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JPH0729105B2 - Water treatment method - Google Patents

Water treatment method

Info

Publication number
JPH0729105B2
JPH0729105B2 JP61164178A JP16417886A JPH0729105B2 JP H0729105 B2 JPH0729105 B2 JP H0729105B2 JP 61164178 A JP61164178 A JP 61164178A JP 16417886 A JP16417886 A JP 16417886A JP H0729105 B2 JPH0729105 B2 JP H0729105B2
Authority
JP
Japan
Prior art keywords
particles
water
treatment
specific gravity
microorganism
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
Application number
JP61164178A
Other languages
Japanese (ja)
Other versions
JPS6320097A (en
Inventor
千明 丹羽
惠之輔 小島
諭 神笠
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.)
Showa Kagaku Kogyo Co Ltd
Shimizu Corp
Original Assignee
Showa Kagaku Kogyo Co Ltd
Shimizu Corp
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 Showa Kagaku Kogyo Co Ltd, Shimizu Corp filed Critical Showa Kagaku Kogyo Co Ltd
Priority to JP61164178A priority Critical patent/JPH0729105B2/en
Publication of JPS6320097A publication Critical patent/JPS6320097A/en
Publication of JPH0729105B2 publication Critical patent/JPH0729105B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は、水溶液を生物学的に処理する水処理法、特に
廃水処理に好適な水処理法に関するものである。
TECHNICAL FIELD The present invention relates to a water treatment method for biologically treating an aqueous solution, and particularly to a water treatment method suitable for wastewater treatment.

「従来技術とその問題点」 生物学的な廃水処理法の一つに、微生物を粒子に担持さ
せ、この粒子(以下、微生物担持粒子と称する)を処理
槽内で流動させて廃水処理を行う流動懸濁型の処理法が
ある。
"Prior art and its problems" As one of biological wastewater treatment methods, microorganisms are supported on particles, and the particles (hereinafter referred to as microorganism-supported particles) are fluidized in a treatment tank to perform wastewater treatment. There is a fluid suspension type processing method.

第2図は、流動懸濁型の処理法を実施する装置の一例を
示すもので、図中符号11は外筒である。この外筒11は有
底円筒状のもので、その内部には同軸的に内筒12が設け
られている。この内筒12は上端および下端が開口した筒
状のものである。外筒11の下部には、内筒12の下方に位
置する曝気部材13が設けられており、ブロア14で加圧さ
れた気体が曝気されるようになっている。そして、この
装置内の被処理水は、図中矢印で示すように、流動され
ている。
FIG. 2 shows an example of an apparatus for carrying out a fluid suspension type processing method, in which reference numeral 11 is an outer cylinder. The outer cylinder 11 has a bottomed cylindrical shape, and an inner cylinder 12 is coaxially provided inside the outer cylinder 11. The inner cylinder 12 has a cylindrical shape with an open upper end and a lower end. An aeration member 13 located below the inner cylinder 12 is provided below the outer cylinder 11 so that the gas pressurized by the blower 14 is aerated. The water to be treated in this device is flowing as shown by the arrow in the figure.

従来、流動懸濁型の廃水処理法には、被処理水重い微生
物担持粒子か、あるいは被処理水より軽い微生物担持粒
子のいずれか一方のみが用いられていた。
Conventionally, in the fluidized suspension type wastewater treatment method, only either the microorganism-supporting particles that are heavy to be treated or the microorganism-bearing particles that are lighter than the water to be treated have been used.

比重の大きな粒子を用いて廃水を処理する場合には、粒
子を主に内筒12内で上昇流によって浮遊させ、外筒部で
は液流とともに下降させるようにしていた。
When the wastewater is treated using particles having a large specific gravity, the particles are mainly floated by the ascending flow in the inner cylinder 12 and are lowered by the liquid flow in the outer cylinder part.

