JPH0616805B2 - Method for producing liquid coagulating sedimentation agent using coal ash as a main raw material - Google Patents

Method for producing liquid coagulating sedimentation agent using coal ash as a main raw material

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Publication number
JPH0616805B2
JPH0616805B2 JP3180188A JP3180188A JPH0616805B2 JP H0616805 B2 JPH0616805 B2 JP H0616805B2 JP 3180188 A JP3180188 A JP 3180188A JP 3180188 A JP3180188 A JP 3180188A JP H0616805 B2 JPH0616805 B2 JP H0616805B2
Authority
JP
Japan
Prior art keywords
coal ash
aggregating
adsorption
coal
sulfuric acid
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
JP3180188A
Other languages
Japanese (ja)
Other versions
JPH01207102A (en
Inventor
滋雄 栗村
育英 大野
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.)
TOHOKU HATSUDEN KOGYO KK
Original Assignee
TOHOKU HATSUDEN KOGYO KK
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Application filed by TOHOKU HATSUDEN KOGYO KK filed Critical TOHOKU HATSUDEN KOGYO KK
Priority to JP3180188A priority Critical patent/JPH0616805B2/en
Publication of JPH01207102A publication Critical patent/JPH01207102A/en
Publication of JPH0616805B2 publication Critical patent/JPH0616805B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、石炭火力発電所から燃焼の際に副産物として
生成する石炭灰を薬品処理することによって、石炭灰含
有成分を変質させ、吸着、凝集沈降効果を持たせること
により、低廉に火力発電所の排煙脱硫排水、工場排水並
びに一般の汚水中に含まれる汚濁成分の除去処理を可能
とする排水処理用凝集沈降剤の製造方法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention is a chemical treatment of coal ash produced as a by-product at the time of combustion from a coal-fired power plant to modify a coal ash-containing component, to adsorb, A method for producing a coagulation-sedimentation agent for wastewater treatment, which enables the removal of pollutants contained in flue gas desulfurization wastewater from thermal power plants, factory wastewater and general wastewater at a low cost by having a coagulation-sedimentation effect Is.

(従来の技術) 近年我国においては、石油依存度を小さくするため数々
の石油代替エネルギーの開発が国家的施策のもと行われ
てきており、その中でも石炭エネルギーが有望視され、
今後石炭火力の拡充等により、昭和70年度には、62
0万トン程度の石炭灰発生が予想され、その有効利用と
処理処分問題が大きな課題となっている。
(Prior Art) In recent years, in Japan, a number of alternative oil energies have been developed under national policies in order to reduce dependence on oil, and coal energy is considered to be promising among them.
Due to the expansion of coal-fired power in the future, 62
The generation of coal ash of about 0,000 tons is expected, and its effective use and disposal problems are major issues.

微粉炭を燃焼させることにより、通常投炭量の10重量
%〜25重量%の石炭灰が発生するが、現在我国におい
ての石炭灰有効利用は、一部セメント混和剤(171万
トン/339万トン),セメント原料,肥料などに利用
されているが、有効利用率は約50%程度であり、その
残りの大部分が捨灰として埋立地などに処理処分されて
いるのが現状である。埋立地確保野厳しい現状から見て
石炭灰の有効利用技術開発が早期に望まれていることか
ら、石炭灰中の有効成分を活用し、従来と異なる水処理
剤の開発を行なったものである。
Combustion of pulverized coal usually produces 10 to 25% by weight of coal ash, which is the amount of coal thrown. Currently, the effective use of coal ash in Japan is partially cement admixture (1710,000 tons / 3,390,000). Tons), cement raw materials, fertilizers, etc., but the effective utilization rate is about 50%, and most of the rest is disposed of in landfills as waste ash. Land reclamation area There is a need for early development of effective utilization technology for coal ash in view of the difficult situation. Therefore, the effective component in coal ash was utilized to develop a water treatment agent different from the conventional one. .

