JPS6265799A - Flocculating, adsorbing, dehydrating and solidifying agent for sludge in waste water - Google Patents

Flocculating, adsorbing, dehydrating and solidifying agent for sludge in waste water

Info

Publication number
JPS6265799A
JPS6265799A JP60204334A JP20433485A JPS6265799A JP S6265799 A JPS6265799 A JP S6265799A JP 60204334 A JP60204334 A JP 60204334A JP 20433485 A JP20433485 A JP 20433485A JP S6265799 A JPS6265799 A JP S6265799A
Authority
JP
Japan
Prior art keywords
sludge
water
adjusted
composition
waste water
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
JP60204334A
Other languages
Japanese (ja)
Inventor
Yasuyuki Morita
泰之 森田
Hidetoshi Ogawa
英俊 小川
Keisuke Kumazawa
熊澤 敬介
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.)
Kihara Sangyo KK
TOKYO GIKEN KOGYO KK
Original Assignee
Kihara Sangyo KK
TOKYO GIKEN KOGYO KK
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 Kihara Sangyo KK, TOKYO GIKEN KOGYO KK filed Critical Kihara Sangyo KK
Priority to JP60204334A priority Critical patent/JPS6265799A/en
Publication of JPS6265799A publication Critical patent/JPS6265799A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/10Production of cement, e.g. improving or optimising the production methods; Cement grinding

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  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To easily flocculate sludge, etc. contg. harmful materials and to make the same settlable by adding a compsn. compounded with granulated blast furnace slag, II type anhydrous gypsum, zeolite powder, Portland cement and sintered and crushed matter to high water-content waste water. CONSTITUTION:The granulated blast furnace slag adjusted to 2000-4000cm<2>/g Blaine value, II type anhydrous gypsum adjusted to 3000-5000cm<2>/g Blaine value, zeolite powder, Portland cement essentially consisting of 3CaO.SiO2 (alite phase) and 2CaO.SiO2 (belite phase) and sintered and crushed matter (hauynite) essentially consisting of 4CaO.3Al2O3(SO)4 adjusted to 3000-4000cm<2>/g Blaine value are respectively compounded. A small amt. of such compsn. is added to the high water-content waste water, by which the sludge of a high viscosity contg. ultrafine particles, high org. components and harmful heavy metals, etc. is flocculated, adsorbed and settled easily from the water and the dehydration efficiency is improved.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、下水道処理及び各種産業廃水処理等により発
生した水底にift積する有害物質を含んだ汚泥やスラ
ッジを処理するための廃水中のスラッジの擬東・吸着・
脱水・固化剤に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is directed to the treatment of sludge in wastewater, which is used to treat sludge and sludge containing harmful substances that accumulate on the bottom of water generated by sewage treatment, various industrial wastewater treatment, etc. Pseudo East・Adsorption・
This relates to dehydration and solidification agents.

従来の技術 近年、経済成長による人口の都市集中化に伴い下水のり
1出吊が増大し・、河川、湖、m等の汚染を防止ザるた
めに下水道整備が急務となっている。
BACKGROUND OF THE INVENTION In recent years, with the concentration of population in cities due to economic growth, the amount of sewage discharged has increased, and there is an urgent need to develop sewage systems to prevent pollution of rivers, lakes, etc.

また工場の地方移転に伴って各地に水質汚染が急速に広
まり、これらの下水道処理及び各種産業廃水処B2等に
より発生した汚泥やスラッジ等は、増大の一途をたどっ
ている。これらの処理に関してはこれまでに多種の処理
剤が開発されているが、ニーズを十分に満足りるものは
未だになく、処理方法に関しても処理剤の開発が未解決
のために、現状では多くの問題点を残したままで処理が
行なわれている。
Furthermore, with the relocation of factories to regional areas, water pollution is rapidly spreading throughout the country, and the amount of sludge and sludge generated from these sewage treatment systems and various industrial wastewater treatment plants, B2, etc., continues to increase. Although many types of processing agents have been developed for these treatments, there are still none that fully satisfy the needs, and there are currently many problems regarding processing methods because the development of processing agents has not been resolved. Processing continues with the points remaining.

さらに、処理設備には大型で複雑化したものが必要とな
るので、多額な処理費用を要し、廃水を水と有機物ある
いは無機物に確実に分前することは非常に国難である。
In addition, large and complex treatment equipment is required, resulting in high treatment costs, and ensuring that wastewater is divided into water and organic or inorganic substances is a national problem.

