JP3742985B2 - Carbonized material for building materials, etc., and method for producing the same - Google Patents
Carbonized material for building materials, etc., and method for producing the same Download PDFInfo
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- JP3742985B2 JP3742985B2 JP2000165229A JP2000165229A JP3742985B2 JP 3742985 B2 JP3742985 B2 JP 3742985B2 JP 2000165229 A JP2000165229 A JP 2000165229A JP 2000165229 A JP2000165229 A JP 2000165229A JP 3742985 B2 JP3742985 B2 JP 3742985B2
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- 239000005539 carbonized material Substances 0.000 title claims description 48
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Description
【0001】
【発明の目的】
この発明は、不燃性の機能性素材、例えば建材用の断熱材、防音材、吸湿材等の素材として好適な炭化素材に関するものであって、セルロース系繊維体、特に高度化した社会の一つの象徴ともいえる大量の廃棄物の中の古紙、あるいは廃材や樹皮、農産副次物である籾殻や藁等といったセルロース系繊維体を容易く原材料とすることが可能であって、しかも極めて安価且つ効率的に生産することができる上、建材用の断熱材、防音材、吸湿材等への利用、加工性についてもかなり有利なものとすることができる、新規な構造からなる建材等用炭化素材、およびそのための新規な製造方法を提供しようとするものである。
【0002】
【従来の技術】
経済的にも文化的にも豊かな環境が整えられていく中、企業経営、家庭生活の区別なく日々大量の物資が消費され、その過程で発生する様々な廃棄物は、今や経済的負担の問題ではなく、自然環境保全の面から、その取扱いが極めて大きな社会問題化してきている。
特に、高度経済社会のバロメータとまでいわれる大量の古紙の取扱いを見てみると、新聞紙や一部雑誌類では、現在どの社でも回収紙を利用した再生紙を使用してはいるものの、その再生紙自体は、100%回収紙だけで作られたものが使用されている訳ではなく、バージンパルプを何割かの割合で加え、品質の安定を図ったものとしての再利用となっているため、それら再生紙の利用に積極的な業界からの協力を以てしても、到底、古紙市場の要求を満たしきれないというのが現状となっている
【0003】
そうした再利用の道のない余剰古紙や、回収されないまま廃棄処分されてしまう古紙は、他の可燃性ゴミ等と一緒に焼却炉で燃やされ、禁制品を含む紙類の燃焼により、有害なダイオキシンを大気中に放散することとなって自然環境を破壊する元凶と目され、その発生の少ない高性能焼却場建設のために多額の社会資本投資を余儀無くされたり、最終処埋立場の確保のために様々な困難覚悟の企画、立案に取り組まなければならない等という政策的課題にいつまでも嘖まされることになる。この廃棄処理の問題は、古紙の外、建築現場や製材所、木工加工所、木材陸揚げ埠頭等から大量に発生する廃材や木屑、あるいは稲作農家等からの籾殻や藁等々といった、その他のセルロース系繊維体全般について同様に抱える問題となっている。
【0004】
セルロース系繊維体を、焼却処分以外の手段で処理、加工するようにした技術としては、例えば、・特開昭62−15645号「繊維状活性炭の製造法」(東邦レーヨン)、・特開平4−231314号「高表面積活性炭の製法」(ユーカー・カーボン・テクノロジーCo.:USA)、・特開平6−56416号「活性炭の製造法」(ウエストヴァコCo.:USA)等に提案のある活性炭化してしまい、活性炭の有する秀れた化学処理機能、即ち脱臭機能や濾過機能、陰イオン発生機能等を必要とする分野への基礎資材としての活用を図るという技術が古くから既に確立している。
【0005】
しかし、これら各種活性炭化する技術によって作り出される活性炭の場合は、その用途が極めて特殊な領域に係わるものであって、需要に見合う素材として高い品質と性能とが要求されるため、処理対象とする原材料の品質に制約を受けた上、高性能の設備機器整備のためにかなりの初期投資を覚悟しなければならないという事情に加え、例えば、上記した・の東邦レーヨン技術であれば、酸化処理工程の所要時間短縮化のため、酸化工程を2分割し、酸素含有量0.5〜5%の不活性雰囲気下、300〜400°Cでの予備酸化処理と、水蒸気、炭酸ガス雰囲気下、700〜1000°Cという高温域での本酸化処理という2段階に渡る酸化処理工程を必要としたり、・のユーカー・カーボン・テクノロジーCo.技術においては、セルロース系物質を燐酸等の添加液で処理した上、450〜1200°Cの不活性雰囲気下で炭化し、更に、700°C以上のスチーム等による酸化雰囲気下で活性化するというものであり、また、・のウエストヴァコCo.技術のように、木材(リグノセルロース)を対象と、それらを微粉砕して炭化してから、再度、炭化した粉末を成形するという具合に、何れも処理工程が煩雑且つ高度な操作性を伴う等の理由も存在していることから、日々大量に発生し、しかも品質にも大きなばらつきのある古紙や廃材等を、処理対象のセルロース系繊維体として扱うことは、品質的にも経済的にも殆ど不可能としなければならないものである。
【0006】
一方、こうした高度な分野への活用ではなく、燃料や土壌改良材、防湿材、断熱材、吸音材等として利用するための伝統的な炭化手段による処理、即ち炭焼きして炭(スミ)としてしまう方法も考えられる。この炭焼き技術は、木質材等を高温で燃焼させ、その後、酸素を遮断し高温による脱水作用によって蒸し焼き状態となし、セルロースを分解、炭化させるようにした製造方法によるものであって、この技術は古の時代から変わっていない。
【0007】
しかし、高温域において燃焼させる過程、その後、酸素を遮断し、不完全燃焼させる過程の何れもが不可欠な炭焼き処理では、何れもの過程において多量の二酸化炭素や一酸化炭素を発生させてしまうことから、直接大気汚染に繋がるという今日的に最も厄介な問題を抱えると共に、古紙や木屑のようなフィルム状あるいは粒状のセルロース系繊維体の炭化には全く不向きな処理手段であるという事実がある。
【0008】
更に不都合なことには、この伝統的な手段で作り出される炭は、その組成中の炭素チェーンが切断された固体構造となってしまうため、当然に柔軟性や弾力性等といった性状は持ち合わせておらず、したがって、防湿材や断熱材、吸音材等として建築躯体や設備機器等の凹凸ある表面や湾曲面に添設使用しようとすれば、一旦、固形状の炭を粉砕した上、その炭素粉末を塗布、接着するようにしたり、樹脂等のバインダーの中に練り込んで成形し直すか、適宜繊維等に混入、付着させ、全体として柔軟性のあるものに成形するかして利用せざるを得ないものであり、利用に際しての二次処理加工が欠かせない上に、当該二次処理加工工程で発生する塵炭対策のために余計な配慮と経費とが必要になるという欠点も附随してくることから、したがって、これまでのところ、この伝統的な炭焼き式の炭化処理についても、日々大量に発生する古紙や廃材等セルロース系繊維体の処理技術として応用、実用化された事実を見い出すことはできない。
【0009】
この発明は、以上のような状況に鑑み、現在までのところ、極めて限られた範囲内でしか有効利用されずじまいで、相当量のものが多額の費用を掛けて焼却あるいは埋立て処分に回されてしまっているセルロース系繊維体、特に古紙に着目すると共に、カーボン(即ち、セルロースを炭化した物)が酸素指数65の不燃性と高い断熱性とを有していることにも誘引され、その大量利用先として建築資材等への応用の可能性を追求すべく、逸早く開発、研究に着手し、幾多の試作実験を試みる等の試行錯誤を繰り返してきた結果、高い燃焼性を有する古紙等のセルロース系繊維体を効率よく炭化させることができる上、古紙のときの柔軟性も維持し続けている新規な構造の建材等用炭化素材と、その建材等用炭化素材を確実且つ経済的に生産することを可能にする新規な建材等用炭化素材の製造方法とを完成するに至ったものである。
【0010】
【発明の構成】
この発明の建材等用炭化素材は、基本的に次のとおりの構成を要旨とするものである。
即ち、燐酸等の燐化合物か、燐化合物と硫酸、硫酸アンモニウム、硼酸、またはそれらの誘導体の何れか一つあるいは二つ以上との混合物かの何れかから成る添加液を含浸状としたセルロース系繊維体を、活性雰囲気下、略65°Cないし400°C程度、望ましくは略80°Cないし300°C程度の温度範囲内であって、添加液濃度に応じた所要時間だけ加熱処理し、加熱または火炎による可燃性ガス発生を抑制しながら脱水、炭化を促進して炭化残渣を増加させ、少なくとも重量減少率40%強に達しさせた炭化素材からなるものとした建材等用炭化素材である。
【0011】