また、比重の小さな粒子を用いる場合には、外筒11と内
筒12の間に粒子を投入し、下降流によって粒子の浮上を
阻止して、粒子を内外筒間の被処理水中に懸濁するよう
にしていた。
When using particles having a small specific gravity, the particles are charged between the outer cylinder 11 and the inner cylinder 12 to prevent the particles from floating due to the downward flow, and the particles are suspended in the water to be treated between the inner and outer cylinders. I was trying to do it.

ところが、上記従来の廃水処理法では、微生物担持粒子
を被処理水中に懸濁するために被処理水を高速で流動さ
せねばならず、装置の運転にコストが嵩む問題があっ
た。また、このような従来の廃水処理法では、粒子を多
量に投入すると粒子の一部が沈降し流動懸濁しなかった
り、さらには全く流動しなかったり、あるいは完全に浮
上してしまい廃水との接触が低下したりするため、有効
に懸濁できる粒子の量が制限され、その結果、廃水処理
の効率を向上できない不満があった。特に、従来使用に
供することができた比重が1より大きい粒子は、砂、活
性炭、アンスラサイトの如く比重2以上のものが多く、
水の比重1よりもかなり重いため、循環流動エネルギー
が多大となる欠点があった。
However, in the above-mentioned conventional wastewater treatment method, in order to suspend the microorganism-supported particles in the water to be treated, the water to be treated must be made to flow at a high speed, and there is a problem that the cost of operating the apparatus increases. In addition, in such a conventional wastewater treatment method, when a large amount of particles are added, a part of the particles settles and does not flow and suspend, or does not flow at all, or completely floats and comes into contact with wastewater. However, the amount of particles that can be effectively suspended is limited, and as a result, the efficiency of wastewater treatment cannot be improved. In particular, many particles having a specific gravity of more than 1 that can be conventionally used are those having a specific gravity of 2 or more such as sand, activated carbon and anthracite.
Since the specific gravity of water is considerably heavier than 1, there is a drawback that the circulating fluid energy becomes large.

本発明者らは、このような問題に対処するため、水とか
なり近い見掛け比重(水が含浸された状態での見掛け比
重)に調整でき、かつ微生物担持能力の優れた浮遊性造
粒物を開発した。この浮遊性造粒物は、被処理溶液より
も見掛け比重が小さい芯材と、被処理溶液よりも比重が
大きい親液性多孔質粉体とからなり、芯材に多孔質粉体
からなる被覆が施されたもの、および芯材と多孔質粉体
が混合されてなるものである。この浮遊性造粒物は、水
とほぼ等しい比重に調整でき、被処理水中に容易に懸濁
し得るので、上記問題に対処できる。
In order to deal with such a problem, the present inventors have prepared a floating granule that can be adjusted to an apparent specific gravity (apparent specific gravity in a state of being impregnated with water) that is quite close to that of water, and that has an excellent ability to support microorganisms. developed. This floating granule is composed of a core material having an apparent specific gravity smaller than that of the solution to be treated and a lyophilic porous powder having a specific gravity larger than that of the solution to be treated, and the core material is coated with the porous powder. And a mixture of a core material and a porous powder. This floating granule can be adjusted to have a specific gravity almost equal to that of water and can be easily suspended in the water to be treated, so that the above problem can be addressed.

ところが、このような浮遊性造粒物を実際に製造する場
合、その比重を厳密に管理すると生産の歩留りが悪化す
る問題がある。そこで、造粒物の比重の管理を緩める
と、造粒物の重さのバラツキが大きくなり、全部の微生
物担持粒子を被処理水中に十分懸濁させて廃水処理に供
するには、廃水処理装置を微妙に制御しなければなら
ず、装置の運転が難しくなる問題があった。
However, when such a floating granule is actually manufactured, if the specific gravity is strictly controlled, there is a problem that the production yield is deteriorated. Therefore, if the control of the specific gravity of the granules is loosened, the dispersion of the weight of the granules will increase, and in order to sufficiently suspend all the microorganism-supporting particles in the water to be treated and provide them for wastewater treatment, a wastewater treatment device Had to be controlled delicately, which made it difficult to operate the device.

