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JPH0520140B2 - - Google Patents
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JPH0520140B2 - - Google Patents

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Publication number
JPH0520140B2
JPH0520140B2 JP6085087A JP6085087A JPH0520140B2 JP H0520140 B2 JPH0520140 B2 JP H0520140B2 JP 6085087 A JP6085087 A JP 6085087A JP 6085087 A JP6085087 A JP 6085087A JP H0520140 B2 JPH0520140 B2 JP H0520140B2
Authority
JP
Japan
Prior art keywords
chloride
water
electromagnetic field
continuous porous
porous body
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP6085087A
Other languages
Japanese (ja)
Other versions
JPS63224733A (en
Inventor
Yoshio Taguchi
Minoru Oowada
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Electric Power Development Co Ltd
Original Assignee
Electric Power Development Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Electric Power Development Co Ltd filed Critical Electric Power Development Co Ltd
Priority to JP6085087A priority Critical patent/JPS63224733A/en
Publication of JPS63224733A publication Critical patent/JPS63224733A/en
Publication of JPH0520140B2 publication Critical patent/JPH0520140B2/ja
Granted legal-status Critical Current

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  • Water Treatment By Sorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

産業上の利用分野 本発明は、工場等から排出される各種廃液等の
中の有害な金属イオン、ガス、臭気を吸着して浄
化すると共に、酸欠状態を防止するために用い、
または屎尿等の生活排水等の臭気を吸着するため
に用い、または水中のミクロコロイドを凝集沈澱
して水の中の各種金属イオンを吸着して浄化する
ために用い、または水中の青粉、赤潮を凝集沈澱
して透明度を向上させると共に酸欠状態を防止す
るために用いる電磁場が与えられた連続多孔体及
びその製造方法に関するものである。 従来の技術 従来、金属イオン及び臭気の吸着剤として活性
炭を用い、また金属イオンの吸着剤として合成ゼ
オライトを用いている。またミクロコロイドを処
理するには、ポリマー系凝集剤を用いて沈澱さ
せ、この凝集沈澱物より水中に溶出する金属イオ
ンを活性炭、若しくは合成ゼオライトにより吸着
している。水中の青粉、赤潮については良好に凝
集沈澱させる材料がなかつた。 発明が解決しようとする課題 しかし、活性炭及び合成ゼオライトは製造に手
数を要し、高価である。また活性炭は液中での吸
着効率に劣る。従つて各種廃液や生活排水等の多
量処理に用いるには膨大な費用を要するので、処
理されないまま排出され、湖、川、海の汚染によ
る公害の原因となつているのが現状である。 一方、ミクロコロイドの処理には、ポリマー系
凝集剤と活性炭、若しくは合成ゼオライトの二種
類を必要とするため、作業性に劣るばかりでな
く、活性炭及び合成ゼオライトには上記問題点が
ある。また水中の青粉、赤潮については良好に凝
集沈澱させる材料がないので、繁殖するにまかせ
る他なく、終には水中が酸欠状態になり、魚介類
が死滅するに至つているのが現状である。 そこで、本発明は、各種廃液等の金属イオンや
臭気等を効率良く吸着することができ、またはミ
クロコロイドを凝集剤を用いることなく、凝集沈
澱させて水中に溶出する金属イオンを効率良く吸
着することができ、または水中の青粉、赤潮を効
率良く凝集沈澱させて水中の酸欠状態を防止する
ことができ、また簡単に製造することができ、コ
ストの低下を図ずことができ、各種廃液等の大量
処理を行うのに適する電磁場連続多孔体及びその
製造方法を提供しようとするものである。 課題を解決するための手段 上記問題点を解決するための本発明の電磁場連
続多孔体は、石炭フライアツシユ及びセメントを
主原料とし、塩化アンモニウム、塩化カリウム、
塩化マグネシウム、塩化ナトリウム、塩化カルシ
ウム、硫酸ナトリウム、クエン酸、塩化コバル
ト、カオリン系粘土及び酸化バリウムが添加さ
れ、電磁場が与えられた連続多孔体に形成され、
水中の金属イオン、臭気を吸着し、水中のミクロ
コロイドを凝集沈澱させて金属イオンを吸着し、
水中の青粉、赤潮を凝集沈澱させるようにしたも
のである。 また上記問題点を解決するための本発明の電磁
場連続多孔体の製造方法は、石炭フライアツシユ
と塩化アンモニウム、塩化カリウムの水溶液とを
混合して乾燥させ、この乾燥後のものとセメン
ト、塩化カリウム、塩化マグネシウム、塩化ナト
リウム、塩化カルシウム、硫酸ナトリウム、クエ
ン酸、塩化コバルト、カオリン系粘土及び酸化バ
リウムの水溶液を混合して乾燥させると共に、反
応途中で電磁場を与えて連続多孔体に形成し、水
中の金属イオン、臭気を吸着し、水中のミクロコ
ロイドを凝集沈澱させて金属イオンを吸着し、水
中の青粉、赤潮を凝集沈澱させるようにしたもの
である。 本発明の電磁場連続多孔体は、主原料である石
炭フライアツシユ1000Kgに対し、セメント2〜20
%、塩化アンモニウム0.04〜0.05%、塩化カリウ
ム0.07〜0.095%、塩化マグネシウム0.015〜0.02
%、塩化ナトリウム0.015〜0.02%、塩化カルシ
ウム0.015〜0.02%、硫酸ナトリウム0.001〜0.002
%、クエン酸0.0005〜0.001%、塩化コバルト
0.0001〜0.0002%、カオリンナイト5〜20%、酸
化バリウム0.001%〜0.01%の配合比で用いる。 そして製造に際し、石炭フライアツシユと塩化
アンモニウム、塩化カリウムの水溶液を混合して
乾燥させる一次処理では、石炭フライアツシユ
1000Kgに対し、塩化アンモニウム0.04〜0.05%、
塩化カリウム0.05〜0.07%、水30〜40%の配合比
で用い、セメント、塩化カリウム、塩化マグネシ
ウム、塩化ナトリウム、塩化カルシウム、硫酸ナ
トリウム、クエン酸、塩化コバルト、カオリンナ
イト、酸化バリウムの水溶液を混合する二次処理
では、石炭フライアツシユ1000Kgに対し、セメン
ト2〜20%、塩化カリウム0.02〜0.025%、塩化
マグネシウム0.015〜0.02%、塩化ナトリウム
0.015〜0.02%、塩化カルシウム0.015〜0.02%、
硫酸ナトリウム0.001〜0.002%、クエン酸0.005〜
0.001%、塩化コバルト0.0001〜0.0002%、カオリ
ンナイト5〜20%、酸化バリウム0.001〜0.01%、
水30〜40%の配合比で用いる。上記配合比で一次
処理と二次処理を行い、二次処理における反応途
中(養生途中)で、電磁場を与える。 石炭フライアツシユと塩化アンモニウム及び塩
化カリウムを混合して一次処理することにより水
分を含んでいる微細な石炭フライアツシユの持つ
ている電荷を脱着し、石炭フライアツシユとセメ
ントの水溶液による混合によりセメントが液相の
時にカルシウムイオン反応を活発にさせると共
に、セメントの固化反応を阻害している高分子化
合物であるフミン酸等を塩化アンモニウム、硫酸
ナトリウム、クエン酸と反応させて除去し、石炭
フライアツシユの主成分であるSiO2,Al2O3
MgO,K,Naの粒子とセメントのカルシウムと
を反応させてセメント本来の働きをさせる。塩化
ナトリウム、塩化カリウムの働きによりセメント
のカルシウムイオンに浸透性を与えることにより
硬化体はセメント固化物と逆の連続多孔体とな
る。カオリンナイトと酸化バリウムは電磁場を与
えたときの磁力の持続力の低下を防止し、塩化カ
ルシウムはセメントと反応させることによりセメ
ントの凝結時間を短縮させることができ、カルシ
ウムイオンと塩化マグネシウムを反応させること
によりセメントの収縮を防止することができ、塩
化コバルトを用いることにより上記各反応を活発
化させることができる。この反応途中(養生途
中)で電磁場を与えて分子結合を変化させる。こ
の電磁場を与えられた連続多孔体の化学組成は
SiO250〜70%、Al2O310〜30%、MgO2〜3%、
CaO10〜20%、Na5〜10%であつて、SiO4四面
体の頂点の酸素原子を共有しながら三次元に連な
り、孔径が50Å〜300Åで比表面積が10m2/g〜
15m2/gとなり、この中の幾つかのSiがAlで置
換されることにより−1価の電荷を生じ、これを
中和する形でNa+,K+,Ca++等の陽イオンを内
部に有するアルミケイ酸化合物となる。 ここで、塩化アンモニウムが0.04%より少ない
と各成分が溶解し難く、0.05%より多いと連続多
孔体の強度が低下する。塩化カリウムが0.07%よ
り少ないとセメントのカルシウムイオンの浸透能
力に劣り、0.095%より多いと溶解し難いばかり
でなく、カルシウムイオンに浸透性を与える効果
が向上しない。塩化マグネシウムが0.015%より
少ないと連続多孔体に収縮クラツクが発生し、
0.02%より多いと連続多孔体が膨張する。塩化ナ
トリウムが0.015%より少ないとセメントのカル
シウムイオンの浸透能力に劣り、0.02%より多い
と溶解し難いばかりでなく、カルシウムイオンに
浸透力を与える効果が向上しない。塩化カルシウ
ムが0.015%より少ないと、連続多孔体の強度を
促進させることができず、0.02%より多いと破水
現象により連続多孔体を破壊するおそれがある。
硫酸ナトリウムが0.001%より少ないとセメント
を急速硬化させることができず、0.002%より多
いとセメントの強度の長期安定性に劣る。クエン
酸が0.0005%より少ないと各成分が溶解し難く、
0.001%より多いと連続多孔体の強度が低下する。
塩化コバルトが0.0001%より少ないと各成分のイ
オン活動を活発にすることができず、0.0002%よ
り多いと効果が向上しないばかりでなく、高価と
なる。カオリンナイトが5%より少ないと、アル
ミ成分及び微量元素が不足して置換能力が低下
し、20%より多いと、配合比でAl2O3が不足して
効力が低下する。酸化バリウムが0.001%より少
ないと、電磁場を与えたときに磁力の永続性がな
くなり、0.01%より多いと、効力が低下するばか
りでなく、高価となる。 また主原料である石炭フライアツシユ中に含ま
れるSiO2,Al2O3の成分が不足する場合には粘土
