JPS6352557B2 - - Google Patents
Info
- Publication number
- JPS6352557B2 JPS6352557B2 JP18997784A JP18997784A JPS6352557B2 JP S6352557 B2 JPS6352557 B2 JP S6352557B2 JP 18997784 A JP18997784 A JP 18997784A JP 18997784 A JP18997784 A JP 18997784A JP S6352557 B2 JPS6352557 B2 JP S6352557B2
- Authority
- JP
- Japan
- Prior art keywords
- wastewater
- flocculant
- microorganisms
- treatment agent
- flocs
- 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
Links
- 239000003795 chemical substances by application Substances 0.000 claims description 17
- 238000004065 wastewater treatment Methods 0.000 claims description 15
- 239000002351 wastewater Substances 0.000 claims description 12
- 229920000642 polymer Polymers 0.000 claims description 7
- 239000010802 sludge Substances 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 6
- 244000005700 microbiome Species 0.000 description 18
- 230000000694 effects Effects 0.000 description 15
- 239000000499 gel Substances 0.000 description 15
- 241000894006 Bacteria Species 0.000 description 13
- 238000006116 polymerization reaction Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 9
- 238000005273 aeration Methods 0.000 description 8
- 229920002401 polyacrylamide Polymers 0.000 description 8
- 239000000178 monomer Substances 0.000 description 5
- 239000003505 polymerization initiator Substances 0.000 description 5
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical group NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 241000244206 Nematoda Species 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 239000003431 cross linking reagent Substances 0.000 description 3
- 206010014881 enterobiasis Diseases 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- MTPJEFOSTIKRSS-UHFFFAOYSA-N 3-(dimethylamino)propanenitrile Chemical compound CN(C)CCC#N MTPJEFOSTIKRSS-UHFFFAOYSA-N 0.000 description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 2
- 239000000783 alginic acid Substances 0.000 description 2
- 235000010443 alginic acid Nutrition 0.000 description 2
- 229920000615 alginic acid Polymers 0.000 description 2
- 229960001126 alginic acid Drugs 0.000 description 2
- 150000004781 alginic acids Chemical class 0.000 description 2
- 229920006318 anionic polymer Polymers 0.000 description 2
- 239000000679 carrageenan Substances 0.000 description 2
- 235000010418 carrageenan Nutrition 0.000 description 2
- 229920001525 carrageenan Polymers 0.000 description 2
- 229940113118 carrageenan Drugs 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000008394 flocculating agent Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- -1 polyoxyethylene Polymers 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 229920001059 synthetic polymer Polymers 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- UHVMMEOXYDMDKI-JKYCWFKZSA-L zinc;1-(5-cyanopyridin-2-yl)-3-[(1s,2s)-2-(6-fluoro-2-hydroxy-3-propanoylphenyl)cyclopropyl]urea;diacetate Chemical compound [Zn+2].CC([O-])=O.CC([O-])=O.CCC(=O)C1=CC=C(F)C([C@H]2[C@H](C2)NC(=O)NC=2N=CC(=CC=2)C#N)=C1O UHVMMEOXYDMDKI-JKYCWFKZSA-L 0.000 description 2
- 241000589565 Flavobacterium Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- KWYHDKDOAIKMQN-UHFFFAOYSA-N N,N,N',N'-tetramethylethylenediamine Chemical compound CN(C)CCN(C)C KWYHDKDOAIKMQN-UHFFFAOYSA-N 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- 229920002873 Polyethylenimine Polymers 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 241000589516 Pseudomonas Species 0.000 description 1
- 241000700141 Rotifera Species 0.000 description 1
- 208000002474 Tinea Diseases 0.000 description 1
- 241000893966 Trichophyton verrucosum Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 229920006317 cationic polymer Polymers 0.000 description 1
- 229920001577 copolymer Chemical class 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000037406 food intake Effects 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 1
