JP2001137900A - Dehydration method for sludge mainly composed of inorganic particle and refining agent for dehydration thereof - Google Patents

Dehydration method for sludge mainly composed of inorganic particle and refining agent for dehydration thereof

Info

Publication number
JP2001137900A
JP2001137900A JP32195999A JP32195999A JP2001137900A JP 2001137900 A JP2001137900 A JP 2001137900A JP 32195999 A JP32195999 A JP 32195999A JP 32195999 A JP32195999 A JP 32195999A JP 2001137900 A JP2001137900 A JP 2001137900A
Authority
JP
Japan
Prior art keywords
sludge
dehydration
titanium
inorganic particles
mainly composed
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.)
Granted
Application number
JP32195999A
Other languages
Japanese (ja)
Other versions
JP3815593B2 (en
Inventor
Susumu Mori
享 森
Osamu Yamashita
修 山下
Hideaki Kameyama
英明 亀山
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.)
Ishigaki Co Ltd
Original Assignee
Ishigaki 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 Ishigaki Co Ltd filed Critical Ishigaki Co Ltd
Priority to JP32195999A priority Critical patent/JP3815593B2/en
Publication of JP2001137900A publication Critical patent/JP2001137900A/en
Application granted granted Critical
Publication of JP3815593B2 publication Critical patent/JP3815593B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a dehydration method for sludge which forms flocculated floc having good filtration dehydratability by using a refining agent for dehydration prepared by using titanium oxysulfate and polymerized silicic acid in combination in place of aluminum salts and iron salts for the sludge mainly composed of inorganic particles, and to obtain a refining agent for dehydration thereof. SOLUTION: This dehydration method for the sludge mainly composed of the inorganic particles consists in adding and mixing the titanium oxysulfate to the sludge mainly composed of the inorganic particles in a range of 5 to 20% in terms of TiO2 per solid of the sludge, then regulating its pH to 8 to 11 by using an alkaline agent, adding the polymerized silicate to the sludge in the range of a molar ratio of 1 to 10, more preferably 3 to 5 to the titanium in the titanium oxysulfate and subjecting the sludge to mixing and agitating to perform floc formation, then subjecting the sludge to a mechanical dehydration treatment with a filter press, or the like. The refining agent is used for this sludge. The highly efficient dehydration treatment and the reduction of the weight of dehydrated cake are made possible. The formed dehydrated cake and separated water are free from the worry about the influence of the free chlorine on the natural environment and the formation of trihalomethanes, or the like, and are environmentally safe.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、無機質粒子を主
体とするスラッジの脱水方法並びにその脱水用調質剤に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for dewatering sludge mainly composed of inorganic particles and a conditioning agent for the dewatering.

【0002】[0002]

【従来の技術】従来、上水の浄水処理にて発生する排水
やスラッジ及び土木工事等で発生する排水などの無機質
粒子を主体とするスラッジは、調質薬剤を用いずに重力
自然沈降濃縮をした後フイルタープレスや遠心分離機等
で脱水処理を行うか、または、従来、無機質粒子の凝集
剤として、硫酸アルミ,ポリ塩化アルミなどのアルミ塩
類や硫酸鉄,塩化鉄などの鉄塩類と消石灰を用いてスラ
ッジのろ過脱水性を改善した後、真空脱水機等で機械脱
水する方法が主としてなされている。
2. Description of the Related Art Conventionally, sludge mainly composed of inorganic particles such as wastewater generated in water purification treatment of water and sludge and wastewater generated in civil engineering works is subjected to gravity sedimentation without using a conditioning agent. After dewatering with a filter press or centrifugal separator, or conventionally, as an aggregating agent for inorganic particles, aluminum salts such as aluminum sulfate and polyaluminum chloride, or iron salts such as iron sulfate and iron chloride and slaked lime are used. A method of improving the filtration dewatering property of sludge by using it and then mechanically dewatering with a vacuum dehydrator or the like is mainly used.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記従
来のスラッジをそのまま脱水処理する方法は、スラッジ
中に多く混入する微細粒子のためにろ過脱水性が著しく
低いものであり、脱水設備が大きくなり、非常に長時間
の脱水処理の稼動が必要となるなどの問題点がある。ま
た、塩化第二鉄と消石灰を用いる方法では、スラッジの
ろ過脱水性は向上するものの、脱水処理にて発生するケ
ーキ量が増大し、その処理処分に多大なコストと労力を
要するなどの欠点がある。そして、これらの金属塩類を
単独で用いて生成させた凝集はフロックが小さく、スラ
ッジのろ過脱水性の向上割合は小さい。この発明は、こ
れら従来の方法の問題点を鑑み、ろ過脱水効率が高く、
しかも発生ケーキ及び分離水にも二次公害となるような
有害物質が含有されない無害なスラッジの脱水処理方法
とその調質剤を提供することを目的とする。
However, the above-mentioned conventional method of dewatering sludge as it is is very low in filtration dewatering property due to fine particles which are largely mixed in the sludge, and the dewatering equipment becomes large. There is a problem that a very long operation of the dehydration process is required. In addition, the method using ferric chloride and slaked lime improves the filtration dewatering property of sludge, but has the drawback that the amount of cake generated in the dewatering treatment increases, and that disposal and disposal requires enormous cost and labor. is there. The flocculation produced by using these metal salts alone has a small floc, and the rate of improvement in the filtration dewaterability of the sludge is small. The present invention, in view of the problems of these conventional methods, high filtration dewatering efficiency,
Moreover, it is an object of the present invention to provide a harmless sludge dewatering method that does not contain a harmful substance that causes secondary pollution in the generated cake and the separated water, and a conditioning agent therefor.