また廃水は大量の汚水として排出されて水と共に処理が
行なわれるケースが殆lυどであるために、河川に放流
されて長い年月の間に湖沼の底あるいは沿海の海底等に
汚泥やスラッジが堆積して、その結果、水質汚染あるい
は周辺環境汚染を引き起こす原因となっていた。
In addition, in most cases wastewater is discharged as large amounts of sewage and treated together with the water, so sludge and sludge accumulate on the bottoms of lakes and marshes or on the seabeds along the coasts over many years after being discharged into rivers. As a result, they were a cause of water pollution and surrounding environment pollution.

汚泥d3」:びスラッジの処理方法の一例としては、廃
水中に苛性ソーダ又は消石灰を添加し、さらに@電荷を
もつアニオン系又は正電荷をもつカチオン系高分子凝集
剤のみを添加することにより、凝集沈澱物のフロックを
作った復に、各種の説水領1或に通して処理を行なうの
みのバッチ方式に近い処理方法が知られているが、苛性
ソーダ又は消石灰の添加とアニオン系又はカチオン系高
分子凝集剤の添加のみでは粘性の高いコロイド状の汚泥
及びスラッジが生成されるため、非常に処理の効率が悪
かった。
An example of a method for treating sludge is to add caustic soda or slaked lime to wastewater, and then add only an anionic polymer flocculant with an @ charge or a cationic polymer flocculant with a positive charge. A treatment method similar to a batch method is known, in which the precipitate is floc-formed and then treated through various water purification systems. Addition of a molecular flocculant alone produces highly viscous colloidal sludge and sludge, resulting in very poor treatment efficiency.

発明が解決しまうと覆る問題点 本発明は上記問題点を解決し、組成物を高含水廃水中に
少量添加ザることにより、超微粒子、窩有磯分及び右害
虫金属等を含む高粘性の汚泥及びスラッジを水より容易
に凝集・吸?1して沈澱することが可能で、しかも、脱
水効率を大幅に向上することが可能な廃水中のスラッジ
の凝集・吸着。
Problems that would be solved if the invention were solved The present invention solves the above problems, and by adding a small amount of the composition to high water content wastewater, a highly viscous material containing ultrafine particles, porous particles, pest metals, etc. Does it coagulate and absorb sludge and sludge more easily than water? 1) Coagulation and adsorption of sludge in wastewater that can be precipitated and greatly improve dewatering efficiency.

脱水・固化剤を提供することを目的とするものである。The purpose is to provide a dehydrating and solidifying agent.

プレーン値を2000〜4000cm2/rJに調整し
た高炉水滓粉砕物100〜300部と、プレーン値を3
000〜5000cm2/gに調整した■型無水石膏粉
末50〜200部と、ゼオライト粉末10〜100部と
、3CaO−8t○2(アリット相)と2CaO−8t
○2 (ベリット相)を主成分としたポルトランドセメ
ント500〜800部と、プレーン値を3000〜40
00cm’/gに調整した4CaO・3Au203  
(SO)4を主成分とした焼結粉砕物(アーウィン)5
0〜100部とをそれぞれ配合したスラッジの凝集、吸
着・脱水・固化剤を廃水中に少量添加すると、次のよう
な特i毀が得られた。
100 to 300 parts of ground blast furnace water slag with a plain value adjusted to 2000 to 4000 cm2/rJ and a plain value of 3
50 to 200 parts of ■-type anhydrite powder adjusted to 000 to 5000 cm2/g, 10 to 100 parts of zeolite powder, 3CaO-8t○2 (allite phase) and 2CaO-8t
○2 500 to 800 parts of Portland cement mainly composed of (berit phase) and a plain value of 3000 to 40 parts.
4CaO・3Au203 adjusted to 00cm'/g
Sintered pulverized product containing (SO)4 as the main component (Irwin) 5
When a small amount of a sludge flocculation, adsorption, dehydration, and solidification agent containing 0 to 100 parts of each was added to wastewater, the following special effects were obtained.

(1)フロックの沈降性が早く行なわれ、水に対する沈
澱性が非常に強い。
(1) The flocs settle quickly and have very strong settling properties in water.

(2)汚泥の凝集性が強く、特に酸性廃水に対しては活
性化したO l−I Wどなってアルカリ性を呈し、中
和作用を生じると共に重金属イオンを捕捉して極めて優
れた凝集性を示し、従来の廃水の中和処理に使用するN
a01−1の添加量を面約することができ、N−へキサ
ンも大幅に吸着づることができる。
(2) Sludge has a strong flocculating property, and especially for acidic wastewater, activated O-I-W exhibits alkalinity, produces a neutralizing effect, and captures heavy metal ions, resulting in extremely excellent flocculating properties. and N used in conventional wastewater neutralization treatment.
The amount of a01-1 added can be reduced, and N-hexane can also be adsorbed to a large extent.

