JPH0796115B2 - Water treatment contact material - Google Patents
Water treatment contact materialInfo
- Publication number
- JPH0796115B2 JPH0796115B2 JP3232551A JP23255191A JPH0796115B2 JP H0796115 B2 JPH0796115 B2 JP H0796115B2 JP 3232551 A JP3232551 A JP 3232551A JP 23255191 A JP23255191 A JP 23255191A JP H0796115 B2 JPH0796115 B2 JP H0796115B2
- Authority
- JP
- Japan
- Prior art keywords
- blast furnace
- water
- granulated blast
- water treatment
- contact material
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Farming Of Fish And Shellfish (AREA)
- Biological Treatment Of Waste Water (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、排水や河川等の生物化
学的浄化処理において、微生物を固定化させて浄化する
ために使用される水処理接触材、特に、高炉水砕スラグ
を原料とした水処理接触材に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention uses, as a raw material, a water treatment contact material used for immobilizing and purifying microorganisms in a biochemical purification treatment of wastewater, rivers, etc., particularly granulated blast furnace slag. Water treatment contact material.
【0002】[0002]
【従来の技術】近年、我が国では湖沼の富栄養化や河川
の汚濁が社会問題となっており、その主な汚染源である
家庭排水や工場排水の浄化処理は勿論のこと、汚染され
た湖沼水や河川水の浄化処理も急務となっている。2. Description of the Related Art In recent years, eutrophication of lakes and marine rivers has become a social problem in Japan, and the main source of pollution is not only purification of domestic wastewater and industrial wastewater but also polluted lake water. Purification of river water is also an urgent task.
【0003】これら汚水の浄化処理法の一つとして、
礫、プラスチック、ゼオライト、セラミックス、コーク
スなどによる水処理接触材を水中に没し、その表面に形
成した微生物膜により生物化学的に処理する方法があ
る。As one of the methods for purifying these sewage,
There is a method in which a water treatment contact material such as gravel, plastic, zeolite, ceramics, and coke is submerged in water and biochemically treated by a microbial film formed on the surface.
【0004】ところで、製鉄工程において大量に副生す
る溶融スラグを吹製して得られる高炉水砕スラグは、各
種骨材等にその大半が有効利用されている。この高炉水
砕スラグは、カルシウム、マグネシウム、鉄、リン等の
微生物の成育を助長する成分を含有していることから、
上記のような目的の水処理接触材の原料にも利用されて
いる。By the way, most of the granulated blast furnace slag obtained by blowing a large amount of molten slag produced as a by-product in the iron making process is effectively used for various aggregates and the like. This granulated blast furnace slag contains components that promote the growth of microorganisms such as calcium, magnesium, iron and phosphorus.
It is also used as a raw material for the water treatment contact material for the above purpose.
【0005】従来、高炉水砕スラグを使用した水処理接
触材としては、例えば次の公報に記載のものが知られて
いる。 <特開昭57−75189号> 直径5mm以上の高炉水砕スラグをそのまま使用する。 <特開昭63−77596号> 40〜150μm程度の高炉水砕微粉末に粘土及び気孔
形成材を配合し、成型、焼成したもの。Conventionally, as a water treatment contact material using granulated blast furnace slag, for example, those described in the following publications are known. <JP-A-57-75189> Granulated blast furnace slag having a diameter of 5 mm or more is used as it is. <JP-A-63-77596> A product obtained by mixing clay and a pore-forming material with ground granulated blast furnace powder having a particle size of about 40 to 150 μm, followed by molding and firing.
【0006】<特開昭63−296891号> 平均粒径200μm程度の高炉水砕微粉末と合成樹脂と
を混練し、サドル形又はリング状に成形したもの。 <特開昭63−296895号> サドル又はリング状に成形した担体素材の表面に接着剤
層を形成し、該接着剤層に平均粒径20〜500μm程
度の高炉水砕微粉末を付着させたもの。<JP-A-63-296891> A granulated blast furnace powder having an average particle size of about 200 μm and a synthetic resin are kneaded and molded into a saddle shape or a ring shape. <JP-A-63-296895> An adhesive layer is formed on the surface of a carrier material formed in a saddle or ring shape, and granulated blast furnace fine powder having an average particle size of about 20 to 500 µm is adhered to the adhesive layer. thing.
【0007】[0007]
【発明が解決しようとする課題】しかし、従来の水処理
接触材では次のような問題点があった。礫によるもの
は、それ自体が気孔率及び吸水率が低いため、微生物の
付着性が悪く、微生物付着しない部分が多くなるため、
重量当たりの有効表面積が小さい。また、重量が重いた
め取り扱いにくく、粒度構成範囲が広いので処理槽に挿
入したときに槽内の空隙率が小さくなり、目詰まりが早
い等々の欠点がある。However, the conventional water treatment contact material has the following problems. The gravel itself has a low porosity and water absorption rate per se, so that the adhesion of microorganisms is poor, and there are many areas where microorganisms do not adhere.
Small effective surface area per weight. Further, since the weight is heavy, it is difficult to handle, and since the particle size range is wide, the porosity in the tank becomes small when it is inserted into the processing tank, and there are disadvantages such that clogging is fast.