【0004】[0004]

【課題を解決するための手段】この発明の要旨は、オキ
シ硫酸チタンと重合ケイ酸を併用し、オキシ硫酸チタン
中のチタンに対するケイ素のモル比が1以上10以下と
なる比率で処理対象スラッジに添加混合し無機質粒子を
凝集させた後、フィルタープレスなどで機械脱水処理を
行なう無機質粒子を主体とするスラッジの脱水方法とそ
のスラッジに用いる調質剤である。
The gist of the present invention is to use a titanium oxysulfate and a polymerized silicic acid together and treat the sludge to be treated with a ratio of silicon to titanium in the titanium oxysulfate of 1 or more and 10 or less. A sludge dewatering method mainly composed of inorganic particles, which is subjected to mechanical dehydration treatment by a filter press or the like after addition and mixing to aggregate the inorganic particles, and a conditioning agent used for the sludge.

【0005】[0005]

【発明の実施の形態】この発明に係る装置は上記のよう
に構成してあり、上水の浄水処理及び土木工事等で発生
する無機質粒子を主体とする排水またはスラッジに、オ
キシ硫酸チタンを添加混合した後、カ性ソーダーまたは
炭酸ソーダーなどのアルカリ剤を用いてpH8〜11に
調整を行い含水酸化チタンを生成させて無機質粒子の凝
集作用を起こさせる。次に、重合ケイ酸を先に添加して
いるオキシ硫酸チタン中のチタンに対するモル比が1以
上10以下となる範囲で添加し、充分に混合撹拌してフ
ロックの形成を行った後、フィルタープレスや遠心分離
機などで脱水
DESCRIPTION OF THE PREFERRED EMBODIMENTS The apparatus according to the present invention is configured as described above, and titanium oxysulfate is added to wastewater or sludge mainly composed of inorganic particles generated in water purification treatment and civil engineering work. After mixing, the pH is adjusted to 8 to 11 using an alkaline agent such as sodium hydroxide or sodium carbonate to generate hydrous titanium oxide to cause the aggregation of the inorganic particles. Next, the polymerized silicic acid is added in a range where the molar ratio to titanium in the titanium oxysulfate to which the previously added silica is added is 1 or more and 10 or less, and the mixture is sufficiently mixed and stirred to form flocs. And dehydration with a centrifuge

【0006】[0006]