そして、この基本的な構成による建材等用炭化素材において、より望ましい構成からなるものとしては、燐酸等の燐化合物か、燐化合物と硫酸、硫酸アンモニウム、硼酸、またはそれらの誘導体の何れか一つあるいは二つ以上との混合物かの何れかから成る添加液を含浸状としたセルロース系繊維シート体を、活性雰囲気下で、略65°Cないし400°C程度、望ましくは略80°Cないし300°C程度の温度範囲内であって、添加液濃度に応じた所要時間だけ加熱処理し、加熱または火炎による可燃性ガス発生を抑制しながら脱水、炭化を促進して炭化残渣を増加させ、少なくとも重量減少率40%強に達しさせ、セルロースの脱水炭化途中の炭素チェーンを残し、シート体形状および可撓性を維持したままの炭化素材とすることにより、単独でかまたは他の素材と組み合わせるかして、単層または積層構造の保形素材として取り扱い可能となるようにしたシート状の建材等用炭化素材が包含されている。
【0012】
この望ましい構成からなる建材等用炭化素材は、燐酸等の燐化合物か、燐化合物と硫酸、硫酸アンモニウム、硼酸、またはそれらの誘導体の何れか一つあるいは二つ以上との混合物かの何れかから成る添加液を含浸状としたセルロース系繊維シート体を、活性雰囲気下、略65°Cないし400°C程度、望ましくは略80°Cないし300°C程度の温度範囲内であって、添加液濃度に応じた所要時間だけ加熱処理し、加熱または火炎による可燃性ガス発生を抑制しながら脱水、炭化を促進して炭化残渣を増加させ、少なくとも重量減少率40%強に達しさせ、セルロースの脱水炭化途中の炭素チェーンを残し、シート体形状および可撓性を維持したままの炭化素材とすることにより、単独でかまたは他の素材と組み合わせるかして、単層または積層構造の保形素材として取り扱い可能となし、不燃断熱材および吸湿材、吸音材、脱臭材となるようにしたシート状の建材等用炭化素材として示すこともできる。
【0013】
更に、上記した基本的な構成、およびその中の望ましい構成によるものとした建材等用炭化素材には、次のような構成によって示すことができる建材等用炭化素材も夫々包含するものである。
燐酸等の燐化合物か、燐化合物と硫酸、硫酸アンモニウム、硼酸、またはそれらの誘導体の何れか一つあるいは二つ以上との混合物かの何れかから成る添加液を含浸状としたセルロース系繊維シート体を、活性雰囲気下、略65°Cないし400°C程度、望ましくは略80°Cないし300°C程度の温度範囲内であって、添加液濃度に応じた所要時間だけ加熱処理し、加熱または火炎による可燃性ガス発生を抑制しながら脱水、炭化を促進して炭化残渣を増加させ、重量減少率40%強に達しさせ、セルロースの脱水炭化途中の炭素チェーンを残し、シート体形状および可撓性を維持したままの炭化素材とした上、硼酸処理を施したものすることにより、木材被覆用としてシロアリ等の害虫防止機能も付与されてなるものとした建材等用炭化素材がそれである。
【0014】
セルロース系繊維体は、最も代表的なものとして新聞紙や雑誌類等の古紙や使い古しの段ボール紙等をその対象とするものであるが、その他、建築現場や製材所、木工加工所、木材陸揚げ埠頭等から大量に発生する廃材や木屑、あるいは稲作農家等からの籾殻や藁等々といった、その他のセルロース系繊維体全般についても対象とし得る外、廃棄物ではなく、積極的に良質の断熱材や吸音、吸湿材等の用に供するようにするための原材料として、例えばペーパータオルのような嵩高な構造に特別に抄紙してなるものや、ロール構造のトイレットペーパーでロール構造のままのもののように、他の用途用に供されているものをそのままか、適宜加工するかしてなるもの等も勿論対象とするものであり、性状についても、平板状のもの、シート状のもの、それらの積層構造のもの、ブロック状のもの、箱や筒等に成形されたもの、粒状あるいは粉末状のもの、ストロー状のもの、棒状のもの等、特に制約しなければならない格別の理由もなく、各種種類、性状のセルロース系繊維体を対象とするものである。
【0015】
添加液は、セルロースの熱分解時の不燃ガスの発生、ガラス化による隠蔽作用、化学変化(エステル化)に依る可燃性ガス生成の何れについても抑制効果等を発揮し、セルロースの脱水、炭化を促進させ炭化残渣の量を増やすことができる機能を果たし得るものでなければならず、燐酸等の燐化合物か、燐化合物と硫酸、硫酸アンモニウム、硼酸、またはそれらの誘導体の何れか一つあるいは二つ以上との混合物かの何れかから成るものとする。
【0016】
上記添加液を含浸状としたセルロース系繊維体を、活性雰囲気下で、略65°Cないし400°C程度、望ましくは略80°Cないし300°C程度の温度範囲内であって、添加液濃度に応じた所要時間だけの加熱処理を施し、重量減少率40%強に達しさせることにより、炭化残渣を増加させて所定の炭化が終了してしまい、素材組成においてセルロースの脱水炭化途中の炭素チェーンを残したままの炭化素材からなる建材等用炭化素材とするものである。
【0017】
なお、略65°Cないし400°C程度の温度範囲内の所定加熱処理温度においても、添加液の含浸量の少ないものの場合には、含浸量の多いものに比べて硬い炭化素材となって柔軟性に差を生じてしまう。これは、添加液の多寡に伴って処理セルロースにおける多糖類の炭素チェーンの残存割合に差が生じ、添加液含浸量の少なさにより、炭素単体まで分解していく結果、その可撓性、即ち柔軟性を無くしてしまうものと考えられ、したがって、添加液含浸量をコントロールすることにより、得られる炭化素材の可撓性の調整が可能になるといえる。
【0018】
このように可撓性を残したままの炭化が可能となるのは、通常の不活性ガス雰囲気中でセルロースを処理した供試体(炭)、および、添加液含浸処理した上、通常の空気中で加熱炭化したこの発明の供試体と、夫々の供試体の原材料としたバージンパルプ(キムタオル…紙)とのX線回折データを対比させてみると、図11に示すとおり、通常の紙(バージンパルプ)は、15°(2θ)のブロードなピークと23°付近のピークを特徴とするものであり、これに対し、供試体(炭)の場合は、20°から30°の弱いブロードの山(ピークとは表現し難い。)としてしか現れていないにも拘わらず、この発明の供試体の場合には、バージンパルプ程のピークにはならないまでも、明らかなピークを現わすことから、添加液含浸処理して得られる炭化素材には、原材料である紙の特徴を少し残し、セルロースの炭化チェーンの一部が炭化素材内に残っており、これが原材料に近い可撓性残存に寄与していると考えられる。
【0019】
一方、この発明の建材等用炭化素材は、そのチャート(炭化層)の酸素指数(酸素指数とは燃焼に必要な酸素濃度)が65であって、原材料のそれが18で易燃性物質であるのに比較し、遥かに高い不燃性と高い断熱性とを有する素材となっており、当然不燃材料としての使用が可能になる上、そのチャートは、比表面積が大きく、しかも高い吸着力を有するため、吸湿材、脱臭材としての機能も果たし得る外、ガスの吸着作用も期待でき、また、チャートは、多量の空気を含み、断熱性能も高いことから、不燃断熱材としての性能を有すると共に、炭素繊維間の減衰効果によって吸音特性も得られるものとなる。
【0020】
【関連する発明】
以上のとおりの構成を要旨とするこの発明の建材等用炭化素材に関連し、この発明には、次のとおりの構成からなる建材等用炭化素材の製造方法を包含している。
即ち、セルロース系繊維体に、燐酸等の燐化合物か、燐化合物と硫酸、硫酸アンモニウム、硼酸、またはそれらの誘導体の何れか一つあるいは二つ以上との混合物かの何れかから成る添加液を含浸状とする工程、添加液を含浸させたセルロース系繊維体を、活性雰囲気下、略65°Cないし400°C程度、望ましくは略80°Cないし300°C程度の温度範囲内であって、添加液濃度に応じた所要時間だけ加熱処理し、加熱または火炎による可燃性ガス発生を抑制しながら脱水、炭化を促進して炭化残渣を増加させる工程、炭化残渣が増加していき、少なくとも重量減少率が40%強に達したところで加熱処理を停止する工程、以上の工程により、セルロースの脱水炭化途中の炭素チェーンを残したままの炭化素材を得るようにした建材等用炭化素材の製造方法である。
【0021】
そして、より望ましい構成によるものとしては、セルロース系繊維体に、燐酸等の燐化合物か、燐化合物と硫酸、硫酸アンモニウム、硼酸、またはそれらの誘導体の何れか一つあるいは二つ以上との混合物かの何れかから成る添加液を含浸状とする工程、添加液を含浸させたセルロース系繊維体を、活性雰囲気下、略65°Cないし400°C程度、望ましくは略80°Cないし300°C程度の温度範囲内であって、添加液濃度に応じた所要時間だけ加熱処理し、加熱または火炎による可燃性ガス発生を抑制しながら脱水、炭化を促進して炭化残渣を増加させる工程、炭化残渣が増加していき、少なくとも重量減少率が40%強に達したところで加熱処理を停止する工程、炭化素材を水洗して残留添加液成分を除去またはできるだけ除去する工程、残留添加液成分の除去された炭化素材を乾燥する工程、以上の工程により、セルロースの脱水炭化途中の炭素チェーンを残したままの炭化素材を得るようにした構成を要旨とする建材等用炭化素材の製造方法とすることができる。
【0022】
なお、上記のとおりの構成からなるこの発明の建材等用炭化素材の製造方法には、セルロース系繊維シート体に添加液を含浸状とする工程の前処理工程として、古新聞や古雑誌のような古紙その他の紙材を最大約2cm程度の厚さを限度に積層状としてなるセルロース系繊維シート体の平面全体に、できるだけ平均化した配置で厚さ方向に貫通する無数の浸透孔を穿設する工程を組み込み、積層紙から厚板状で可撓性を維持したままの炭化シート積層体を得るようにしたシート状の建材等用炭化素材の製造方法が包含されている。