【0008】プラスチックは、気孔率及び吸水率が小さ
く、表面が滑らか過ぎるため微生物の付着安定性が悪
い。セラミックやゼオライトは成型が難しく、また高価
である。コークスは、気孔率及び吸水率の点においては
上記の原料のいずれにも劣ることはないが、使用中に粉
化して目詰まりを起こし、また、もともと燃料として使
用されるものであるためコストが高く、水処理接触材と
しての大量利用には不向きである。[0008] Plastic has a low porosity and a low water absorption rate, and its surface is too smooth, so that the adhesion stability of microorganisms is poor. Ceramics and zeolites are difficult to mold and expensive. Coke is not inferior to any of the above raw materials in terms of porosity and water absorption, but it is pulverized and clogged during use, and since it is originally used as a fuel, cost is low. It is expensive and not suitable for large-scale use as a water treatment contact material.
【0009】また、上記のような原料を使用した場合、
表面積を大きくして微生物の付着を容易にするため、水
処理接触材の形状として、紐状、筒状、ネット状、ハニ
カム構造などとしているが、複雑な形状、構造となるた
め製造コストの増大は避けられなかった。When the above raw materials are used,
In order to increase the surface area and facilitate the attachment of microorganisms, the shape of the water treatment contact material is string-shaped, tubular, net-shaped, honeycomb structure, etc., but the manufacturing cost increases because of the complicated shape and structure. Was inevitable.
【0010】直径5mm以上の高炉水砕スラグをそのま
ま使用するものでは、その形状が一定でなく、表面の凹
凸が大きいため処理水の偏流を生じたり、粒度構成が広
範囲であるため、処理槽内で目詰まりを生ずる等の欠点
がある。When the granulated blast furnace slag having a diameter of 5 mm or more is used as it is, the shape of the blast furnace is not constant, and the unevenness of the surface is large, so that the treated water is unevenly flowed and the particle size composition is wide. However, there are drawbacks such as clogging.
【0011】高炉水砕微粉末に粘土及び気孔形成材を混
ぜて成型、焼成したものは、高温処理が必要であるた
め、コスト高である。また、高炉水砕微粉末と合成樹脂
とを混練し、サドル形又はリング状に成形したものは、
気孔率や吸水率が低い。更に、サドル又はリング状に成
形した担体素材の表面の接着剤層に高炉水砕微粉末を付
着させたものは、担体素材の製造工程、高炉水砕スラグ
を粉砕する工程、接着工程が必要で、製造が複雑であ
り、しかも高価な接着剤を必要とするなど、コストの非
常に高いものとなる。A product obtained by mixing granulated blast furnace fine powder with clay and a pore-forming material and molding and baking it requires high-temperature treatment, and thus is costly. Further, the granulated blast furnace fine powder and synthetic resin are kneaded and molded into a saddle shape or a ring shape,
Porosity and water absorption are low. Furthermore, the one in which the granulated blast furnace granulated powder is adhered to the adhesive layer on the surface of the carrier material shaped like a saddle or ring requires the carrier material manufacturing step, the step of crushing granulated blast furnace slag, and the bonding step. However, the manufacturing cost is very high because the manufacturing process is complicated and an expensive adhesive is required.
【0012】そこで、本発明の目的は、高炉水砕スラグ
を使用して低廉に得られ、しかも気孔率及び吸水率が高
くて微生物の付着性が良好である半面、目詰まりするこ
とも少なく、かつ軽量で作業性の良い水処理接触材を提
供することにある。[0012] Therefore, the object of the present invention is to obtain inexpensively by using granulated blast furnace slag, high porosity and water absorption and good adhesion of microorganisms, but less clogging, Another object of the present invention is to provide a water treatment contact material that is lightweight and has good workability.
【0013】[0013]
【課題を解決するための手段】本発明による水処理接触
材は、1〜5mmに粒度調整した多孔質の高炉水砕スラ
グを主原料としてその1重量部に対し、高炉水砕微粉末
又はこれに生石灰を混合したものを水硬性バインダーと
して0.1〜0.4重量部添加し、調湿・混練し、所要
の形体に成型してなるものである。The water treatment contact material according to the present invention comprises, as a main raw material, a granulated blast furnace granulated slag having a particle size adjusted to 1 to 5 mm to 1 part by weight of the granulated blast furnace fine powder or this 0.1 to 0.4 parts by weight of a mixture of quick lime and a hydraulic binder is added, the humidity is adjusted and the mixture is kneaded, and the mixture is molded into a desired shape.
【0014】[0014]
【作用】本発明による水処理接触材は高炉水砕スラグを
主原料とする。製鉄工程において副生する溶融状態のス
ラグは、冷却の方法により異なった種々の性状となる。
その一つの方法として、溶融状態の高炉スラグを吹製装
置に流し、1〜3Kg/cm2の圧力水によって冷却す
ると、瞬時に粒状化し高炉水砕スラグとなる。この場合
の高炉水砕スラグの大半は砂状で、外観は灰黄色のガラ
ス質粒子が大部分を占め、粒子は無数の気泡を有し、角
張った形状を呈している。そのため、気孔率が高く、表
面積が大である。The water treatment contact material according to the present invention is mainly composed of granulated blast furnace slag. The molten slag produced as a by-product in the iron-making process has various properties depending on the cooling method.
