JPH11192402A - Inorganic flocculant - Google Patents

Inorganic flocculant

Info

Publication number
JPH11192402A
JPH11192402A JP10012139A JP1213998A JPH11192402A JP H11192402 A JPH11192402 A JP H11192402A JP 10012139 A JP10012139 A JP 10012139A JP 1213998 A JP1213998 A JP 1213998A JP H11192402 A JPH11192402 A JP H11192402A
Authority
JP
Japan
Prior art keywords
aggregate
inorganic
component
sludge
cement
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.)
Pending
Application number
JP10012139A
Other languages
Japanese (ja)
Inventor
Motoyasu Nakanishi
幹育 中西
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.)
Suzuki Sogyo Co Ltd
Original Assignee
Suzuki Sogyo 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 Suzuki Sogyo Co Ltd filed Critical Suzuki Sogyo Co Ltd
Priority to JP10012139A priority Critical patent/JPH11192402A/en
Publication of JPH11192402A publication Critical patent/JPH11192402A/en
Pending legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To obtain an inorganic flucculant enabling to simply neutralize water for dehydration treatment of sludge and waste water treatment to form sufficient flocks and also control a precipitation degree, and perform stable coagulation and solid separation from liquid, especially in the dehydration treatment of submarine sludge. SOLUTION: This inorganic flocculant consists of an inorganic flocculation component and aggregate, and cement is used as the aggregate, and the inorganic flocculation component is incorporated by 2-10 pts.wt. for 10 pts.wt. aggregate and is powdery. Thus, water quality is adjusted from around the inorganic flocculation component and the flocks are formed without degrading coagulation power, and a stabilized coagulation power can be exhibited and also solid can be promptly separated from liquid.

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】本発明は、海水や河川水、湖
沼水、下水、し尿、各種事業所の汚水処理用の凝集剤
や、またこれらより生じた汚泥の脱水処理用の凝集剤に
関するものであり、特に、海中汚泥の脱水処理において
も、安定した凝集力で固液分離できる無機凝集剤に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coagulant for treating seawater, river water, lake water, sewage, human waste, and wastewater from various business establishments, and a coagulant for dewatering sludge produced therefrom. In particular, the present invention relates to an inorganic coagulant capable of performing solid-liquid separation with stable cohesion even in dewatering of marine sludge.

【0002】[0002]

【発明の背景】従来、環境保全の一環として、海や河
川、湖沼の底に堆積した汚泥の回収がおこなわれてい
る。汚泥の回収は、ショベル式やサンドポンプ式の浚渫
装置による浚渫方法を用いるのが一般的であり、浚渫船
などで水底から汚泥を効率よく回収している。これをシ
ックナーなどで濃縮し、それを自然脱水や真空脱水、加
圧脱水、遠心脱水などで脱水処理されるのであるが、こ
の際分離した水には、微細で沈殿しにくい泥粒や不純物
などの浮遊物質(いわゆる、SS成分)が含まれている
ため、これを除去するために、凝集剤を添加して、浮遊
物質を凝集・沈降させて固液分離させている。
BACKGROUND OF THE INVENTION Conventionally, as part of environmental protection, sludge deposited on the bottom of the sea, rivers, lakes and marshes has been recovered. In general, sludge is collected using a dredging method using a shovel-type or sand-pump-type dredging device, and sludge is efficiently collected from the water bottom using a dredger or the like. This is concentrated with a thickener and dewatered by natural dehydration, vacuum dehydration, pressure dehydration, centrifugal dehydration, etc. At this time, the separated water contains fine and hard-to-precipitate mud particles and impurities. Since a suspended substance (so-called SS component) is contained, a coagulant is added to remove the suspended substance, and the suspended substance is coagulated and settled to be solid-liquid separated.

【0003】ところで、汚泥には、各家庭や事業所から
排出される様々な不純物が沈降堆積したものが含まれ、
また、汚水中には、沈降しにくい微細な泥粒や不純物な
どの浮遊物質が含まれる。これらは、腐敗したりして水
質を酸性にすることが多い。さらに、汚水中には様々な
物質がイオン状態で存在し、特に、海水においては、海
水中の成分としてナトリウムや塩素やカルシウムなどの
イオンやその他ミネラル分が多く含まれる。
[0003] By the way, the sludge includes those in which various impurities discharged from each home or business are settled and deposited.
In addition, sewage contains suspended solids such as fine mud particles and impurities that are unlikely to settle. These often rot and make the water quality acidic. Furthermore, various substances exist in an ionic state in sewage, and particularly in seawater, a large amount of ions such as sodium, chlorine and calcium and other minerals are contained as components in seawater.