により補充し、また連続多孔体としての強度を大
きくする必要がある場合には骨材として砂を用い
ればよく、この場合、砂は石炭フライアツシユ
1000Kgに対し、20〜40%用いるのが望ましい。 作 用 上記本発明の電磁場を与えられた連続多孔体
は、ミクロ孔とマクロ孔による連続多孔に構成さ
れているので、水、空気を良好に流通させること
ができ、しかも全体として空隙、即ち比表面積が
大きい。また疎水性吸着と親水性吸着の性能、所
謂、液相、気相両方の吸着性能を持つと共に
Na+,K+,Ca++等の陽イオンを電気的に捕捉し
ている。而して本発明の電磁場連続多孔体と接触
している廃液等の中に含まれている各種金属イオ
ンが多数のミクロ孔、マクロ孔に入り込み、電気
的に捕捉されている陽イオンとイオン交換されて
吸着される。例えばCa++イオンを含む溶液が
Na+イオンを電気的に捕捉している本発明の電磁
場連続多孔体と接触した場合、下記の交換反応を
示す。 2A→Na++Ca++→A2Ca+2Na また廃液等の中の臭気も多数のミクロ孔、マク
ロ孔に入り込んで物理的に吸着される。アルカリ
悪臭成分と酸性悪臭成分に対する本発明の電磁場
連続多孔体の反応式を下記に示す。 〔アルカリ悪臭成分に対する反応式〕 NH3+A−H→NH4−A (CH33+A−H→(CH33NH−A H2S+B−OH→B−HS+H2O CH3SH+B−OH→CH3S−B+H2O 〔酸性悪臭成分に対する反応式〕 NO+KMnO4→KNO3+MnO2 3H2S+8KMnO4→3K2SO4+8MnO2+2KOH
+2H2O CH3SH+2KMnO4→CH3SO3K+2MnO2
KOH 3(CH32S+4KMnO4+2H2O→3(CH32
SO2+4MnO2+4KOH 上記のような交換吸着能を持つた連続多孔体の
電磁場を与えることによつて上記の本来の吸着交
換能を向上させることができることに加えて水中
のミクロコロイド、青粉、赤潮を電磁場の性質に
より急速に沈澱させることができ、これによつて
長期的に水を浄化させる。即ち、単独水分子の構
造は分子中に存在する10個の電子(5対)のう
ち、1対の電子(内部)は酸素核近くに配置さ
れ、残り4対の電子(外部)のうち、1対は酸素
核と個々の陽子との間に共有され、他の2対は陽
子との化学結合により非分割のまま残り、陽子と
反対側の四面体頂点を占める。このように水はそ
の中に水素結合の鎖が存在する協同系であるの
で、隣接分子との水素結合を容易にする。そして
水は常に溶解したミクロ不純物を含有し、水分子
とその化合物や水和イオン、或は不純物のミクロ
粒子が一定のエネルギーに相当する振動移動を行
つているが、この系に最適周波数の電磁場が作用
すると、上記結合をひずませて構造特性を変化さ
せ、エネルギーの発生を伴う共振が可能になる。
電磁場による水自体の性質の変化は水分子の原子
価角を変化させる。即ち分子の双極子モーメント
の増大と分子間相互作用を変化させ、それらの重
合体を粗大化させる。水の磁化率は正分極磁気の
ペクトルと負の反磁成分の総和である分子相互間
の結合の強化につれて増大し、分子の磁化度はそ
の化学的ポテンシヤルが大きいほど大きくなる。
△F>0のときは偽欠陥内の水の磁化度が偽骨格
内よりも大きい。△F<0の時は逆の相互関係が
成立する。電磁場の作用化における磁化度の差は
分子の分布の変化をもたらし、これが水中の化学
反応の進行条件に影響を与える。従つて電磁場の
作用は水の構造や水和能力を増大させることがで
き、親水性、疎水性吸着の性能を持ち、電磁場を
与えた連続多孔体は水が含有している重金属イオ
ン、臭気、ガスに対し吸着効果があり、ミクロコ
ロイド、青粉、赤潮に対し凝集沈澱効果がある。 また上記本発明の製造方法によれば、石炭フラ
イアツシユ等の主原料と各種添加剤を混合、乾燥
し、しかもその途中で電磁場を与えるだけの簡単
な工程により製造することができる。 実施例 石炭フライアツシユ1000Kg、ポルトランドセメ
ント130Kg、砂300Kgに対し、塩化アンモニウム
400g、塩化カリウム900g、塩化マグネシウム
175g、塩化ナトリウム175g、塩カルシウム175
g、硫酸ナトリウム15g、クエン酸7.5g、塩化
コバルト1.5g、カオリンナイト200Kg、酸化バリ
ウム1Kgの配合比となるように選定した。 上記配合比により次のようにして電磁場連続多
孔体を製造した。 一次処理として、石炭フライアツシユ1000Kg
と、混合して粉末化してある塩化アンモニウム
400g及び塩化カリウム600gを水150gに溶解し、
ミキサーで混合して20℃(5〜80℃の間で適宜選
択することができる)で乾燥させ、石炭フライア
ツシユに吸着されているイオンを中和させた。次
に二次処理として、上記一次処理後の石炭フライ
アツシユに砂300Kgを加えて混合し、続いてポル
トランドセメント130Kgを加えて混合した。続い
て混合して粉末化してある塩化カリウム300g、
塩化マグネシウム175g、塩化ナトリウム175g、
塩化カルシウム175g、硫酸ナトリウム15g、ク
エン酸7.5g、塩化コバルト1.5g、カオリンナイ
ト200Kg及び酸化バリウム1Kgを水100の中に溶
解して水溶液にし、この水溶液を上記混合中のミ
キサーの中にスプレーにより添加し、混合して80
℃(5〜80℃の間で適宜選択することができ、温
度を高くすることにより硬化を促進させることが
できる)で乾燥(養生)させた。その乾燥反応途
中(1日〜2日)で電磁波発生装置(TDK社製)
により2000ガウスで1秒、電磁場を与えた。そし
て、約28日で養生を終え、粒状の電磁場連続多孔
体を形成することができた。 このようにして製造した電磁場連続多孔体を模
式的に表わすと図に示すようになり、この電磁場
連続多孔体はSiO4・Al2O4四面体が酸素原子を共
有して酸素環を形成させ、これを連続させた三次
元骨組構造となつており、孔1a(小)、1b(大)
の径が50Å〜300Åであり、比表面積が10〜15
m2/gであつた。石炭フライアツシユの比表面積
は0.9〜1m2/gであるので、本発明による電磁
場連続多孔体はこれを大幅に増大することができ
た。 上記本発明の電磁場を与えた連続多孔体と、比
較例である電磁場を与えない連続多孔体により下
記の試験条件で各種金属イオンの吸着試験を行つ
た結果、即ち吸着能(飽和)を下記第1表に示
す。 試験条件 試験装置:カラム通水試験 試験方法:Pb,Hg,Mn,Cd,Zn,Ni,Cu
を含んだ模擬排水 通水条件:SV(Space Velocity)=10H-1 LV(Line Velocity)=1.6m/H 測定法:原子吸光法
Industrial Application Field The present invention is used to adsorb and purify harmful metal ions, gases, and odors in various waste liquids discharged from factories, etc., and to prevent oxygen deficiency conditions.
It is also used to adsorb the odor of domestic wastewater such as human waste, or it is used to coagulate and precipitate microcolloids in water to adsorb and purify various metal ions in water, or it is used to purify blue powder and red tide in water. The present invention relates to a continuous porous body provided with an electromagnetic field for use in coagulating and precipitating to improve transparency and preventing an oxygen deficiency state, and a method for manufacturing the same. Prior Art Conventionally, activated carbon has been used as an adsorbent for metal ions and odors, and synthetic zeolite has been used as an adsorbent for metal ions. Furthermore, in order to treat microcolloids, they are precipitated using a polymer flocculant, and metal ions eluted into water from the coagulated precipitate are adsorbed by activated carbon or synthetic zeolite. Regarding blue powder and red tide in the water, there was no material that could be well coagulated and precipitated. Problems to be Solved by the Invention However, activated carbon and synthetic zeolite require time and effort to produce and are expensive. Additionally, activated carbon has poor adsorption efficiency in liquid. Therefore, it costs a huge amount of money to treat large amounts of various waste liquids and domestic wastewater, so the current situation is that they are discharged untreated and cause pollution by contaminating lakes, rivers, and the sea. On the other hand, since the treatment of microcolloids requires two types of coagulants: a polymer flocculant and activated carbon or synthetic zeolite, the workability is not only poor, but activated carbon and synthetic zeolite also have the above-mentioned problems. In addition, since there is no material to properly coagulate and precipitate blue powder and red tide in the water, there is no choice but to let them reproduce, and the current situation is that the water eventually becomes oxygen-deficient, leading to the death of fish and shellfish. be. Therefore, the