As one of the methods, when blast furnace slag in a molten state is flown through a blowing apparatus and cooled with pressure water of 1 to 3 kg / cm 2 , it is instantly granulated to form granulated blast furnace slag. Most of the granulated blast furnace slag in this case is sandy, and the appearance is mostly grayish yellow glassy particles, and the particles have an infinite number of bubbles and have an angular shape. Therefore, it has a high porosity and a large surface area.
【0015】高炉水砕スラグには、カルシウム、マグネ
シウム、鉄、リン等が含有されており、これら含有成分
の処理水に与える影響は次のとおりである。 (1)カルシウム 処理水を循環させることにより窒素が硝酸化し、処
理水が酸性化することに対応して、高炉水砕スラグから
溶出したCaイオンが中和作用の働きをし、微生物が成
育し易い環境を提供することができる。 湖沼などの富栄養化の原因とされているリンが高炉
水砕スラグから溶出したCaイオンに反応し、リン酸カ
ルシウムの形で固定できる。 高炉水砕スラグから溶出したCaイオンは、処理水
中のSS(浮遊懸濁物質)の凝集沈澱作用を促進させる
効果がある。 (2)マグネシウム、鉄、リン マグネシウム、鉄、リンは微生物の成育を助長させる働
きを有する。特に高炉水砕スラグはマグネシウム含有量
が高く、リンの含有量は少ない。The granulated blast furnace slag contains calcium, magnesium, iron, phosphorus and the like, and the effects of these components on the treated water are as follows. (1) Calcium Corresponding to the fact that nitrogen is nitrated by circulating the treated water and the treated water is acidified, Ca ions eluted from the granulated blast furnace slag act as a neutralizing agent to grow microorganisms. An easy environment can be provided. Phosphorus, which is said to be the cause of eutrophication in lakes and marshes, reacts with Ca ions eluted from granulated blast furnace slag and can be fixed in the form of calcium phosphate. The Ca ions eluted from the granulated blast furnace slag have the effect of promoting the coagulation and precipitation action of SS (suspended suspended solids) in the treated water. (2) Magnesium, iron and phosphorus Magnesium, iron and phosphorus have the function of promoting the growth of microorganisms. In particular, granulated blast furnace slag has a high magnesium content and a low phosphorus content.
【0016】しかし、高炉水砕スラグをただ有姿又は粒
調して粉分を除去したもの等を充填層に装入し、対象水
を通水すると、有姿の場合は粒度構成の範囲が広いため
SS分が影響し目詰まりを起こし、また粒調品はその表
面が大きいため処理水の偏流を招く欠点がある。そこ
で、高炉水砕スラグにセメントを加えて所要の形体に成
型し、流動抵抗を減少させることが考えられるが、高炉
水砕スラグをセメントで固化成形した場合には、上記の
ように微生物の成長を助長する成分を有する高炉水砕ス
ラグがセメントに包み込まれ、その効果が半減してしま
う。[0016] However, when granulated blast furnace slag is put into a packed bed in a mere form or in a grained state to remove powder, and the target water is passed through, the range of particle size composition is reduced in the case of a solid form. Since it is wide, the SS content affects and causes clogging, and since the grain preparation has a large surface, it has the drawback of causing a nonuniform flow of treated water. Therefore, it is conceivable to add cement to the granulated blast furnace slag to mold it into a desired shape and reduce the flow resistance.However, when the granulated blast furnace slag is solidified with cement, the growth of microorganisms as described above is performed. The granulated blast furnace slag, which has a component that promotes slag, is wrapped in cement and its effect is halved.
【0017】そこで、本発明では、セメントに代わる水
硬性バインダーとして、高炉水砕スラグと同様の効能を
有する高炉水砕微粉末を採用したものである。すなわ
ち、高炉水砕微粉末をバインダーとした高炉水砕スラグ
の固化成形物は、高炉水砕スラグを、これと同じ効能を
有する高炉水砕微粉末が包み込んだ形となるため、高炉
水砕スラグの効能を損なわずに生物化学的水処理が可能
となる。Therefore, in the present invention, granulated blast furnace fine powder having the same effect as granulated blast furnace slag is adopted as a hydraulic binder in place of cement. That is, the solidified molded product of the granulated blast furnace slag using the granulated blast furnace slag as a binder has a form in which the granulated blast furnace granulated slag is wrapped with the granulated blast furnace granulated slag having the same effect, Biochemical water treatment is possible without impairing the efficacy of.
【0018】また、バインダーが高炉水砕微粉末のみで
は成形物に十分な初期強度を持たせることができない場
合もあるので、本発明では必要に応じて生石灰を刺激剤
として使用する。種々ある刺激剤の中から生石灰を選ん
だ理由は、それから溶出するCaイオンが上記ないし
で説明した効能を有しているからである。すなわち、
生石灰は、高炉水砕微粉末と反応して潜在水硬性を促進
し、成型品の形状を保持するとともに、その主成分がC
aOであるので、これを本発明の水処理接触材に配合し
た場合、高炉水砕スラグ及び高炉水砕微粉末と同様に、
処理水の中性化、SSの凝集沈澱促進、リンの除去等の
効果を発揮する。In addition, quick lime is used as a stimulant in the present invention, if necessary, since the binder may not be able to have a sufficient initial strength when the ground granulated blast furnace powder is used alone. The reason why quick lime is selected from various stimulants is that Ca ions eluted from it have the effects described above. That is,
Quick lime reacts with ground granulated blast furnace powder to promote latent hydraulicity, maintain the shape of the molded product, and its main component is C
Since it is aO, when it is blended with the water treatment contact material of the present invention, like blast furnace granulated slag and blast furnace granulated fine powder,
It exerts effects such as neutralization of treated water, promotion of coagulation and precipitation of SS, and removal of phosphorus.