【0004】このため、汚泥、特に海中汚泥の脱水処理
においては、分離した水から浮遊物質を除去しようとし
ても、これらの水質やイオンなどにより、凝集剤の凝集
力が阻害され、フロックがなかなか生成されなかった
り、生成してもひどく脆くて崩れやすかったり、なかな
か沈降し難かったりして、固液分離し難いものであり、
さらに、海水においては真水に比べ浮力が強く働くの
で、フロックの沈降を妨げる傾向がある。
[0004] Therefore, in the dewatering treatment of sludge, especially marine sludge, even if an attempt is made to remove suspended solids from the separated water, the flocculence of the flocculant is impeded by these water qualities and ions, and floc is not easily formed. It is difficult to settle, and it is difficult to settle, and it is difficult to settle.
Furthermore, seawater has a stronger buoyancy than fresh water, and thus tends to hinder floc sedimentation.

【0005】そこで、従来、汚泥の脱水処理や汚水処理
において、例えば、予め石灰を投入するなどの前処理を
おこなって水を中和して凝集し易くしているのである
が、その処理ではフロックの沈降具合までも積極的にコ
ントロールして固液分離できるものではなく、また、面
倒且つ大がかりな装置を必要とするものであった。この
ため、もっと簡便に水を中和して、十分なフロックを形
成できるとともに、沈降具合をコントロールでき、特
に、海中汚泥の脱水処理においても、安定した凝集と固
液分離することのできる凝集剤の登場が強く望まれてい
る。
Therefore, conventionally, in the sludge dewatering treatment and the sewage treatment, for example, a pretreatment such as lime is previously performed to neutralize the water to make it easy to coagulate. However, solid-liquid separation cannot be carried out by positively controlling the degree of sedimentation, and a cumbersome and large-scale apparatus is required. For this reason, the flocculant can neutralize water more easily, form a sufficient floc, control the degree of sedimentation, and can perform stable coagulation and solid-liquid separation, especially in the dewatering of marine sludge. Is strongly desired.

【0006】[0006]

【解決を試みた技術的事項】本出願人は、このような状
況に鑑み、凝集成分や骨材を選定しその配合や形態を研
究し、最適な配合を見いだし、海水を大量に含む汚泥に
対しても安定した凝集力を示し固液分離することのでき
る無機凝集剤を提供するものである。
[Technical matters to be solved] In view of such a situation, the present applicant has selected an agglomerated component and aggregate, studied the composition and form thereof, found an optimal composition, and found an optimum composition for sludge containing a large amount of seawater. It is another object of the present invention to provide an inorganic flocculant which exhibits a stable flocculation force and can perform solid-liquid separation.

【0007】[0007]

【課題を解決するための手段】すなわち、本願に係わる
第1の発明たる無機凝集剤は、無機質凝集成分と骨材と
から成り、骨材にはセメントを用い、無機凝集成分は骨
材10重量部に対して2〜10重量部有し粉末状とした
ことを特徴とするものである。そして、このような発明
特定事項を手段とすることによって、海中汚泥の脱水処
理や排水処理に対しても、無機質凝集成分の周りから水
質を調整して、凝集力を低下させることなくフロックを
形成し、安定した凝集力を発揮できるとともに、速やか
に固液分離できようになる。
That is, the inorganic coagulant according to the first invention of the present application comprises an inorganic coagulation component and an aggregate, cement is used as the aggregate, and the inorganic coagulation component is 10 wt. And 2 to 10 parts by weight per part, and is in the form of a powder. And, by using such specific features of the invention as a means, even for dewatering and drainage of marine sludge, water quality is adjusted from around the inorganic coagulation component to form flocs without reducing cohesion. In addition, stable cohesion can be exhibited, and solid-liquid separation can be quickly performed.

