JP2991588B2 - Method for dewatering sludge containing calcium compound - Google Patents
Method for dewatering sludge containing calcium compoundInfo
- Publication number
- JP2991588B2 JP2991588B2 JP5136173A JP13617393A JP2991588B2 JP 2991588 B2 JP2991588 B2 JP 2991588B2 JP 5136173 A JP5136173 A JP 5136173A JP 13617393 A JP13617393 A JP 13617393A JP 2991588 B2 JP2991588 B2 JP 2991588B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- calcium
- polymer flocculant
- calcium compound
- dewatering
- 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
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION
【0001】[0001]
【産業上の利用分野】本発明は、例えば半導体工場のフ
ッ酸排水や、火力発電所の排煙脱硫排水等のフッ素含有
排水に消石灰や塩化カルシウム等のカルシウム化合物を
添加してフッ素をフッ化カルシウムとして沈殿除去する
排水処理工程から発生するフッ化カルシウムを主として
含む汚泥、あるいはセメント工業、石灰製造業等から発
生するカルシウム化合物を主として含有する汚泥等の、
カルシウム化合物を主として含有する汚泥(以下、単に
カルシウム化合物含有汚泥ということもある)の脱水方
法に関するものである。BACKGROUND OF THE INVENTION The present invention relates to a fluorine-containing wastewater such as a hydrofluoric acid wastewater from a semiconductor plant or a flue gas desulfurization wastewater from a thermal power plant, which is added with a calcium compound such as slaked lime or calcium chloride to fluorinate fluorine. Such as sludge mainly containing calcium fluoride generated from a wastewater treatment step of precipitation and removal as calcium, or sludge mainly containing calcium compounds generated from the cement industry, lime manufacturing industry, etc.
The present invention relates to a method for dehydrating a sludge mainly containing a calcium compound (hereinafter sometimes simply referred to as a sludge containing a calcium compound).
【0002】[0002]
【従来の技術】上記のカルシウム化合物を主として含有
する汚泥中には、消石灰、炭酸カルシウム、フッ化カル
シウム、硫酸カルシウム、リン酸カルシウム等の水に不
溶性、あるいは難溶性のカルシウム化合物と、カルシウ
ム化合物以外に界面活性剤等の化学物質、あるいは一般
排水の生物処理工程からの有機物等が含まれていること
が多い。2. Description of the Related Art In a sludge mainly containing the above-mentioned calcium compound, a calcium compound which is insoluble or hardly soluble in water such as slaked lime, calcium carbonate, calcium fluoride, calcium sulfate, calcium phosphate, etc. It often contains chemicals such as activators or organic matter from biological treatment processes of general wastewater.
【0003】従来、カルシウム化合物を主として含有す
る汚泥を脱水する方法として、無薬注で脱水する方法、
アニオン性高分子凝集剤またはカチオン性高分子凝集剤
を添加して凝集・脱水する方法、アニオン性高分子凝集
剤およびカチオン性高分子凝集剤を併用して凝集・脱水
する方法が知られている。[0003] Conventionally, sludge containing mainly calcium compounds is dehydrated without chemical injection.
A method of adding and flocculating and dehydrating an anionic polymer flocculant or a cationic polymer flocculant, and a method of flocculating and dehydrating using an anionic polymer flocculant and a cationic polymer flocculant in combination are known. .
【0004】しかし無薬注で脱水する方法では、脱水の
際に汚泥を凝集させる必要のあるベルトプレス型脱水機
やスクリュープレス型脱水機等の脱水機を使用すること
ができないため、脱水機がフィルタープレス型脱水機に
限定され、脱水効率が悪いという欠点があった。[0004] However, in the method of dehydrating without chemical injection, a dehydrator such as a belt press dehydrator or a screw press dehydrator that needs to coagulate sludge during dehydration cannot be used. It is limited to a filter press type dehydrator, and has a disadvantage that the dehydration efficiency is poor.