【0019】湖沼、地下水、海洋中には広く硫酸塩が存
在しているが、この硫酸塩はセメントによって生じた水
酸化カルシウムと反応して硫酸カルシウムを生成する。
次に、この硫酸カルシウムの一部が石膏不足に起因する
3CaO・Al2O3(アルミ酸化カルシウム)の単独
水和物4CaO・Al2O3・XH2Oと反応してエト
リンガイドを生成し、その際に大きな体積膨張を起こし
て成形体を破壊する。しかし、高炉水砕微粉末は、ポル
トランドセメントに比べAl2O3分が格段に多いのに
も拘わらず、これの混合セメントの耐硫酸塩性は、むし
ろポルトランドセメントよりも優れている。この理由
は、アルミネート相の組成と構造の違いに起因している
ものと思われる。Sulfates are widely present in lakes, groundwater, and the ocean, and these sulfates react with calcium hydroxide produced by cement to produce calcium sulfate.
Next, generate a d [pi] n guide reacts alone hydrate 4CaO · Al 2 O 3 · XH 2 O in 3CaO · Al 2 O 3 where part of the calcium sulfate is due to gypsum deficient (aluminum calcium oxide) At that time, a large volume expansion is caused to destroy the molded body. However, although the ground granulated blast furnace powder has much more Al 2 O 3 content than Portland cement, the sulfate resistance of this mixed cement is rather superior to that of Portland cement. The reason seems to be due to the difference in composition and structure of the aluminate phase.
【0020】一方、本発明の水処理接触材は、淡水処理
に限らず海水(例えば養魚用水)処理にも用いるため、
ポルトランドセメントをバインダーとした水処理材では
上記理由から海水中の硫酸塩により膨張崩壊する恐れが
ある。そこで、本発明はこのようなことも鑑み、バイン
ダーとして高炉水砕微粉末又はこれに生石灰を混合した
ものを使用したものである。On the other hand, the water treatment contact material of the present invention is used not only for the treatment of fresh water but also for treatment of sea water (for example, water for fish farming).
For the above-mentioned reason, the water treatment material using Portland cement as a binder may expand and collapse due to the sulfate in seawater. In view of the above, the present invention uses, as a binder, granulated blast furnace fine powder or a mixture thereof with quicklime.
【0021】本発明の水処理接触材の成型方法として
は、パン型ペレタイザーを使用する転動造粒法やブリケ
ットマシンを使用する圧縮成型法などが一般的である
が、これらの方法による成型は原料に対して微粒部分が
要求されるため、高炉水砕スラグそのままでは成型出来
ず、それを粉砕することによって始めて成型が可能とな
る。しかも、出来上がった成型体は緻密なものとなり、
水処理接触材として使用するに当たって成型体内部まで
処理水が十分に行き渡らず、微生物との接触においては
甚だ効率の悪いものとなる。As the method for molding the water treatment contact material of the present invention, a rolling granulation method using a pan type pelletizer and a compression molding method using a briquette machine are generally used. Since the fine particles are required for the raw material, the granulated blast furnace slag cannot be molded as it is, and can be molded only by grinding it. Moreover, the finished molded body becomes dense,
When it is used as a water treatment contact material, the treated water does not reach the inside of the molded body sufficiently, resulting in extremely low efficiency in contact with microorganisms.
【0022】本発明では、このような問題を解決するた
め、高炉水砕スラグを篩分けて1〜5mmに粒度調整し
たものを原料として使用する。粒度が1mm以下である
と、成型体が緻密になるので通水性が悪化し、また5m
m以上であると成型体構成粒子の表面積が小さくなって
処理効率が悪くなるとともに、強度的に脆弱になる。1
〜5mmに粒度調整したものであると、成型体とした場
合にも、高炉水砕スラグの上記のような性状、つまり無
数の気泡を有する角張った性状をフルに発揮させること
ができるに加え、水硬性バインダーによる固着及び成型
体の形状保持の上でも適度な粒度である。In the present invention, in order to solve such a problem, granulated blast furnace slag is sieved and used to have a particle size adjusted to 1 to 5 mm as a raw material. If the particle size is 1 mm or less, the molded body becomes dense and the water permeability deteriorates.
When it is m or more, the surface area of the particles constituting the molded body becomes small, the treatment efficiency deteriorates, and the strength becomes weak. 1
In addition to being able to fully exhibit the above-mentioned properties of the granulated blast furnace slag, that is, the angular properties having innumerable bubbles, when the particle size is adjusted to ~ 5 mm, even if it is formed into a molded body, The particle size is appropriate for fixing with a hydraulic binder and maintaining the shape of the molded product.