【0008】また、本願に係わる第2の発明たる無機凝
集剤は、前記無機質凝集成分は酸化アルミニウムと炭酸
ナトリウムの何れか一方又は双方であって、前記骨材は
骨材主成分をセメントとし骨材補助成分としてシリカ、
硫酸バンド、無水石膏のうち何れか1つ乃至全部を有す
ることを特徴とするものである。そして、このような発
明特定事項を手段とすることによって、凝集力を高めフ
ロックを形成しやすくできると共に、沈降しやすくな
り、より安定した凝集力を示し固液分離できるようにな
る。
[0008] In the inorganic coagulant according to a second aspect of the present invention, the inorganic coagulant is one or both of aluminum oxide and sodium carbonate. Silica as a material auxiliary component,
It is characterized by having one or all of a sulfate band and an anhydrous gypsum. By using such specific features of the invention as a means, the cohesive force can be increased and flocs can be easily formed, and sedimentation can be easily performed, so that solid-liquid separation can be achieved with more stable cohesive force.

【0009】[0009]

【発明の実施の形態】以下、本発明の無機凝集剤につい
て具体的に説明する。本発明の無機凝集剤は、無機質凝
集成分として、例えば、酸化アルミニウムや炭酸ナトリ
ウムなど無機系の凝集剤を用いることができる。この無
機質凝集成分は無機質であり化学的に安定であるため、
海水中の成分によっても物性変化を起こすことなく、浮
遊物質を凝集させることができる。
BEST MODE FOR CARRYING OUT THE INVENTION The inorganic coagulant of the present invention will be specifically described below. The inorganic flocculant of the present invention can use, for example, an inorganic flocculant such as aluminum oxide or sodium carbonate as the inorganic flocculant. Since this inorganic coagulation component is inorganic and chemically stable,
Suspended substances can be agglomerated without changing physical properties even by components in seawater.

【0010】そして、本願の無機凝集剤は、上記無機質
凝集成分とあわせて骨材たるセメントとを有するもので
ある。このようにすることにより、骨材たるセメントは
その成分中に石灰などを含むものであるから、従来の汚
泥の脱水処理や汚水処理に必要とされる前処理工程と同
様に水を中和することができるのであるが、無機質凝集
剤の周辺に存在するセメント付近の水から中和しはじめ
るため、無機質凝集成分は常に安定した凝集力を発揮す
ることができる。さらに、この骨材たるセメントは、い
わゆる無機質の接着機能を有する粉末なので、水分を含
むと無機質凝集成分やフロックとくっつくようになる。
そして、水分を含んだセメントは水よりも重くなるた
め、特に海水であっても比重の影響を受け難く沈降し
て、次第に汚泥の表面に堆積する。このため、固液分離
したフロックを回収する際に多少波立っても、堆積した
セメントが汚泥やフロックの舞い上がりを抑制する機能
を有するのである。なお、セメントは汚泥中に残留する
が、無毒なので安全に使用できる。
The inorganic coagulant of the present invention has cement as an aggregate in addition to the inorganic coagulant. By doing so, cement as an aggregate contains lime and the like in its components, so that water can be neutralized in the same manner as in the conventional pretreatment step required for sludge dewatering and sewage treatment. Although it is possible, neutralization starts from the water near the cement existing around the inorganic coagulant, so that the inorganic coagulation component can always exhibit a stable cohesion. Furthermore, since the cement as the aggregate is a powder having a so-called inorganic adhesive function, if it contains moisture, it will stick to the inorganic coagulation component and floc.
And, since the cement containing water is heavier than water, even if it is seawater in particular, it is settled down without being affected by the specific gravity, and gradually accumulates on the surface of the sludge. For this reason, even if the floc that has been separated into solids and liquids is slightly wavy, the deposited cement has a function of suppressing the sludge and the flocks from rising. The cement remains in the sludge, but is non-toxic and can be used safely.