【0005】またアニオン性高分子凝集剤またはカチオ
ン性高分子凝集剤の何れか一方を用いる方法では、汚泥
中のカルシウム化合物含有率の変化、カルシウム化合物
以外の他の成分の組成および含有量の変化に対応しにく
く安定した脱水処理が困難であり、また、生成するフロ
ックの強度が弱いため効率の良い脱水処理ができない欠
点があった。In the method using either an anionic polymer flocculant or a cationic polymer flocculant, a change in the calcium compound content in the sludge, a change in the composition and content of other components other than the calcium compound, and the like. It is difficult to perform stable dehydration treatment, and there is a drawback that efficient dehydration treatment cannot be performed because the strength of generated flocs is weak.
【0006】アニオン性高分子凝集剤およびカチオン性
高分子凝集剤の両方を使用する方法では、それぞれの単
独使用の場合よりカルシウム化合物含有汚泥の性状変化
には対応しやすいが、安定した処理を行なうにはいまだ
充分ではない。また、効率的な脱水処理を行なうには、
生成するフロックの強度が充分ではなかった。In the method using both an anionic polymer flocculant and a cationic polymer flocculant, it is easier to cope with the property change of the calcium compound-containing sludge than in the case of using each of them alone, but a stable treatment is performed. Is still not enough. Also, to perform efficient dehydration processing,
The strength of the flocs generated was not sufficient.
【0007】[0007]
【本発明が解決しようとする課題】本発明は上述した従
来技術の欠点を解消し、フッ化カルシウム含有汚泥の性
状の変化に影響を受けず、効率良くフッ化カルシウム含
有汚泥中の懸濁物質を固液分離し、脱水する、フッ化カ
ルシウム含有汚泥の脱水方法を提供することを目的とす
るものである。SUMMARY OF THE INVENTION The present invention solves the above-mentioned drawbacks of the prior art, and is not affected by the change in the properties of the calcium fluoride- containing sludge, so that the calcium fluoride- containing sludge can be efficiently produced. Solid-liquid separation and dehydration of suspended solids
It is an object of the present invention to provide a method for dehydrating a sludge containing lucium .
【0008】[0008]
【課題を解決するための手段】上記目的を実現するため
に、本発明者等は種々の方法を険討した結果、安定して
効率よくカルシウム化合物含有汚泥を脱水する方法を見
出し、本発明を完成するに至った。Means for Solving the Problems In order to achieve the above object, the present inventors have studied various methods, and as a result, have found a method for stably and efficiently dewatering a sludge containing a calcium compound, and have achieved the present invention. It was completed.
【0009】すなわち本発明は、フッ化カルシウムを主
として含有する汚泥に、一分子中にカチオン基およびア
ニオン基を有する両性高分子凝集剤を添加して懸濁物質
を凝集し、脱水することを特徴とするカルシウム化合物
含有汚泥の脱水方法に関するものである。That is, the present invention is characterized in that an amphoteric polymer coagulant having a cationic group and an anionic group in one molecule is added to sludge mainly containing calcium fluoride to coagulate a suspended substance and dehydrate it. And a method for dewatering sludge containing calcium compounds.
【0010】本発明におけるフッ化カルシウムを主とし
て含有する汚泥とは、例えば半導体工場のフッ酸排水や
火力発電所の排煙脱硫排水等のフッ素含有排水に、消石
灰や塩化カルシウム等を添加してフッ素をフッ化カルシ
ウムとして沈殿、除去する工程から排出されるフッ化カ
ルシウムを主として含む汚泥が挙げられる。[0010] The sludge containing mainly calcium fluoride in the present invention, the fluorine-containing waste water, such as waste water of flue gas desulfurization of hydrofluoric acid wastewater and thermal power plants of the semiconductor factory if example embodiment, with the addition of slaked lime and calcium chloride precipitate fluorine as calcium fluoride, and a sludge containing mainly calcium fluoride discharged from removing.