【0023】
セルロース系繊維体は、前記したこの発明の基本を成す建材等用炭化素材において既述の如く、各種種類、性状のセルロース系繊維体を対象とするものであり、また、添加液も、セルロースの熱分解時の不燃ガスの発生、ガラス化による隠蔽作用、化学変化(エステル化)に依る可燃性ガス生成の何れについても抑制効果等を発揮し、セルロースの脱水、炭化を促進させ炭化残渣の量を増やすことができる機能を果たし得るものでなければならず、燐酸等の燐化合物か、燐化合物と硫酸、硫酸アンモニウム、硼酸、またはそれらの誘導体の何れか一つあるいは二つ以上との混合物かの何れかから成るものとし、適宜手段、例えば浸漬法や塗布あるいは噴霧等、セルロース系繊維体の表面だけではなく、厚み方向内部にまでできるだけ均質に含浸できる適宜手段によってセルロース系繊維体全体に添加液が含浸条となるようにする。
【0024】
なお、この添加液含浸工程は、対象となるセルロース系繊維体がシート体からなるものの場合には、複数枚を積層状となるように一まとめにして実施することも可能であり、その際には、添加液の浸透効率を高め、且つ厚み方向内部にまで均質な浸透状態が実現されるようにするため、積層状としたセルロース系繊維シート体の平面全体に、できるだけ平均化した配置で厚さ方向に貫通する無数の浸透孔を穿設する前処理工程を施してから、添加液含浸処理工程に入るようにすべきであり、更に、添加液含浸処理工程に続く加熱処理工程において、加熱温度が、積層状としたセルロース系繊維シート体の表面側から厚み方向奥部にまで短時間の中に均質に伝達されたものとなって、表面側および奥部とも均質な炭化が進行し、素材全体の品質を安定させるようにするため、積層厚の限度を略2cm程度に制限したものとするのが望ましい。
【0025】
こうして添加液を均質に含浸状としたセルロース系繊維体は、そのまま湿潤な状態でか、一旦乾燥状とした上で加熱処理される。
通常のセルロースの熱分解は、約300°C程度から始まり、図2で示される分子構造のセルロースが、熱分解によって、図3のレポグルコサン(β−グルコサン C6H10O5)となり、更に可燃性ガス(フルフリルアルコール C5H6O2、フルフラール C5H4O2、メタノール CH4O、エタノール C2H6O、アセトアルデヒド C2H6O、グリオキサール C2H2O2等)に分解する経過を辿ることになる。
【0026】
この発明の製造方法では、それら通常のセルロースの熱分解過程におけるレボグルコサンを生成させない熱分解を進行させ、そのことによってその後の可燃ガスへの分解を抑え込み、炭化残渣を増加させるようにするものである。
したがって、この発明の加熱工程では、対象とするセルロース系繊維体が、予め上記した添加液含浸工程を必須とし、セルロースの熱分解に際してもレボグルコサンを生成させないよう、燐酸や硫酸の強力な脱水作用や、燐酸等の酸によるエステル化反応を起こさせ、セルロースを急激に分解させず、ヘミセルロースから多糖類の燐酸エステルに分解していくことにより、タール分や可燃性ガスの生成を抑へ、効率よく炭化を行うものである。
【0027】
この加熱工程は、上記した過程で所定の程度まで炭化が進行したことを確認する上での目安となる重量減少率40%強に達するまで、少なくとも継続されなければならず、その間の加熱処理では、加熱または火炎による可燃性ガス発生を抑制しながら脱水、炭化を促進することになる。
【0028】
セルロースの燐酸によるエステル化からの脱水反応と脱水位置、生成組織が図4に示されている。
そして、エステル化からの脱水反応は、図4−1のヘミセルロースは、図4−2のように、燐酸処理によってエステル化した上、継続する加熱処理によって再度燐酸が分離する時に脱水を伴いながらセルロースを分解することになる。
このように、燐酸等の脱水反応により、セルロースは、レボグルコサンになることを阻害される結果、可燃性ガスの発生は抑えられ、火炎を伴うことなく効率的な脱水炭化が行われる。 この反応は、通常セルロースの熱分解が起こるといわれる300°C以下の低い温度においても実現することが確認されている。
【0029】
セルロースに燐酸を添加し、加熱時のセルロースの吸発熱反応を示唆熱分析(DTA)で測定すると、図5に示されているように、燐酸の添加量の増加と共に、セルロースの吸熱ピークが低温側にシフトしていくことが知られており、 この事実から、セルロースの脱水反応は、レポグルコサン等の生成に優先して起こることが判明する。また、セルロースに燐酸化合物を添加して加熱すると、図6ように、リンの添加量の増加と共に発熱速度が遅くなっていくことから、セルロースの燃焼は緩やかに行われ、火炎を伴わない酸化反応に移行していくことも判明する。
【0030】
図7から図9は、セルロースへの燐酸処理濃度と恒温乾燥機による加熱温度による減少重量を表し、図10から図12は、その減少率を示すものである。
図7および図10からも判るように、100°C設定の乾燥機においては、燐酸未処理のセルロース(キムタオル白)の重量変化は、付着水分と思われる1時間以内の重量変化後72時間後も重量変化は見られない(微量変化は測定までの僅かな間の吸湿)。しかし、この発明の燐酸含浸で加熱処理したものでは、燐酸の処理濃度と共に重量減少が大きくなる。
【0031】
したがって、通常のセルロースの分解温度(250°C)以下である100°Cでも燐酸の濃度次第では十分脱水反応が起こるものであり、更に、硫酸アンモニウムを混合したものを添加液にすると、アンモニアの離脱温度である65°C以降でも炭化が起こることが確認されている。
【0032】
また、図8および図11に示すように、150°C設定の乾燥機においては、100°C以上に顕著な脱水炭化が起こり、低濃度の燐酸処理品においても大きな重量減少が見られ、8時間以内の重量減少が23%から40%発生しているが、添加液未処理品では、1時間以内の初期減量後は殆ど重量変化が見られない。即ち、通常、150°Cにおいてセルロースは分解しないものが、添加液含浸後の加熱処理によれば脱水炭化が起こっていることが判る。
【0033】
200°Cとなると、図9および図12のように、脱水炭化作用は顕著に現れ、1時間以内の重量変化が最大であり、その後の重量変化は、添加液含浸処理量の少ないセルロースの方が大きくなっている。
また、添加液未処理のセルロースも、24時間以降に分解が始まり、72時間後には添加液含浸処理品と同等まで重量減少が見られたが、その表面状況は明らかに異なり、添加液未処理品は表面が褐色に近く、また、タール分の付着が見られたが、添加液含浸処理品は黒色で、1時間以降の表面の変化は見られなかったが、添加液含浸処理量の少ない(1.1%P)は、添加液含浸処理量の多いものに比べ、硬く柔軟性がない炭化シートとなった。
【0034】
これは、セルロースの添加液含浸処理により、多糖類の炭素チェーンの残存による柔軟性が、添加液含浸処理量の少なさに応じ、炭素単体まで分解していく結果、無くなってきたと考えられる。この事実から、添加液含浸処理量を変えることよって、炭化素材の柔軟性を調整可能にするということが判る。
そして、通常の不活性ガス雰囲気中でセルロースを処理した供試体、およびこの発明による供試体と、原材料であるバージンパルプ(キムタオル…紙)とのX線回折データ結果(図1)から、添加液含浸処理して加熱処理したこの発明の炭化素材が、セルロースの炭化チェーンの一部が炭化シート内に残り、紙の特徴を少し残しているとする事実については既述したとおりである。
【0035】
【実施例1】
紙、木綿等のセルロース系繊維体に燐酸を主成分とする添加液の含浸処理を施した上、略65°Cないし400°C程度、望ましくは略80°Cないし300°C程度の温度範囲内で加熱処理し、炭化進行程度の確認の目安となる重量減少率で40%強に達するまで加熱処理を続けた後、必要に応じて残留燐酸等を水洗、中和等の処理することによる燐酸の昇華等により、残留添加液の除去や作用を抑え、柔軟性のある炭化シートや炭化フェルトを安価に製造する。
【0036】
【実施例2】
この実施例は、セルロース系繊維体を一旦解繊した上、適宜手段によってボード状にしたものを炭化するようにした代表的な実施例を示すもので、図13に示した工程図に従い、より具体的な説明を加えていくことにする。
先ず、解繊工程として、原材料として運ばれてきた古紙や稲藁等を、シュレッダーや粗砕機等公知の手段によって細分化し、本や雑誌等の場合には、ホチキス等の止め金が破砕、混入してしまう外、回収段階に異物が紛れ込む虞れもあることから、併せて空気分級や磁選機によってそれら金属や石等の異物を除去する工程も平行して実施するようにすべきである。
なお、解繊手段は、湿式、半乾式、乾式等公知の何れによるものとしても差し支えはない。
【0037】
添加液は、その経済的な理由から市販の燐酸液、例えばメッキ添加液や、硫安、燐安等の肥料を使用することも可能であり、どのような燐酸が結う液を採用するかは、処理後の炭化素材の使用目的等によって適宜選択、採用するようにすればよい。また、安価な硼酸や硼砂の併用も白蟻防除等に効果的であり、これら添加液含浸工程に送られる
【0038】
この工程に用いる添加液は、その経済的な理由から市販の燐酸液、例えばメッキ添加液や、硫安、燐安等の肥料を使用することも可能であり、どのような 燐酸が結う液を採用するかは、処理後の炭化素材の使用目的等によって適宜選択、採用するようにすればよい。また、安価な硼酸や硼砂の併用も白蟻防除等に効果的であり、これらの混合剤の使用も有効である。