(発明が解決しようとする問題点) 本発明は、前述の諸問題に鑑み、石炭灰の有効利用を図
るべく、数々の諸試験を重ね、石炭灰が含有するアルミ
ナ、シリカ、鉄等の有効成分の変質化により、石炭火力
発電所の排煙脱硫排水、工場排水並びに汚水中に含まれ
る汚濁成分を吸着、凝集沈降させる特性を見出し、それ
を排水処理用凝集沈降剤として活用すべく、石炭灰を原
料として排水処理用凝集沈降剤を製造することを目的と
して行なったものである。
(Problems to be Solved by the Invention) In view of the above-mentioned problems, the present invention has been subjected to various tests in order to effectively utilize coal ash, and is effective in alumina, silica, iron, etc. contained in coal ash. Due to the alteration of the components, we have found the characteristics of adsorbing and coagulating sediment components contained in flue gas desulfurization wastewater of coal-fired power plants, factory wastewater and wastewater, and using it as a coagulating sedimentation agent for wastewater treatment, coal It was carried out for the purpose of producing a coagulating sedimentation agent for wastewater treatment using ash as a raw material.

一般的な排水処理には、無機凝集剤あるいは有機凝集剤
を用いて各種の排水処理が行なわれてきている。例に挙
げると、無機凝集剤には、硫酸アルミニウム、ポリ塩化
アルミニウム、アルミン酸ナトリウム、硫酸鉄、塩化
鉄、塩化コッパラスなどがあり、有機凝集剤としては、
アニオン系、カチオン系、ノニオン系などの高分子凝集
剤が数多く用いられている。しかし、無機凝集剤あるい
は有機凝集剤などの排水処理剤は、それぞれ有効的な特
徴を持つが、フロックの浮遊問題、多種の処理薬品の問
題、処理設備工程の複雑化に伴問題などにより、処理水
当たりのコスト高等の問題が挙げられる。
In general wastewater treatment, various wastewater treatments have been performed using an inorganic coagulant or an organic coagulant. As an example, the inorganic coagulant includes aluminum sulfate, polyaluminum chloride, sodium aluminate, iron sulfate, iron chloride, coppar chloride, and the like, and as the organic coagulant,
Many polymer flocculants such as anion type, cation type and nonion type are used. However, wastewater treatment agents such as inorganic coagulants and organic coagulants have effective characteristics, but due to floc floating problems, problems with various treatment chemicals, and problems associated with complication of treatment equipment process, etc. There are problems such as high cost per water.

そこで本発明は、石炭灰の有効成分を変質し、活用する
ことにより、前述の諸問題を解決あるいは回避しうる排
水処理用凝集沈降剤の製造方法を提供しようとするもの
である。
Therefore, the present invention is intended to provide a method for producing a coagulating sedimentation agent for wastewater treatment, which can solve or avoid the above-mentioned problems by modifying and utilizing the active ingredient of coal ash.

(問題点を解決する手段) 本発明は、石炭灰中に含まれる有用成分(表−1参照)
を化学処理し、変質させることにより、吸着、凝集、沈
降効果を持つ液状の石炭灰とするものである。
(Means for Solving Problems) The present invention relates to useful components contained in coal ash (see Table-1).
It is made into a liquid coal ash having an adsorption, aggregation, and sedimentation effect by chemically treating and degrading.

すなわち、石炭灰を水酸化ナトリウム水溶液5〜50重
量%濃度のものに加え、石炭灰中のガラス質相が溶解あ
るいは膨潤化状態になるまで加熱処理(常温下で80℃
〜95℃)し、ケイ酸化合物類、アルミニウム化合類、
水酸化化合物類を生成させることにより、吸着、凝集沈
降効果を持つ物質を得ることができる。さらに、この水
酸化化合物類に、硫酸10〜98量%濃度のものを酸性
域(PH=1〜2)になるまで注入攪拌することによっ
て、ケイ酸化合物類、アルミニウム化合物類、硫酸化合
物類を生成させることにより、吸着,凝集沈降効果を持
つ物質を得ることができる。
That is, coal ash was added to a sodium hydroxide aqueous solution having a concentration of 5 to 50% by weight, and heat treatment was performed until the glassy phase in the coal ash became dissolved or swollen (80 ° C. at room temperature).
~ 95 ° C), silicic acid compounds, aluminum compounds,
By producing the hydroxylated compounds, it is possible to obtain a substance having an adsorption, aggregation and sedimentation effect. Further, by injecting and stirring sulfuric acid compounds having a concentration of 10 to 98% by weight into the hydroxylated compounds until an acidic range (PH = 1 to 2), silicic acid compounds, aluminum compounds, and sulfuric acid compounds are obtained. By generating it, a substance having an adsorption / aggregation sedimentation effect can be obtained.