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 1
- 231100001231 less toxic Toxicity 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- ZIUHHBKFKCYYJD-UHFFFAOYSA-N n,n'-methylenebisacrylamide Chemical compound C=CC(=O)NCNC(=O)C=C ZIUHHBKFKCYYJD-UHFFFAOYSA-N 0.000 description 1
- UBTYFVJZTZYJHZ-UHFFFAOYSA-N n-[2-(prop-2-enoylamino)propyl]prop-2-enamide Chemical compound C=CC(=O)NC(C)CNC(=O)C=C UBTYFVJZTZYJHZ-UHFFFAOYSA-N 0.000 description 1
- CHDKQNHKDMEASZ-UHFFFAOYSA-N n-prop-2-enoylprop-2-enamide Chemical compound C=CC(=O)NC(=O)C=C CHDKQNHKDMEASZ-UHFFFAOYSA-N 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 description 1
- 229920002717 polyvinylpyridine Polymers 0.000 description 1
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 description 1
- KAQHZJVQFBJKCK-UHFFFAOYSA-L potassium pyrosulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OS([O-])(=O)=O KAQHZJVQFBJKCK-UHFFFAOYSA-L 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 238000007717 redox polymerization reaction Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical class [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1205—Particular type of activated sludge processes
- C02F3/1215—Combinations of activated sludge treatment with precipitation, flocculation, coagulation and separation of phosphates
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
- C02F3/105—Characterized by the chemical composition
- C02F3/108—Immobilising gels, polymers or the like
-
- 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
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- 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、廃水中の有機物質を微生物学的に分
解除去するための活性の高い廃水の処理剤に関す
る。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a highly active wastewater treatment agent for microbiologically decomposing and removing organic substances in wastewater.
従来の技術
廃水中の有機物質を分解するには、従来、微生
物(Pseudomonas、Flavobacterium)のフロツ
クを曝気槽内に浮遊させて用いる浮遊型活性汚泥
法又は微生物を膜の形で用いる接触曝気法、回転
円板法或いは散水床法等が実施されている。こ
のような方法では、微生物が廃水と直接接触する
ために、細菌を摂食する廃水中の大型の生物であ
る糸ミミズ、輪虫、つりがね虫等により微生物が
食べられ、微生物の量が減少し、廃水中の有機物
質を長期間安定して分解できないという欠点があ
つた。Conventional technology To decompose organic substances in wastewater, conventional methods include a floating activated sludge method in which flocs of microorganisms (Pseudomonas, Flavobacterium) are suspended in an aeration tank, or a contact aeration method in which microorganisms are used in the form of a membrane. The rotating disk method, the sprinkled bed method, etc. are used. In this method, since the microorganisms come into direct contact with the wastewater, the microorganisms are eaten by large organisms in the wastewater that feed on bacteria, such as threadworms, rotifers, and ringworms, and the amount of microorganisms is reduced. The drawback was that organic substances in wastewater could not be stably decomposed over a long period of time.
また、最近、各種の菌をポリアクリルアミド等
の合成ポリマー、カラギーナン、アルギン酸のゲ
ルに包括固定した廃水処理剤が提案されている。 Recently, wastewater treatment agents have been proposed in which various bacteria are encased and immobilized in gels of synthetic polymers such as polyacrylamide, carrageenan, and alginic acid.
発明が解決しようとする問題点
これらのゲルに菌を固定化した処理剤では、比
較的大型の微生物に菌が摂食される欠点は解消さ
れるが、固定化した菌の活性低下及び長期間廃水
処理に用いた際の耐久性が問題となる。Problems to be Solved by the Invention These treatment agents in which bacteria are immobilized in gel solve the disadvantage that bacteria are eaten by relatively large microorganisms, but the activity of the immobilized bacteria decreases and the long-term Durability is an issue when used for wastewater treatment.
カラギーナンやアルギン酸等の自然界に存在す
る毒性の少ない物質をゲルとして使用した場合に
は、固定した菌の活性低下は軽微であるが、物理
的強度が小さく、耐久性に問題がある。 When a naturally occurring less toxic substance such as carrageenan or alginic acid is used as a gel, the activity of immobilized bacteria is only slightly reduced, but the gel has low physical strength and durability.