【0039】
添加液処理は、スプレー塗布や浸漬等の手段による外、添加液粉末と解繊した繊維を乾式のまま混合した上、蒸気に依って馴染ませ、更に余熱を行うようにした方法や、湿式においては、起泡剤、発泡剤等を混入し、空気を連衝する方法も考えられる。また、上気した解繊工程における解繊時に、同時に水溶液スプレー等によって粉塵飛散防止兼添加液含浸処理を行うようにする方法もある。
【0040】
こうして添加液含浸処理を終えたセルロース系繊維体は、引き続き加熱工程に回る。この工程は、処理済みのセルロース系繊維体を脱水炭化するため、できる限り乾燥状態で行うようにするのが加熱エネルギーのロスに繋がる上、特に65〜100℃のような低温域での加熱処理ではこの乾燥工程は必須の条件となる。加熱処理用の熱源は、硫安、燐安混合物や硫酸を使用すると65℃辺りの低温域から炭化が起きるため、電気、ガス、石油等の他に廃熱の利用が容易であり、低い温度の場合、反応が緩やかに起きるため、セルロースの分解途中の材料の入手が可能であり、肥料その他への応用が可能である。また、火炎によって直接加熱しても添加液効果により、可燃性ガスを制御しながら炭化していくため、火災の心配が少なくなる。(添加液濃度が低濃度の場合や硫酸基を含まない配合によるものの場合には、高温においては着火する虞れも出てくるため、添加液の配合には十分な注意が必要となる。)
【0041】
この加熱工程に要する処理時間は、添加液濃度(1.5〜15%)と加熱温度(65〜400°C)との相関関係で、重量現象率が少なくとも40%強程度に達する段階まで継続して実施されるようにしなければならない。加熱処理の熱源は、硫安、燐安混合物や硫酸を使用すると65°Cから炭化が起きることから、電気、ガス、石油等の他に廃熱の利用も可能になる上、低温域の加熱処理では、反応が緩やかに起きるため、セルロースの分解途中における材料の利用も可能となり、肥料その他への応用が可能である。また、火炎によって直接加熱しても、添加液効果によって可燃性ガスを抑制しながら炭化していくことになるため、火災の心配が少なくなる。(添加液濃度が低濃度の場合や硫酸基を含まない配合によるものの場合には、高温においては着火する虞れもあるので、その配合には十分な注意が必要となる。)
【0042】
【実施例3】
古紙繊維とロックウール等無機繊維とを混合、成形し、上記実施例3に使用した添加液を含浸処理した後、熱風乾燥機180°Cにて加熱(高周波での加熱も可)して炭化し、高い保形強度と柔軟性を持ったボードを成形する。
【0043】
【作用効果】
以上のとおりの構成からなるこの発明の建築用等炭化素材、およびその製造方法は、セルロースの熱分解機構に注目し、薬剤によって可燃性ガスを発生を抑制し、炭化させることができるとの知見に基づくものであって、セルロース系繊維体に燐酸を主成分とする添加液を含浸処理した上、炭化が完了したことを確認する目安となる重量減少率40%強に達するまでの加熱処理を施し、加熱または火炎による可燃性ガス発生を抑制しながら脱水、炭化を促進するようにしたことから、高温の空気中(不活性ガス雰囲気中や酸素遮断を行わない)においても、レボグルコサン(タール成分)を生成しないため、可燃性ガスの生成がなく、脱水炭化に火炎を伴わず(火災の危険が少なくなる。)、したがって、製造過程において、大気汚染を来す虞れは全くなく、また火災の発生を防止でき、作業の安全性が確保でき、効率よく炭素を生成することができるという大きな特徴を有している。
【0044】
また、セルロース系繊維体に含浸する燐酸濃度は、1%以下では炭化が殆ど進まず、また20%を超えた濃度では、可撓性のある炭化素材を得る上で、温度コントロールが極めて微妙になって実用的ではなく、したがって、濃度1〜20%、望ましくは1.5〜15%以上にすると共に、加熱温度も、実用的な65〜400°C、望ましくは80〜300°C前後の温度帯で加熱処理するようにしたことから、炭化素材内に炭素チェーンを残すことが可能となり、柔軟性のある炭化素材を実現可能にするものであり、断熱材や吸音材、床下吸湿材、耐火被覆材といった建材等への製造に際しても、炭化素材からの粉末飛散が殆ど無くなり、極めて作業性がよくなり、効率的な製造を可能にする上、添加液として安価な薬剤(硫安や燐安等は肥料として販売されている)の使用であって、しかも簡単な加熱装置による製造を可能にするものであって、高機能の建材等をかなり安価に提供することが可能になるという秀れた効果が期待できることになる。
【0045】
また、この発明では、これまでのところ、廃棄物として埋め立てられたり、焼却されるしか有効な処理方法のなかつた膨大な量のたりされるセルロース系繊維体、即ち、新聞紙や雑誌類等の古紙や使い古しの段ボール紙、あるいは、建築現場や製材所、木工加工所、木材陸揚げ埠頭等から大量に発生する廃材や木屑、あるいは稲作農家等からの籾殻や藁等々といった、様々なセルロース系繊維体全般を対象とすることができることから、有効な廃棄物処理手段としても活用できるという利点を有している。
特に、この発明を代表する実施例として示した建材等用炭化素材、およびその製造方法の事例によるものでは、これら特徴を確実に達成可能とするものであって極めて実用的なものとすることができる。
【0046】
叙述の如く、この発明の新規な構成からなる建材等用炭化素材、およびその製造方法は、所期の目的を普く達成可能にするものであり、日夜大量に発生する古紙をはじめとする廃棄物としてセルロース系繊維体の有効な活用手段として高く評価されると共に、それら廃棄物を全くダイオキシン等の有害副産物の生成なしに簡便且つ確実に処理できる手段としても、関連部署から十分な信頼を得ることになって、広範に渡って採用、普及していくものになると予想される。
【図面の簡単な説明】
【図1】原料であるセルロース(バージンパルプ)と燐酸処理し炭化した炭および通常の不活性雰囲気中で加熱処理した炭の3種類をX線回折により組成分析を行った対比グラフである。
【図2】セルロースの構造式である。
【図3】セルロースが通常の熱分解で生成するレボグルコサン(タール分)のの熱分解で生成される可燃性ガスの構造式である。
【図4】セルロースの燐酸脱水反応の構造式 である。
【図4−1】セルロースの脱水による変化を示す構造式 である。
【図4−2】燐酸によるエステル化からの脱水作用を説明する構造式 である。
【図5】燐酸で処理したセルロースの加熱時の示差熱分析(吸熱、発熱の測定)データで濃度の違いによる吸発熱の変化を対比したグラフである。
【図6】燐酸化合物で処理したセルロース(木綿)の燃焼時の発熱速度の変化を表すグラフである。
【図7】セルロースの燐酸処理濃度の違いによる加熱温度100°Cの重量変化を示すグラフである。
【図8】セルロースの燐酸処理濃度の違いによる加熱温度150°Cの重量変化を示すグラフである。
【図9】セルロースの燐酸処理濃度の違いによる加熱温度200°Cの重量変化を示すグラフである。
【図10】セルロースの燐酸処理濃度の違いによる加熱温度100°Cの重量変化率を示すグラフである。
【図11】セルロースの燐酸処理濃度の違いによる加熱温度150°Cの重量変化率を示すグラフである。
【図12】セルロースの燐酸処理濃度の違いによる加熱温度200°Cの重量変化率を示すグラフである。
【図13】一旦解繊したセルロース系繊維体によるボードを炭化する代表的な実施例の製造工程図である。[0001]
OBJECT OF THE INVENTION
The present invention relates to a carbonized material suitable as a nonflammable functional material, for example, a heat insulating material for building materials, a soundproofing material, a hygroscopic material, and the like, and is a cellulosic fiber body, particularly one of an advanced society. Cellulosic fiber bodies such as waste paper in a large amount of waste that can be symbolized, waste wood, bark, and agricultural by-products such as rice husks and straws can be easily used as raw materials, and it is extremely inexpensive and efficient. Carbonized materials for building materials, etc. with a new structure, which can be used for heat insulating materials for building materials, soundproofing materials, hygroscopic materials, etc. A new manufacturing method for this purpose is to be provided.