present invention can efficiently adsorb metal ions, odors, etc. from various waste liquids, or can efficiently adsorb metal ions eluted into water by coagulating and precipitating microcolloids without using a flocculant. It can efficiently coagulate and precipitate blue powder and red tide in water to prevent oxygen deficiency in the water, and it can be easily manufactured and can be used to reduce costs. The present invention aims to provide an electromagnetic field continuous porous body suitable for large-scale treatment of waste liquid, etc., and a method for producing the same. Means for Solving the Problems The electromagnetic field continuous porous body of the present invention to solve the above problems uses coal fly ash and cement as main raw materials, and contains ammonium chloride, potassium chloride,
Magnesium chloride, sodium chloride, calcium chloride, sodium sulfate, citric acid, cobalt chloride, kaolin clay and barium oxide are added, and an electromagnetic field is applied to form a continuous porous body.
Adsorbs metal ions and odors in water, coagulates and precipitates microcolloids in water, and adsorbs metal ions.
It is designed to coagulate and precipitate blue powder and red tide in the water. Further, in order to solve the above-mentioned problems, the method for producing an electromagnetic field continuous porous body of the present invention is to mix and dry coal fly ash and an aqueous solution of ammonium chloride and potassium chloride, and to mix the dried material with cement, potassium chloride, Aqueous solutions of magnesium chloride, sodium chloride, calcium chloride, sodium sulfate, citric acid, cobalt chloride, kaolin clay, and barium oxide are mixed and dried, and an electromagnetic field is applied during the reaction to form a continuous porous body. It adsorbs metal ions and odors, coagulates and precipitates microcolloids in water, adsorbs metal ions, and coagulates and precipitates blue powder and red tide in water. The electromagnetic field continuous porous body of the present invention has 2 to 20 kg of cement per 1000 kg of coal flyash, which is the main raw material.
%, ammonium chloride 0.04-0.05%, potassium chloride 0.07-0.095%, magnesium chloride 0.015-0.02
%, sodium chloride 0.015-0.02%, calcium chloride 0.015-0.02%, sodium sulfate 0.001-0.002
%, citric acid 0.0005-0.001%, cobalt chloride
It is used at a blending ratio of 0.0001 to 0.0002%, kaolinite 5 to 20%, and barium oxide 0.001% to 0.01%. During production, coal fly ash is mixed with an aqueous solution of ammonium chloride and potassium chloride and then dried.
Ammonium chloride 0.04-0.05% for 1000Kg,
A mixture of cement, potassium chloride, magnesium chloride, sodium chloride, calcium chloride, sodium sulfate, citric acid, cobalt chloride, kaolinite, and barium oxide is used at a mixing ratio of 0.05 to 0.07% potassium chloride and 30 to 40% water. In the secondary treatment, 2 to 20% cement, 0.02 to 0.025% potassium chloride, 0.015 to 0.02% magnesium chloride, and sodium chloride are added to 1000 kg of coal flyash.
0.015-0.02%, calcium chloride 0.015-0.02%,
Sodium sulfate 0.001~0.002%, citric acid 0.005~
0.001%, cobalt chloride 0.0001-0.0002%, kaolinite 5-20%, barium oxide 0.001-0.01%,
Use at a blending ratio of 30 to 40% water. Primary treatment and secondary treatment are performed at the above-mentioned mixing ratio, and an electromagnetic field is applied during the reaction (during curing) in the secondary treatment. The primary treatment of mixing coal fly ash with ammonium chloride and potassium chloride desorbs the charge held by the fine coal fly ash containing water, and by mixing the coal fly ash with an aqueous solution of cement, when the cement is in the liquid phase, In addition to activating the calcium ion reaction, humic acid, which is a polymer compound that inhibits the cement solidification reaction, is removed by reacting with ammonium chloride, sodium sulfate, and citric acid, and SiO, the main component of coal fly ash, is removed. 2 , Al2O3 ,
The particles of MgO, K, and Na react with the calcium in the cement to perform its original function. By imparting permeability to calcium ions in the cement through the action of sodium chloride and potassium chloride, the hardened material becomes a continuous porous material, which is the opposite of a solidified cement product. Kaolinite and barium oxide prevent the decrease in the persistence of magnetic force when an electromagnetic field is applied, and calcium chloride can shorten the setting time of cement by reacting with cement, and reacts with calcium ions and magnesium chloride. By using cobalt chloride, shrinkage of cement can be prevented, and by using cobalt chloride, each of the above reactions can be activated. During this reaction (during curing), an electromagnetic field is applied to change the molecular bonds. The chemical composition of a continuous porous material given this electromagnetic field is
SiO2 50-70%, Al2O3 10-30 %, MgO2-3%,
CaO 10-20%, Na 5-10%, connected in three dimensions while sharing the oxygen atoms at the vertices of the SiO 4 tetrahedron, with a pore diameter of 50 Å to 300 Å and a specific surface area of 10 m 2 /g.