一方、ポリアクリルアミドゲルを使用した場合
には、物理的強度は大きく、耐久性は良いが、固
定化する際に使用するアクリルアミドモノマー、
架橋剤、重合開始剤等が菌に毒性作用を及ぼすの
で、活性低下を招きやすいという欠点がある。 On the other hand, when polyacrylamide gel is used, it has high physical strength and good durability, but the acrylamide monomer used for immobilization,
Since the crosslinking agent, polymerization initiator, etc. exert a toxic effect on bacteria, there is a drawback that the activity tends to decrease.
従つて、本発明は、ポリアクリルアミドゲル等
の合成ポリマーゲルの内部に包括固定する際に使
用されるモノマー及び添加剤の毒性作用を出来る
だけ少なくして、活性の高い処理剤を提供するこ
とを目的とする。 Therefore, the present invention aims to minimize the toxic effects of monomers and additives used for entrapping immobilization inside synthetic polymer gels such as polyacrylamide gels, and to provide highly active processing agents. purpose.
問題点を解決するための手段
本発明による廃水の処理剤は、凝集剤を用いて
活性汚泥をフロツク状に凝集させ、得られた凝集
物をポリマーゲル内部に包括固定して成ることを
特徴とする。Means for Solving the Problems The wastewater treatment agent according to the present invention is characterized in that activated sludge is flocculated into flocs using a flocculant, and the resulting flocs are encased and fixed inside a polymer gel. do.
本発明の廃水の処理剤は、活性汚泥に凝集剤を
添加してフロツク状に凝集させ、得られた凝集物
をポリマーゲル内部に包活固定することによつて
製造することができる。 The wastewater treatment agent of the present invention can be produced by adding a flocculant to activated sludge to flocculate it into flocs, and then encasing and fixing the resulting flocs inside a polymer gel.
凝集剤は無機又は有機凝集剤であつてよい。無
機凝集剤としては、硫酸アルミニウム、硫酸第二
鉄、任意の公知無機凝集剤を使用することができ
る。有機凝集剤は、カチオン性、アニオン性及び
ノニオン性の高分子凝集剤のいずれでもよい。カ
チオン性高分子凝集剤としては、例えばポリビニ
ルピリジン塩酸塩、ポリエチレンイミン等が挙げ
られ、アニオン性高分子凝集剤としては、ポリア
クリル酸ナトリウム、マレイン酸共重合物塩、ポ
リアクリルアミド部分加水分解物塩等が挙げられ
る。また、ノニオン性高分子凝集剤としては、ポ
リアクリルアミド、ポリオキシエチレン等が挙げ
られる。 The flocculant may be an inorganic or organic flocculant. As the inorganic flocculant, aluminum sulfate, ferric sulfate, or any known inorganic flocculant can be used. The organic flocculant may be any of cationic, anionic, and nonionic polymer flocculants. Examples of the cationic polymer flocculant include polyvinylpyridine hydrochloride and polyethyleneimine, and examples of the anionic polymer flocculant include sodium polyacrylate, maleic acid copolymer salt, and polyacrylamide partial hydrolyzate salt. etc. Furthermore, examples of the nonionic polymer flocculant include polyacrylamide, polyoxyethylene, and the like.
本発明においては、前記のような凝集剤を用い
て活性汚泥を100μm以上の大きさのフロツク状の
凝集剤に凝集させるのが好ましい。 In the present invention, it is preferable to use the above-mentioned flocculant to flocculate activated sludge into a flocculant having a size of 100 μm or more.
こうして得られた凝集物を固定化するには、ア
クリルアミド等のモノマー、架橋剤、重合促進剤
等を含む溶液に凝集菌と重合開始剤を混合し、重
合反応を行わせる。 In order to immobilize the aggregate thus obtained, the aggregated bacteria and a polymerization initiator are mixed in a solution containing a monomer such as acrylamide, a crosslinking agent, a polymerization promoter, etc., and a polymerization reaction is performed.
重合方法としては、モノマーの性質により、ラ
ジカル重合、放射線重合、レドツクス重合等、公
知方法を使用することができる。 As the polymerization method, known methods such as radical polymerization, radiation polymerization, redox polymerization, etc. can be used depending on the properties of the monomer.