[0002]
[Prior art]
Amid a rich environment both economically and culturally, a large amount of material is consumed every day regardless of corporate management and family life, and the various wastes generated in the process are now an economic burden. It is not a problem but its handling has become a very big social problem from the viewpoint of natural environment conservation.
In particular, looking at the handling of a large amount of used paper, which is said to be a barometer of advanced economic society, newspapers and some magazines currently use recycled paper using recovered paper, but that Recycled paper itself is not made of 100% recovered paper, but it is reused as a product that stabilizes quality by adding virgin pulp at some percentage. The current situation is that, even with the cooperation of the industry that actively uses recycled paper, the demand of the used paper market cannot be satisfied.
[0003]
Such surplus waste paper that cannot be reused or waste paper that is discarded without being collected is burned in an incinerator together with other combustible waste, etc., and harmful dioxins are produced by burning paper containing prohibited items. It is considered to be a major cause of the destruction of the natural environment as a result of being released into the atmosphere, and a large amount of social capital investment is required for the construction of a high-performance incineration plant that is less likely to occur, or a final landfill position is secured. For this reason, the government will be engulfed by policy issues such as planning for various difficulties and having to work on planning. This waste disposal problem is caused by other cellulosic materials, such as waste paper and wood waste generated in large quantities from waste paper, construction sites, sawmills, woodworking processing plants, timber landing wharfs, etc. It is a problem that the fiber body as a whole has as well.
[0004]
Examples of techniques for treating and processing cellulosic fiber bodies by means other than incineration disposal include, for example, Japanese Patent Application Laid-Open No. 62-15645, “Production Method of Fibrous Activated Carbon” (Toho Rayon), Japanese Patent Application Laid-Open No. Hei 4 No. 231314 “Method for producing high surface area activated carbon” (Eucer Carbon Technology Co .: USA), Japanese Patent Application Laid-Open No. 6-56416 “Method for producing activated carbon” (West Vaco Co .: USA), etc. Has been established for a long time as a basic material for fields that require the excellent chemical treatment function of activated carbon, that is, the deodorization function, filtration function, anion generation function, etc. .
[0005]
However, in the case of activated carbon produced by these various active carbonization technologies, its use is related to a very special field, and high quality and performance are required as a material that meets the demand, so it should be treated. In addition to the fact that the quality of raw materials is limited and a considerable initial investment is required for the development of high-performance equipment, for example, the Toho Rayon Technology mentioned above, the oxidation process In order to shorten the required time, the oxidation process is divided into two parts, a pre-oxidation treatment at 300 to 400 ° C. in an inert atmosphere with an oxygen content of 0.5 to 5%, a steam and carbon dioxide atmosphere, 700 It requires a two-step oxidation process called the main oxidation process in a high temperature range of ˜1000 ° C., or Yuker Carbon Technology Co. In the technology, the cellulose-based material is treated with an additive solution such as phosphoric acid, carbonized in an inert atmosphere of 450 to 1200 ° C., and further activated in an oxidizing atmosphere such as steam of 700 ° C. or higher. And Westvaco Co. Like technology, wood (lignocellulose) is targeted, they are finely pulverized and carbonized, and then the carbonized powder is molded again, both of which involve complicated processing steps and high operability. Therefore, it is economically and economically to treat waste paper and waste materials that occur in large quantities every day and have large variations in quality as cellulosic fibers to be treated. Is something that should be almost impossible.
[0006]
On the other hand, it is not used in such advanced fields, but is processed by traditional carbonization means for use as fuel, soil improvement materials, moisture-proof materials, heat insulating materials, sound absorbing materials, etc. A method is also conceivable. This charcoal burning technique is based on a manufacturing method in which wood materials and the like are burned at a high temperature, then oxygen is cut off and steamed by a dehydration action at a high temperature, and cellulose is decomposed and carbonized. It has not changed since ancient times.
[0007]
However, in the charcoal burning process in which both the process of burning in a high temperature region and the subsequent process of shutting off oxygen and incomplete combustion are indispensable, a large amount of carbon dioxide and carbon monoxide are generated in any process. In addition, it has the most troublesome problem today that directly leads to air pollution, and there is a fact that it is completely unsuitable for carbonization of film-like or granular cellulosic fibrous bodies such as waste paper and wood chips.
[0008]
To make matters worse, the charcoal produced by this traditional means has a solid structure in which the carbon chain in the composition is cut, so naturally it does not have properties such as flexibility and elasticity. Therefore, if it is intended to be used as a moisture-proof material, heat insulating material, sound absorbing material, etc. on an uneven surface or curved surface of a building frame, equipment, etc., once solid carbon is pulverized, the carbon powder Can be applied and bonded, kneaded into a binder such as resin, or remolded, or mixed and adhered to fibers as appropriate, and molded into a flexible product as a whole. In addition to this, secondary treatment processing is indispensable for use, and there are also the disadvantages that extra consideration and cost are required for countermeasures against dust coal generated in the secondary treatment processing step. Came from What so far, the carbonization of the traditional charcoal type is also applied as the processing technique used paper and waste materials such as cellulose fiber material to generate a large amount everyday, it is impossible to find the facts that have been put to practical use.
[0009]
In view of the circumstances as described above, the present invention has not been effectively used so far within a very limited range, and a considerable amount of it is used for incineration or landfill disposal at a large cost. Attention is also focused on the cellulosic fiber body that has been made, especially waste paper, and carbon (that is, carbonized cellulose) is also attracted to the non-flammability of oxygen index 65 and high thermal insulation, In order to pursue the possibility of application to building materials, etc. as a large-scale usage destination, we have quickly started development and research, and repeated trial and error such as trying many trial experiments, etc. As a result, waste paper with high flammability etc. Can be carbonized efficiently, and the carbonized material for building materials with a new structure that maintains the flexibility of used paper and the carbonized material for building materials can be reliably and economically used. Produce Which has led to the completion of the manufacturing process of new construction materials for carbide material that allows.
[0010]
[Structure of the invention]
The carbonized material for building materials and the like according to the present invention basically has the following configuration.
That is, a cellulosic fiber impregnated with an additive solution comprising either a phosphorous compound such as phosphoric acid or a phosphorous compound and any one or a mixture of sulfuric acid, ammonium sulfate, boric acid, or derivatives thereof. The body is heated in an active atmosphere within a temperature range of about 65 ° C. to 400 ° C., preferably about 80 ° C. to 300 ° C. for a required time according to the concentration of the added solution, Or it is a carbonization material for building materials etc. which consists of the carbonization material which accelerated | stimulated dehydration and carbonization, increased the carbonization residue, suppressing the generation | occurrence | production of the combustible gas by a flame, and reached at least 40% of weight reduction rate.