このことは、石炭灰の未利用分野での有効利用が図られ
るほか、従来の無機凝集剤あるいは有機凝集剤に比べ、
短時間かつ低廉で排水処理が可能となるものである。
This means that coal ash can be effectively used in unused fields, and compared to conventional inorganic or organic flocculants,
Wastewater can be treated in a short time and at low cost.

一般排水については、従来の活性汚泥処理方法とは異な
る凝集沈降効果を持つもので新分野での利用にも期待が
持たれる。
General wastewater has a coagulation-sedimentation effect different from the conventional activated sludge treatment method, and is expected to be used in new fields.

(作用) すなわち、石炭灰を水酸化ナトリウム水溶液を用いて加
熱処理することにより、石炭灰のガラス質相を形成して
いたアルミノシリケートは溶解あるいは膨潤状態となっ
て分解する。
(Operation) That is, when the coal ash is heat-treated with an aqueous sodium hydroxide solution, the aluminosilicate forming the glassy phase of the coal ash is dissolved or swelled and decomposes.

そのことにより、いままで石炭灰のガラス質相に閉じ込
められていたシリカが水酸化ナトリウムと反応し、ケイ
酸ナトリウムが生成する。さらにその他の高含有物質で
あるアルミナとの反応により、ケイ酸アルミニウムの生
成、その他物質の水酸化化合物が同時に生成し、吸着,
凝集,沈降効果を持つ物質に変質する。
As a result, silica, which has been confined in the glassy phase of coal ash, reacts with sodium hydroxide to produce sodium silicate. Furthermore, by reaction with alumina, which is another substance with a high content, aluminum silicate is produced, and a hydroxide compound of other substances is simultaneously produced, adsorbed,
It transforms into a substance with the effect of aggregation and sedimentation.

また、これに硫酸を加えることによって、ケイ酸ナトリ
ウムのゲル化により、シリカ,硫酸ナトリウムの生成,
水酸化アルミニウム、アルミン酸ナトリウムの硫酸アル
ミニウムの生成、水酸化鉄の硫酸鉄生成等のほか、その
他含有物質も硫酸化合物となり、吸着,凝縮,沈降効果
を持つ物質に変質する。
In addition, by adding sulfuric acid to this, gelation of sodium silicate produces silica and sodium sulfate,
In addition to the generation of aluminum sulfate from aluminum hydroxide and sodium aluminate, the generation of iron sulfate from iron hydroxide, etc., other substances contained also become sulfuric acid compounds, which are transformed into substances with adsorption, condensation and sedimentation effects.

これらの作用を簡単に説明すると次のようになる。 The operation will be briefly described below.

1.石炭灰のアルカリ処理 水酸化ナトリウム水溶液に石炭灰を加え、加熱処理を行
なうと、一部溶解し、またゲル状物質が沈殿する。これ
は、石炭灰の化学成分が水酸化ナトリウムと反応し、吸
着、凝集、沈降能力を有する、として以下の化学物質を
含む組成物に変化する。
1. Alkali treatment of coal ash When coal ash is added to an aqueous sodium hydroxide solution and subjected to heat treatment, it partially dissolves and a gel-like substance precipitates. This is a chemical composition of coal ash that reacts with sodium hydroxide and has the ability to adsorb, agglomerate, and settle into a composition containing the following chemicals:

2.石炭灰の酸処理 前項1のアルカリ処理した溶液に酸性(PH=1〜2)
になるまで硫酸を加えると、吸着,凝集,沈降能力を有
する、主として以下の化学物質を含む組成物に変化す
る。
2. Acid treatment of coal ash Acidic (PH = 1 to 2) to the alkali-treated solution of the above 1
When sulfuric acid is added to the composition, the composition is changed to a composition mainly having the following chemical substances, which has adsorption, aggregation and sedimentation ability.