【0023】成型は、粒度調整した高炉水砕スラグに水
硬性バインダーとして高炉水砕微粉末又はこれに生石灰
を混合したものを添加し、調湿・混練(水を加えて混練
する)して型枠に流し込む。調湿・混練に当たっては、
コンクリートミキサーやローラーミキサー等の一般的な
ミキシング装置、また流し込み成型に当たっては、所要
の形状及び大きさの木型や金型等の型枠を使用すること
ができる。Molding is performed by adding granulated blast furnace granulated slag with hydraulic granulated blast furnace granulated powder or a mixture of quick lime to this as a hydraulic binder, and adjusting the humidity and kneading (mixing with water) Pour into the frame. When adjusting the humidity and kneading,
A general mixing device such as a concrete mixer or a roller mixer, or a casting mold such as a wooden mold or a mold having a required shape and size can be used for the casting.
【0024】成型品は、いわば粟おこし状の透水性に富
んだ成型体となるので、高炉水砕スラグの気孔率を低下
させることがなく、しかも成型表面及び内部もポーラス
となるので、微生物の付着性が非常に良いものとなる。Since the molded product is, so to speak, a milled rice-like molded product rich in water permeability, it does not lower the porosity of the granulated blast furnace slag, and the molded surface and the inside are also porous, so that the microbial The adhesion is very good.
【0025】本発明では、高炉水砕スラグを主原料とす
るが、型枠への流し込み成型時における成型性の向上を
目的とした粒度構成改善や、成型品の気孔率の改善など
を目的として、高炉スラグを原料として製造されるロッ
クウールの規格外品、いわゆる屑綿を高炉水砕スラグに
少し添加しても構わない。In the present invention, granulated blast furnace slag is used as the main raw material, but the purpose is to improve the grain size composition for the purpose of improving the moldability during casting into a mold and to improve the porosity of the molded product. A non-standard item of rock wool produced from blast furnace slag as a raw material, so-called waste cotton, may be added to the granulated blast furnace slag.
【0026】水硬性バインダーである高炉水砕微粉末又
はこれに生石灰を混合したもの添加量は、粒度調整した
高炉水砕スラグ1重量部に対して0.1〜0.4重量部
である。0.1重量部以下では、成型品の強度が不足
し、運搬等のハンドリング中や処理槽に挿入した際に崩
壊する恐れがあり、またCaOの溶出が少なく、上記の
ような効果が薄れる。一方、0.4重量部以上では、成
型品の強度は向上するが、成型品が緻密になり過ぎて気
孔率が低下するので、水処理接触材としての機能が低下
するとともに、コスト高となる。The amount of ground granulated blast furnace powder which is a hydraulic binder or a mixture of quick lime mixed with this is 0.1 to 0.4 part by weight per 1 part by weight of granulated blast furnace granulated slag. When the amount is 0.1 parts by weight or less, the strength of the molded product is insufficient, and there is a risk of collapsing during handling such as transportation or when inserted into a processing tank, and CaO elution is small, and the above effects are diminished. On the other hand, when the content is 0.4 parts by weight or more, the strength of the molded product improves, but the molded product becomes too dense and the porosity decreases, so that the function as a water treatment contact material decreases and the cost increases. .
【0027】[0027]
【実施例】図2に本発明による水処理接触材の製造手順
を示す。表1に示すような成分の高炉水砕スラグを、篩
い分け機により粒度が1〜5mmの範囲内のものだけ篩
い分けた。図1にその粒度調整した高炉水砕スラグを示
す。この粒度1〜5mmの高炉水砕スラグ85%に対し
て、水硬性バインダーとしての生石灰5%、高炉水砕微
粉末10%と、適量の水を加えて混練機で混練した後、
型枠に流し込んで縦70mm、横70mm、高さ20m
mの板状の水処理接触材を成型した。成型後、養生室に
て3日間養生し、型枠から取り出して図3に示すような
製品とした。この製品(第1例)の比重は1.40、吸
水率は27%であった。また、粒度1〜5mmの高炉水
砕スラグ85%に対して、生石灰10%、高炉水砕微粉
末5%としたもの(第2例)、高炉水砕微粉末15%と
したもの(第3例)をそれぞれ上記と同じ大きさに成型
した。EXAMPLE FIG. 2 shows a procedure for producing a water treatment contact material according to the present invention. The granulated blast furnace slag having the components shown in Table 1 was sieved by a sieving machine only in a range of particle size of 1 to 5 mm. Fig. 1 shows granulated blast furnace granulated slag. To 85% of the granulated blast furnace slag having a particle size of 1 to 5 mm, 5% of quick lime as a hydraulic binder and 10% of granulated blast furnace fine powder, and an appropriate amount of water were added and kneaded in a kneader,
Pour into formwork, length 70mm, width 70mm, height 20m
m plate-shaped water treatment contact material was molded. After molding, the product was aged in a curing room for 3 days and taken out from the mold to obtain a product as shown in FIG. The specific gravity of this product (first example) was 1.40, and the water absorption rate was 27%. Further, with respect to 85% of granulated blast furnace slag having a particle size of 1 to 5 mm, quick lime 10% and granulated blast furnace fine powder 5% (second example), granulated blast furnace fine powder 15% (third example) Examples) were molded into the same size as above.