「問題点を解決するための手段」 そこで、本発明の水処理法では、処理槽として、水が含
浸された状態で約1〜1.3の見掛け比重を有する微生物
担持粒子を投入される処理槽と、約0.7〜1の見掛け比
重を有する微生物担持粒子が投入される処理槽を設けて
水処理すると共に、これら処理槽で使用されて後述する
理由により流動懸濁し得ない状態となった微生物担持粒
子を各槽から引き抜き、あるいは一定量を各槽から定期
的に引き抜き、この引き抜かれた微生物担持粒子に剪断
力を加えて肥大化した生物膜を剥離して粒子を再生し、
この再生された微生物担持粒子を比重分離して、上記2
種類の処理槽のいずれかに返送することによって、上記
問題点の解決を図った。
"Means for solving the problem" Therefore, in the water treatment method of the present invention, as a treatment tank, a treatment tank in which microbial-supported particles having an apparent specific gravity of about 1 to 1.3 in the state of being impregnated with water are added. , Provided with treatment tanks into which microorganism-supporting particles having an apparent specific gravity of about 0.7 to 1 are placed, and performing water treatment, and microorganism-supporting particles used in these treatment tanks in a state in which they cannot be fluidized and suspended due to the reason described below. From each tank, or a fixed amount is regularly extracted from each tank, the extracted microorganism-carrying particles are subjected to shearing force to remove the enlarged biofilm to regenerate the particles,
The regenerated microorganism-supporting particles are separated by specific gravity to obtain the above-mentioned 2
The above problem was solved by returning to one of the processing tanks of the type.

「実施例」 以下、図面を参照して本発明の水処理法を詳しく説明す
る。
"Example" Hereinafter, the water treatment method of the present invention will be described in detail with reference to the drawings.

第1図は、本発明の水処理法を実施するのに好適な処理
装置の概略構成を示すもので、図中符号1、2は処理
槽、符号3は再生装置、符号4は分離装置である。処理
槽1,2のうち一方の処理槽1は、水が含浸された状態で
約1〜1.3の見掛け比重を有する微生物担持粒子が投入
される槽である。また、他方の処理槽2は、水が含浸さ
れた状態で約1〜0.7の見掛け比重を有する微生物担持
粒子が投入される槽である。これら処理槽1,2には、同
一構造のものを利用できるが、一般的には構造の異なっ
たものが用いられる。
FIG. 1 shows a schematic configuration of a treatment apparatus suitable for carrying out the water treatment method of the present invention. In the figure, reference numerals 1 and 2 are treatment tanks, reference numeral 3 is a regenerator, and reference numeral 4 is a separator. is there. One of the processing tanks 1 and 2 is a tank into which the microorganism-supporting particles having an apparent specific gravity of about 1 to 1.3 are added while being impregnated with water. The other treatment tank 2 is a tank into which microorganism-supporting particles having an apparent specific gravity of about 1 to 0.7 are added while being impregnated with water. The treatment tanks 1 and 2 can have the same structure, but generally have different structures.

上記、再生装置3は、微生物担持粒子を板体に衝突させ
たり、水エジェクタや機械攪拌で掻き回すことによっ
て、粒子表面に成長した生物膜を剥離するものである。
また、上記分離装置4は、比重によって粒子を分離する
装置である。これら再生装置3および分離装置4は、独
立して設けられても、一体に設けられても良い。
The above-mentioned regeneration device 3 is for peeling the biofilm grown on the particle surface by colliding the microbial-supported particles with the plate or by agitating with a water ejector or mechanical stirring.
The separating device 4 is a device that separates particles by specific gravity. The reproducing device 3 and the separating device 4 may be provided independently or integrally.

次に、上記処理装置によって実施される本発明の水処理
法について説明する。
Next, the water treatment method of the present invention carried out by the above treatment apparatus will be described.