【実施例】この発明に係る本発明の無機質粒子を主体と
するスラッジの脱水方法及びその調質剤は、オキシ硫酸
チタンと重合ケイ酸を併用し、オキシ硫酸チタン中のチ
タンに対するケイ素のモル比が1以上10以下となる比
率で添加混合し、無機質粒子の凝集フロックを生成させ
た後、スラッジの脱水処理を行う方法である。これらの
金属塩類を用いて無機性粒子の凝集作用を起こさせるた
めには、金属の水酸化物を生成させることが必要であ
る。オキシ硫酸チタンをそのままスラッジに添加混合す
るだけは、オキシ硫酸チタンの解離による水酸化物が生
成せず、殆ど凝集作用を生じないがアルカリ剤を用いて
pHを8〜11の範囲で調整することにより、含水酸化
チタンが生成し凝集作用を生じるものとなる。しかし、
金属塩による凝集フロックは小さくろ過脱水性の向上は
小さく、オキシ硫酸チタンをアルカリ調整して生成させ
た凝集フロックも同様となる。
DETAILED DESCRIPTION OF THE INVENTION The sludge dewatering method comprising inorganic particles as a main component of the present invention and a conditioning agent for the same are prepared by using titanium oxysulfate and polymerized silicic acid in combination, and the molar ratio of silicon to titanium in titanium oxysulfate. Is added and mixed at a ratio of not less than 1 and not more than 10 to generate aggregated flocs of inorganic particles, and then subjecting the sludge to dehydration treatment. In order to cause the inorganic particles to aggregate using these metal salts, it is necessary to generate a metal hydroxide. Simply adding titanium oxysulfate to sludge as it is and mixing does not produce hydroxide due to dissociation of titanium oxysulfate and hardly causes agglomeration, but adjust the pH in the range of 8 to 11 using an alkali agent. As a result, hydrated titanium oxide is generated and causes an agglomeration action. But,
The flocculation floc due to the metal salt is small and the improvement in filtration dehydration property is small, and the flocculation floc produced by adjusting titanium oxysulfate with alkali is also the same.

【0007】一次凝集させた含水酸化チタンに重合ケイ
酸を添加混合すると、分子量の大きな重合ケイ酸の作用
によって、小さなフロックが成長して大きなろ過脱水性
の高い凝集フロックとなる。オキシ硫酸チタンの添加率
は、TiO2としてスラッジの固形物当り5〜20%の
範囲が適性である。オキシ硫酸チタンの添加率5%以下
では、ろ過脱水性の向上が殆どなく、また20%以上添
加しても向上割合が非常に小さいものとなる。また、チ
タンとケイ素のモル比は、固形物濃度が小さいときはモ
ル比を大きくし、固形物濃度が高い場合はモル比を小さ
くする方が良好なろ過脱水処理ができる。モル比を高く
するほど重合ケイ酸量が多くなり、スラッジ粘性が増大
するので、通常ではモル比を3〜5の範囲とするのが適
当である。
When polymerized silicic acid is added to and mixed with the primary agglomerated hydrous titanium oxide, a small floc grows due to the action of the polymerized silicic acid having a large molecular weight to form a large flocculated floc having high dewaterability. Addition ratio of titanium oxysulfate in the range of solids per 5-20% of the sludge as TiO 2 is proper. When the addition ratio of titanium oxysulfate is 5% or less, there is almost no improvement in the dehydration by filtration, and even when added in an amount of 20% or more, the improvement ratio becomes very small. The molar ratio between titanium and silicon can be increased by increasing the molar ratio when the solid concentration is low, and decreasing the molar ratio when the solid concentration is high. As the molar ratio increases, the amount of the polymerized silicic acid increases and the sludge viscosity increases. Therefore, it is usually appropriate to set the molar ratio in the range of 3 to 5.

【0008】この発明のスラッジの脱水方法と従来の方
法のろ過脱水試験をフイルタープレス用いて実施した結
果は以下の通りであった。先ず、無機質粒子を主体とす
るスラッジとして、実稼動中の浄水場より重力自然沈降
濃縮スラッジを採取し、このスラッジを、スラッジの
圧入圧力0.5Mp、圧搾圧力1.5Mp、雑時間
10分としてろ過速度を算出し、小型フイルタープレス
を用いて脱水操作を行ない、含水率とろ過速度を比較し
た。
[0008] The results of the sludge dewatering method of the present invention and the filtration dewatering test of the conventional method were carried out using a filter press, and the results are as follows. First, as a sludge mainly composed of inorganic particles, gravity sedimentation concentrated sludge is collected from a water purification plant in operation, and this sludge is subjected to a sludge injection pressure of 0.5 MPa, a pressing pressure of 1.5 MPa, and a miscellaneous time of 10 minutes. The filtration speed was calculated, dewatering operation was performed using a small filter press, and the water content and the filtration speed were compared.