(実施例1) 実排水を用いて、石炭灰を水酸化ナトリウム水溶液12
重量%濃度のものに浸漬攪拌し、加熱処理(アルカリ処
理)して生成した凝集沈降剤の凝集沈降試験を行なっ
た。サンプル水については、排煙脱硫 装置石膏分離上
澄み水を用いて行なった。その結果を(表−2)に示
す。
(Example 1) Using actual wastewater, coal ash was treated with an aqueous sodium hydroxide solution 12
A flocculation-sedimentation test of a flocculation-sedimentation agent produced by subjecting the mixture to a concentration of wt% by immersion, stirring, and heat treatment (alkali treatment) was performed. For the sample water, the flue gas desulfurization equipment gypsum separation clear water was used. The results are shown in (Table-2).

処理対象排水にアルカリ処理した凝集沈降剤を適量加
え、処理水によく溶解させ、任意のpH値に調整処理す
ることによって、水酸化アルミニウム、アルミン酸ナト
リウム重合体への汚濁成分除去、ケイ酸アルミニウムへ
の重金属類等の吸着が行なわれ、それら重合体に同時に
取り込められ、自重を大きくし、急速に沈降分離される
とともに、分離汚泥の濃縮化に寄与する。
By adding an appropriate amount of alkali-treated coagulating sedimentation agent to the wastewater to be treated, dissolving it well in the treated water and adjusting it to an arbitrary pH value, aluminum hydroxide, sodium aluminate polymer removal of contaminants, aluminum silicate Adsorption of heavy metals and the like to the polymer is simultaneously taken up by these polymers, the self-weight is increased, the sediment is rapidly separated, and the sludge is concentrated.

(実施例2) 実排水を用いて、石炭灰を水酸化ナトリウム水溶液12
重量%濃度のものに浸漬攪拌し加熱処理して生成した液
状水酸化化合物に、25重量%濃度の硫酸をPHが1〜
2になるまで注入攪拌して生成(硫酸処理)した凝集沈
降剤の凝集沈降試験を行なった。サンプル水について
は、排煙脱硫装置冷却除塵搭液を用いて行ない、処理水
のPH調整には、水酸化カルシウム5重量%水溶液を用
いて調整した。その結果を(表−3)に示す。
(Example 2) Using actual wastewater, coal ash is treated with an aqueous sodium hydroxide solution 12
A liquid hydroxide compound produced by dipping, stirring and heat-treating in a solution having a concentration of 25% by weight contains 25% by weight of sulfuric acid with a pH of 1 to 1.
A coagulation-sedimentation test was conducted on the coagulation-sedimentation agent produced (sulfuric acid treatment) by pouring and stirring until it reached 2. The sample water was subjected to a flue gas desulfurization apparatus cooling dust removal tower liquid, and the pH of the treated water was adjusted using a 5 wt% calcium hydroxide aqueous solution. The results are shown in (Table 3).

処理対象排水に硫酸処理した凝集沈降剤を適量加え、処
理水によく溶解させ、任意のpH値に調整処理すること
によって、ケイ酸ナトリウムのゲル化により、シリカ,
硫酸ナトリウムの生成、水酸化アルミニウム,アルミン
酸ナトリウムの硫酸アルミニウムの生成、水酸化鉄の硫
酸鉄生成等のほか、その他含有物質も硫酸化合物とな
り、吸着,凝集,沈降効果を持つ。
A suitable amount of a sulfuric acid-treated coagulating sedimentation agent is added to the wastewater to be treated, and it is dissolved in the treated water well and adjusted to an arbitrary pH value. By gelation of sodium silicate, silica,
In addition to the formation of sodium sulfate, aluminum hydroxide, sodium aluminate sulfate, iron hydroxide and iron sulfate, other substances also become sulfuric acid compounds, which have adsorption, aggregation and sedimentation effects.