【0011】さらにまた、骨材には、骨材補助成分とし
てシリカ、硫酸バンド、無水石膏のうち何れか1種乃至
全種を有することができる。これらは、セメントの吸水
性や接着性、沈降具合などのセメントの機能を高めると
ともに、水中の浮遊物質の電荷を中和して無機質凝集成
分の凝集力を高めることができる。ちなみに、ここでい
う骨材補助成分とは、セメント成分中に含まれるシリカ
や石膏などを示すのでなく、セメントの成分とは別にさ
らに配合させるものである。なお、無水石膏は、天然の
石膏でなく硫酸カルシウムを用いてもよい。
Further, the aggregate may have any one or all of silica, a sulfate band, and anhydrous gypsum as an aggregate auxiliary component. These can enhance the function of the cement such as the water absorption, adhesiveness, and sedimentation of the cement, and can also neutralize the charge of the suspended substances in water to increase the cohesion of the inorganic coagulation component. Incidentally, the aggregate auxiliary component mentioned here does not indicate silica, gypsum or the like contained in the cement component, but is further compounded separately from the cement component. The anhydrous gypsum may use calcium sulfate instead of natural gypsum.

【0012】これら無機質凝集成分と骨材から成る粉末
を形成するにあたっては、例えば、公知のセメントの製
造工程を用いて形成することができる。このセメントの
製造において、例えば、乾式法によるセメントの製造装
置を用いる場合には、消石灰やケイ石を粉砕しふるいに
かけた後回転窯で焼成する際に、無機質凝集成分や骨材
補助成分を添加すれば、製造されたセメントの粉末中
に、無機質凝集成分や骨材補助成分を有することができ
る。なお、この製造方法は一例であって、その他の方法
で本発明の無機凝集剤を形成してもよく、要は、無機質
凝集成分と骨材とが配合された粉末を形成できればよ
い。このようにして、無機質凝集成分と骨材とが適当量
配合した無機凝集剤を得ることができる。
In forming the powder comprising the inorganic aggregate component and the aggregate, the powder can be formed, for example, by using a known cement manufacturing process. In the production of this cement, for example, when using a cement production device by a dry method, when crushed slaked lime or silica stone is sieved and then fired in a rotary kiln, an inorganic aggregate component and an aggregate auxiliary component are added. In this case, the produced cement powder can have an inorganic coagulation component and an aggregate auxiliary component. Note that this production method is an example, and the inorganic coagulant of the present invention may be formed by another method. In short, it is only necessary to form a powder in which the inorganic coagulation component and the aggregate are mixed. Thus, an inorganic flocculant in which the inorganic flocculant and the aggregate are mixed in an appropriate amount can be obtained.

【0013】そして、上記適当量とは、無機質凝集成分
は骨材10重量部に対して2〜10重量部配合するもの
である。この分量であれば、無機質凝集成分が凝集力を
低下させることなく、常に安定した凝集力を発揮できる
とともに、速やかに固液分離できようになる。ちなみ
に、無機質凝集成分に対して骨材の分量が多すぎたり少
なすぎると、固液分離し難くなってしまう。例えば、無
機質凝集成分が骨材10重量部に対して10重量部を越
えたものであると、骨材が少なすぎるため水質を中和す
る働きが弱くなり、無機質凝集成分の凝集力が低下する
と共に沈降し難くなったりし、汚泥表面に沈殿する骨材
たるセメントの量が不足して汚泥やフロックが舞い上が
りやすくなってしまう。また、無機質凝集成分が骨材1
0重量部に対して2重量部に満たないものであると、無
機質凝集成分に対して骨材が多すぎて、水質が極端にア
ルカリ性になり凝集力を低下させてしまう。何れにし
ろ、無機質凝集成分と骨材との分量が適当でないと、凝
集するのに支障をきたすのである。
The above-mentioned appropriate amount means that the inorganic coagulation component is blended in an amount of 2 to 10 parts by weight with respect to 10 parts by weight of the aggregate. With this amount, the inorganic aggregating component can always exhibit a stable aggregating force without lowering the aggregating force, and can quickly perform solid-liquid separation. Incidentally, if the amount of the aggregate is too large or too small with respect to the inorganic aggregate component, solid-liquid separation becomes difficult. For example, when the amount of the inorganic aggregate component exceeds 10 parts by weight with respect to 10 parts by weight of the aggregate, the amount of the aggregate is too small, the function of neutralizing the water quality is weakened, and the aggregating power of the inorganic aggregate component is reduced. At the same time, it becomes difficult to settle down, and the amount of cement as aggregate that precipitates on the sludge surface is insufficient, so that sludge and flocs tend to rise. In addition, the aggregated inorganic component is aggregate 1
If the amount is less than 2 parts by weight with respect to 0 parts by weight, the amount of aggregate is too large with respect to the inorganic agglomerated component, whereby the water quality becomes extremely alkaline and the cohesive strength is reduced. In any case, if the amount of the inorganic coagulation component and the aggregate is not appropriate, coagulation is hindered.

【0014】また、骨材補助成分の分量は、汚水中に含
まれるイオン状態により適宜調整すればよいが、通常、
骨材補助成分の分量としては、骨材10重量部に対し3
〜30重量部配合させるとよい。この分量の骨材補助成
分を配合することにより、無機質凝集成分や骨材の機能
をコントロールでき、汚泥や排水の処理に対し、より安
定した凝集力と沈降しやすさを示し固液分離することが
できる。ちなみに、ここでいう骨材補助成分とは、セメ
ントの成分中に含まれるシリカや石膏等を示すのでな
く、セメントの成分とは別にさらに配合させるものであ
る。なお、無水石膏は、天然の石膏でなく硫酸カルシウ
ムを用いてもよいこと勿論である。
The amount of the aggregate auxiliary component may be appropriately adjusted according to the ionic state contained in the wastewater.
The amount of the aggregate auxiliary component was 3 parts per 10 parts by weight of the aggregate.
It is advisable to mix up to 30 parts by weight. By blending this amount of aggregate auxiliary component, it is possible to control the function of inorganic coagulation component and aggregate, and to show more stable coagulation force and ease of sedimentation for sludge and wastewater treatment, and to perform solid-liquid separation. Can be. Incidentally, the aggregate auxiliary component here does not indicate silica, gypsum or the like contained in the cement component, but is further compounded separately from the cement component. In addition, it is a matter of course that calcium sulfate may be used as the anhydrous gypsum instead of natural gypsum.

【0015】このような無機質凝集成分や骨材を用い粉
末状とした本発明の無機凝集剤の一例として、表1に示
す割合で配合した無機凝集剤を示す。
As an example of the inorganic coagulant of the present invention which is made into a powder using such an inorganic coagulant or an aggregate, an inorganic coagulant mixed in the ratio shown in Table 1 is shown.

【0016】[0016]

【表1】 −−−−−−−−−−−−−−−−−−−−−−−−−− 無機質凝集成分:酸化アルミニウム :20重量部 :炭酸ナトリウム : :(それぞれ同量づつ配合): −−−−−−−−−−−−−−−−−−−−−−−−−− 骨材主成分 :セメント :40重量部 −−−−−−−−−−−−−−−−−−−−−−−−−− 骨材補助成分 :シリカ :40重量部 :硫酸バンド : :無水石膏 : :(それぞれ同量づつ配合): −−−−−−−−−−−−−−−−−−−−−−−−−−[Table 1]------------------------------------------------------------------------------------------------------------ Blend):---------------------------------------------------------------------------------------------------------- −−−−−−−−−−−−−−− Aggregate auxiliary component: Silica: 40 parts by weight: Sulfuric acid band:: Anhydrite:: (Blended in the same amount):----------- −−−−−−−−−−−−−−−−−−−−−

【0017】[0017]

【実施例】以下、実施例により、本発明の無機凝集剤を
用いて海中汚泥を凝集して固液分離した例を示す。な
お、本実施例では、表1に示す割合で配合した無機凝集
剤を用いた。
EXAMPLES Hereinafter, examples will be described in which marine sludge is coagulated and solid-liquid separated using the inorganic coagulant of the present invention. In this example, an inorganic coagulant mixed in the ratio shown in Table 1 was used.

【0018】浚渫した海中汚泥を採取し、海中汚泥と海
水の混ざり具合を調整して、SS濃度の異なる4種類の
水溶液を作成した。この4種類の水溶液のSS濃度は、
それぞれ、6844mg/l,14863mg/l,3
3522mg/l,55135mg/lであった。そし
て、これら水溶液をそれぞれビーカーに200ml取
り、本発明の無機凝集剤を規定量添加した後、120r
pmで5分間攪拌した。ここで、無機凝集剤の規定量
は、水溶液1リットル当たり250mg,500mg,
1000mg,2000mgとした。この水溶液をメス
シリンダーに100ml分取し、無機凝集剤を添加しな
い原液の水溶液や、無機凝集剤をそれぞれ規定量添加し
た水溶液の固液分離状態を観察した。そして、上澄み液
の透明具合と沈降したフロックの堆積量を確認し、上澄
み液がほぼ透明になってフロックの堆積量がほぼ増加し
なくなるまでの時間を観察し、その時間によりA〜Eま
でレベル分けしたところ、水溶液の固液分離状態は表2
のとおりとなった。
The dredged sea sludge was collected, and the mixing condition of the sea sludge and seawater was adjusted to prepare four types of aqueous solutions having different SS concentrations. The SS concentration of these four aqueous solutions is
6844 mg / l, 14863 mg / l, 3 respectively
3522 mg / l and 55135 mg / l. Then, 200 ml of each of these aqueous solutions was placed in a beaker, and after adding a prescribed amount of the inorganic flocculant of the present invention,
Stirred at pm for 5 minutes. Here, the prescribed amount of the inorganic coagulant is 250 mg, 500 mg,
1000 mg and 2000 mg were used. 100 ml of this aqueous solution was dispensed into a measuring cylinder, and the solid-liquid separation state of an undiluted aqueous solution to which no inorganic coagulant was added and an aqueous solution to which a prescribed amount of each inorganic coagulant was added was observed. Then, the degree of transparency of the supernatant liquid and the amount of sedimented floc were checked, and the time until the supernatant liquid became almost transparent and the amount of floc accumulated almost did not increase was observed. Table 2 shows the solid-liquid separation state of the aqueous solution.
It was as follows.

【0019】[0019]

【表2】 −−−−−−−−−−−−−−−−−−−−−−−−−−−−−− SS濃度 : 原液 : 無機凝集剤 添加量(mg/l) (ppm): : 250: 500:1000:2000 −−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 6844: E : B : A : A : A −−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 14863: X : D : C : B : A −−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 33522: X : D : D : C : B −−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 55153: X : E : D : D : C −−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 固液分離状態 A=2分以内で分離した B=4分以内で分離した C=6分以内で分離した D=6分では濁りがやや残る E=6分ではかなり濁りが残る X=ほとんど固液分離せずTable 2----------------------------------------------------------------------------------------------------------------- ppm):: 250: 500: 1000: 2000 ----------------------------------------------------------- 6844: E: B: A: A : A −−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 14863: X: D: C: B: A −−−−−−−− ----------------------------------------------------------- 33522: X: D: D: C: B ---------------- −−−−−−−−−−−−−−− 55153: X: E: D: D: C −−−−−−−−−−−−−−−−−−−−−−−−−−−−− −−−−− Solid-liquid separation state A = separated within 2 minutes B = within 4 minutes Without significant turbidity remains X = Most solid-liquid separation in E = 6 min turbidity slightly remains at D = 6 min separated by C = within 6 minutes of release

【0020】実施例では、本発明の無機凝集剤を海中汚
泥に添加したところ、速やかにフロックを形成して沈降
した。SS濃度や無機凝集剤の添加量によっては沈降具
合やフロックの大きさは異なったものの、無機凝集剤を
添加した水溶液は、数分のうちにほぼ完全に固液分離し
た。一方、原液の水溶液では、ほとんど固液分離しなか
った。なお、これら固液分離させた水溶液からフロック
を回収するにあたり、メスシリンダーから濾紙(ADV
ANTEC社製 No.101)をフィルターとして吸
引濾過したところ、無機凝集剤を添加した水溶液は、フ
ロックは型崩れせず容易に回収でき、濾液はほぼ透明で
あった。一方、原液の水溶液は、浮遊物質がほとんど回
収できずに濾紙を通過してしまい、濾液はかなり濁って
しまった。なお、河川や湖沼の汚泥については、海中汚
泥と比べ、海水中の成分が含まれない分さらに固液分離
し易いため、試験を略した。
In the examples, when the inorganic flocculant of the present invention was added to marine sludge, floc was quickly formed and settled. Although the degree of sedimentation and the size of floc differed depending on the SS concentration and the amount of the added inorganic coagulant, the aqueous solution to which the inorganic coagulant was added was almost completely solid-liquid separated within a few minutes. On the other hand, the aqueous solution of the stock solution hardly separated into solid and liquid. In recovering floc from the solid-liquid separated aqueous solution, filter paper (ADV) was collected from a measuring cylinder.
No. manufactured by ANTEC When suction filtration was performed using 101) as a filter, the aqueous solution to which the inorganic flocculant had been added could easily recover flocs without collapse, and the filtrate was almost transparent. On the other hand, the aqueous solution of the stock solution passed through the filter paper with almost no suspended solids recovered, and the filtrate became considerably turbid. The test was omitted for sludge of rivers and lakes, as compared to marine sludge, because the components in seawater were not included and solid-liquid separation was easier.

【0021】[0021]

【発明の効果】以上述べたとおり、本願発明の無機凝集
剤は、無機質凝集成分と骨材とから成り、骨材にはセメ
ントを用い、無機凝集成分は骨材10重量部に対して2
〜10重量部有し粉末状としたことによって、海中汚泥
の脱水処理や排水処理に対し、無機質凝集成分の周りか
ら水質を調整して、凝集力を低下させることなくフロッ
クを形成し、安定した凝集力を発揮できるとともに、速
やかに固液分離することができる。また、前記無機質凝
集成分には酸化アルミニウムと炭酸ナトリウムの何れか
一方又は双方を用いて、前記骨材には骨材主成分をセメ
ントとして骨材補助成分にはシリカ、硫酸バンド、無水
石膏のうち何れか1つ乃至全部を有することによって、
フロックの形成や沈降具合などをコントロールして、よ
り安定した凝集力を示し固液分離することができる。
As described above, the inorganic flocculant of the present invention comprises an inorganic flocculant and an aggregate, cement is used as the aggregate, and the inorganic flocculant is added to 10 parts by weight of the aggregate.
10 to 10 parts by weight and in powder form, for dewatering and drainage of marine sludge, adjust the water quality from around the inorganic coagulation component, form flocs without lowering the cohesion, and stabilize As well as exerting cohesive force, solid-liquid separation can be performed quickly. In addition, one or both of aluminum oxide and sodium carbonate are used for the inorganic coagulation component, and the aggregate is mainly composed of cement and the aggregate auxiliary component is silica, sulfate band, and anhydrite. By having any one or all,
By controlling the formation of flocs and the degree of sedimentation, solid-liquid separation can be achieved with more stable cohesion.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 無機質凝集成分と骨材とから成り、骨材
にはセメントを用い、無機凝集成分は骨材10重量部に
対して2〜10重量部有し粉末状としたことを特徴とす
る無機凝集剤。
1. An aggregate comprising an inorganic aggregate component and an aggregate, cement is used as the aggregate, and the inorganic aggregate component is 2 to 10 parts by weight with respect to 10 parts by weight of the aggregate, and is in powder form. Inorganic flocculant.
【請求項2】 前記無機質凝集成分は酸化アルミニウム
と炭酸ナトリウムの何れか一方又は双方であって、前記
骨材は骨材主成分をセメントとし骨材補助成分としてシ
リカ、硫酸バンド、無水石膏のうち何れか1つ乃至全部
を有することを特徴とする請求項1記載の無機凝集剤。
2. The inorganic coagulation component is one or both of aluminum oxide and sodium carbonate, and the aggregate is a cement containing a main component of the aggregate and silica, a sulfate band, and an anhydrous gypsum as an auxiliary component of the aggregate. The inorganic coagulant according to claim 1, wherein the inorganic coagulant has any one or all of them.
JP10012139A 1998-01-05 1998-01-05 Inorganic flocculant Pending JPH11192402A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10012139A JPH11192402A (en) 1998-01-05 1998-01-05 Inorganic flocculant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10012139A JPH11192402A (en) 1998-01-05 1998-01-05 Inorganic flocculant

Publications (1)

Publication Number Publication Date
JPH11192402A true JPH11192402A (en) 1999-07-21

Family

ID=11797190

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10012139A Pending JPH11192402A (en) 1998-01-05 1998-01-05 Inorganic flocculant

Country Status (1)

Country Link
JP (1) JPH11192402A (en)

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