The fired high temperature substrate is gradually replaced with the mixed gas as the combustion gas is expelled, adheres to the surface of the substrate, and the silica and salt gas on the surface cause a hatching reaction due to the high temperature, and the hydrocarbon gas is mixed. Hatching as it is. The steam gas mixed in the mixed gas improves the adhesion of the mixed gas to the substrate, and the boric acid gas is blown for 50 to 60 minutes while helping to hatch and improve gloss.
[0030]
The mixed gas continuing to blow is entered into the exhaust gas incinerator 31 and incinerated by the incinerator burner 33, and the hydrocarbon gas in the mixed gas is burned and removed. Non-burning boric acid gas and salt gas enter the purification tank 35, descend in the spray of the sodium hydroxide solution, come into contact with the salt gas, and are reduced to salt by a reduction reaction to form salt water particles. The liquid drops to the bottom of 35 and accumulates in the solution tank 39 through the on-off valve 40. It is sucked up again by the power pump 38 and repeatedly circulated for purification. The exhaust gas from which the salt gas has been removed in the purification tank 35 becomes an exhaust gas containing only boric acid gas having no harmful substances, enters the purification gas exhaust pipe 43, and further enters the chimney 11 and is discharged to the atmosphere. Generation of gas from the dry distillation furnace 45 is dry distillation in 50 to 60 minutes, and gas generation ends.
[0031]
When the dry distillation is approaching the end, the mixed exhaust gas from the blower loses momentum, and the color of the exhaust gas, which is black, becomes nearly transparent. At that time, the kiln stop work is started. In the operation of stopping the kiln, the combustion of the heating burner 50 of the heating kiln 58 is stopped, and then the water adjustment valve 53 is closed to stop the flow of water. Further, the exhaust gas vent pipe opening / closing valve 30 is closed, and then the combustion of the incinerator burner 33 is stopped, and the exhaust gas outlet 32 is covered and sealed with the outlet lid 34. Further, the power pump 38 is turned off, the open / close valve 40 below the purification tank 35 is closed, the exhaust gas open / close valve 44 is further closed, and the kiln stop is completed. If one hour has passed after the kiln stop, the next is the cooling stage. First, do not open the vent pipe opening / closing valve 30 and the circulation opening / closing valve 42 at a time, open them little by little in three portions every 20 minutes, fully open the third time, and leave it until the kiln is opened for cooling. Do.
[0032]
By performing the above operation, the high temperature gas in the kiln starts to rise, passes through the exhaust gas hole 27 and enters the exhaust gas chamber 28, further passes through the exhaust gas vent pipe 29 and enters the exhaust gas incineration chamber 31, where it is cooled and cooled. The gas enters the upper part of the purification tank 35. The gas that has been cooled and has increased in specific gravity descends in the tank, reaches the flue 10 through the circulation vent pipe 41, and flows sideways through the flue 10 in the firing kiln 1. When the gas with a high specific gravity descends one after another, the gas in the flue 10 passes through the suction port 26 directly above the flue 10 and flows into the bottom of the firing kiln 1, and the gas with a high specific gravity flows from the bottom of the kiln. A gas with a low specific gravity is pushed up from below. The pushed up light gas rises one after another, enters the exhaust gas hole 27 again, rises further, passes through the exhaust gas chamber 28 and the exhaust gas vent pipe 29, enters the exhaust gas incineration chamber 31, and is cooled. Descent and repeat circulation. Cooling is performed by a cooling method using a convection action, and when the temperature is 300 ° C. or lower, the entrance door 4 is gradually opened and the kiln is removed.
[0033]
The waste liquid collected in the purification tank 39 as salt water by spraying the sodium hydroxide solution after purification is strongly alkaline, so dilute sulfuric acid is added to neutralize it to PH 7.0 to PH 8.0. Perform sink treatment.
[0034]
【The invention's effect】
Since the present invention is configured as described above, the following effects are achieved.
[0035]
A mixed gas generator is installed outside the firing kiln, and a mixed gas material of salt, pine resin, and boric acid is placed in a dry distillation kiln, heated, and water droplets are injected from a water tank to produce salt gas, hydrocarbon gas, boric acid gas. The four kinds of gas, water vapor gas, can obtain a high-temperature mixed gas with a good balance according to the input amount, and the product is 95% or more of the first-class product.