【0011】本発明において用いられる両性高分子凝集
剤は、一分子中にカチオン基およびアニオン基を有する
高分子化合物であれば特に限定されないが、例えばジメ
チルアミノエチル(メタ)アクリレートの3級塩および
4級塩等から選ばれた一種以上のカチオン性単量体とア
クリル酸塩、2−アクリルアミド−2−メチルプロパン
スルホン酸塩等から選ばれた一種以上のアニオン性単量
体との共重合物、あるいは上記のカチオン性単量体およ
びアニオン性単量体とアクリルアミド等のノニオン性単
量体との三元共重合物が挙げられる。The amphoteric polymer flocculant used in the present invention is not particularly limited as long as it is a polymer compound having a cationic group and an anionic group in one molecule. For example, a tertiary salt of dimethylaminoethyl (meth) acrylate and Copolymer of one or more cationic monomers selected from quaternary salts and the like and one or more anionic monomers selected from acrylates, 2-acrylamido-2-methylpropanesulfonate and the like Alternatively, a ternary copolymer of the above cationic monomer and anionic monomer with a nonionic monomer such as acrylamide may be used.
【0012】本発明で使用される両性高分子凝集剤の単
量体構成割合は特に限定されないが、カチオン性単量体
8〜95モル%、アニオン性単量体4〜30モル%及び
ノニオン性単量体85モル%以下であることが好まし
い。The monomer composition ratio of the amphoteric polymer flocculant used in the present invention is not particularly limited, but is 8 to 95 mol% of a cationic monomer, 4 to 30 mol% of an anionic monomer and a nonionic It is preferable that the monomer content is 85 mol% or less.
【0013】第2の発明は、カルシウム化合物を主とし
て含有する汚泥に、一分子中にカチオン基およびアニオ
ン基を有する両性高分子凝集剤を添加した後、さらにア
ニオン性高分子凝集剤を添加して懸濁物質を凝集し、脱
水することを特徴とするカルシウム化合物含有汚泥の脱
水方法に関するものである。[0013] In the second invention, an amphoteric polymer flocculant having a cationic group and an anionic group in one molecule is added to a sludge mainly containing a calcium compound, and then an anionic polymer flocculant is further added. The present invention relates to a method for dewatering calcium compound-containing sludge, which comprises coagulating and dewatering a suspended substance.
【0014】両性高分子凝集剤を添加した後に、アニオ
ン性高分子凝集剤を添加する第2の発明は、アニオン性
高分子凝集剤により更にフロック強度が増し、得られる
脱水ケーキの含水率、SS回収率の点でより好ましい結
果が得られる。The second invention in which an anionic polymer flocculant is added after an amphoteric polymer flocculant is added, is to further increase the floc strength by the anionic polymer flocculant, and to obtain a water content, SS More favorable results are obtained in terms of recovery.
【0015】第2の発明において用いられるアニオン性
高分子凝集剤としては、例えばアクリル酸塩とアクリル
アミドの共重合物、アクリルアミドとアクリル酸塩と2
−アクリルアミドー2−メチルプロパンスルホン酸塩の
三元共重合物、ポリアクリル酸塩等が挙げられる。The anionic polymer coagulant used in the second invention is, for example, a copolymer of acrylate and acrylamide, acrylamide and acrylate
Tertiary copolymer of acrylamide-2-methylpropanesulfonate, polyacrylate and the like.
【0016】本発明で脱水の際に用いられる脱水機は特
に限定されないが、例えばスクリュープレス型脱水機、
ベルトプレス型脱水機、遠心脱水機が挙げられ、特にス
クリュ一プレス型脱水機が好ましい。The dehydrator used for dehydration in the present invention is not particularly limited. For example, a screw press type dehydrator,
Examples thereof include a belt press type dehydrator and a centrifugal dehydrator, and a screw press type dehydrator is particularly preferable.