15m 2 /g, and some of the Si in this is replaced with Al, creating a −1 valent charge, and cations such as Na + , K + , Ca ++ are added to neutralize this charge. It becomes an aluminum silicate compound contained inside. Here, if ammonium chloride is less than 0.04%, each component will be difficult to dissolve, and if it is more than 0.05%, the strength of the continuous porous body will decrease. If potassium chloride is less than 0.07%, the cement's ability to penetrate calcium ions will be poor, and if it is more than 0.095%, it will not only be difficult to dissolve, but the effect of imparting permeability to calcium ions will not improve. If the magnesium chloride content is less than 0.015%, shrinkage cracks will occur in the continuous porous material.
If it exceeds 0.02%, the continuous porous material will expand. If sodium chloride is less than 0.015%, the cement's ability to penetrate calcium ions will be poor; if it is more than 0.02%, not only will it be difficult to dissolve, but the effect of imparting penetrating power to calcium ions will not improve. If calcium chloride is less than 0.015%, the strength of the continuous porous body cannot be enhanced, and if it is more than 0.02%, there is a risk that the continuous porous body may be destroyed due to water rupture phenomenon.
If sodium sulfate is less than 0.001%, the cement cannot be hardened rapidly, and if it is more than 0.002%, the long-term stability of the cement strength is poor. If the citric acid content is less than 0.0005%, each component will be difficult to dissolve.
If it is more than 0.001%, the strength of the continuous porous body will decrease.
If cobalt chloride is less than 0.0001%, the ionic activity of each component cannot be activated, and if it is more than 0.0002%, not only will the effect not be improved, but it will also be expensive. If the content of kaolinite is less than 5%, the aluminum component and trace elements will be insufficient, resulting in a decrease in substitution ability, and if it is more than 20%, Al 2 O 3 will be insufficient in the blending ratio, resulting in a decrease in efficacy. If barium oxide is less than 0.001%, the magnetic force will not persist when an electromagnetic field is applied, and if it is more than 0.01%, it will not only be less effective but also more expensive. In addition, if the SiO 2 and Al 2 O 3 components contained in coal fly ash, which is the main raw material, are insufficient, they can be replenished with clay, and if it is necessary to increase the strength of a continuous porous body, it can be used as aggregate. Sand may be used; in this case, the sand is
It is desirable to use 20-40% for 1000Kg. Function The continuous porous body to which an electromagnetic field is applied according to the present invention is configured with continuous pores consisting of micropores and macropores, so water and air can be circulated well, and moreover, there are no voids as a whole, i.e. Large surface area. In addition, it has hydrophobic adsorption and hydrophilic adsorption performance, so-called adsorption performance in both liquid phase and gas phase.
Cations such as Na + , K + , Ca ++ are captured electrically. As a result, various metal ions contained in the waste liquid etc. that are in contact with the electromagnetic field continuous porous material of the present invention enter many micropores and macropores, and undergo ion exchange with the electrically captured cations. and is absorbed. For example, a solution containing Ca ++ ions
When contacted with the electromagnetic field continuous porous material of the present invention that electrically traps Na + ions, the following exchange reaction occurs. 2A→Na + +Ca ++ →A 2 Ca+2Na Also, the odor in waste liquid etc. enters the many micropores and macropores and is physically adsorbed. The reaction formula of the electromagnetic field continuous porous material of the present invention with respect to an alkaline malodorous component and an acidic malodorous component is shown below. [Reaction formula for alkaline malodorous components] NH 3 +A-H→NH 4 -A (CH 3 ) 3 +A-H→(CH 3 ) 3 NH-A H 2 S+B-OH→B-HS+H 2 O CH 3 SH+B- OH→CH 3 S−B+H 2 O [Reaction formula for acidic malodorous components] NO+KMnO 4 →KNO 3 +MnO 2 3H 2 S+8KMnO 4 →3K 2 SO 4 +8MnO 2 +2KOH
+2H 2 O CH 3 SH+2KMnO 4 →CH 3 SO 3 K+2MnO 2
KOH 3(CH 3 ) 2 S+4KMnO 4 +2H 2 O→3(CH 3 ) 2
SO 2 +4MnO 2 +4KOH By applying an electromagnetic field to a continuous porous body having the above-mentioned exchange-adsorption capacity, in addition to improving the above-mentioned original adsorption-exchange capacity, microcolloids in water, blue powder, Due to the nature of the electromagnetic field, red tide can be rapidly precipitated, resulting in long-term water purification. In other words, the structure of a single water molecule is that among the 10 electrons (5 pairs) present in the molecule, one pair of electrons (inside) is located near the oxygen nucleus, and of the remaining 4 pairs of electrons (outside), One pair is shared between the oxygen nucleus and each proton, while the other two pairs remain undivided by chemical bonds with the proton and occupy the tetrahedral vertices opposite the proton. Water is thus a cooperative system with chains of hydrogen bonds in it, which facilitates hydrogen bonding with neighboring molecules. Water always contains dissolved micro-impurities, and water molecules and their compounds, hydrated ions, or impurity micro-particles undergo vibrational movement corresponding to a certain amount of energy. acts to distort the above-mentioned bonds and change the structural properties, allowing resonance accompanied by the generation of energy.