(実施例3) 実排水を用いて、石炭灰を水酸化ナトリウム水溶液12
重量%濃度のものに浸漬攪拌し加熱処理して生成した液
状水酸化化合物に、25重量%濃度の硫酸をPHが1〜
2になるまで注入攪拌して生成(硫酸処理)した凝集沈
降剤を添加後、水酸化カルシウム水溶液でPH調整した
場合の吸着凝集沈降試験を行なった。サンプル水につい
ては、排煙脱硫装置冷却除塵塔液を用いて行ない、処置
水のPH調整には、水酸化カルシウム5重量%水溶液を
用いて調整した。その結果を(表−4)に示す。
(Example 3) Using actual wastewater, coal ash is treated with an aqueous sodium hydroxide solution 12
A liquid hydroxide compound produced by dipping, stirring and heat-treating in a solution having a concentration of 25% by weight contains 25% by weight of sulfuric acid with a pH of 1 to 1.
After adding the aggregating-precipitating agent produced by pouring and stirring until 2 (sulfuric acid treatment), an adsorption aggregating-sedimentation test was carried out when the pH was adjusted with an aqueous calcium hydroxide solution. The sample water was prepared by using a flue gas desulfurizer cooling dust removal tower liquid, and the pH of the treatment water was adjusted by using a 5 wt% calcium hydroxide aqueous solution. The results are shown in (Table 4).

PH調整処理に水酸化カルシウム水溶液を加えることに
より、一般にマイナスに帯電している汚濁成分の電荷中
和による凝集,沈降による除去、硫酸処理した凝集沈降
剤の含有物質である硫酸アルミニウム,硫酸鉄等の水酸
化アルミニウム、水酸化鉄等の重合体への汚濁成分の吸
着、さらにケイ酸アルミニウムへの重金属類等の吸着が
行なわれ、水酸化アルミニウムのフロックに包み込まれ
るかたちとなり、フロックが大きく成長し沈降除去され
る。また、水酸化カルシウムの添加により、中和反応が
起き石膏を生成する。その際の中和による石膏生成時
に、固相吸着,共沈現象によっても吸着あるいは凝集沈
降効果が助長される。また、石膏は、水に対する溶解度
が低いため、それも、フロック中に取り込められ、さら
に沈降分離速度,分離汚泥の濃縮化に寄与する。
By adding an aqueous solution of calcium hydroxide to the pH adjusting treatment, the negatively charged pollutant components are aggregated by charge neutralization and removed by sedimentation, and aluminum sulfate, iron sulfate, etc., which are the substances containing a flocculating precipitant treated with sulfuric acid, etc. Adsorption of pollutant components to the aluminum hydroxide, iron hydroxide, and other polymers, and adsorption of heavy metals and the like to aluminum silicate, resulting in the inclusion of aluminum hydroxide flocs, resulting in large growth of the flocs. The sediment is removed. Further, the addition of calcium hydroxide causes a neutralization reaction to generate gypsum. At that time, when gypsum is produced by neutralization, the adsorption or coagulation sedimentation effect is promoted by the solid phase adsorption and coprecipitation phenomenon. In addition, since gypsum has a low solubility in water, it is also taken into flocs, and further contributes to the sedimentation separation rate and the concentration of separated sludge.

(実施例4) 既存無機凝集剤との凝集時間の比較を行なうため、硫酸
アルミニウム,アニオン高分子とを用いて実験を行なっ
た。サンプル水については、排煙脱硫装置石膏分離上澄
み水を用いて行ない、判定基準についてはフロックがお
およそ沈降したと認められる時間で判定した。その結果
を(表−5)に示す。
(Example 4) In order to compare the aggregation time with the existing inorganic aggregating agent, an experiment was conducted using aluminum sulfate and an anionic polymer. For the sample water, the flue gas desulfurization device gypsum separation supernatant water was used, and the criterion was determined by the time when it was recognized that the flocs were approximately settled. The results are shown in (Table-5).

(発明の効果) 本発明は、以上のような化学処理を石炭灰に施すことに
より、工場排水ならびに一般汚水中に含まれる汚濁成分
を吸着、凝集、沈降させる特徴をもち、さらに、石炭灰
を主原料とすることからも低廉に製造することができ
る。また、他の無機凝集剤と比較した場合、フロックの
沈降効果が優れていること、処理排水の吸着等の問題も
ないことや、ケイ酸アルミニウムへの有害な重金属等の
吸着など効率的な排水処理が可能となる。
(Effects of the Invention) The present invention has a feature of adsorbing, aggregating, and settling pollutant components contained in factory wastewater and general wastewater by subjecting the coal ash to the above-described chemical treatment. It can be manufactured at low cost because it is used as the main raw material. In addition, when compared with other inorganic coagulants, the floc sedimentation effect is excellent, there is no problem of adsorption of treated wastewater, and efficient drainage of harmful heavy metals such as adsorption of aluminum silicate. Processing becomes possible.