本発明においてポリマーゲルとしては、ポリア
クリルアミド、光硬化性樹脂等のゲルを使用する
ことができるが、以下に、ポリアクリルアミドゲ
ルを使用する場合について説明する。 In the present invention, gels such as polyacrylamide and photocurable resin can be used as the polymer gel, and the case where polyacrylamide gel is used will be described below.
アクリルアミドの架橋剤としては、N,N′―
メチレンビスアクリルアミド、N,N′―プロピ
レンビスアクリルアミド、ジアクリルアミドジメ
チルエーテル、1,2―ジアクリルアミドエチレ
ングリコール又は、N,N′―ジアクリル酒石酸
ジアミド等を使用することができる。 As a crosslinking agent for acrylamide, N,N'-
Methylenebisacrylamide, N,N'-propylenebisacrylamide, diacrylamide dimethyl ether, 1,2-diacrylamide ethylene glycol, N,N'-diacryltartaric acid diamide, etc. can be used.
重合促進剤としては、3―ジメチルアミノプロ
ピオニトリル、N,N,N′,N′―テトラメチル
エチレンジアミン等を使用することができる。ま
た重合開始剤としては、通常、ペルオクソ二硫酸
カリウムを使用する。 As the polymerization accelerator, 3-dimethylaminopropionitrile, N,N,N',N'-tetramethylethylenediamine, etc. can be used. Further, as a polymerization initiator, potassium peroxodisulfate is usually used.
重合により得られたゲルを0.5mm〜5mmの大き
さの球、円柱、板、繊維、中空繊維等の形状に成
形する。 The gel obtained by polymerization is molded into the shape of a sphere, cylinder, plate, fiber, hollow fiber, etc. with a size of 0.5 mm to 5 mm.
このようにして、予め微生物のフロツクを作つ
た後、モノマーの重合溶液に混合して重合させる
と、長期間にわたつて高い活性を示し、強度にお
いても優れ、高い耐久性を示す固定化微生物が得
られる。 In this way, if a floc of microorganisms is prepared in advance and then mixed with a monomer polymerization solution and polymerized, immobilized microorganisms that exhibit high activity over a long period of time, excellent strength, and high durability can be obtained. can get.
作 用
フロツクの形成に使用した凝集剤は微生物を包
み込み、その結果、重合反応の際にモノマーや重
合開始剤の毒性がフロツクの内部まで侵入しない
ため、微生物の死滅する割合を著しく減少し、高
い活性を有する固定化微生物を生じる。Effect The flocculant used to form the floc envelops the microorganisms, and as a result, the toxicity of the monomer and polymerization initiator does not penetrate into the inside of the floc during the polymerization reaction, which significantly reduces the rate of microorganisms being killed. yields immobilized microorganisms with activity.
更に、ポリマーゲルはその内部に包括固定化し
た微生物を比較的大型の微生物による摂食から保
護し、また、物理的耐久性において優れた担体と
して作用する。 Furthermore, the polymer gel protects the microorganisms entrapped and immobilized therein from being eaten by relatively large microorganisms, and also acts as a carrier with excellent physical durability.
実施例
次に、実施例に基づいて本発明を詳述するが、
本発明はこれに限定されるものではない。Examples Next, the present invention will be described in detail based on examples.
The present invention is not limited to this.