【0009】この発明の脱水方法の濾過脱水試験に用い
たスラッジ及び薬剤は、試験に用いたスラッジの固形
物濃度40g/L、オキシ硫酸チタン(市販試薬)、
組成TiOSO4nH2O、含有TiO2量33.1%、
TiO2添加率10%(対スラッジ固形物当たり)
水ガラス(試薬1級品)組成SiO2/Na2O(モル比
=2〜2.3)、純度52〜57%を設定してスラッジ
の調質操作を行なった。まず、所定量のスラッジにオキ
シ硫酸チタンをTiO2として、スラッジ固形物当たり
10%となるように秤量し添加混合し、炭酸ソーダーま
たはカ性ソーダーを急速撹拌しながら添加して、スラッ
ジのpHが8〜11程度となるように調整を行った。次
に、添加したアルカリ剤を充分に混合撹拌を行った後、
水ガラス5〜10%添加した希釈溶液を緩速撹拌を行い
ながら、Tiに対してSiのモル比が1,または3,ま
たは5となるように添加混合し約10分間程度の緩速撹
拌を行なった凝集スラッジを上記のフイルタープレスで
脱水操作をおこなった。その結果は表1の通りであっ
た。
The sludge and the chemical used in the filtration and dehydration test of the dehydration method of the present invention are as follows: the sludge used in the test has a solid concentration of 40 g / L, titanium oxysulfate (a commercially available reagent),
Composition TiOSO 4 nH 2 O, TiO 2 content 33.1%,
TiO 2 addition rate 10% (per sludge solids)
Water glass (reagent first grade product) composition SiO 2 / Na 2 O (mole ratio = 2 to 2.3), was carried out tempering operation of the sludge by setting the 52-57% purity. First, titanium oxysulfate is converted to TiO 2 to a predetermined amount of sludge, weighed and mixed so as to be 10% based on the sludge solid matter, and sodium carbonate or caustic soda is added with rapid stirring to adjust the pH of the sludge. Adjustment was made so as to be about 8 to 11. Next, after sufficiently mixing and stirring the added alkaline agent,
While slowly diluting the diluted solution added with 5 to 10% of water glass, the mixture is added and mixed so that the molar ratio of Si to Ti is 1, or 3, or 5, and the mixture is slowly stirred for about 10 minutes. The coagulated sludge thus obtained was subjected to a dehydration operation using the above-mentioned filter press. The results are shown in Table 1.

【0010】[0010]

【表1】 [Table 1]

【0011】この発明は、上記の三種類の調質剤の添加
により、脱水操作の圧入時間5分、圧搾時間13〜14
分であり、脱水ケーキの含水率55.9〜56.4%の
汚泥が得られ、ろ過速度は2.56〜3.56kg/m
2hであった。なお、Tiに対してSiのモル比が3,
または5の調質剤を用いたスラッジは、モル比1の調質
剤よりもろ過速度が1.00〜1.18kg/m2h速
いことが分かった。
According to the present invention, the addition of the three kinds of the above-mentioned heat-treating agents allows the press-in time of the dewatering operation to be 5 minutes and the pressing time to be 13 to 14 hours.
And the sludge having a water content of 55.9 to 56.4% of the dehydrated cake is obtained, and the filtration rate is 2.56 to 3.56 kg / m.
2 h. Note that the molar ratio of Si to Ti is 3,
Alternatively, it was found that the sludge using the conditioner of No. 5 had a filtration speed of 1.00 to 1.18 kg / m 2 h faster than the conditioner of the molar ratio of 1.

【0012】実施例に使用した同一のスラッジを用い
て、従来から行われている、無薬注脱水法(スラッジ
に何も添加せず、そのまま脱水機にて脱水処理する方
法)、塩化第二鉄・消石灰法(最初に塩化第二鉄を対
スラッジ固形物当たり10%添加混合した後、消石灰を
対固形物当たり30%添加し充分に撹拌を行った後、脱
水機へ圧入して脱水処理を行う方法)、ポリ塩化アル
ミ法(ポリ塩化アルミを対スラッジ固形物当たり10%
添加混合した後、炭酸ソーダーを用いて、pHを8〜1
0の範囲で調製した後脱水機にて脱水処理する方法)の
三種類の各方法について脱水試験を実施した。その結果
は以下の通りであった。
Using the same sludge used in the examples, a conventional chemical-free dehydration method (a method of dehydrating the sludge without adding anything to the sludge and using a dehydrator as it is), Iron and slaked lime method (First add 10% ferric chloride to sludge solids and mix, then add 30% slaked lime to solids and mix thoroughly, then press into dehydrator to dehydrate. Method), polyaluminum chloride method (polyaluminum chloride is 10% per sludge solids)
After addition and mixing, the pH was adjusted to 8 to 1 using sodium carbonate.
(A method of dehydrating with a dehydrator after preparing in the range of 0), a dehydration test was carried out for each of the three methods. The results were as follows.