(3)汚泥等の沈澱物は粒状体のように緻密で容量が小
さく、従来の方法であるNa 01イあるいはCa  
<○Hノ2処理と比較して約1/2の容量となり、しか
も脱水性が優れているため、冊本時間を大幅に短縮する
ことができ、脱水1わの沈澱物はJみいかに固形化夛る
(3) Precipitates such as sludge are dense like granules and have a small volume, so conventional methods such as Na 01 or Ca
<○The volume is approximately 1/2 compared to H-2 treatment, and it has excellent dehydration properties, so the book time can be significantly shortened, and the precipitate after dehydration is reduced to J-Mika solid. Increasing numbers.

(l;)汚泥を70℃の低温、30分間の試験条件でI
X風乾燥を行なうと、汚泥が完全乾燥に近い状態の粒子
状の固形物となり、乾燥コストを安価にすることができ
る。
(l;) Sludge was tested at a low temperature of 70°C for 30 minutes.
When X-air drying is performed, the sludge becomes a particulate solid that is almost completely dry, and the drying cost can be reduced.

(5)組成物の主成分がFe 、Mg、Af、Ca 。(5) The main components of the composition are Fe, Mg, Af, and Ca.

S等からなり、自然の土壌と同じような鉱物組成に近い
ため、汚泥中の有機成分とこれらのミネラル成分との相
乗効果により、汚泥を脱水処理後、そのままの状態で散
布しても有機土壌栄養分どして自然に還元することがで
きる。
Since the mineral composition is close to that of natural soil, the synergistic effect between the organic components in the sludge and these mineral components makes it possible to form organic soil even if the sludge is sprayed as is after dehydration treatment. Nutrients can be returned to nature.

また、汚泥のコロイド状粒子は通常においては、負に荷
電して互いに反発し、分散しながら溶液中に堆積してい
るので、本発明の組成物を添加すると、正のイオンが供
給されて、溶液中の負荷電粒子とファン・デル・ワール
ス吸着により相互に結合すると共にカチオン系高分子凝
集剤の添加によって結合単位が架橋結合となり、粒子が
ざらに大きなフロック状を形成し、機械的な力によって
相互の大きな粒子間に介在する余剰水を簡単に排除して
脱水するため、脱水効率を大幅に向上することができる
In addition, colloidal particles of sludge are normally negatively charged and repel each other, and are deposited in a solution while being dispersed, so when the composition of the present invention is added, positive ions are supplied, Negatively charged particles in the solution are bonded to each other by van der Waals adsorption, and the bonding units become cross-linked by the addition of a cationic polymer flocculant, and the particles form a rough, large floc-like structure, which is then subjected to mechanical force. Since the excess water interposed between large particles can be easily removed and dehydrated, the dehydration efficiency can be greatly improved.

さらに、本発明の組成物の一つである急冷高炉水滓粉砕
物は多孔ガラス質の組織であるので、添加後の反応性が
大きく、ポルトランドセメントの水和によるCa  (
OH)2あるいは■型態水石・店粉末等の刺激を受けて
活性1ヒサれるため、一段と優れた凝集・固化力を発揮
でき、組成物の一つであるゼオライト粉末は高いカチオ
ン交換機能と吸着力とを有しているため、汚泥中の有償
成分を吸着すると共に脱水処理した後散布した場合、還
元土壌の透水性を損なうことがなく、土壌の肥料成分保
存力を増大させる利点を十分に生かすことができる。ま
た、組成物の一つである特殊な焼結粉砕物(アーウィン
)の反応は、4 Ca O・3A−1203(SO) 
4+5Ca  (OH)2 +3CaSO4 + 29 ト12 0 →3(3CaO−A1203・CaSO4・12H20
)+5O3 3CaO−△ρ203 ・ Ca SO4・12 ト1
20 +2CaSOs +201−120 ’−)3Ca  O−A12 03  ・ 3Ca  
SO4・となり、エトリンジヤイト中の大きな針状結晶
に汚泥に含まれた余剰水を多積に固定する力と、有刷物
によって生ずる固化障害を受けることがないという特殊
な性質を有し、水和物を析出して早期に余剰水を固定ブ
る力が多洛に生成されるために、特に超微粒子、高有機
分及び重金属等を含む高粘性の汚泥あるいはスラッジに
対して有効なものとなり、汚泥あるいはスラッジ中に含
まれる有害物質等の固化に伴ってエトリンジヤイト中の
アルミニウム原子がイオン半径の近似したTt。
Furthermore, since the pulverized rapidly cooled blast furnace water slag, which is one of the compositions of the present invention, has a porous glass structure, it has high reactivity after addition, and Ca (
The zeolite powder, which is one of the compositions, has a high cation exchange function and adsorption because it becomes active when stimulated by OH) 2 or ■ type Suiseki powder, etc. Because it has the ability to adsorb paid components in sludge and is applied after dehydration treatment, it does not impair the water permeability of the reduced soil and has the full advantage of increasing the soil's ability to preserve fertilizer components. You can make use of it. In addition, the reaction of a special sintered pulverized product (Irwin), which is one of the compositions, is 4 Ca O 3A-1203 (SO)
4+5Ca (OH)2 +3CaSO4 + 29 To12 0 →3(3CaO-A1203・CaSO4・12H20
)+5O3 3CaO-△ρ203 ・Ca SO4・12 To1
20 +2CaSOs +201-120'-)3Ca O-A12 03 ・3Ca
It becomes SO4, and has the power to fix surplus water contained in sludge in large acicular crystals in ettringite, and has the special property of not being affected by solidification problems caused by printed matter, and is hydrated. Because it has the ability to precipitate substances and quickly fix excess water, it is particularly effective against highly viscous sludge or sludge containing ultrafine particles, high organic content, and heavy metals. As the sludge or harmful substances contained in the sludge solidify, the aluminum atoms in ettringite have an ionic radius close to Tt.

Cr 、Mn原子等と容易に置換される1嬰れた重金属
固定義能を有する。そして、特殊な焼結粉砕物によりこ
れらの組成物の一つ一つが有する複数の利点が、粒度、
比率によって相乗幼果を発揮して、凝集力や吸着力を強
力なものとして、どのような簡単な脱水処理方法でも容
易に高含水あるいは高有機系スラッジを脱水処理するこ
とができ、汗化槽汚泥や生し原汚泥、食品加工工程で発
生する有償汚泥<BOD廃水)あるいは!!!装廃水等
の汚泥処理を容易に行なうことができ、それぞれの組成
物の配合比率を選定づ゛ることによって何れの汚泥及び
スラッジを容易に連続的に処理することができる。
It has the ability to fix heavy metals, easily replacing Cr, Mn, etc. atoms. The multiple advantages of each of these compositions are achieved through special sintered and ground products, such as particle size,
Depending on the ratio, synergistic young fruit is exhibited and strong cohesive force and adsorption power are used, making it possible to easily dehydrate high water content or high organic sludge using any simple dehydration treatment method. Sludge, raw sludge, paid sludge generated in food processing processes <BOD wastewater) or! ! ! Sludge treatment of waste water and the like can be easily carried out, and any sludge or sludge can be easily and continuously treated by selecting the blending ratio of each composition.

なあ、脱水処理した汚泥あるいは有害重金属を含んだス
ラッジ等を同化処理する際には、水相による吸着反応を
促進するために、アルミナ成分を多聞に含有している組
成物である水酸化アルミニウムを配合する6 問題点を解決するための手段 本発明の廃水中のスラッジの凝集・吸着・脱水・固化剤
は、プレーン値を 2000〜4000C1/[+に調
整し7た高炉水滓粉砕物と、プレーン値を3000〜5
000Cm2/g1.:調整した■型無水石膏粉末と、
ゼオライト粉末と、3Ca○・5i02 (7リツト相
)と2CaO”St○2(ベリット相)を主成分とした
ポルトランドぜメン1〜と、プレーン値を3000〜4
000 cm2/qに調整した4CaO・3Ai203
 (SO)4を主成分とした焼結粉砕物(アーウィン)
とをそれぞれ配合した組成物からなることを特徴とする
RIt成を有するbのである。
By the way, when assimilating dehydrated sludge or sludge containing harmful heavy metals, aluminum hydroxide, a composition containing a large amount of alumina, is used to promote adsorption reactions in the aqueous phase. 6 Means for Solving the Problems The agent for coagulating, adsorbing, dehydrating, and solidifying sludge in wastewater of the present invention is a pulverized blast furnace water slag whose plain value has been adjusted to 2000 to 4000C1/[+7. Plain value 3000~5
000Cm2/g1. : Adjusted ■ type anhydrite powder,
Zeolite powder, Portland Zemen 1~ whose main components are 3Ca○・5i02 (7 lit phase) and 2CaO"St○2 (berit phase), and a plain value of 3000~4
4CaO・3Ai203 adjusted to 000 cm2/q
Sintered pulverized product containing (SO)4 as the main component (Irwin)
It has an RIt composition characterized by being composed of a composition containing the following.

実施例 以下、本発明の詳細な説明する。Example The present invention will be explained in detail below.

第1表を組成物の最適配合値として、これに従って組成
物を混合し、それぞれの添加量に塁づいて汚泥水に添加
して使用し実験を行なった。
Using Table 1 as the optimum blending values of the compositions, the compositions were mixed according to the values, and experiments were conducted by adding them to sludge water based on the respective addition amounts.

(i)実験例1 第1実験例においては、浄化槽汚泥と生し原汚泥とを混
合した汚泥(水分98%、固形分2%)に硫酸第1鉄を
汚泥固形分に対して30%添加して1分間撹拌を行なっ
た後、汚泥固形分に対して本発明の組成物を30%添加
して100分間撹拌行ない、その後、カチオン系高分子
凝集剤(三洋化成製商品名ナンフロック009P)を汚
泥固形分に対し0゜1%添加して5分間撹拌を行なった
(i) Experimental example 1 In the first experimental example, ferrous sulfate was added to sludge (moisture 98%, solid content 2%) that was a mixture of septic tank sludge and raw sludge at a rate of 30% based on the sludge solid content. After stirring for 1 minute, 30% of the composition of the present invention was added to the solid content of the sludge and stirring was carried out for 100 minutes, and then a cationic polymer flocculant (trade name: Nanfloc 009P manufactured by Sanyo Chemical Co., Ltd.) was added. It was added in an amount of 0.1% based on the solid content of the sludge and stirred for 5 minutes.

その後ベルト式脱水装置で汚泥の脱水を行ない、対照方
法では上記と同様の汚泥に汚泥固形分に対してカチオン
系高分子凝集剤を0゜5%添加して3分間撹拌を行ない
、混合した後ベルト式脱水装置で汚泥の脱水を行ない、
脱水汚泥についての脱水・凝集効果、乾燥効果1重金属
の固着及び−軸圧縮強度等を試験した結果、次のような
結果をくた。
The sludge was then dehydrated using a belt-type dewatering device. In the control method, 0.5% of a cationic polymer flocculant was added to the sludge based on the solid content of the sludge, stirred for 3 minutes, and then mixed. The sludge is dehydrated using a belt-type dewatering device.
As a result of testing the dewatering/coagulation effect, drying effect, fixation of heavy metals, and -axial compressive strength of dehydrated sludge, the following results were obtained.

本発明の組成物を用いた処理と対照方法による処理とは
明確な差が顕著に現われている。
A clear difference between the treatment using the composition of the present invention and the treatment according to the control method is noticeable.

(1)脱水・凝集効果 第 2 表   脱水汚泥中の水分測定表この第2表に
示す実験結果からもわかるように、対照方法では水分が
86.1%で粘性の高いコロイド状であるのに対して、
本発明の組成物を添加すると水分が48.7%で汚泥が
ザラザラとした完全な粒状体となった。
(1) Dehydration and flocculation effect Table 2 Table for measuring moisture in dehydrated sludge As can be seen from the experimental results shown in Table 2, in the control method, the moisture content was 86.1%, which was in the form of a highly viscous colloid. for,
When the composition of the present invention was added, the water content was 48.7%, and the sludge became coarse and complete granules.

(2)乾燥効果 ベルト式脱水装置により脱水した脱水汚泥をそれぞれ電
気乾燥器を使用して70”C±10℃の低温で送風乾燥
を行なった、汚泥中の乾燥水分を測定して比較すると、
第3表に示すような実験結果となった。
(2) Drying effect Dehydrated sludge dehydrated using a belt-type dewatering device was air-dried using an electric dryer at a low temperature of 70"C ± 10°C. The dry moisture in the sludge was measured and compared.
The experimental results were as shown in Table 3.

第 3 表   脱水汚泥中の乾燥水分測定式この結果
からもわかるように、対照方法による脱水汚泥の乾燥水
分は84.6%で脱水率か1.7%と悪く、電気送風機
にJ、って5時間乾燥したものに比べても本発明の組成
物を添加した脱水汚泥の乾燥水分は30.6%で脱水率
が37.2%ど従来に比べてはるかに脱水効率が良く、
脱水が非常に容易に行なわれることが明確である。
Table 3 Formula for measuring dry moisture in dehydrated sludge As can be seen from this result, the dry moisture of the dehydrated sludge obtained by the control method was 84.6%, and the dewatering rate was poor at 1.7%. Even compared to the sludge dried for 5 hours, the dry water content of the dehydrated sludge to which the composition of the present invention was added was 30.6%, and the dewatering rate was 37.2%, which is much better than the conventional method.
It is clear that dehydration takes place very easily.

(3)有害物質の固着効果 脱水汚泥中の有害物質の固着に関して、従来の高分子凝
集剤により処理した汚泥中の有害1カ質と本発明の組成
物を添加して処理した汚泥中の有害物質とを測定して仕
較づるど第4表に示すような実験結果となる。
(3) Adhesion effect of harmful substances Regarding the adhesion of harmful substances in dehydrated sludge, one harmful substance in sludge treated with a conventional polymer flocculant and one harmful substance in sludge treated with the composition of the present invention were examined. When the substances are measured and compared, the experimental results are shown in Table 4.

第 4 表   汚泥中の有害物質の測定表このように
、本発明の組成物の特徴というべき特殊な焼結粉砕物か
らの水和物の析出によって固化構造体中での物理・(ヒ
学的吸着効果が著しいが、水和反応により生じる水酸化
カルシウムで重金属イオンが水酸化物を生じて固定され
ていることが明確である。
Table 4 Measurement table of harmful substances in sludge As described above, physical and (hypothetical) precipitation in the solidified structure is caused by the precipitation of hydrates from the special sintered and crushed material, which is a feature of the composition of the present invention. Although the adsorption effect is remarkable, it is clear that heavy metal ions are fixed in the form of hydroxides with calcium hydroxide produced by the hydration reaction.

(4)−軸圧縮強度 本発明の組成物を脱水汚泥に対して30%。(4) - Axial compressive strength 30% of the composition of the present invention relative to dewatered sludge.

50%、70%それぞれ添加して一軸圧縮強度の変化を
測定して見た結果、高分子凝集剤に対して特に効果のあ
ることがわかる。
The results of measuring the change in unconfined compressive strength after adding 50% and 70% respectively show that it is particularly effective against polymer flocculants.

所定の割合(30%、50%、70%)で本発明の組成
物をそれぞれ添加して、脱水処理を行なった後の汚泥を
ホバートミキサーによって混練した後、径5cm長さ1
0cmの円筒形の形枠中に汚泥を詰めて成形し、所定の
材令まで室温20℃、湿度60%以上で湿空養生したあ
との一軸圧縮強度を試験したところ第5表に示すような
測定結果となった。
After adding the compositions of the present invention at predetermined ratios (30%, 50%, 70%) and dehydrating the sludge, the sludge was kneaded using a Hobart mixer, and then mixed into sludge with a diameter of 5 cm and a length of 1.
Sludge was filled into a 0cm cylindrical frame and molded, and the unconfined compressive strength was tested after curing at a room temperature of 20℃ and a humidity of 60% or more until the specified material age, as shown in Table 5. Here are the measurement results.

第 5 表   材令に対する一軸圧縮強度測定表そし
て、この測定結果をグラフに表わすと図に示すようにな
り、本発明の組成物を脱水汚泥に対してこう0%、50
%、70%それぞれ添加して一軸圧縮強度の変化を見た
結果、高分子凝集剤に対して特に効果のあることがわか
った。これは、特に水分の多い汚泥などの固形化に有効
なエトリンジヤイト(3CaO−Ai203・3CaS
○4 ・321−120)により32分子の水を結晶水
として固定でき、早期に汚泥を生成する特徴を有するた
めである。
Table 5 Unconfined compressive strength measurement table for material age The measurement results are expressed in a graph as shown in the figure.
% and 70% respectively, and observed changes in unconfined compressive strength, and found that it was particularly effective for polymer flocculants. This is especially effective for solidifying water-rich sludge.
This is because 32 molecules of water can be fixed as crystallized water by 4.321-120), and sludge can be generated early.

(ii >実験例2 次に、第2実験例では、食品加エエ稈によって発生する
0機汚泥(BOD廃水)を曝気9al!l!(微生物処
理)することにより発生する余剰汚泥に本発明の組成物
を添加して、第1実験例と同様に脱水・凝集効果、乾燥
効果及び特に有害物の固着効果等についての試験をそれ
ぞれ行なった。
(ii > Experimental Example 2) Next, in the second experimental example, the present invention was applied to surplus sludge generated by aerating (microbial treatment) 0 machine sludge (BOD wastewater) generated by food processing culms. The compositions were added, and tests were conducted on dehydration/coagulation effects, drying effects, and especially harmful substances fixation effects, etc., in the same manner as in the first experimental example.

(1)脱水・凝集効果 有機汚泥の余剰汚泥(水分99%、固形分1%)に第1
表に示す本発明の組成物を汚泥固形分に対して30%添
加して撹拌を行ない混合した後、前記余剰汚泥をベルト
式脱水装置で脱水処理をを行ない、脱水汚泥中の水分を
測定したところ、第6表に示すようになった。
(1) Dehydration and flocculation effect
After adding 30% of the composition of the present invention shown in the table to the sludge solid content and stirring and mixing, the excess sludge was dehydrated using a belt-type dewatering device, and the water content in the dehydrated sludge was measured. However, the results are as shown in Table 6.

第 6 表   脱水汚泥中の水分測定衣このように、
高分子凝集剤を添加づる従来の方法では、水分が88.
4%で粘性が大きいために脱水が不可能であるのに比べ
て、本発明の組成物を添加すると水分が62.1%と低
く、粘性はあるが乾燥が行ない易い。
Table 6 Clothes for measuring moisture in dehydrated sludge Thus,
In the conventional method of adding a polymer flocculant, the water content is 88%.
When the composition of the present invention is added, the moisture content is as low as 62.1%, and it is easy to dry although it is viscous.

(2)乾燥効果 余剰汚泥を脱水処理した脱水汚泥に第1実験例と同様に
電気送風機を使用して送I!′l乾燥を行ない、汚泥中
の乾燥水分を測定すると、第7表に示すような結果とな
った。
(2) Drying effect Excess sludge is dehydrated and dehydrated sludge is sent using an electric blower in the same way as in the first experimental example. When the sludge was dried and the dry water content in the sludge was measured, the results shown in Table 7 were obtained.

第 7 表   脱水汚泥中の乾燥水分測定衣1品 この結果からもわかるように、従来の方法では脱水汚泥
の乾燥水分は86.1%T:脱水率が2.6%と悪く、
5時間乾燥した脱水汚泥と比べても、本発明の組成物を
添加することにより乾燥水分が30.9%で脱水率が5
0.2%と将来の方法に比べて脱水効率が良いことが明
確である。
Table 7: Measurement of dry moisture in dehydrated sludge (1 item) As can be seen from this result, in the conventional method, the dry moisture in dehydrated sludge was 86.1%T: The dewatering rate was poor at 2.6%;
Even when compared to dehydrated sludge dried for 5 hours, the addition of the composition of the present invention resulted in a dry moisture content of 30.9% and a dewatering rate of 5.
It is clear that the dehydration efficiency is 0.2%, which is better than future methods.

(3)有害物質の固着効果 有機汚泥(BOD廃水)の曝気処理によって発生した余
剰汚泥に本発明の組成物をそれぞれ10%、30%添加
して、イj害物(BOD)を測定した実験結果を第8表
に示す。
(3) Effect of fixation of harmful substances Experiment in which 10% and 30% of the composition of the present invention was added to surplus sludge generated by aeration treatment of organic sludge (BOD wastewater), and harmful substances (BOD) were measured. The results are shown in Table 8.

第 8 表   汚泥中の有害物質測定式この測定結果
より、添加率を10%から30%と添加率を増すに従っ
てSODの濃度が激減し、特に重金属及び有害物質の固
着に関して大きな固着機能を有しており、一般に塗料及
び塗料廃水等の産業廃棄物を処理するのに際して非常に
有効な手段となる。
Table 8: Hazardous substance measurement formula in sludge From this measurement result, as the addition rate increases from 10% to 30%, the concentration of SOD decreases dramatically, and it has a great fixing function especially in terms of fixing heavy metals and harmful substances. In general, it is a very effective means for treating industrial waste such as paint and paint wastewater.

これらは、特殊な組成物の焼結粉砕物から生成された水
酸化物によって、有害物質との共沈効果あるいはイオン
置換効果等の相乗効果が得られ、水和物結晶が構成する
核内への吸着現像が作用するためと考えられる。
The hydroxide produced from the sintered and crushed product of a special composition has a synergistic effect such as a coprecipitation effect with harmful substances or an ion replacement effect, and is absorbed into the core of the hydrate crystal. This is thought to be due to the effect of adsorption development.

(ili )実施例3 次に、第3実験例においては、塗料廃水に本発明の組成
物を0.5%添加した試験結果を第9表に示す。
(ili) Example 3 Next, in the third experimental example, Table 9 shows the test results in which 0.5% of the composition of the present invention was added to paint wastewater.

第 9 表   汚泥中の有害物質の吸着聞測定表この
ように、有害物質の吸着率が非常に優れており、大きな
固定機能を有していることが明確となり、塗料及び塗料
廃水の凝集・沈澱効果に対しても、従来の方法であるN
a01」処理では凝集・沈澱までに約3時間を要したが
、本発明の組成物を30%添加して試験を行なった結果
約15分間の短い時間で完全な凝集・沈澱効果が見られ
た。
Table 9 Measurement table for adsorption of harmful substances in sludge As shown above, it is clear that the adsorption rate of harmful substances is very good and that it has a great fixing function, and it is possible to prevent the coagulation and sedimentation of paint and paint wastewater. Regarding the effect, the conventional method N
a01'' treatment required approximately 3 hours for aggregation and precipitation to occur, but as a result of a test with 30% of the composition of the present invention added, complete aggregation and precipitation effects were observed in a short time of approximately 15 minutes. .

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

図は、本発明の第1実験例における材令に対する一軸圧
縮強度を示すグラフである。
The figure is a graph showing the unconfined compressive strength with respect to material age in the first experimental example of the present invention.