【0028】[0028]
【表1】 [Table 1]
【0029】上記4種類の製品の効果を確認するため次
のような実験を行った。その実験方法は、図4に示すよ
うに散水濾床法を想定して多数の水処理接触材1を内法
寸法80mm×80mm、高さ100mmの角形容器2
内に充填し、縦300mm、横300mm、高さ100
mmの水槽3から、対象水として屎尿処理場の一次処理
排水を定量ポンプ4で角形容器2の上部に散水し、水処
理接触材1を通過した処理水を角形容器2の下部出口か
ら水槽3へ返流した。7はそのリサイクル処理水を示
す。このときの経時変化に伴う対象水のCOD、BO
D、T−N、T−Pを測定した。球状プラスチックによ
る従来品についても同様に測定した。その測定結果を表
2及び表3に示す。これらの表から分かるように本発明
による水処理接触材はCOD、BOD、T−N、T−P
の除去に関し従来品よりも格段に優れている。The following experiment was conducted to confirm the effects of the above four kinds of products. As the experimental method, as shown in FIG. 4, assuming that a sprinkling filter method is used, a large number of water treatment contact materials 1 are provided in a rectangular container 2 having an inner dimension of 80 mm × 80 mm and a height of 100 mm.
Fill inside, length 300mm, width 300mm, height 100
From the water tank 3 of mm, the primary treatment wastewater of the human waste treatment plant is sprayed on the upper portion of the rectangular container 2 by the metering pump 4 as the target water, and the treated water that has passed through the water treatment contact material 1 is discharged from the lower outlet of the rectangular container 2 to the water tank 3. Returned to. Reference numeral 7 indicates the recycled treated water. COD and BO of the target water due to changes with time at this time
D, TN and TP were measured. The same measurement was performed on the conventional product made of spherical plastic. The measurement results are shown in Tables 2 and 3. As can be seen from these tables, the water treatment contact material according to the present invention is COD, BOD, TN, TP.
It is far superior to conventional products in terms of removing.
【0030】[0030]
【表2】 [Table 2]
【0031】[0031]
【表3】 [Table 3]
【0032】また、図5に示すような実験を行った。す
なわち、浸漬濾床法を想定して多数の水処理接触材1を
縦200mm、横300mm、高さ250mmの上端部
に流出口を有する処理槽5に充填し、縦300mm、横
500mm、高さ400mmの水槽3に、対象水として
屎尿処理場の一次処理排水を入れ、その水を定量ポンプ
4で処理槽5に送り、水処理接触材1を通過した処理水
を水槽3へ返流した。また、水槽3ではエアーレーショ
ン装置6で空気によるバブリングを行い、経時変化に伴
う対象水のCOD、BOD、T−N、T−Pを測定し
た。球状プラスチックによる従来品についても同様に測
定した。その測定結果を表4から表6に示す。この場合
も本発明による水処理接触材はCOD、BOD、T−
N、T−Pの除去に関し従来品よりも格段に優れてい
る。Further, an experiment as shown in FIG. 5 was conducted. That is, assuming a dipping filter method, a large number of water treatment contact materials 1 are filled in a treatment tank 5 having an outlet of 200 mm in length, 300 mm in width, and 250 mm in height at the upper end, and 300 mm in length, 500 mm in width, and height. Primary treatment wastewater of a human waste treatment plant was put into a 400 mm water tank 3 as target water, the water was sent to a treatment tank 5 by a metering pump 4, and the treated water that passed through the water treatment contact material 1 was returned to the water tank 3. Further, in the water tank 3, bubbling with air was performed by the aeration device 6, and COD, BOD, T-N, and T-P of the target water with the lapse of time were measured. The same measurement was performed on the conventional product made of spherical plastic. The measurement results are shown in Tables 4 to 6. Also in this case, the water treatment contact material according to the present invention is COD, BOD, T-.
It is far superior to conventional products in removing N and T-P.
【0033】[0033]
【表4】 [Table 4]
【0034】[0034]
【表5】 [Table 5]
【0035】[0035]
【表6】 [Table 6]
【0036】図5に示した実験装置において対象水を水
道水に替え、図6に示すように水槽3に淡水魚を3匹入
れて表7に示すようにバブリングと対象水の循環を行
い、COD変化に伴う淡水魚の生息状況を観察した。In the experimental apparatus shown in FIG. 5, the target water was replaced with tap water, three freshwater fish were placed in the water tank 3 as shown in FIG. 6, and bubbling and target water circulation were performed as shown in Table 7 to obtain COD. We observed the habitation of freshwater fish with changes.
【0037】[0037]
【表7】 [Table 7]
【0038】表7において、試験番号1では、試験開始
当初からバブリングと水処理接触材への対象水循環を行
い、40日目からは水処理接触材への循環を止め、バブ
リングのみを行った。40日目までのCODは6.8〜
9.7mg/lと低い値を示し続けたが、40日目以降
はその値が次第に上昇し、47日目には17mg/l以
上となって魚は死亡した。In Table 7, in Test No. 1, bubbling and target water circulation to the water treatment contact material were performed from the beginning of the test, and from the 40th day, the circulation to the water treatment contact material was stopped and only bubbling was performed. COD by the 40th day is 6.8 ~
The value continued to show a low value of 9.7 mg / l, but the value gradually increased from the 40th day onward, and became 17 mg / l or more on the 47th day, and the fish died.