[0011]
In the carbonization material for building materials and the like according to this basic structure, a more desirable structure includes a phosphorous compound such as phosphoric acid, a phosphorous compound and sulfuric acid, ammonium sulfate, boric acid, or a derivative thereof, or A cellulosic fiber sheet body impregnated with an additive liquid consisting of any of a mixture of two or more is about 65 ° C to 400 ° C, preferably about 80 ° C to 300 ° C in an active atmosphere. Heat treatment within the temperature range of about C and for the required time according to the concentration of the additive solution, while increasing the carbonization residue by promoting dehydration and carbonization while suppressing the generation of flammable gas by heating or flame, at least weight By reaching a reduction rate of slightly over 40%, leaving a carbon chain in the middle of dehydration carbonization of cellulose, and making it a carbonized material that maintains its sheet shape and flexibility And either combined with either alone or in other materials, a single layer or sheet-like building materials for carbide material was made to be handled as a shape retaining material of the laminated structure is included.
[0012]
The carbonized material for building materials and the like having such a desirable structure is composed of either a phosphorus compound such as phosphoric acid, or a mixture of the phosphorus compound and one or more of sulfuric acid, ammonium sulfate, boric acid, or derivatives thereof. The cellulosic fiber sheet body impregnated with the additive solution is within a temperature range of about 65 ° C. to 400 ° C., preferably about 80 ° C. to 300 ° C. in an active atmosphere, and the concentration of the additive solution Heat treatment for the required time according to the conditions, dehydration and carbonization are promoted while suppressing the generation of flammable gas by heating or flame, carbonization residue is increased, and at least a weight reduction rate of 40% is reached. By leaving the carbon chain in the middle and making it a carbonized material that maintains the sheet shape and flexibility, it can be used alone or in combination with other materials to form a single layer. None allows handled as shape retaining material of the laminated structure, may also indicate incombustible insulation material and absorbent material, sound absorbing material, as a sheet-like building materials for carbide material was made to deodorizing material.
[0013]
Furthermore, the carbonization materials for building materials and the like which are based on the basic configuration described above and the desirable configurations therein include the carbonization materials for building materials and the like which can be shown by the following configurations.
Cellulosic fiber sheet body impregnated with a phosphorous compound such as phosphoric acid, or an additive liquid composed of any one of phosphorous compounds and sulfuric acid, ammonium sulfate, boric acid, or a mixture thereof. In an active atmosphere within a temperature range of about 65 ° C. to 400 ° C., preferably about 80 ° C. to 300 ° C., for a required time according to the concentration of the additive solution, While suppressing the generation of flammable gas due to the flame, dehydration and carbonization are promoted to increase the carbonization residue, and the weight reduction rate reaches 40%, leaving the carbon chain in the middle of the dehydration carbonization of cellulose, and the sheet body shape and flexibility Charcoal for building materials that has been given a pest control function, such as termites, for wood coating by making it a carbonized material that maintains its properties and then treating with boric acid. Material is it.
[0014]
Cellulosic fiber bodies are the most representative ones such as used paper such as newspapers and magazines, and used corrugated paper, but other construction sites, lumber mills, woodworking factories, wood landing wharves, etc. It can also be applied to other cellulosic fibers in general, such as waste materials and wood chips generated in large quantities from rice farms, rice husks and straws from rice farmers, etc. As a raw material to be used for hygroscopic materials, etc., for example, paper made specially in a bulky structure such as a paper towel, roll paper toilet paper, etc. Of course, it is also intended to be used as it is or processed as appropriate, and the properties are also flat, sheet-like Special reasons that must be particularly restricted, such as those having a laminated structure, a block shape, a box or a cylinder, a granular or powdery shape, a straw shape, a rod shape, etc. However, it is intended for cellulosic fiber bodies of various types and properties.
[0015]
The additive liquid exerts an inhibitory effect on the generation of incombustible gas during pyrolysis of cellulose, concealing action due to vitrification, and generation of flammable gas due to chemical change (esterification). It must be capable of promoting the function of increasing the amount of carbonized residue, and either one or two of phosphorous compounds such as phosphoric acid, phosphorous compounds and sulfuric acid, ammonium sulfate, boric acid, or derivatives thereof It shall consist of any of the above mixtures.
[0016]
The cellulosic fiber body impregnated with the additive solution is within a temperature range of about 65 ° C. to 400 ° C., preferably about 80 ° C. to 300 ° C., under an active atmosphere. By performing heat treatment only for the required time according to the concentration and reaching a weight reduction rate of more than 40%, the carbonization residue is increased and the predetermined carbonization ends, and carbon during the dehydration carbonization of cellulose in the material composition Carbonized material for building materials, etc. made of carbonized material with the chain remaining.
[0017]
Even at a predetermined heat treatment temperature within a temperature range of about 65 ° C. to 400 ° C., a material with a small amount of impregnation with the additive liquid becomes a hard carbonized material and is softer than a material with a large amount of impregnation. It makes a difference in sex. This is due to the difference in the residual ratio of the carbon chain of the polysaccharide in the treated cellulose as the amount of the additive solution increases, and as a result of decomposition to carbon alone due to the small amount of the additive solution impregnated, the flexibility, that is, Therefore, it can be said that the flexibility of the obtained carbonized material can be adjusted by controlling the amount of the additive liquid impregnated.
[0018]
Carbonization with flexibility remaining in this way is possible in the normal air after the test piece (charcoal) treated with cellulose in a normal inert gas atmosphere and the additive solution impregnation treatment. When comparing the X-ray diffraction data of the specimen of the present invention heated and carbonized with virgin pulp (Kim towel ... paper) as the raw material of each specimen, as shown in FIG. Pulp) is characterized by a 15 ° (2θ) broad peak and a peak around 23 °, whereas in the case of the specimen (charcoal), a weak broad peak of 20 ° to 30 °. In the case of the specimen of the present invention, although it appears only as (it is difficult to express as a peak), an apparent peak appears even if it does not become a peak as much as virgin pulp. Obtained by liquid impregnation treatment The carbonized material has some characteristics of the paper that is the raw material, and a part of the carbonized chain of cellulose remains in the carbonized material, which is considered to contribute to the flexibility remaining close to the raw material.
[0019]
On the other hand, the carbonized material for building materials of this invention has an oxygen index (oxygen index is the oxygen concentration necessary for combustion) of the chart (carbonized layer) of 65, and that of the raw material is 18 and is a flammable substance. Compared to other materials, the material has much higher incombustibility and heat insulation, and naturally it can be used as an incombustible material, and its chart has a large specific surface area and high adsorption power. Because it has a function as a moisture absorbent and deodorant, it can also be expected to adsorb gas, and since the chart contains a large amount of air and has high heat insulation performance, it has performance as an incombustible heat insulation material. At the same time, sound absorption characteristics are also obtained by the damping effect between the carbon fibers.
[0020]
[Related invention]
In relation to the carbonized material for building materials according to the present invention having the above-described configuration, the present invention includes a method for producing the carbonized material for building materials having the following configuration.
That is, the cellulose fiber body is impregnated with an additive liquid comprising either a phosphorous compound such as phosphoric acid, or a phosphor compound and any one or a mixture of sulfuric acid, ammonium sulfate, boric acid, or derivatives thereof. A cellulose fiber body impregnated with the additive solution in an active atmosphere, in a temperature range of about 65 ° C to 400 ° C, preferably about 80 ° C to 300 ° C, Heat treatment for the required time according to the concentration of the additive solution, while suppressing the generation of flammable gas by heating or flame, promoting dehydration and carbonization to increase the carbonization residue, the carbonization residue increases, at least weight reduction The process of stopping the heat treatment when the rate reaches over 40%, the building material etc. that has obtained the carbonized material leaving the carbon chain in the middle of dehydration carbonization of cellulose by the above process, etc. A method for producing a carbide material.
[0021]
According to a more desirable configuration, the cellulosic fiber body may be a phosphorous compound such as phosphoric acid, or a mixture of phosphorous compound and one or more of sulfuric acid, ammonium sulfate, boric acid, or derivatives thereof. The step of impregnating the additive liquid composed of any of the above, and the cellulosic fiber body impregnated with the additive liquid in an active atmosphere at about 65 ° C to 400 ° C, preferably about 80 ° C to 300 ° C. A process of increasing the carbonized residue by promoting dehydration and carbonization while suppressing the generation of flammable gas due to heating or flame, within a temperature range of The process of stopping the heat treatment at least when the weight loss rate reaches over 40%, and removing the residual additive liquid component as much as possible by washing the carbonized material with water The process of drying the carbonized material from which the remaining additive liquid component has been removed, and the above-described process, for building materials and the like having a configuration in which the carbonized material is left with the carbon chain in the middle of dehydration carbonization of cellulose remaining. It can be set as the manufacturing method of a carbonization raw material.