実施例 1
松戸市K下水処理場の活性汚泥を40000mg/
の菌体濃度に濃縮し、アニオン性高分子凝集剤プ
レストール444K(ニユーメタルス・アンド・ケミ
カル社製)を菌体乾物量当たり0.5%添加し、凝
集菌を作つた。別に、アクリルアミドモノマー32
%及びN,N′―メチレンジスアクリルアミド2
%を含む溶液を作り、この溶液と凝集菌とを同容
積比で混合し、次いで重合促進剤として3―ジメ
チルアミノプロピオニトリルを0.5%になるよう
に添加し、更に、重合開始剤としてペルオクソ二
硫酸カリウムを0.25%になるように添加し、重合
させて凝集菌を包括固定した。こうして包括固定
した凝集菌を含むポリアクリルアミドゲルを直径
2.6mm、高さ2.6mmの円柱に成形した。Example 1 Activated sludge from Matsudo City K sewage treatment plant was 40,000mg/
Anionic polymer flocculant Prestol 444K (manufactured by Nu-Metals & Chemicals) was added at 0.5% based on the dry weight of the bacteria to produce flocculated bacteria. Separately, acrylamide monomer 32
% and N,N'-methylenedisacrylamide 2
%, mix this solution and flocculated bacteria in the same volume ratio, then add 3-dimethylaminopropionitrile as a polymerization accelerator to 0.5%, and further add peroxo as a polymerization initiator. Potassium disulfate was added to a concentration of 0.25%, and the flocculated bacteria were immobilized by polymerization. The diameter of the polyacrylamide gel containing the aggregated bacteria that has been comprehensively fixed in this way is
It was molded into a cylinder with a length of 2.6 mm and a height of 2.6 mm.
こうして得た廃水処理剤を第1図に示す曝気槽
1に充填率40%に充填した。第1図に示した曝気
槽1は上昇管2及び下降管3からなり、廃水は廃
水入口4から注入され、処理水出口5から流出す
る。空気は送気管6から送られ、気泡は上昇管2
を上昇し、エアリフト効果により廃水処理剤7を
流動させ、廃水と接触させて有機物質を分解す
る。BOD60〜220mg/の下水を滞留時間3時間
で処理した結果を第2図に示す。 The waste water treatment agent thus obtained was filled into the aeration tank 1 shown in FIG. 1 at a filling rate of 40%. The aeration tank 1 shown in FIG. 1 consists of an ascending pipe 2 and a descending pipe 3, and wastewater is injected from a wastewater inlet 4 and flows out from a treated water outlet 5. Air is sent from the air pipe 6, and bubbles are sent from the riser pipe 2.
is raised, the wastewater treatment agent 7 is made to flow due to the air lift effect, and brought into contact with the wastewater to decompose organic substances. Figure 2 shows the results of treating sewage with a BOD of 60 to 220 mg for a residence time of 3 hours.
比較のため、従来法として、プラスチツクの波
板を40%充填し、波板の表面に微生物の膜を形成
させて接触曝気法を実施した。この接触曝気法に
より前記の廃水と同じ廃水を処理した結果を第2
図に示す。 For comparison, as a conventional method, a contact aeration method was carried out by filling a 40% plastic corrugated plate and forming a microbial film on the surface of the corrugated plate. The results of treating the same wastewater as the above using this contact aeration method were
As shown in the figure.
第2図から判るように、従来法では運転25日目
以後に糸ミミズが大量に発生し、微生物の量が減
少し、処理水質が悪化した。これに対し、本発明
の廃水処理剤を用いた場合には、廃水中に糸ミミ
ズが発生しても、処理水質は安定して良好であつ
た。 As can be seen from Figure 2, with the conventional method, a large number of threadworms appeared after the 25th day of operation, the amount of microorganisms decreased, and the quality of the treated water deteriorated. On the other hand, when the wastewater treatment agent of the present invention was used, the quality of the treated water was stable and good even if threadworms were generated in the wastewater.
実施例 2
実施例1と同様にして微生物のフロツクを作つ
たが、径の異なるフロツクを種々製造し、それぞ
れ実施例1と同様に包括固定し、直径3mm、長さ
3mmの円柱に成形した。得られた廃水処理剤の活
性を測定し、結果を第3図に示す。Example 2 Microorganism flocs were prepared in the same manner as in Example 1, but various flocs with different diameters were manufactured, each was fixed encirclingly in the same manner as in Example 1, and formed into a cylinder with a diameter of 3 mm and a length of 3 mm. The activity of the obtained wastewater treatment agent was measured and the results are shown in FIG.
活性は酸素摂取速度(mgO2/h)で測定した。
活性の残存率は、包括固定する前の酸素摂取速度
と包括固定したときの酸素摂取速度との比率であ
る。 Activity was measured by oxygen uptake rate (mgO 2 /h).