【0039】試験番号2では、試験開始当初からバブリ
ングのみを行ったところ、7日目にはCODが16mg
/lとなり、9日目になって魚は全て死亡した。死亡し
た魚を取り除き、そのままバブリングのみを続けたとこ
ろ、40日目にはCODが52mg/lと非常に高い値
を示すに至った。この汚染された対象水を40日目から
はバブリングと水処理接触材への循環を行った結果、C
ODは次第に減少し、55日目には7.4mg/lと魚
が生息できる状態まで回復した。In test No. 2, when only bubbling was performed from the beginning of the test, COD was 16 mg on the 7th day.
/ L, and all the fish died on the 9th day. When the dead fish was removed and only bubbling was continued as it was, COD reached a very high value of 52 mg / l on the 40th day. From the 40th day, this contaminated target water was bubbled and circulated to the water treatment contact material.
The OD gradually decreased, and on day 55, it was recovered to 7.4 mg / l to a condition where fish could live.
【0040】この実験から、本発明の水処理接触材を用
いて対象水の浄化処理を行っている間は、CODは低い
値を示し、魚は生息しているが、バブリングのみではC
OD値は次第に増加し、数日後には魚が死亡するほどに
増加することが判明した。また、本発明の水処理接触材
は魚の生息に対して無害であることも判明した。From this experiment, COD shows a low value while the target water is purified using the water treatment contact material of the present invention, and the fish live but the bubbling alone causes C
It was found that the OD value gradually increased, and after a few days, the fish died. It was also found that the water treatment contact material of the present invention is harmless to fish inhabitation.
【0041】図5に示した実験装置において、対象水を
COD値の低い河川水に替えてバブリングと対象水の循
環を行い、本発明の水処理接触材による浄化能力を確認
した。測定項目は上記と同じくCOD、BOD、T−
N、T−Pで、その測定結果を表8に示す。この表から
判るように、本発明の水処理接触材は低COD水に対し
ても顕著な浄化作用を示す。In the experimental apparatus shown in FIG. 5, the target water was replaced with river water having a low COD value, bubbling and circulation of the target water were performed, and the purification capacity of the water treatment contact material of the present invention was confirmed. Measurement items are COD, BOD, T-
Table 8 shows the measurement results for N and T-P. As can be seen from this table, the water treatment contact material of the present invention exhibits a remarkable purifying action even for low COD water.
【0042】[0042]
【表8】 [Table 8]
【0043】[0043]
【発明の効果】以上述べたように本発明の水処理接触材
によれば、多孔質の高炉水砕スラグを主原料とするの
で、処理水を中性に保つことが可能で、COD、BO
D、T−N、T−Pの除去性能も非常に良好である。ま
た、従来の水処理接触材は、高COD水に対してはその
除去率は高くとも、低COD水に対しては効果が少なか
ったが、本発明の水処理接触材は低COD水に対しても
十分な浄化作用を発揮するとともに、魚の生息に関して
も無害であることから、安全性の高いものである。更
に、主原料が高炉水砕スラグを1〜5mmに粒度調整し
たものであるので、安価に得られ、またバインダーも高
炉水砕微粉末、生石灰を使用するので、高炉水砕スラグ
の優れた生物化学的水処理性能及び気孔率を損なわずに
所要の形体に固化成形できるに加え、総合的に経済性に
富むとともに、軽量であるので作業性が良好である。As described above, according to the water treatment contact material of the present invention, since the porous blast furnace granulated slag is used as the main raw material, the treated water can be kept neutral, and COD, BO
The removal performance of D, T-N, and T-P is also very good. Further, although the conventional water treatment contact material has a high removal rate for high COD water, it has little effect on low COD water, but the water treatment contact material of the present invention is effective for low COD water. However, it has a high degree of safety because it exerts a sufficient purification action and is harmless to fish habitat. Furthermore, since the main raw material is granulated blast furnace slag whose particle size is adjusted to 1 to 5 mm, it can be obtained at a low cost, and since the binder also uses blast furnace granulated fine powder and quick lime, it is an excellent organism for granulated blast furnace slag. In addition to being able to be solidified and molded into a desired shape without impairing the chemical water treatment performance and porosity, it is highly economical overall and is light in weight, so workability is good.
【図1】本発明の主原料となる粒度調整した高炉水砕ス
ラグの現物写真である。FIG. 1 is an actual photograph of granulated blast furnace slag with a controlled particle size, which is the main raw material of the present invention.
【図2】本発明の水処理接触材の製造手順を示すフロー
チャートである。FIG. 2 is a flowchart showing a manufacturing procedure of the water treatment contact material of the present invention.
【図3】本発明の水処理接触材の一例の現物写真であ
る。FIG. 3 is an actual photograph of an example of the water treatment contact material of the present invention.
【図4】本発明の水処理接触材の性能試験例の示す説明
図である。FIG. 4 is an explanatory view showing a performance test example of the water treatment contact material of the present invention.
【図5】別の試験例の説明図である。FIG. 5 is an explanatory diagram of another test example.
【図6】更に別の試練例の説明図である。FIG. 6 is an explanatory diagram of still another trial example.