Claims (2)

【特許請求の範囲】[Claims] (1)プレーン値を2000〜4000cm^2/gに
調整した高炉水滓粉砕物と、プレーン値を3000〜5
000cm^2/gに調整したII型無水石膏粉末と、ゼ
オライト粉末と、3CaO・SiO_2(アリット相)
と2CaO・SiO_2(ベリット相)を主成分とした
ボルトランドセメントと、プレーン値を3000〜40
00cm^2/gに、調整した4CaO・3Al_2O
_3(SO)_4を主成分とした焼結粉砕物(アーウィ
ン)とをそれぞれ配合した組成物からなることを特徴と
する廃水中のスラッジの凝集・吸着・脱水・固化剤。
(1) Ground blast furnace water slag with a plain value adjusted to 2000-4000 cm^2/g and a plain value adjusted to 3000-5
Type II anhydrite powder adjusted to 000cm^2/g, zeolite powder, and 3CaO・SiO_2 (alite phase)
and 2CaO・SiO_2 (berit phase) as the main components, and the plain value is 3000 to 40.
4CaO・3Al_2O adjusted to 00cm^2/g
An agent for flocculating, adsorbing, dehydrating, and solidifying sludge in wastewater, characterized by comprising a composition containing a sintered pulverized product (Irwin) containing _3 (SO) and _4 as main components.
(2)上記組成物に水酸化アルミニウムを配合した特許
請求の範囲第1項記載の廃水中のスラッジの凝集・吸着
・脱水・固化剤。
(2) The agent for coagulating, adsorbing, dehydrating, and solidifying sludge in wastewater according to claim 1, wherein aluminum hydroxide is blended into the composition.
JP60204334A 1985-09-18 1985-09-18 Flocculating, adsorbing, dehydrating and solidifying agent for sludge in waste water Pending JPS6265799A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60204334A JPS6265799A (en) 1985-09-18 1985-09-18 Flocculating, adsorbing, dehydrating and solidifying agent for sludge in waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60204334A JPS6265799A (en) 1985-09-18 1985-09-18 Flocculating, adsorbing, dehydrating and solidifying agent for sludge in waste water

Publications (1)

Publication Number Publication Date
JPS6265799A true JPS6265799A (en) 1987-03-25

Family

ID=16488776

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60204334A Pending JPS6265799A (en) 1985-09-18 1985-09-18 Flocculating, adsorbing, dehydrating and solidifying agent for sludge in waste water

Country Status (1)

Country Link
JP (1) JPS6265799A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01111499A (en) * 1987-10-23 1989-04-28 Nkk Corp Dehydration/dephosphorization process using water granulated slug as auxiliary
CN103553375A (en) * 2013-09-29 2014-02-05 南京工业大学 Composite soil solidifying agent, and preparation and application thereof
CN104108915A (en) * 2014-07-09 2014-10-22 上海理工大学 Sintering-free method for preparing bricks from dredged sediment

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5067280A (en) * 1973-10-22 1975-06-05
JPS52124753A (en) * 1976-04-13 1977-10-20 Denki Kagaku Kogyo Kk Solidifying material for sludge
JPS55140746A (en) * 1979-04-18 1980-11-04 Denki Kagaku Kogyo Kk Low heat cement shrinkage reducing material
JPS5610399A (en) * 1979-07-09 1981-02-02 Chichibu Cement Co Ltd Solidifying treating material for improvement of foundation, sludge. noxious waste, etc.
JPS56163797A (en) * 1980-05-20 1981-12-16 Fujisash Co Dehydrating and solidifying method of sewer sludge

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5067280A (en) * 1973-10-22 1975-06-05
JPS52124753A (en) * 1976-04-13 1977-10-20 Denki Kagaku Kogyo Kk Solidifying material for sludge
JPS55140746A (en) * 1979-04-18 1980-11-04 Denki Kagaku Kogyo Kk Low heat cement shrinkage reducing material
JPS5610399A (en) * 1979-07-09 1981-02-02 Chichibu Cement Co Ltd Solidifying treating material for improvement of foundation, sludge. noxious waste, etc.
JPS56163797A (en) * 1980-05-20 1981-12-16 Fujisash Co Dehydrating and solidifying method of sewer sludge

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01111499A (en) * 1987-10-23 1989-04-28 Nkk Corp Dehydration/dephosphorization process using water granulated slug as auxiliary
JPH0535040B2 (en) * 1987-10-23 1993-05-25 Nippon Kokan Kk
CN103553375A (en) * 2013-09-29 2014-02-05 南京工业大学 Composite soil solidifying agent, and preparation and application thereof
CN103553375B (en) * 2013-09-29 2016-06-01 南京工业大学 A kind of combined soil solidifying agent and Synthesis and applications thereof
CN104108915A (en) * 2014-07-09 2014-10-22 上海理工大学 Sintering-free method for preparing bricks from dredged sediment

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