まず、本発明の水処理法には、水が含浸された状態で約
1.3〜0.7の見掛け比重を有する微生物担持粒子が用いら
れる。この微生物担持粒子は、まず分離装置4に投入さ
れる。この分離装置4には、比重が約1である水などが
収容されており、投入された粒子のうち比重1よりも大
のものは沈降し、小のものは浮上して互いに分離され
る。そして、沈降した粒子は分離装置4の下部から引き
抜かれて処理槽1に送られ、浮上した粒子は上部から引
き抜かれて処理槽2に送られる。各槽1,2に送られた粒
子は、それぞれ目的とする処理に供される(水処理工
程)。ここで見掛け比重1とは、厳密に管理する必要は
なく、ある範囲の比重の粒子はいずれの処理槽1,2に投
入されても良い。
First, the water treatment method of the present invention is about
Microorganism-supporting particles having an apparent specific gravity of 1.3 to 0.7 are used. The microorganism-supporting particles are first put into the separation device 4. The separator 4 contains water having a specific gravity of about 1, and the particles having a specific gravity of more than 1 are settled and the particles having a smaller specific gravity float and are separated from each other. Then, the settled particles are extracted from the lower part of the separating device 4 and sent to the processing tank 1, and the floating particles are extracted from the upper part and sent to the processing tank 2. The particles sent to the tanks 1 and 2 are each subjected to the intended treatment (water treatment step). Here, the apparent specific gravity 1 does not need to be strictly controlled, and particles having a specific gravity within a certain range may be put into any of the processing tanks 1 and 2.

各処理槽1,2で処理に供された粒子は、その表面に成長
した生物膜(比重1.05程度)や、生物膜内に取り込まれ
たCO2やN2などの生成ガスなどによって、その比重が徐
々に初期のものと異なってくる。このような比重が変化
して、各槽1,2で流動懸濁し難くなった粒子は、槽1,2の
上部に浮上しあるいは下部に沈降する。このように浮上
・沈降した微生物担持粒子は、間欠的あるいは連続的に
槽1,2から引き抜かれて、再生装置3に送られる。
Particles treated in each treatment tank 1 and 2 have a specific gravity due to the biofilm that has grown on the surface (specific gravity of about 1.05) and the generated gases such as CO 2 and N 2 that are taken into the biofilm. Gradually becomes different from the initial one. Particles whose specific gravity has changed and are difficult to flow and suspend in the tanks 1 and 2 float to the upper part of the tanks 1 and 2 or settle to the lower part. The microorganism-supporting particles thus floated / settled are withdrawn intermittently or continuously from the tanks 1 and 2 and sent to the regenerator 3.

再生装置3では、微生物担持粒子を板体に衝突させた
り、水エジェクタや機械攪拌で掻き回すことによって剪
断力を加え、肥大化した生物膜を剥離して、粒子を再生
する(再生工程)。
In the regenerator 3, the microorganism-supporting particles are collided with the plate or agitated by a water ejector or mechanical stirring to apply a shearing force to peel off the enlarged biofilm and regenerate the particles (regeneration step).

こうして再生された微生物担持粒子は、再び分離装置4
で比重分離されて、上記2種類の処理槽1,2のいずれか
に返送される(分離返送工程)。また、再生時に剥離さ
れた生物膜は、余剰汚泥として再生装置3等から引き抜
かれて適宜処理される。
The microorganism-supported particles thus regenerated are separated again by the separation device 4
The specific gravity is then separated and returned to either of the above two types of processing tanks 1 and 2 (separation returning step). In addition, the biofilm that has been peeled off during regeneration is extracted as excess sludge from the regeneration device 3 or the like and appropriately treated.

「作用」 このような水処理法によれば、水よりも若干大きな比重
を有する粒子から若干小さな比重を有する粒子までが混
在する微生物担持粒子を用いて水処理を行っても、各粒
子は常に流動懸濁し易い運転条件の処理槽1,2に導入さ
れて処理に供されることとなる。
[Operation] According to such a water treatment method, even if water treatment is performed using a microorganism-supporting particle in which particles having a slightly larger specific gravity than particles having a slightly smaller specific gravity than water are mixed, each particle is always It is introduced into the treatment tanks 1 and 2 under operating conditions where it is easily fluidized and suspended, and is used for treatment.