【0013】[0013]

【表2】 [Table 2]

【0014】この従来の三種類の各方法は、脱水操作の
圧入時間5分、圧搾時間17〜19分であり、脱水ケー
キの含水率64.3〜66.7%の汚泥が得られ、ろ過
速度は1.78〜2.10kg/m2hであった。従っ
て、この発明と従来方法を比較すると、この発明のスラ
ッジの脱水方法は、圧搾操作の圧搾時間で3〜6分短縮
され、脱水ケーキの含水率で7.9〜10.8%低く、
ろ過速度でも0.46〜1.78kg/m2h速いろ過
速度の結果が得られた。
Each of the three conventional methods has a press-in time of 5 minutes and a press time of 17 to 19 minutes in the dewatering operation, and a sludge having a water content of 64.3 to 66.7% of the dewatered cake is obtained. The speed was between 1.78 and 2.10 kg / m 2 h. Therefore, comparing the present invention with the conventional method, the sludge dewatering method of the present invention reduces the pressing time of the pressing operation by 3 to 6 minutes and lowers the water content of the dewatered cake by 7.9 to 10.8%,
A result of 0.46 to 1.78 kg / m < 2 > h faster filtration speed was obtained also in the filtration speed.

【0015】[0015]

【発明の効果】以上のように、この発明の無機質を主体
とするスラッジの脱水方法は、従来用いられているアル
ミ塩類や鉄塩類に代わり、オキシ硫酸チタンと重合ケイ
酸を併用した脱水用調質剤を用いることにより、ろ過脱
水性の良好な凝集フロックを生成するものであり、従来
の方法に比べて高効率な脱水処理ができ、しかも発生す
る脱水ケーキの量も少なく、且つ脱水ケーキ及び分離水
も遊離塩素による自然環境への影響やトリハロメタンの
生成などの危惧がなく、環境に対して安全となるもので
ある。
As described above, the method for dewatering sludge mainly composed of inorganic matter according to the present invention is a method for dehydration using titanium oxysulfate and polymerized silicic acid in combination with the conventionally used aluminum salts and iron salts. The use of a precipitant produces a flocculent floc having good filtration and dehydration properties, enables a more efficient dehydration treatment than the conventional method, and furthermore, generates a smaller amount of dewatered cake, The separated water is also safe for the environment, without fear of affecting the natural environment or producing trihalomethane due to free chlorine.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 オキシ硫酸チタンと重合ケイ酸を併用
し、オキシ硫酸チタン中のチタンに対するケイ素のモル
比が1以上10以下となる比率で処理対象スラッジに添
加混合し無機質粒子を凝集させた後、フィルタープレス
などで機械脱水処理を行なうことを特徴とする無機質粒
子を主体とするスラッジの脱水方法。
1. A method in which titanium oxysulfate and polymerized silicic acid are used in combination and added to a sludge to be treated at a ratio of silicon to titanium in the titanium oxysulfate of 1 to 10 to coagulate inorganic particles. A method for dewatering sludge mainly composed of inorganic particles, wherein a mechanical dewatering treatment is performed by a filter press or the like.
【請求項2】 上記無機質粒子を主体とするスラッジ
に、スラッジの固形物当りTiOとして5〜20%の
範囲でオキシ硫酸チタンを添加混合した後、アルカリ剤
を用いてpH8〜11に調整を行い、次に、重合ケイ酸
をオキシ硫酸チタン中のチタンに対するモル比が1以上
10以下、好ましくはモル比が3〜5の範囲でスラッジ
に添加し、混合撹拌してフロックの形成を行った後、フ
ィルタープレスなどで機械脱水処理を行なうことを特徴
とする請求項1に記載の無機質粒子を主体とするスラッ
ジの脱水方法。
To 2. A sludge consisting mainly of the inorganic particles, was added and mixed titanium oxysulfate with solids per 5-20% range as TiO 2 of the sludge, the adjustment pH8~11 with an alkaline agent Then, the polymerized silicic acid was added to the sludge in a molar ratio of 1 to 10 or less, preferably a molar ratio in the range of 3 to 5, to titanium in titanium oxysulfate, and mixed and stirred to form flocs. 2. The method for dewatering sludge comprising mainly inorganic particles according to claim 1, wherein a mechanical dewatering treatment is carried out by a filter press or the like.
【請求項3】 オキシ硫酸チタンと重合ケイ酸とを併用
し、オキシ硫酸チタン中のチタンに対するケイ素のモル
比が1以上10以下とすることを特徴とする請求項1に
記載の脱水用調質剤。
3. The heat treatment for dehydration according to claim 1, wherein titanium oxysulfate and polymerized silicic acid are used in combination, and the molar ratio of silicon to titanium in the titanium oxysulfate is 1 or more and 10 or less. Agent.
JP32195999A 1999-11-12 1999-11-12 Method for dewatering sludge mainly composed of inorganic particles and refining agent for dewatering Expired - Fee Related JP3815593B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32195999A JP3815593B2 (en) 1999-11-12 1999-11-12 Method for dewatering sludge mainly composed of inorganic particles and refining agent for dewatering