【0017】本発明はカルシウム化合物を主として含有
する汚泥に一分子中にカチオン基とアニオン基の両方を
持つ両性高分子凝集剤を添加し汚泥中の懸濁物質を凝集
させた後、脱水するものであり、従来法と比ベ安定した
脱水効果を得られるものである。本発明によりこのよう
な効果が得られるメカニズムは明確ではないが、カルシ
ウム化合物含有汚泥はアニオン性高分子凝集、カチオン
性高分子凝集剤の何れでも凝集する場合が多くカルシウ
ム化合物含有汚泥中の汚泥粒子にはアニオン基、カチオ
ン基のそれぞれが作用する部位が存在するものと考えら
れ、一分子中にアニオン基、カチオン基の両方を持つ両
性高分子凝集剤はその両方の部位に作用することにより
強固なフロックが生成するものと推測される。The present invention relates to a method of adding an amphoteric polymer coagulant having both a cationic group and an anionic group in one molecule to a sludge mainly containing a calcium compound, coagulating a suspended substance in the sludge, and then dehydrating the sludge. Thus, a more stable dewatering effect can be obtained as compared with the conventional method. The mechanism by which this effect is obtained by the present invention is not clear, but calcium compound-containing sludge often aggregates with any of anionic polymer flocculants and cationic polymer flocculants. Is thought to have a site where each of the anion group and the cation group acts, and the amphoteric polymer flocculant having both the anion group and the cation group in one molecule is strong by acting on both sites. It is presumed that a large floc is generated.
【0018】以上説明したように本発明によればカルシ
ウム化合物を主として含有する汚泥の性状等が大きく変
化しても安定した凝集、脱水効果を得ることができる。As described above, according to the present invention, a stable coagulation and dewatering effect can be obtained even if the properties of sludge mainly containing a calcium compound are largely changed.
【0019】以下に本発明の実施例を説明するが本発明
は以下の実施例に限定されるものではない。An embodiment of the present invention will be described below, but the present invention is not limited to the following embodiment.
【0020】[0020]
【実施例】実施例と比較例において使用した各両性高分
子凝集剤、アニオン性高分子凝集剤及びカチオン性高分
子凝集剤を表1に、実施例および比較例で使用した汚泥
の性状と、懸濁物質の主成分を表2に示す。なお、使用
した汚泥はいずれも半導体工場のフッ酸排水処理工程か
ら発生した、フッ化カルシウムを含有する汚泥である。EXAMPLES Table 1 shows the amphoteric polymer flocculants, anionic polymer flocculants and cationic polymer flocculants used in Examples and Comparative Examples, and the properties of the sludge used in Examples and Comparative Examples. Table 2 shows the main components of the suspended substance. The sludge used was sludge containing calcium fluoride, which was generated from a hydrofluoric acid wastewater treatment process in a semiconductor factory.
【0021】[0021]
【表1】 [Table 1]
【0022】[0022]
【表2】 [Table 2]
【0023】表2から明らかなように、使用した汚泥中
に含まれている懸濁物質の構成成分としては何れもフッ
素とカルシウムが多く、したがって、これらの汚泥中に
はカルシウム化合物としてフッ化カルシウムが多く含ま
れていることが明らかである。また、各汚泥については
汚泥B,Cにはこの他にアルミニウムが多く含まれてお
り、さらに汚泥Bにはケイ素も多く含まれている。As is clear from Table 2, the suspended solids contained in the used sludge contain a large amount of fluorine and calcium. Therefore, these sludges contain calcium fluoride as a calcium compound. It is clear that a lot is included. In each of the sludges, the sludges B and C contain a large amount of aluminum, and the sludge B also contains a large amount of silicon.
【0024】実施例1〜3、比較例1〜3 表2に示した供試汚泥A〜Cに、表3で示す割合で高分
子凝集剤を添加し、撹拌することにより懸濁物質を凝集
させ、生成した凝集フロックをスクリュープレス型脱水
機(商品名「SPS−305CPHS」、オルガノ株式
会社製)により脱水処理した。Examples 1 to 3 and Comparative Examples 1 to 3 Polymer flocculants were added to the test sludges A to C shown in Table 2 at the ratios shown in Table 3, and the suspension was agglomerated by stirring. The flocculated floc thus formed was dehydrated by a screw press type dehydrator (trade name “SPS-305CPHS”, manufactured by Organo Corporation).
【0025】なお、実施例3および比較例3の併用系の
場合は、供試汚泥に第一高分子凝集剤を添加・撹拌した
後、第二高分子凝集剤を添加・撹拌し、生成した凝集フ
ロックを同様に脱水処理することにより行なった。In the case of the combined system of Example 3 and Comparative Example 3, the first polymer flocculant was added to the test sludge and stirred, and then the second polymer flocculant was added and stirred to produce sludge. The coagulation floc was similarly dehydrated by performing a dehydration treatment.
【0026】脱水試験の結果を表4に示す。表4中のフ
ロック強度は、◎が最も強く、以下〇、△、×の順で弱
くなることを示す。Table 4 shows the results of the dehydration test. The floc strength in Table 4 indicates that ◎ is the strongest and weakens in the order of Δ, Δ, and × below.
【0027】[0027]
【表3】 [Table 3]
【0028】[0028]
【表4】 [Table 4]
【0029】表4の結果から明らかなように、本発明で
ある両性高分子凝集剤を単独で使用した実施例1、実施
例2は脱水処理を行うのに十分な大きさと強度を有する
フロックが生成し、SS回収率及び脱水ケーキ含水率の
全てにおいて良好な結果が得られた。また、両性高分子
凝集剤とアニオン性高分子凝集剤を併用する実施例3
は、いずれの汚泥に対してもSS回収率、脱水ケーキ含
水率ともにさらに良好であり、安定した脱水処理が行え
た。As is evident from the results in Table 4, Examples 1 and 2 in which the amphoteric polymer flocculant of the present invention was used alone had flocs having a size and strength sufficient for dehydration treatment. Good results were obtained in both the SS recovery rate and the water content of the dehydrated cake. Example 3 using an amphoteric polymer flocculant and an anionic polymer flocculant in combination
For both sludges, the SS recovery rate and the water content of the dewatered cake were even better, and a stable dewatering treatment could be performed.
【0030】これに対しアニオン性高分子凝集剤、カチ
オン性高分子凝集剤の各々の単独使用である比較例1、
比較例2はフロック強度、SS回収率及び脱水ケーキ含
水率の何れも本発明よりも悪く、汚泥によっては脱水が
不可能な場合があった。On the other hand, Comparative Example 1 in which each of the anionic polymer flocculant and the cationic polymer flocculant was used alone,
In Comparative Example 2, all of the floc strength, the SS recovery rate, and the water content of the dewatered cake were worse than those of the present invention, and there were cases where dewatering was impossible depending on the sludge.
【0031】また、カチオン性高分子凝集剤とアニオン
性高分子凝集剤を併用した比較例3は比較例l、比較例
2に比ベるとフロック強度、SS回収率及び脱水ケーキ
含水率の何れも良くなるが本発明よりも劣り、効率的な
脱水を行なうには十分ではなかった。Comparative Example 3 in which a cationic polymer flocculant and an anionic polymer flocculant were used in combination was compared with Comparative Example 1 and Comparative Example 2 in any of floc strength, SS recovery rate and dehydrated cake water content. However, it was inferior to that of the present invention, and was not sufficient for efficient dehydration.
【0032】本発明法は、いずれのカルシウム化合物含
有汚泥に対しても従来法よりSS回収率及び脱水ケーキ
含水率とも良好であり、効率的な脱水処理が行えた。In the method of the present invention, the SS recovery rate and the water content of the dewatered cake were better than those of the conventional method for any of the calcium compound-containing sludges, and efficient dehydration treatment was performed.