従って、本発明の水処理法によれば、各処理槽1,2には
性向の揃った粒子が供給されるので、各槽1,2に供給さ
れた粒子と被処理水とが十分懸濁し得る運転条件を容易
に決定できることとなる。
Therefore, according to the water treatment method of the present invention, since particles having a uniform tendency are supplied to the respective treatment tanks 1 and 2, the particles supplied to the respective tanks 1 and 2 and the water to be treated are sufficiently suspended. The operating conditions to be obtained can be easily determined.

なお、本発明の水処理法は、好気性の処理法、嫌気性の
処理法のいずれでも実施することができる。その場合、
一方の処理槽で嫌気性処理を行い、他方の処理槽で好気
性処理を行うこともできる。
The water treatment method of the present invention can be carried out by either an aerobic treatment method or an anaerobic treatment method. In that case,
It is also possible to perform anaerobic treatment in one treatment tank and aerobic treatment in the other treatment tank.

また、本発明の水処理法によれば、廃水の有機成分の好
気或は嫌気除去、硝化、脱窒などを行えることは勿論で
ある。
Further, according to the water treatment method of the present invention, it is needless to say that aerobic or anaerobic removal of organic components of waste water, nitrification, denitrification, etc. can be performed.

さらに、本発明の水処理法は上記実施例に限られるもの
ではなく、例えば各槽からの微生物担持粒子の引き抜き
は、一定量を定期的に行うようにしても良い。
Furthermore, the water treatment method of the present invention is not limited to the above-mentioned embodiment, and for example, the withdrawal of the microorganism-supporting particles from each tank may be performed at a fixed amount on a regular basis.

「発明の効果」 以上説明したように、本発明の水処理法は、水とかなり
近似する重さを有する微生物担持粒子を用い、水より大
きな比重を有する微生物担持粒子を投入する処理槽と、
水より小さな比重を有する微生物担持粒子を投入する処
理槽を設けて水処理すると共に、これら処理槽で使用さ
れて比重が変わり流動し得なくなった粒子を各槽から引
き抜き、この引き抜かれた微生物担持粒子に剪断力を加
えて成長した生物膜を剥離、再生し、この再生された微
生物担持粒子を比重分離して、上記2種類の処理槽のい
ずれかに返送する処理法なので、少ないエネルギーで微
生物を流動懸濁させることができる。よって、この水処
理法によれば、水処理を経済的に行うことができると共
に、多量の微生物担持粒子を流動懸濁せしめることがで
きるので、単位体積当たりに廃水処理率を高め廃水処理
装置の小形化を実現できる。
"Effects of the Invention" As described above, the water treatment method of the present invention uses a microorganism-supporting particle having a weight substantially similar to that of water, and a treatment tank for introducing a microorganism-supporting particle having a specific gravity larger than water,
A treatment tank for introducing microbe-supported particles having a specific gravity smaller than that of water is provided for water treatment, and the particles used in these treatment tanks whose specific gravity has changed and cannot flow are drawn out from each tank, and the extracted microbe-supported The biofilm grown by applying shearing force to the particles is peeled off and regenerated, and the regenerated microorganism-supporting particles are separated by specific gravity and returned to either of the above two types of treatment tanks, so the microorganisms can be consumed with less energy. Can be fluidly suspended. Therefore, according to this water treatment method, it is possible to economically perform the water treatment, and it is possible to fluidize and suspend a large amount of the microorganism-supporting particles, so that the wastewater treatment rate can be increased per unit volume of the wastewater treatment apparatus. It can be miniaturized.

また、本発明の水処理法では、各処理槽には性向の整っ
た粒子が供給されるので、被処理水と微生物担持粒子と
を十分懸濁する運転条件を容易に決定でき、よって処理
装置の運転が容易となる。
Further, in the water treatment method of the present invention, since particles having a well-balanced tendency are supplied to each treatment tank, it is possible to easily determine the operating conditions for sufficiently suspending the water to be treated and the microorganism-supporting particles, and thus the treatment apparatus. Driving becomes easier.