The residual rate of activity is the ratio of the oxygen uptake rate before comprehensive fixation to the oxygen uptake rate after comprehensive fixation.
第3図から明らかなとおり、フロツク径100μm
未満の微生物(凝集剤無添加)を包括固定した廃
水処理剤の活性の残存率は15%以下であつたが、
凝集剤を添加し、フロツク径を100μm以上として
凝集菌を包括固定した廃水処理剤の活性の残存率
は25〜45%であり、活性を大幅に向上することが
できた。 As is clear from Figure 3, the floc diameter is 100μm.
The residual activity of the wastewater treatment agent that comprehensively immobilized microorganisms (no flocculant added) was less than 15%;
The residual activity of the wastewater treatment agent in which a flocculant was added and flocculates were fixed to a flocculate diameter of 100 μm or more was 25 to 45%, and the activity was significantly improved.
前記の実施例では凝集剤として、プレストール
444Kを使用したが、他の有機又は無機凝集剤を
使用しても同様の結果が得られる。 In the above examples, Prestol was used as the flocculant.
Although 444K was used, similar results can be obtained using other organic or inorganic flocculants.
発明の効果
本発明によれば、比較的大型の微生物の摂食に
よる微生物の量の減少を防止でき、微生物の活性
が高く、物理的強度が大きく、耐久性に優れた廃
水処理剤が得られる。Effects of the Invention According to the present invention, a reduction in the amount of microorganisms due to ingestion by relatively large microorganisms can be prevented, and a wastewater treatment agent with high microbial activity, high physical strength, and excellent durability can be obtained. .
第1図は本発明の実施例に使用した曝気槽の略
示断面図、第2図は実施例1における廃水及び処
理水のBOD濃度の経日変化図、第3図はフロツ
ク径と活性の残存率との関係図である。
1…曝気槽、2…上昇管、3…下降管、7…廃
水処理剤。
Figure 1 is a schematic cross-sectional view of the aeration tank used in the example of the present invention, Figure 2 is a diagram of the daily change in BOD concentration of wastewater and treated water in Example 1, and Figure 3 is a graph of floc diameter and activity. It is a relationship diagram with a residual rate. 1...Aeration tank, 2...Rising pipe, 3...Downcomer pipe, 7...Wastewater treatment agent.
Claims (1)
水の処理剤において、凝集剤を用いて活性汚泥を
フロツク状に凝集させ、得られた凝集物をポリマ
ーゲル内部に包括固定して成ることを特徴とする
廃水の処理剤。 2 100μm以上の大きさの活性汚泥フロツクを固
定して含む特許請求の範囲第1項記載の処理剤。[Scope of Claims] 1. A wastewater treatment agent that microbiologically decomposes organic substances in wastewater, which uses a flocculant to flocculate activated sludge into flocs and enclose the resulting flocs inside a polymer gel. A wastewater treatment agent characterized by being fixed. 2. The treatment agent according to claim 1, which contains fixed activated sludge flocs with a size of 100 μm or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59189977A JPS6168196A (en) | 1984-09-11 | 1984-09-11 | Treating agent for waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59189977A JPS6168196A (en) | 1984-09-11 | 1984-09-11 | Treating agent for waste water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6168196A JPS6168196A (en) | 1986-04-08 |
JPS6352557B2 true JPS6352557B2 (en) | 1988-10-19 |
Family
ID=16250336
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59189977A Granted JPS6168196A (en) | 1984-09-11 | 1984-09-11 | Treating agent for waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6168196A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62279887A (en) * | 1986-05-28 | 1987-12-04 | Sanki Eng Co Ltd | Surface immobilized anaerobic bacteria granule and treatment of waste water using same |
US4746457A (en) * | 1987-03-05 | 1988-05-24 | Calgon Corporation | Flocculation of suspended solids from aqueous solutions |
-
1984
- 1984-09-11 JP JP59189977A patent/JPS6168196A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6168196A (en) | 1986-04-08 |
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