[0036]
From the start of the hatching operation to the end of the firing chamber, a non-concentrated mixed gas is simultaneously ejected from the entire floor bottom, so that only the hydrocarbon gas first contacts the substrate to form a carbon film, and the salt gas contacts. But it does not cause a hatching reaction. In addition, even when the salt gas lacking the hydrocarbon gas comes into contact, no unreasonable phenomenon such as no formation of a silvery soot has occurred.
[0037]
A gas generating mixed gas generator is provided separately from the firing chamber, and heating is continued in the dry distillation furnace, and a high temperature mixed gas is sent to the firing kiln, so that salt, coal, and soot are introduced into the firing kiln. The combustion chamber like time does not quench rapidly. When the kiln is cooled rapidly, the kiln walls and refractory bricks are cracked and severely damaged. In addition, the product may be a product with poor hatching due to rapid cooling, but this does not happen.
[0038]
Furthermore, by generating mixed gas in a dry distillation kiln, it becomes unnecessary to make a large fire bed by burning a large amount of coal and firewood, and there is no need to scrape a large amount of hot coal or coke when opening the kiln. It was. In addition, since there is no heat stored in charcoal or coke, it is now possible to perform the kiln out process easily.
[0039]
After stopping the kiln, high-temperature gas in the firing kiln is guided outside the kiln and circulated by convection through the exhaust gas incineration chamber and purification tank, making it possible to accelerate cooling by using existing equipment together. .
[0040]
The method of hatching the surface of the substrate of the present invention is not a method of applying a conventional glaze to dissolve the glaze at a high temperature, but the silica existing in the substrate of the fired product comes into contact with the salt gas in the mixed gas. By causing a hatching reaction and obtaining hatching, the base material finished in a small work is also hatched as it is. No small work is buried by hatching or rounded corners.
[0041]
In the treatment of the mixed exhaust gas exhausted from the firing kiln, the hydrocarbon gas in the mixed exhaust gas burns in the combustion chamber, and the salt gas comes into contact with the spray of sodium hydroxide solution in the purification tank. A reduction reaction takes place and the salt gas is reduced to salt water. The salt gas is removed and the harmful gas is purified and no longer causes pollution.
[Brief description of the drawings]
FIG. 1 is a cross-sectional view of the entire apparatus.
FIG. 2 is a sectional view taken along line BB. 8 in the figure is a view of the lid (8) as viewed from above.
FIG. 3 is a cross-sectional view taken along the line CC.
FIG. 4 is a cross-sectional view taken along the line AA. It is the figure which looked at a partial baking chamber (24) from the top.
[Explanation of symbols]
1 Firing kiln 31 Exhaust gas incinerator
2 Kiln wall 32 Exhaust gas outlet
3 Kiln floor 33 Incinerator burner
4 Entrance door 34 Exhaust gas outlet cover
5 F 35 Purification tank
6 焚 36 spray nozzle
7 Burner 37 Pipe
8 Mouth cover 38 Power pump
9 Stopper 39 Solution tank
10 Flue 40 Open / close valve
11 Chimney 41 Circulation vent pipe
12 Flue entrance 42 Circulation on-off valve
13 Flue lid 43 Purified gas exhaust pipe
14 Control door 44 Exhaust gas on-off valve
15 Firing room floor 45
16 shore 46 heating chamber
17 Underfloor Railway 47 Entrance
18 gas trunk 48 kiln lid
19 Gas branch pipe 49 Heating outlet
20 Gas outlet 50 Heating burner
21 Firing room 51 Heating kiln chimney
22 hole 52 water tank
23 Fixed fire door 53 Water adjustment valve
24 Combustion chamber 54 Water pipe
25 Removal fire door style 55 Steam generation pipe
26 Suction mouth 56 Metal fiber
27 Exhaust gas hole 57 Steam pipe
28 Exhaust gas chamber 58 Heating kiln
29 Exhaust gas vent pipe 59 Puddle
30 Vent pipe open / close valve

Claims (4)

釉化作業が終了すれば排ガス開閉弁(42)、排ガス焚口(32)を密封し、循環開閉弁(44)を開き焼成窯(1)の高温ガス気体は上昇して、排ガス穴(27)を通って排ガス室(28)に入り、更に排ガス焼却室(31)を通り抜け、外気に冷やされ浄化タンク(35)内を降下し、循環通気管(41)を抜けて焼成窯(1)の底部に入り、再び上昇循環を繰り返して冷却を行なう。
以上の工程を有し、焼成窯(1)の高温ガスを窯外の装置に流出させて、循環を繰り返し冷却を行なう、燻し銀色釉の焼成物を得る窯の冷却方法。
When the hatching operation is completed, the exhaust gas on / off valve (42) and the exhaust gas outlet (32) are sealed, the circulation on / off valve (44) is opened, and the high temperature gas in the firing kiln (1) rises to the exhaust gas hole (27). Passes through the exhaust gas chamber (28), passes through the exhaust gas incineration chamber (31), is cooled by the outside air, descends in the purification tank (35), passes through the circulation vent pipe (41), and enters the firing kiln (1). Enter the bottom and repeat the up-circulation again to cool.