【0033】[0033]
【発明の効果】本発明の方法によれば、フッ化カルシウ
ムを主として含有する汚泥の脱水処理において、生成す
るフロックが十分な強度を有し、SS回収率の向上、脱
水ケーキの含水率の低減などが可能となる。また、フッ
化カルシウムを主として含有する汚泥の性状、成分等の
変化に対して対応しやすく、効率的な脱水処理を可能と
する。According to the method of the present invention , calcium fluoride
In the dehydration treatment of sludge mainly containing water, the generated flocs have sufficient strength, and it is possible to improve the SS recovery rate, reduce the water content of the dewatered cake, and the like. In addition, fluoride
It is easy to respond to changes in properties, components, and the like of sludge mainly containing calcium chloride, and enables efficient dehydration treatment.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭64−90098(JP,A) 特開 昭64−4207(JP,A) 特開 平2−14799(JP,A) 特開 平4−193308(JP,A) 特開 昭62−238000(JP,A) (58)調査した分野(Int.Cl.6,DB名) C02F 11/00 - 11/20 B01D 21/01 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-64-90098 (JP, A) JP-A-64-4207 (JP, A) JP-A-2-14799 (JP, A) JP-A-4- 193308 (JP, A) JP-A-62-238000 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) C02F 11/00-11/20 B01D 21/01
Claims (3)
泥に、一分子中にカチオン基およびアニオン基を有する
両性高分子凝集剤を添加して懸濁物質を凝集し、脱水す
ることを特徴とするカルシウム化合物含有汚泥の脱水方
法。1. Calcium characterized in that a suspended substance is flocculated by adding an amphoteric polymer flocculant having a cationic group and an anionic group in one molecule to sludge mainly containing calcium fluoride to dehydrate the sludge. A method for dewatering compound-containing sludge.
泥に、一分子中にカチオン基およびアニオン基を有する
両性高分子凝集剤を添加した後、さらにアニオン性高分
子凝集剤を添加して懸濁物質を凝集し、脱水することを
特徴とするカルシウム化合物含有汚泥の脱水方法。2. A sludge containing mainly calcium fluoride, to which an amphoteric polymer flocculant having a cationic group and an anionic group in one molecule is added, and further an anionic polymer flocculant is added to the sludge. A method for dewatering calcium compound-containing sludge, comprising coagulating and dewatering.
することを特徴とする請求項1または請求項2に記載の
脱水方法。 3. Dehydration using a screw press type dehydrator.
The method according to claim 1 or 2, wherein
Dehydration method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5136173A JP2991588B2 (en) | 1993-06-07 | 1993-06-07 | Method for dewatering sludge containing calcium compound |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5136173A JP2991588B2 (en) | 1993-06-07 | 1993-06-07 | Method for dewatering sludge containing calcium compound |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06343998A JPH06343998A (en) | 1994-12-20 |
JP2991588B2 true JP2991588B2 (en) | 1999-12-20 |
Family
ID=15169036
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5136173A Expired - Lifetime JP2991588B2 (en) | 1993-06-07 | 1993-06-07 | Method for dewatering sludge containing calcium compound |
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Country | Link |
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JP (1) | JP2991588B2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4661665B2 (en) * | 2006-04-06 | 2011-03-30 | 日本錬水株式会社 | Method for coagulating sedimentation of ion-containing wastewater |
CN107973503B (en) * | 2017-12-11 | 2023-03-28 | 浙江大学 | Integrated granular sludge sulfurization decalcification device and method |
CN107879578B (en) * | 2017-12-27 | 2023-03-28 | 浙江大学 | Granular sludge in-situ flotation calcium removal reactor and method thereof |
JP7103608B2 (en) * | 2020-08-27 | 2022-07-20 | テクニカ合同株式会社 | Manufacturing method of recycled material using unused ready-mixed concrete |
FR3137303A1 (en) * | 2022-07-04 | 2024-01-05 | Ocp Sa | Method and system for separating a solid and at least one liquid from a suspension |
-
1993
- 1993-06-07 JP JP5136173A patent/JP2991588B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
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JPH06343998A (en) | 1994-12-20 |
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