Changes in the properties of water itself caused by electromagnetic fields change the valence angle of water molecules. That is, it increases the dipole moment of molecules and changes intermolecular interactions, making these polymers coarser. The magnetic susceptibility of water increases as the bond between molecules, which is the sum of the positive polarization magnetic spectrum and the negative diamagnetic component, strengthens, and the magnetic susceptibility of a molecule increases as its chemical potential increases.
When ΔF>0, the magnetization of water within the pseudo defect is greater than that within the pseudo skeleton. When ΔF<0, the opposite correlation holds true. Differences in magnetization under the action of an electromagnetic field lead to changes in the distribution of molecules, which influence the conditions for the progression of chemical reactions in water. Therefore, the action of an electromagnetic field can increase the structure and hydration ability of water, and it has the performance of hydrophilic and hydrophobic adsorption, and the continuous porous body subjected to an electromagnetic field can absorb heavy metal ions, odors, and other substances contained in water. It has an adsorption effect on gases, and has a flocculation and precipitation effect on microcolloids, blue powder, and red tide. Further, according to the manufacturing method of the present invention, it can be manufactured by a simple process of mixing the main raw material such as coal fly ash and various additives, drying, and applying an electromagnetic field during the process. Example: Ammonium chloride for 1000Kg of coal flyash, 130Kg of Portland cement, and 300Kg of sand.
400g, potassium chloride 900g, magnesium chloride
175g, sodium chloride 175g, calcium salt 175
The blending ratio was selected to be 15 g of sodium sulfate, 7.5 g of citric acid, 1.5 g of cobalt chloride, 200 kg of kaolinite, and 1 kg of barium oxide. An electromagnetic field continuous porous body was manufactured in the following manner using the above blending ratio. Coal fly ash 1000Kg as primary treatment
ammonium chloride mixed with powdered
Dissolve 400g and 600g of potassium chloride in 150g of water,
The mixture was mixed with a mixer and dried at 20°C (which can be appropriately selected between 5 and 80°C) to neutralize the ions adsorbed on the coal flyash. Next, as a secondary treatment, 300 kg of sand was added to and mixed with the coal fly ash after the above primary treatment, and then 130 kg of Portland cement was added and mixed. Next, 300g of potassium chloride, which has been mixed and powdered,
Magnesium chloride 175g, sodium chloride 175g,
175 g of calcium chloride, 15 g of sodium sulfate, 7.5 g of citric acid, 1.5 g of cobalt chloride, 200 kg of kaolinite, and 1 kg of barium oxide were dissolved in 100 g of water to make an aqueous solution, and this aqueous solution was sprayed into the mixer during the above mixing. Add and mix 80
It was dried (cured) at a temperature of 0.degree. During the drying reaction (1 to 2 days), an electromagnetic wave generator (manufactured by TDK)
An electromagnetic field was applied for 1 second at 2000 Gauss. After curing in about 28 days, we were able to form a granular electromagnetic field continuous porous material. The electromagnetic field continuous porous material produced in this way is schematically shown in the figure, and this electromagnetic field continuous porous material consists of SiO 4 Al 2 O 4 tetrahedrons sharing oxygen atoms to form oxygen rings. , it has a three-dimensional framework structure in which these are connected, and holes 1a (small) and 1b (large)
The diameter is 50 Å to 300 Å, and the specific surface area is 10 to 15
m 2 /g. Since the specific surface area of coal fly ash is 0.9 to 1 m 2 /g, the electromagnetic field continuous porous body according to the present invention was able to significantly increase this area. Adsorption tests for various metal ions were conducted under the following test conditions using the continuous porous material of the present invention to which an electromagnetic field was applied and the comparative continuous porous material to which no electromagnetic field was applied. It is shown in Table 1. Test conditions Test equipment: Column water flow test Test method: Pb, Hg, Mn, Cd, Zn, Ni, Cu
Simulated wastewater containing water flow conditions: SV (Space Velocity) = 10H -1 LV (Line Velocity) = 1.6m/H Measurement method: Atomic absorption method

【表】 上記試験結果より明らかなように電磁場を与え
ない連続多孔体でも吸着能に優れているが、本発
明実施例の電磁場を与えた連続多孔体を用いれ
ば、吸着能においてそれより更に10%以上向上さ
せることができる。 次に本発明の電磁場連続多孔体により水中の青
粉の凝集沈澱試験を行つた結果について説明す
る。 茨城県水戸市の千波湖より青粉を含む水を採取
し、8個のビーカーに均等に分配した。1個のビ
ーカーには本発明の電磁場連続多孔体を投入せ
ず、残る7個のビーカーにはそれぞれ1%、3
%、5%、7%、10%、15%、20%の割合で本発
明の電磁場連続多孔体を投入した。そして28時間
経過後、青粉の凝集沈澱状況を調べた。その結
果、本発明の電磁場連続多孔体を投入しなかつた
ビーカーにおいては全体が濁つていたのに対し、
本発明の電磁場連続多孔体を投入したビーカーに
おいては投入量が増加するに従い次第に青粉の凝
集沈澱量が増し、それに伴い透明度も高くなつ
た。特に5%以上投入した場合にその効果は著し
かつたが、それ以下でも実用上問題ない程度の凝
集沈澱効果を得ることができた。また5%以上投
入した場合、あまり凝集沈澱効果が変わらず、ま
たそれ以下の量でも充分な凝集沈澱効果を得るこ
とができ、経済性を考慮すると、0.05%〜5%の
範囲で平均的に敷くのが望ましいことが判明し
た。 上記のように青粉を凝集沈澱させることができ
たことにより水中懸濁物、赤潮等についても凝集
沈澱させることができることは明らかである。 また窒素化合物についても上記悪臭成分に対す
る反応式より明らかなように本発明の電磁場連続
多孔体に吸着させることができる。 本発明の電磁場を与えられた連続多孔体が上記
イオン交換吸着能、水中汚染物質の凝集沈澱にお
いて優れた効果を発揮することができることは、
上記電磁場連続多孔体を接触させた水が下記のよ
うな各磁力と接触時間によつて水中酸素イオン濃
度を増加することからも明らかである。 本発明の第1〜第4実施例として、磁力をそれ
ぞれ10,30,100,130H・KAmに設定し、接触
時間、3時間と5時間の2回、水中酸素イオン濃
度を測定した結果は下記の第2表の通りである
(電磁場連続多孔体を接触させなかつた水を放置
して3時間と5時間後に水中酸素イオン濃度を測
定すると、それぞれ26.72mg/であつた。)。
[Table] As is clear from the above test results, even a continuous porous material not applied with an electromagnetic field has excellent adsorption capacity, but if a continuous porous material applied with an electromagnetic field of the example of the present invention is used, the adsorption capacity is even higher than that by 10%. % or more. Next, the results of a coagulation-sedimentation test of blue powder in water using the electromagnetic field continuous porous material of the present invention will be explained. Water containing blue powder was collected from Lake Senba in Mito City, Ibaraki Prefecture, and distributed equally into eight beakers. One beaker was not filled with the electromagnetic field continuous porous material of the present invention, and the remaining seven beakers were filled with 1% and 3%, respectively.
%, 5%, 7%, 10%, 15%, and 20% of the electromagnetic field continuous porous material of the present invention. After 28 hours had passed, the coagulation and sedimentation status of the blue powder was examined. As a result, the entire beaker in which the electromagnetic field continuous porous material of the present invention was not charged was cloudy, whereas
In the beaker into which the electromagnetic field continuous porous material of the present invention was charged, the amount of blue powder coagulated and precipitated gradually increased as the amount added increased, and the transparency also increased accordingly. In particular, the effect was remarkable when it was added in an amount of 5% or more, but it was possible to obtain a flocculation-sedimentation effect to the extent that there were no practical problems even when the amount was less than 5%. In addition, when adding 5% or more, the coagulation-sedimentation effect does not change much, and a sufficient coagulation-sedimentation effect can be obtained even if the amount is less than that. Considering economic efficiency, the average amount in the range of 0.05% to 5% It turned out that it is desirable to lay it down. Since blue powder can be coagulated and precipitated as described above, it is clear that suspended matter in water, red tide, etc. can also be coagulated and precipitated. Furthermore, nitrogen compounds can also be adsorbed to the electromagnetic field continuous porous material of the present invention, as is clear from the reaction formula for the malodorous components described above. The fact that the continuous porous body provided with the electromagnetic field of the present invention can exhibit excellent effects in the above-mentioned ion exchange adsorption capacity and coagulation and precipitation of pollutants in water is as follows:
This is also clear from the fact that the water brought into contact with the electromagnetic field continuous porous body increases the oxygen ion concentration in the water depending on the magnetic force and contact time as described below. As the first to fourth embodiments of the present invention, the magnetic force was set to 10, 30, 100, and 130 H・KAm, respectively, and the oxygen ion concentration in water was measured twice for contact time of 3 hours and 5 hours.The results are as follows. (The oxygen ion concentration in the water was measured 3 hours and 5 hours after the water was left in contact with the electromagnetic field continuous porous material, and it was 26.72 mg/.)

【表】 上記のように本発明の電磁場連続多孔体を用い
ることにより重金属類及びガス、臭気を吸着する
ので、水質の汚染等、公害の原因を除去すること
ができ、また本発明の電磁場連続多孔体は接触水
を軟化する性質を有することが実験的に確められ
ており、これにより水の腐敗を防止し、活性化す
ることができ、しかも上記のように水中懸濁物、
青粉、赤潮を凝集して沈澱させることができ、透
明度を向上させ、酸欠を防止することができる。 なお、本発明の電磁場連続多孔体は上記二次処
理後、三次処理として、粉末化してある過マンガ
ン酸カリウム50gを水100に溶解して加え、ミ
キサーで混合し、20℃(5〜80℃で適宣選択する
ことができる)で乾燥させることにより過マンガ
ン酸カリウムを担持させることができ、これによ
り臭気の離脱を防止することができる。この場合
にはこの三次処理による乾燥反応途中で電磁場を
与えればよい。 発明の効果 以上要するに本発明の電磁場連続多孔体は、
水、空気を良好に流通させる微細孔を備えた連続
多孔体であつて、比表面積も大きく、疎水性吸着
性及び親水性吸着性を有すると共に電荷を有し、
しかも電磁場が与えられているので、各種廃液等
の金属イオンや臭気等を効率良く吸着することが
でき、またはミクロコロイドを凝集剤を用いるこ
となく、凝集沈澱させて水中に溶出する金属イオ
ンを効率良く吸着することができ、または水中の
青粉、赤潮を効率良く凝集沈澱させて水中の酸欠
状態を防止することができる。 また本発明の製造方法によれば、石炭フライア
ツシユ等の主原料と各種添加剤を混合、乾燥し、
しかもその途中で電磁場を与えるだけの簡単な工
程により製造することができ、コストの低下を図
ることができる。従つて各種廃液等の大量処理を
行うのに適する。
[Table] As mentioned above, by using the electromagnetic field continuous porous material of the present invention, it adsorbs heavy metals, gases, and odors, so it is possible to eliminate causes of pollution such as water pollution. It has been experimentally confirmed that porous materials have the property of softening the water they come into contact with, which can prevent water from spoiling and activate it.
It can aggregate and precipitate blue powder and red tide, improve transparency, and prevent oxygen deficiency. After the above secondary treatment, the electromagnetic field continuous porous body of the present invention is subjected to a tertiary treatment by dissolving 50 g of powdered potassium permanganate in 100 g of water, mixing with a mixer, and heating at 20°C (5 to 80°C). Potassium permanganate can be supported by drying with a drying agent (which can be selected as appropriate), thereby preventing the release of odor. In this case, an electromagnetic field may be applied during the drying reaction by this tertiary treatment. Effects of the Invention In summary, the electromagnetic field continuous porous body of the present invention has the following features:
It is a continuous porous body with fine pores that allow water and air to circulate well, has a large specific surface area, has hydrophobic adsorption and hydrophilic adsorption, and has an electric charge.
Furthermore, since an electromagnetic field is applied, it is possible to efficiently adsorb metal ions and odors from various waste liquids, etc., or to coagulate and precipitate microcolloids without using a flocculant to efficiently remove metal ions eluted into water. It can be well adsorbed, or it can efficiently coagulate and precipitate blue powder and red tide in water to prevent oxygen deficiency in water. Further, according to the manufacturing method of the present invention, main raw materials such as coal fly ash and various additives are mixed, dried,
Moreover, it can be manufactured through a simple process of just applying an electromagnetic field during the process, and costs can be reduced. Therefore, it is suitable for processing large quantities of various waste liquids, etc.