1 水処理接触材 2 角形容器 3 水槽 4 定量ポンプ 5 処理槽 6 エアーレーション装置 7 リサイクル処理水 1 Water Treatment Contact Material 2 Square Container 3 Water Tank 4 Metering Pump 5 Treatment Tank 6 Aeration Device 7 Recycled Water
───────────────────────────────────────────────────── フロントページの続き (72)発明者 服部 勝夫 千葉県君津市君津1番地 株式会社鐵原君 津支店内 (72)発明者 鍋倉 和則 千葉県君津市君津1番地 株式会社鐵原君 津支店内 (72)発明者 加藤 範行 千葉県君津市君津1番地 株式会社鐵原君 津支店内 (72)発明者 前川 洋司 東京都千代田区富士見1丁目4番4号 株 式会社鐵原内 (56)参考文献 特開 昭63−296891(JP,A) 特開 昭57−9840(JP,A) 特開 昭63−83231(JP,A) 特開 昭63−287596(JP,A) ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Katsuo Hattori 1 Kimitsu, Kimitsu-shi, Chiba Prefecture, in Tetsuhara Kimitsu Co., Ltd. (72) Inventor Noriyuki Kato 1 Kimitsu, Kimitsu-shi, Chiba Within Kumihara Kimitsu Branch (72) Inventor, Yoji Maekawa 1-4-4 Fujimi, Chiyoda-ku, Tokyo Iron and steel company (56) References JP-A-63-296891 (JP, A) JP-A-57-9840 (JP, A) JP-A-63-83231 (JP, A) JP-A-63-287596 (JP, A)
Claims (1)
砕スラグを主原料としてその1重量部に対し、高炉水砕
微粉末又はこれに生石灰を混合したものを水硬性バイン
ダーとして0.1〜0.4重量部添加し、調湿・混練
し、所要の形体に成型してなることを特徴とする水処理
接触材。1. A granulated blast-furnace slag having a particle size adjusted to 1 to 5 mm as a main raw material to 1 part by weight of the granulated blast-furnace pulverized powder or a mixture thereof with quick lime as a hydraulic binder. A water treatment contact material, characterized in that 1 to 0.4 parts by weight is added, the humidity is adjusted and kneaded, and the product is formed into a desired shape.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3232551A JPH0796115B2 (en) | 1991-08-21 | 1991-08-21 | Water treatment contact material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3232551A JPH0796115B2 (en) | 1991-08-21 | 1991-08-21 | Water treatment contact material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0550085A JPH0550085A (en) | 1993-03-02 |
| JPH0796115B2 true JPH0796115B2 (en) | 1995-10-18 |
Family
ID=16941102
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3232551A Expired - Lifetime JPH0796115B2 (en) | 1991-08-21 | 1991-08-21 | Water treatment contact material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0796115B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2471512C (en) * | 2001-03-29 | 2010-09-21 | Nippon Steel Chemical Co., Ltd. | Acidic-wastewater treating material and method of treating acidic wastewater |
| CN116603998A (en) * | 2023-05-19 | 2023-08-18 | 攀钢集团攀枝花钢铁研究院有限公司 | Alloy cushion block for large walking beam type heating furnace and preparation method thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0671597B2 (en) * | 1987-05-28 | 1994-09-14 | 新日本製鐵株式会社 | Method for producing immobilized carrier for microorganisms |
-
1991
- 1991-08-21 JP JP3232551A patent/JPH0796115B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0550085A (en) | 1993-03-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN112441804B (en) | A preparation method of phosphorus and nitrogen removal type biological filter material and its application in integrated rural domestic sewage treatment equipment | |
| CN103910503B (en) | The unburned method of granulating of a kind of sludge solidification | |
| KR100798893B1 (en) | Manufacturing method of concrete product using sludge | |
| JP2008263928A (en) | Soil Block for Sone Installation | |
| KR20020067084A (en) | Water processing system and processing material of high adsorption | |
| CN106044919A (en) | Method for increasing ammonium nitrogen in river water | |
| KR100994335B1 (en) | Manufacturing methods of water purification concrete using micro-organisms and solution | |
| JPH0796115B2 (en) | Water treatment contact material | |
| JP2001113165A (en) | Adsorbent | |
| JPH0796116B2 (en) | Water treatment contact material | |
| JPH0434479B2 (en) | ||
| WO1995025586A1 (en) | Dephosphorizing material and dephosphorizing method | |
| JP2000117020A (en) | Contact purifying material and its production | |
| JP2007054732A (en) | Sewage treatment material and its production method | |
| JP2001121179A (en) | Porous cleaning material and method for manufacturing the same | |
| JP3240480B2 (en) | Filter media for sewage purification | |
| JP2000070960A (en) | Dephosphorization material produced by utilizing building waste | |
| JPH0971777A (en) | Neutralization method for solidification of sludge and soft soil | |
| JP3308196B2 (en) | Manufacturing method of phosphorus removal material | |
| JP3249945B2 (en) | Concrete with water purification ability | |
| JPH0155914B2 (en) | ||
| JP3480668B2 (en) | Porous concrete member for water purification for phosphorus removal | |
| CN106477725A (en) | A kind of artificial swamp compounded mix for rural domestic sewage treatment | |
| JP3338414B2 (en) | Sashimi block with water purification ability | |
| JPH0378157B2 (en) |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 19960409 |