また、無機物から構成されていることから2次公害の心
配も回避され、石炭灰の有効利用範囲の拡大、処理設備
の省略化、処理コストの低減にも大きく寄与するもので
あり、処理された水は、水質基準に適合した清水として
の排水が可能となり有用な水質源の再利用面でも効果は
大きい。
In addition, since it is composed of an inorganic substance, the concern about secondary pollution is avoided, which greatly contributes to the expansion of the effective use range of coal ash, the omission of treatment equipment, and the reduction of treatment costs. Water can be discharged as fresh water that conforms to the water quality standards, and it is very effective in terms of reusing useful water sources.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】石炭火力発電所から発生する微粉炭燃焼灰
(石炭灰)を水酸化ナトリウム水溶液5〜50重量%濃
度のものに浸漬攪拌し、石炭灰含有するアルミナ成分、
シリカ成分などの化学物質が溶解あるいは膨潤状態とな
るまで加熱処理して液状水酸化化合物を生成させ、吸
着、凝集沈降効果を持たせることを特徴とする凝集沈降
剤の製造方法。
1. An alumina component containing coal ash, which is obtained by immersing and stirring pulverized coal combustion ash (coal ash) generated from a coal-fired power plant in a sodium hydroxide aqueous solution having a concentration of 5 to 50% by weight.
A method for producing an aggregating and precipitating agent, which comprises subjecting a liquid hydroxide compound to heat treatment until a chemical substance such as a silica component is dissolved or swelled to produce a liquid hydroxide compound, which has adsorption and aggregating and sedimenting effects.
【請求項2】特許請求の範囲第1項に記載の製造方法に
より得られた液状水酸化化合物に10〜98重量%濃度
の硫酸をPHが1〜2になるまで注入攪拌して液状の硫
酸化合物を生成させ、吸着、凝集沈降効果を持たせるこ
とを特徴とする凝集沈降剤の製造方法。
2. A liquid sulfuric acid obtained by the method according to claim 1, in which sulfuric acid having a concentration of 10 to 98% by weight is poured into the liquid hydroxide compound until pH becomes 1 to 2, and the mixture is stirred. A method for producing an aggregating and precipitating agent, which comprises producing a compound and having an adsorption and an aggregating and sedimenting effect.
JP3180188A 1988-02-16 1988-02-16 Method for producing liquid coagulating sedimentation agent using coal ash as a main raw material Expired - Lifetime JPH0616805B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3180188A JPH0616805B2 (en) 1988-02-16 1988-02-16 Method for producing liquid coagulating sedimentation agent using coal ash as a main raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3180188A JPH0616805B2 (en) 1988-02-16 1988-02-16 Method for producing liquid coagulating sedimentation agent using coal ash as a main raw material

Publications (2)

Publication Number Publication Date
JPH01207102A JPH01207102A (en) 1989-08-21
JPH0616805B2 true JPH0616805B2 (en) 1994-03-09

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Cited By (1)

* Cited by examiner, † Cited by third party
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CN103803564A (en) * 2013-12-13 2014-05-21 中国神华能源股份有限公司 Method for preparing silicon dioxide micropowder by using pulverized fuel ash extracted aluminum residue as raw material and silicon dioxide micropowder

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CN113896305A (en) * 2021-10-26 2022-01-07 广州市芦苇环保科技有限责任公司 Preparation method of polyaluminum ferric chloride water purifying agent
CN114368817B (en) * 2022-01-18 2023-09-08 齐鲁工业大学 Coal gasification coarse slag-based composite flocculant and preparation method and application thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103803564A (en) * 2013-12-13 2014-05-21 中国神华能源股份有限公司 Method for preparing silicon dioxide micropowder by using pulverized fuel ash extracted aluminum residue as raw material and silicon dioxide micropowder

Also Published As

Publication number Publication date
JPH01207102A (en) 1989-08-21

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