【図面の簡単な説明】[Brief explanation of the drawing]

図は本発明の電磁場連続多孔体を示す模式図で
ある。
The figure is a schematic diagram showing the electromagnetic field continuous porous body of the present invention.

Claims (1)

【特許請求の範囲】 1 石炭フライアツシユ及びセメントを主原料と
し、塩化アンモニウム、塩化カリウム、塩化マグ
ネシウム、塩化ナトリウム、塩化カルシウム、硫
酸ナトリウム、クエン酸、塩化コバルト、カオリ
ン系粘土及び酸化バリウムが添加され、電磁場が
与えられた連続多孔体に形成され、水中の金属イ
オン、臭気を吸着し、水中のミクロコロイドを凝
集沈澱させて金属イオンを吸着し、水中の青粉、
赤潮を凝集沈澱させる電磁場連続多孔体。 2 石炭フライアツシユと塩化アンモニウム、塩
化カリウムの水溶液とを混合して乾燥させ、この
乾燥後のものとセメント、塩化カリウム、塩化マ
グネシウム、塩化ナトリウム、塩化カルシウム、
硫酸ナトリウム、クエン酸、塩化コバルト、カオ
リン系粘土及び酸化バリウムの水溶液を混合して
乾燥させると共に、反応途中で電磁場を与えて連
続多孔体に形成し、水中の金属イオン、臭気を吸
着し、水中のミクロコロイドを凝集沈澱させて金
属イオンを吸着し、水中の青粉、赤潮を凝集沈澱
させる電磁場連続多孔体の製造方法。
[Claims] 1 Coal fly ash and cement are the main raw materials, ammonium chloride, potassium chloride, magnesium chloride, sodium chloride, calcium chloride, sodium sulfate, citric acid, cobalt chloride, kaolin clay and barium oxide are added, Formed in a continuous porous body that is applied with an electromagnetic field, it adsorbs metal ions and odors in water, coagulates and precipitates microcolloids in water, adsorbs metal ions, and removes blue powder in water.
An electromagnetic field continuous porous body that coagulates and precipitates red tide. 2. Mix coal fly ash with an aqueous solution of ammonium chloride and potassium chloride, dry it, and mix this dried product with cement, potassium chloride, magnesium chloride, sodium chloride, calcium chloride,
An aqueous solution of sodium sulfate, citric acid, cobalt chloride, kaolin clay, and barium oxide is mixed and dried, and an electromagnetic field is applied during the reaction to form a continuous porous body, which adsorbs metal ions and odors in the water. A method for producing a continuous porous body using an electromagnetic field that coagulates and precipitates microcolloids to adsorb metal ions, and coagulates and precipitates blue powder and red tide in water.
JP6085087A 1987-03-16 1987-03-16 Electromagnetic field continuous porous body and its manufacturing method Granted JPS63224733A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6085087A JPS63224733A (en) 1987-03-16 1987-03-16 Electromagnetic field continuous porous body and its manufacturing method

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Application Number Priority Date Filing Date Title
JP6085087A JPS63224733A (en) 1987-03-16 1987-03-16 Electromagnetic field continuous porous body and its manufacturing method

Publications (2)

Publication Number Publication Date
JPS63224733A JPS63224733A (en) 1988-09-19
JPH0520140B2 true JPH0520140B2 (en) 1993-03-18

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JP6085087A Granted JPS63224733A (en) 1987-03-16 1987-03-16 Electromagnetic field continuous porous body and its manufacturing method

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Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03183A (en) * 1989-05-26 1991-01-07 Chugoku Electric Power Co Inc:The Method for removing cod by use of coal ash
JP2981623B2 (en) * 1991-06-04 1999-11-22 大成建設株式会社 Manufacturing method of water retention material
CN104998611B (en) * 2015-07-17 2017-03-08 河海大学 A kind of preparation method and application of barium-based modified bentonite
CN115678108B (en) * 2022-09-30 2024-09-17 贺州学院 Pore-forming agent and application thereof, breathable film and preparation method thereof

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