また、本発明の水処理法によれば、見掛け比重(水が含
浸された状態での見掛け比重)が1前後のものが混在す
る微生物担持粒子を水処理に用いることができることと
なるので、微生物担持粒子を製造する際、その比重を厳
密に管理する必要がなくなり、微生物担持粒子の生産の
歩留りを向上することができる。
Further, according to the water treatment method of the present invention, it is possible to use the microorganism-supporting particles in which apparent specific gravity (apparent specific gravity in a state of being impregnated with water) of about 1 is mixed in the water treatment. When manufacturing the supported particles, it is not necessary to strictly control the specific gravity thereof, and the yield of production of the microorganism-supported particles can be improved.

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

第1図は本発明の水処理法の一例を実施するのに好適な
処理装置を示す概略構成図、第2図は従来の水処理法で
使用されていた処理装置の一例を示す断面図である。 1,2…処理槽、3…再生装置、4…分離装置。
FIG. 1 is a schematic configuration diagram showing a treatment apparatus suitable for carrying out an example of the water treatment method of the present invention, and FIG. 2 is a sectional view showing an example of a treatment apparatus used in a conventional water treatment method. is there. 1, 2 ... Treatment tank, 3 ... Regeneration device, 4 ... Separation device.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】微生物を担持した微生物担持粒子を処理槽
内に投入して、これを被処理水と共に流動懸濁させて水
溶液を処理する水処理法において、 処理槽を2種類設け、一方の処理槽に水が含浸された状
態で約1〜1.3の見掛け比重を有する微生物担持粒子を
投入し、他方の処理槽に水が含浸された状態で約0.7〜
1の見掛け比重を有する微生物担持粒子を投入して被処
理水の処理を行う水処理工程と、 これら処理槽から微生物担持粒子を引き抜き、この引き
抜かれた微生物担持粒子に剪断力を加え肥大化した生物
膜を剥離して粒子を再生する再生工程と、 再生された微生物担持粒子を比重分離して、上記処理槽
に返送する分離工程とからなることを特徴とする水処理
法。
1. A water treatment method in which microorganism-supporting particles supporting microorganisms are put into a treatment tank, and the suspension is flow-suspended together with water to be treated to treat an aqueous solution. Two kinds of treatment tanks are provided, and one of the treatment tanks is provided. Microorganism-supporting particles having an apparent specific gravity of about 1 to 1.3 are charged in a treatment tank impregnated with water, and about 0.7 to about 0.7 in a state where the other treatment tank is impregnated with water.
A water treatment process in which microbial-supported particles having an apparent specific gravity of 1 are introduced to treat the water to be treated, and the microbial-supported particles are extracted from these treatment tanks, and the extracted microbial-supported particles are subjected to a shearing force to be enlarged. A water treatment method comprising a regeneration step of regenerating particles by peeling off a biofilm and a separation step of separating the regenerated microorganism-supported particles by specific gravity and returning them to the treatment tank.
JP61164178A 1986-07-12 1986-07-12 Water treatment method Expired - Lifetime JPH0729105B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61164178A JPH0729105B2 (en) 1986-07-12 1986-07-12 Water treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61164178A JPH0729105B2 (en) 1986-07-12 1986-07-12 Water treatment method

Publications (2)

Publication Number Publication Date
JPS6320097A JPS6320097A (en) 1988-01-27
JPH0729105B2 true JPH0729105B2 (en) 1995-04-05

Family

ID=15788197

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61164178A Expired - Lifetime JPH0729105B2 (en) 1986-07-12 1986-07-12 Water treatment method

Country Status (1)

Country Link
JP (1) JPH0729105B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100535801C (en) 2002-09-19 2009-09-02 西铁城控股株式会社 Electronic clock
AU2010271391B2 (en) 2009-07-08 2015-12-10 Saudi Arabian Oil Company Low concentration wastewater treatment system and process
WO2011005928A1 (en) 2009-07-08 2011-01-13 Saudi Arabian Oil Company Wastewater treatment system and process including irradiation of primary solids

Also Published As

Publication number Publication date
JPS6320097A (en) 1988-01-27

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