A method for cooling a kiln having the above-described steps, wherein a high temperature gas of the firing kiln (1) is discharged to an apparatus outside the kiln, and cooling is repeated to obtain a fired silver-colored fired product.
焼成窯(1)外に設けた加熱窯(58)の乾留窯(45)を加熱バーナー(50)で加熱を行い、塩、松脂、硼酸を混合したガス材を投入し、窯蓋(48)を閉めて、水タンク(52)から水滴状に水を落下させつつ燃焼を続け、炭化水素ガス、塩ガス、硼酸ガス、水蒸気ガスを発生させ、高温の混合ガスとして焼成窯(1)内に送入し、混合ガスと素地表面のシリカと接触させ、釉反応を起こして燻し銀色の釉の被膜を形成可能とする、混合ガスによる燻し銀色の釉の焼成物の形成方法。  The dry distillation kiln (45) of the heating kiln (58) provided outside the firing kiln (1) is heated with a heating burner (50), and a gas material mixed with salt, pine resin, and boric acid is charged, and the kiln lid (48) Is closed, and combustion continues while dropping water from the water tank (52) to generate hydrocarbon gas, salt gas, boric acid gas, and water vapor gas, and into the firing kiln (1) as a high-temperature mixed gas. A method of forming a fired product of sintered silvery cocoons with a mixed gas, which is fed and brought into contact with the mixed gas and the silica on the surface of the substrate to cause a cocoon reaction to form a silvery cocoon film. 燻し銀色の釉を得るため、乾留窯(45)内へ混合ガス資材を投入し、加熱を行い混合ガス発生を行なう、塩、硼酸、松脂の混合ガス発生を可能にする混合資材。  A mixed material that enables mixed gas generation of salt, boric acid, and pine resin, in which a mixed gas material is introduced into a dry distillation kiln (45) and heated to generate a mixed gas in order to obtain a tanned silver-colored cocoon. 焼成窯(1)の釉化反応を終わって排出する混合ガス排煙を、排ガス焼却室(31)に流入させ、焼却室バーナー(33)を用いて炭化水素ガスを燃焼し、次に炭化水素ガスを除去した混合排ガスを浄化タンク(35)に流入し、浄化タンク(35)の天井部から水酸化ナトリウム溶液を噴霧し、塩ガス排煙を還元反応により塩水の水滴となって落下し、溶液タンク(39)に溜まる燻し銀色釉の焼成物を得る焼成窯(1)の排煙の浄化方法。  The mixed gas flue gas discharged after the hatching reaction of the firing kiln (1) is caused to flow into the exhaust gas incinerator (31), and the hydrocarbon gas is burned using the incinerator burner (33), and then the hydrocarbon The mixed exhaust gas from which the gas has been removed flows into the purification tank (35), sprayed with a sodium hydroxide solution from the ceiling of the purification tank (35), and salt gas flue gas falls as salt water droplets by a reduction reaction, A method for purifying flue gas from a firing kiln (1) to obtain a fired silver candy fired product accumulated in a solution tank (39).
JP2002327604A 2002-10-04 2002-10-04 Kiln apparatus and method for producing fired product of tanned silver candy Expired - Fee Related JP4421815B2 (en)

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