[0022]
In addition, in the manufacturing method of the carbonized material for building materials and the like of the present invention having the above-described configuration, as a pretreatment step of impregnating the cellulose-based fiber sheet body with an additive liquid, as in an old newspaper or an old magazine Infinite number of permeation holes that penetrate the thickness direction in the averaged arrangement as much as possible on the entire plane of the cellulosic fiber sheet that is laminated with a maximum of about 2 cm thickness of used waste paper and other paper materials The manufacturing method of the carbonization raw material for sheet-like building materials etc. which incorporated the process to carry out and obtained the carbonization sheet laminated body which maintained the flexibility with thick board form from laminated paper is included.
[0023]
The cellulosic fiber body is intended for cellulosic fiber bodies of various types and properties as described above in the carbonization materials for building materials and the like that form the basis of the present invention. Inhibits non-combustible gas generation during pyrolysis, concealing action due to vitrification, and generation of flammable gas due to chemical change (esterification), and promotes dehydration and carbonization of cellulose to increase the amount of carbonized residue It must be capable of increasing the function of phosphorous compounds such as phosphoric acid, or a mixture of phosphorous compounds and one or more of sulfuric acid, ammonium sulfate, boric acid, or derivatives thereof Any suitable means such as dipping, coating, or spraying is included as homogeneously as possible not only in the surface of the cellulosic fiber body but also in the thickness direction. Solution added to the entire cellulosic fibrous body is made to be impregnated strip by suitable means capable.
[0024]
In addition, this additive liquid impregnation step can be carried out collectively so that a plurality of sheets are laminated when the cellulosic fiber body as a target is a sheet body. In order to increase the penetration efficiency of the additive liquid and to achieve a homogeneous penetration state in the thickness direction, the thickness of the laminated cellulosic fiber sheet body is as average as possible over the entire plane. The pretreatment process should be performed after drilling innumerable penetration holes penetrating in the vertical direction before entering the additive liquid impregnation treatment process. Further, in the heat treatment process following the additive liquid impregnation treatment process, heating is performed. The temperature is homogeneously transmitted in a short time from the surface side of the cellulosic fiber sheet body made into a laminated shape to the back in the thickness direction, and uniform carbonization proceeds on the surface side and the back, Overall material quality To stabilize, it is desirable to a restricted limit of lamination thickness of about approximately 2 cm.
[0025]
Thus, the cellulosic fiber body in which the additive solution is uniformly impregnated is heat-treated in a wet state or once in a dry state.
Normal pyrolysis of cellulose starts at about 300 ° C., and the cellulose having the molecular structure shown in FIG. 2 is converted to repoglucosan (β-glucosan C6H10O5) in FIG. 3 by pyrolysis, and further combustible gas (furfuryl). Alcohol C5H6O2, furfural C5H4O2, methanol CH4O, ethanol C2H6O, acetaldehyde C2H6O, glyoxal C2H2O2, etc.).
[0026]
In the production method of the present invention, thermal decomposition that does not produce levoglucosan in the normal pyrolysis process of cellulose proceeds, thereby suppressing subsequent decomposition into combustible gas and increasing carbonization residue. .
Therefore, in the heating process of the present invention, the subject cellulose-based fiber body requires the above-described additive solution impregnation step in advance, and the strong dehydration action of phosphoric acid and sulfuric acid so as not to produce levoglucosan even during the thermal decomposition of cellulose. By causing esterification reaction with acids such as phosphoric acid and decomposing cellulose into hemicellulose phosphates without rapidly decomposing cellulose, the production of tar and flammable gas is efficiently suppressed. Carbonization is performed.
[0027]
This heating step must be continued at least until reaching a weight reduction rate of slightly over 40%, which is a guideline for confirming that carbonization has progressed to a predetermined degree in the above-described process. Then, dehydration and carbonization are promoted while suppressing generation of combustible gas by heating or flame.
[0028]
FIG. 4 shows the dehydration reaction from the esterification of cellulose with phosphoric acid, the position of dehydration, and the resulting structure.
Then, the dehydration reaction from esterification is carried out as follows. The hemicellulose of FIG. 4-1 is esterified by phosphoric acid treatment as shown in FIG. 4-2, and then the cellulose is dehydrated when the phosphoric acid is separated again by continuous heat treatment. Will be disassembled.
As described above, cellulose is prevented from becoming levoglucosan by a dehydration reaction such as phosphoric acid. As a result, generation of combustible gas is suppressed, and efficient dehydration carbonization is performed without accompanying a flame. It has been confirmed that this reaction can be realized even at a low temperature of 300 ° C. or less, which is said to cause thermal decomposition of cellulose.
[0029]
As shown in FIG. 5, when the phosphoric acid is added to the cellulose and the endothermic reaction of the cellulose during heating is measured by thermal analysis (DTA), the endothermic peak of the cellulose decreases as the amount of phosphoric acid increases. It is known that the dehydration reaction of cellulose occurs in preference to the production of repoglucosan and the like. Further, when a phosphoric acid compound is added to the cellulose and heated, as shown in FIG. 6, the rate of heat generation decreases with an increase in the amount of phosphorus added, so that the cellulose is burned slowly and an oxidation reaction without a flame. It turns out that it will move to.
[0030]
FIGS. 7 to 9 show the weight loss due to the phosphoric acid treatment concentration on the cellulose and the heating temperature by a constant temperature dryer, and FIGS. 10 to 12 show the reduction rate.
As can be seen from FIGS. 7 and 10, in the dryer set at 100 ° C., the weight change of untreated cellulose (Kim towel white) is 72 hours after the weight change within 1 hour which seems to be adhering water. However, no change in weight is observed (a slight change is moisture absorption until measurement). However, in the case of heat treatment by phosphoric acid impregnation of the present invention, the weight loss increases with the treatment concentration of phosphoric acid.
[0031]
Therefore, even at 100 ° C, which is lower than the normal cellulose decomposition temperature (250 ° C), a sufficient dehydration reaction occurs depending on the concentration of phosphoric acid. It has been confirmed that carbonization occurs even after the temperature of 65 ° C.
[0032]
Further, as shown in FIGS. 8 and 11, in a dryer set at 150 ° C., remarkable dehydration carbonization occurs at 100 ° C. or higher, and a large weight reduction is observed even in a low concentration phosphoric acid treated product. Although the weight loss within the time is 23% to 40%, the untreated product of the additive solution shows almost no change in weight after the initial weight loss within 1 hour. That is, although cellulose does not decompose at 150 ° C., it can be seen that dehydration carbonization occurs by heat treatment after impregnation with the additive solution.
[0033]
At 200 ° C., as shown in FIG. 9 and FIG. 12, dehydration carbonization action appears remarkably, and the weight change within one hour is the largest. Is getting bigger.
In addition, the cellulose not treated with the additive solution also started to decompose after 24 hours, and after 72 hours, the weight decreased to the same level as that of the additive-impregnated treated product. The surface of the product was close to brown, and the tar content was observed, but the additive-impregnated product was black and no surface change was observed after 1 hour, but the amount of additive-impregnated treatment was small (1.1% P) was a carbonized sheet that was harder and less flexible than the one with a large amount of additive liquid impregnation.
[0034]
This is considered to be due to the fact that the flexibility due to the remaining carbon chain of the polysaccharide is lost by the cellulose impregnation liquid impregnation treatment, as a result of decomposition to carbon alone according to the small amount of the additive liquid impregnation treatment. From this fact, it can be seen that the flexibility of the carbonized material can be adjusted by changing the amount of the additive liquid impregnation treatment.
And from the X-ray diffraction data result (FIG. 1) of the specimen treated with cellulose in a normal inert gas atmosphere, the specimen according to the present invention, and virgin pulp (Kim towel ... paper) as a raw material, the additive solution The fact that the carbonized material of the present invention that has been impregnated and heat-treated remains part of the carbonized chain of cellulose in the carbonized sheet, leaving a little of the characteristics of the paper, as described above.
[0035]
[Example 1]
A cellulosic fiber body such as paper or cotton is impregnated with an additive liquid containing phosphoric acid as a main component, and a temperature range of about 65 ° C to 400 ° C, preferably about 80 ° C to 300 ° C. Heat treatment until the weight loss rate, which is a standard for confirming the degree of carbonization, reaches 40% or more, and then the remaining phosphoric acid is washed with water or neutralized as necessary. The sublimation of phosphoric acid and the like suppress the removal and action of the residual additive solution, and produce a flexible carbonized sheet and carbonized felt at low cost.
[0036]
[Example 2]
This example shows a typical example in which a cellulosic fiber body is defibrated once and then carbonized in a board shape by appropriate means. According to the process diagram shown in FIG. We will add specific explanations.
First, as a defibration process, waste paper and rice straw that have been transported as raw materials are subdivided by known means such as shredders and crushers, and in the case of books and magazines, staples such as staples are crushed and mixed. In addition, since foreign matter may be mixed in at the recovery stage, the process of removing foreign matter such as metals and stones by air classification or magnetic separation should be performed in parallel.
It should be noted that the defibrating means may be any of known methods such as wet, semi-dry, and dry methods.
[0037]
As the additive liquid, commercially available phosphoric acid liquid, for example, plating additive liquid, fertilizer such as ammonium sulfate, phosphoric acid, and the like can be used for economical reasons. What is necessary is just to make it select and employ | adopt suitably according to the intended purpose etc. of the carbonized material after a process. In addition, the combination of inexpensive boric acid and borax is also effective for controlling white ants, etc., and is sent to these additive liquid impregnation processes.
[0038]
As the additive solution used in this process, commercially available phosphoric acid solutions such as plating additive solutions and fertilizers such as ammonium sulfate and phosphorous acid can be used for economic reasons, and any phosphoric acid binding solution is used. Whether or not to do so may be appropriately selected and adopted depending on the purpose of use of the carbonized material after the treatment. In addition, the combined use of inexpensive boric acid or borax is effective for controlling white ants, and the use of these admixtures is also effective.
[0039]
In addition to spray coating and dipping, the additive solution treatment can be performed by mixing the additive solution powder and the defibrated fiber in a dry manner, then mixing them with steam and further preheating, or in a wet process. A method of mixing air with a foaming agent, a foaming agent, etc., and confronting air is also conceivable. There is also a method of performing dust scattering prevention and additive liquid impregnation treatment by an aqueous solution spray or the like at the same time during the defibration in the defibrating process.
[0040]
The cellulosic fiber body that has been subjected to the additive liquid impregnation treatment is then continued to the heating step. In this process, in order to dehydrate and carbonize the treated cellulosic fiber body, it is preferable to perform it in a dry state as much as possible, resulting in a loss of heating energy, and particularly in a low temperature region such as 65 to 100 ° C. Then, this drying step is an essential condition. The heat source for heat treatment is carbonization from a low temperature around 65 ° C when ammonium sulfate, phosphorous mixture or sulfuric acid is used, so it is easy to use waste heat in addition to electricity, gas, oil, etc. In this case, since the reaction occurs slowly, it is possible to obtain materials during the decomposition of cellulose, and it can be applied to fertilizers and the like. Moreover, even if heated directly by a flame, the carbonization is performed while controlling the combustible gas due to the additive liquid effect, so that there is less fear of fire. (In the case where the concentration of the additive solution is low, or in the case of a formulation containing no sulfate group, there is a risk of ignition at a high temperature. Therefore, sufficient care must be taken in the formulation of the additive solution.)
[0041]
The processing time required for this heating process is continued until the weight phenomenon rate reaches at least about 40%, depending on the correlation between the concentration of the additive solution (1.5 to 15%) and the heating temperature (65 to 400 ° C.). Must be implemented. The heat source for heat treatment is the use of ammonium sulfate, phosphoric acid mixture or sulfuric acid, which causes carbonization from 65 ° C. In addition to electricity, gas, oil, etc., waste heat can be used, and heat treatment in a low temperature range. In this case, since the reaction takes place slowly, it becomes possible to use materials during the decomposition of cellulose, and it can be applied to fertilizers and others. Further, even when heated directly by a flame, carbonization is performed while suppressing the flammable gas due to the additive liquid effect, so that there is less concern about fire. (In the case where the concentration of the additive solution is low, or in the case of a formulation containing no sulfate group, there is a possibility of ignition at a high temperature, so that sufficient care is required for the formulation.)
[0042]
[Example 3]
Waste paper fibers and inorganic fibers such as rock wool are mixed and molded, impregnated with the additive solution used in Example 3 above, then heated in a hot air dryer at 180 ° C (high-frequency heating is also possible) and carbonized. And molding a board with high shape retention strength and flexibility.
[0043]
[Function and effect]
The knowledge that the carbonization material for construction, etc. of the present invention having the structure as described above, and the method for producing the same, pay attention to the thermal decomposition mechanism of cellulose, can suppress the generation of flammable gas by chemicals, and can be carbonized. In addition, the cellulose fiber body is impregnated with an additive solution containing phosphoric acid as a main component, and heat treatment is performed until the weight reduction rate reaches 40% or more, which is a guideline for confirming that carbonization is completed. In order to promote dehydration and carbonization while suppressing the generation of flammable gas due to heating or flame, levoglucosan (tar component) even in high-temperature air (in an inert gas atmosphere or without oxygen blocking) ) Does not generate flammable gas, does not cause flame in dehydration carbonization (the risk of fire is reduced), and thus causes air pollution in the manufacturing process Re or no, also possible to prevent the occurrence of a fire, it is possible to ensure the safety of operations, and has a great feature that it is possible to efficiently produce carbon.
[0044]
In addition, the concentration of phosphoric acid impregnated into the cellulosic fiber body is hardly carbonized at 1% or less, and when it exceeds 20%, the temperature control is very delicate in obtaining a flexible carbonized material. Therefore, the concentration is 1 to 20%, preferably 1.5 to 15% or more, and the heating temperature is also practical 65 to 400 ° C, preferably about 80 to 300 ° C. Since heat treatment is performed in the temperature zone, it is possible to leave a carbon chain in the carbonized material, and it is possible to realize a flexible carbonized material, including a heat insulating material, a sound absorbing material, an underfloor moisture absorbing material, Even in the production of building materials such as fireproof coatings, powder scattering from carbonized materials is almost eliminated, the workability is extremely improved, efficient production is possible, and inexpensive chemicals (such as ammonium sulfate and phosphorous acid) are added. Etc. is fertilizer And is capable of manufacturing with a simple heating device, and has the excellent effect of being able to provide highly functional building materials etc. at a relatively low cost. It can be expected.
[0045]
Further, in the present invention, so far, the cellulose-based fibrous body which is buried in the waste as a waste or has an effective processing method that can only be incinerated, that is, used paper such as newspapers and magazines. Various cellulosic fibers such as used and used corrugated paper, waste materials and wood chips generated in large quantities from construction sites, sawmills, woodworking plants, timber landing wharves, rice husks and straws from rice farmers, etc. Can be used as an effective waste treatment means.
In particular, in the case of the carbonization material for building materials and the like shown as an example representing the present invention and the example of the manufacturing method thereof, these characteristics can be surely achieved and should be extremely practical. it can.
[0046]
As described above, the carbonized material for building materials and the like, which has a novel structure of the present invention, and the method for producing the carbonized material are capable of achieving the intended purpose in general, and are disposed of in large quantities, such as waste paper, generated day and night. It is highly evaluated as an effective means of utilizing cellulosic fibrous materials as a product, and it also gains sufficient trust from the related departments as a means for easily and reliably processing these wastes without the generation of harmful by-products such as dioxins. As a result, it is expected to be widely adopted and disseminated.
[Brief description of the drawings]
FIG. 1 is a comparison graph in which composition analysis is performed by X-ray diffraction for three types of raw material cellulose (virgin pulp), phosphoric acid-treated charcoal and charcoal heat-treated in a normal inert atmosphere.
FIG. 2 is a structural formula of cellulose.
FIG. 3 is a structural formula of a flammable gas produced by pyrolysis of levoglucosan (tar content) produced by normal pyrolysis of cellulose.
FIG. 4 is a structural formula of phosphoric acid dehydration reaction of cellulose.
FIG. 4-1 is a structural formula showing a change due to dehydration of cellulose.
FIG. 4-2 is a structural formula illustrating dehydration action from esterification with phosphoric acid.
FIG. 5 is a graph comparing changes in endothermic heat due to differences in concentration in differential thermal analysis (endothermic, exothermic measurement) data during heating of cellulose treated with phosphoric acid.
FIG. 6 is a graph showing a change in heat generation rate during combustion of cellulose (cotton) treated with a phosphoric acid compound.
FIG. 7 is a graph showing changes in weight at a heating temperature of 100 ° C. due to differences in the phosphoric acid treatment concentration of cellulose.
FIG. 8 is a graph showing changes in weight at a heating temperature of 150 ° C. due to differences in the phosphoric acid treatment concentration of cellulose.
FIG. 9 is a graph showing changes in weight at a heating temperature of 200 ° C. due to differences in the phosphoric acid treatment concentration of cellulose.
FIG. 10 is a graph showing the weight change rate at a heating temperature of 100 ° C. depending on the difference in the phosphoric acid treatment concentration of cellulose.
FIG. 11 is a graph showing the weight change rate at a heating temperature of 150 ° C. depending on the difference in the phosphoric acid treatment concentration of cellulose.
FIG. 12 is a graph showing the weight change rate at a heating temperature of 200 ° C. due to the difference in the phosphoric acid treatment concentration of cellulose.
FIG. 13 is a production process diagram of a typical embodiment for carbonizing a board made of cellulosic fibrous material once defibrated.
Claims (7)
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