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32195999A JP3815593B2 (en) 1999-11-12 1999-11-12 Method for dewatering sludge mainly composed of inorganic particles and refining agent for dewatering

Publications (2)

Publication Number Publication Date
JP2001137900A true JP2001137900A (en) 2001-05-22
JP3815593B2 JP3815593B2 (en) 2006-08-30

Family

ID=18138346

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32195999A Expired - Fee Related JP3815593B2 (en) 1999-11-12 1999-11-12 Method for dewatering sludge mainly composed of inorganic particles and refining agent for dewatering

Country Status (1)

Country Link
JP (1) JP3815593B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105417925A (en) * 2015-12-28 2016-03-23 山东大学 Preparation method of sludge conditioning agent for deep dehydration of sludge
CN111977930A (en) * 2020-08-13 2020-11-24 杨兰 Ozone oxidation and photocatalytic magnetic field enhanced sludge treatment method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105417925A (en) * 2015-12-28 2016-03-23 山东大学 Preparation method of sludge conditioning agent for deep dehydration of sludge
CN111977930A (en) * 2020-08-13 2020-11-24 杨兰 Ozone oxidation and photocatalytic magnetic field enhanced sludge treatment method
CN111977930B (en) * 2020-08-13 2022-12-13 长治市博奇环保科技有限公司 Ozone oxidation and photocatalytic magnetic field enhanced sludge treatment method

Also Published As

Publication number Publication date
JP3815593B2 (en) 2006-08-30

Similar Documents

Publication Publication Date Title
US3066095A (en) Water purification agents and method of using same
FI78888C (en) Mineral particles in suspension containing compositions and processes for treating aqueous systems with them
US2217466A (en) Composition of matter for water treatment
US5573674A (en) Activated silica sol
US3388060A (en) Process and composition for purification of water supplies and aqueous wastes
CN104556331B (en) PAC (polyaluminium chloride)-modified sodium alginate inorganic-organic composite flocculant and preparation method thereof
JPH0693246A (en) Preparation of chemical for coagulation
WO2007023872A1 (en) Method for processing waste water containing silicon powder
CN109628751A (en) A method of silicon in removing zinc oxide fumes leaching process
JP4508600B2 (en) Method and apparatus for treating fluorine-containing wastewater
CN111039375A (en) Flocculating agent for mine beneficiation wastewater treatment and preparation method and application thereof
WO2005082789A1 (en) Method for treating papermaking waste water and method for utilizing silica sol in papermaking
JP2001137900A (en) Dehydration method for sludge mainly composed of inorganic particle and refining agent for dehydration thereof
JP4495007B2 (en) Papermaking wastewater treatment method and utilization method of silica sol in papermaking
JP3840857B2 (en) Method for dewatering sludge mainly composed of inorganic particles and refining agent for dewatering
CN109019946B (en) Method for reducing suspended particles in wastewater produced by wet white carbon black production
US3535259A (en) Process and flocculating agent produced thereby of the reaction products of sulfuric acid and allophane
JP2000202207A (en) Coagulant for water treatment and production thereof
JP2010075928A (en) Treatment method and treatment device for fluorine-containing waste water
JP2001129309A (en) Powder type flocculating and precipitating agent
JP2019206469A (en) Silicon-containing basic aluminum chloride aqueous solution
JP2000154013A (en) Production of activated silica
JPS6125700A (en) Dehydrating method of organic sludge
JP4524796B2 (en) Method and apparatus for treating fluorine-containing wastewater
KR100284368B1 (en) Manufacturing method of cohesive chemical

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040624

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20060518

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20060531

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090616

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100616

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100616

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110616

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120616

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130616

Year of fee payment: 7

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees