JPS60153998A - Waste water treating agent and its preparation - Google Patents
Waste water treating agent and its preparationInfo
- Publication number
- JPS60153998A JPS60153998A JP59009326A JP932684A JPS60153998A JP S60153998 A JPS60153998 A JP S60153998A JP 59009326 A JP59009326 A JP 59009326A JP 932684 A JP932684 A JP 932684A JP S60153998 A JPS60153998 A JP S60153998A
- Authority
- JP
- Japan
- Prior art keywords
- bacteria
- flocculated
- molecular flocculant
- nitrifying bacteria
- org
- 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.)
- Granted
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
- Biological Treatment Of Waste Water (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、廃水中の窒素化合物を微生物学的に硝化処理
するための、硝化活性の高い廃水処理剤及びその製造方
法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a wastewater treatment agent with high nitrification activity for microbiologically nitrifying nitrogen compounds in wastewater, and a method for producing the same.
廃水中の窒素化合物を硝化処理するには、従来、硝化菌
(Nitrosomonas、、N1trobacto
r等)のフロックを曝気槽内に浮遊させて用いる浮遊型
活性lr:i泥法、又は硝化菌を膜の形で用い、接触曝
気法、回転円板法、散水r床法等が実施されている。こ
のような方法では、硝化菌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ス
、輪生、つりがね虫等により硝化菌が食べられ、硝化菌
の量が減少し、アンモニア態の窒素化合物を長期間安定
し°ζ酸化できない欠点、があった。Conventionally, nitrifying bacteria (Nitrosomonas, N1trobacterium) have been used to nitrify nitrogen compounds in wastewater.
The floating activated lr:i mud method, in which flocs of (r, etc.) are suspended in an aeration tank, or the contact aeration method, rotating disk method, watering r bed method, etc., using nitrifying bacteria in the form of a membrane, have been carried out. ing. In this method, the nitrifying bacteria come into direct contact with the wastewater, so the nitrifying bacteria are eaten by large organisms in the wastewater, such as threadworms, whorls, and ringworms, which feed on bacteria, resulting in nitrification. It had the disadvantage that the amount of bacteria decreased and that nitrogen compounds in the ammonia state could not be stably oxidized for a long period of time.
また、最近では、各種の菌をポリアクリルアミド、カラ
ギーナン、アルギン酸等のゲルに包括固定化した廃水処
理剤が提案されCいる。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1■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。カラギーナ
ン、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、固定化した菌の活 □
性紙下は軽微であるが、物理的強度が小さく、耐久性に
問題がある。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ばずので、活性低下を
招きやすいという欠点がある。Recently, wastewater treatment agents have been proposed in which various bacteria are entrappingly immobilized in gels such as polyacrylamide, carrageenan, and alginic acid. With these treatment agents in which bacteria are immobilized in gel, the disadvantage that bacteria are eaten by relatively large microorganisms is overcome, but the activity of the immobilized bacteria decreases and when used for long-term wastewater treatment. Durability becomes an issue. When using less toxic substances that exist in nature such as carrageenan and alginic acid as a gel, the activity of immobilized bacteria can be reduced □
Although the damage is slight, the physical strength is low and there are problems with durability. On the other hand, when polyacrylamide gel is used, it has high physical strength and good durability, but the acrylamide monomer used for immobilization, the crosslinking agent,
Since the polymerization initiator and the like do not have a toxic effect on bacteria, there is a drawback that the activity tends to decrease.
特に、硝化菌は増殖速度が遅く、毒性物質に対して鋭敏
な性質を有しているので、活性低下が著しい。このため
、硝化活性が高く、物理的耐久性の大きい廃水処理剤が
望まれている。In particular, nitrifying bacteria have a slow growth rate and are sensitive to toxic substances, so their activity is significantly reduced. Therefore, a wastewater treatment agent with high nitrification activity and high physical durability is desired.
本発明の目的は、前記の従来技術の欠点を解消し、比較
的大型の微生物の摂食による硝化菌の減少を防止でき、
硝化活性が高く、物理的強度が大きい廃水処理剤及びそ
の製造方法を提供することにあり、この目的は本発明に
よれば、硝化菌の凝iI−物をポリアクリルアミドゲル
で固定化することによって達成される。The purpose of the present invention is to eliminate the drawbacks of the prior art described above, and to prevent the reduction of nitrifying bacteria due to feeding by relatively large microorganisms.
It is an object of the present invention to provide a wastewater treatment agent with high nitrification activity and high physical strength, and a method for producing the same. achieved.
即し、本発明の廃水処理剤は、有機高分子凝集剤を用い
てモ11化菌をフロック状に凝集させて得た凝集物をポ
リアクリルアミドゲル内部に包括固定化して成ることを
特徴とする。That is, the wastewater treatment agent of the present invention is characterized in that it is formed by entrapping and immobilizing the aggregates obtained by agglomerating Mo. 11 bacteria into flocs using an organic polymer flocculant inside a polyacrylamide gel. .
本発明に使用する有機高分子凝集剤は、カチオン性、ア
ニオン性及びノニオン性のいずれでもよい。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る。アニオン性高
分子凝集剤としては、ポリアクリル酸すトリウム、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、また、ノニオン性高分子凝簗剤として
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 organic polymer flocculant used in the present invention may be cationic, anionic, or nonionic. Examples of the cationic polymer flocculant include polyvinylpyridine hydrochloride, polyethyleneimine, and the like. Examples of anionic polymer flocculants include storium polyacrylate, maleic acid copolymer salts, polyacrylamide partial hydrolyzate salts, and examples of nonionic polymer flocculants include polyacrylamide and polyacrylamide. Examples include oxyethylene.
前記のような凝集剤を用いて硝化菌を凝集させて100
μm11以上の大きさのフロック状の凝集物を作り、そ
の後、ポリアクリルアミドゲルV旧i1−に包括固定化
する。Nitrifying bacteria were flocculated using a flocculant as described above, and 100
A floc-like aggregate with a size of μm11 or more is prepared, and then entrapping immobilized on polyacrylamide gel Vold i1-.
61!J化菌の凝集物を固定他害るには、)′クリルア
ミドモノマー、架橋剤、重合促進剤及び重合開始剤等を
含む溶液に凝集菌を混合し、重合反応を行う。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’〜ジアリル
酒石酸ジアミド等を使用することができる。重合促進剤
とし“Cは、β−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、ベルオクソニ硫酸カリウムを使用する。61! In order to fix or otherwise damage aggregates of J-forming bacteria, the aggregates are mixed with a solution containing acrylamide monomer, a crosslinking agent, a polymerization accelerator, a polymerization initiator, etc., and a polymerization reaction is carried out. As a crosslinking agent for acrylamide, N,N"-methylenebisacrylamide, N,N'-propylenebisacrylamide, diacrylamide dimethyl ether, 1,2-diacrylamide ethylene glycol, or N,N'-diallyltartaric acid diamide, etc. are used. As a polymerization accelerator, "C" is β-dimethylaminopropionitrile, N
, N, N', N'-tetramethylethylenediamine, etc. can be used. Moreover, as a polymerization initiator, potassium belloxonisulfate is usually used.
重合により得られたゲルを2〜4I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 shaped into a sphere, cylinder, plate, fiber, hollow fiber, etc. having a size of 2 to 4 I.
このようにして予め硝化菌のフロックを作ってからアク
リルアミドの重合溶液に混合して重合さゼると、長期間
にわたっ′ζ高い硝化活性を示し、強度におい“ζも優
れ、高い一11久性を示す固定化硝化菌が得られる。こ
れは、使用した高分子凝集剤が4ii’j化菌を包み込
み、その結果、重合反応の際にアクリルアミ;°モノマ
ーや重合開始剤の毒性がフロックの内部まで侵入しない
ため、硝化菌の死滅する割合を著しく減少するためと考
えられる。When flocs of nitrifying bacteria are prepared in advance in this way and then mixed with an acrylamide polymerization solution and polymerized, they exhibit high nitrification activity over a long period of time, have excellent strength and odor, and have a long lifespan. This is because the polymer flocculant used envelops the nitrifying bacteria, and as a result, during the polymerization reaction, the toxicity of the acrylamide monomer and polymerization initiator is removed from the flocs. This is thought to be because the rate at which nitrifying bacteria are killed is significantly reduced because they do not penetrate into the interior of the nitrifying bacteria.
更に、本発明による廃水処理剤は、硝化菌が比較的大型
の微生物による摂食から保護されており、物理的耐久性
において優れているので、長期間にわたって高い硝化活
性を示す。Furthermore, the wastewater treatment agent according to the present invention protects the nitrifying bacteria from being eaten by relatively large microorganisms and has excellent physical durability, so it exhibits high nitrification activity over a long period of time.
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。Next, the present invention will be described in detail based on Examples, but the present invention is not limited thereto.
実施例1
下水を活性汚泥処理した二次処理水(N Ha−N15
〜30■/l)を原水とし、滞留時間6時間で馴養した
硝化菌を使用した。この菌を菌体濃度40000mg/
nに濃縮し、高分子凝集剤プレス(・−ル444K に
ューメタルス・エン1゛・ケミカル社製)を菌体乾物量
当たり0.5%添加し、凝集菌を作った。別に、アクリ
ルアミドモノマー32%及びN、N’−メチレンヒスア
クリルアミド2%を含む溶液を作り、この溶液と凝集菌
懸濁液とを同容積比で混合し、次いで重合促進剤として
β−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ベルオクソニ硫酸
カリウムを0.25%になるように添加し、凝集菌を包
括固定した。この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3龍、高さ3順の円柱に成形した。Example 1 Secondary treated water (N Ha-N15) obtained by treating sewage with activated sludge
~30 .mu./l) was used as raw water, and nitrifying bacteria that had been acclimatized for a residence time of 6 hours were used. This bacteria has a bacterial cell concentration of 40,000 mg/
Then, a polymer flocculant press (L444K, manufactured by New Metals En-1 Chemical Co., Ltd.) was added at 0.5% based on the dry weight of the bacterial cells to form flocculated bacteria. Separately, a solution containing 32% acrylamide monomer and 2% N,N'-methylenehis-acrylamide was prepared, and this solution and the flocculant suspension were mixed in the same volume ratio, and then β-dimethylaminopropylene was used as a polymerization accelerator. Pionitrile was added at a concentration of 0.5%, and potassium belloxonisulfate was further added as a polymerization initiator at a concentration of 0.25% to entrap and immobilize the flocculated bacteria. The polyacrylamide gel containing the entrapping and immobilized aggregated bacteria was molded into a cylinder with a diameter of 3 mm and a height of 3 mm.
こうして得た廃水処理剤を第1図に示す曝気槽に充填率
35%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、廃水は廃水人口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
水処理剤を流動させ、廃水と接触してアンモニア態窒素
化合物を硝化処理する。NH4−N l 5〜30+n
g/ 1.(D廃水をメ11′I留時間6時間で処理し
た結果を第2図に7で示す。The wastewater treatment agent thus obtained was filled into the aeration tank shown in FIG. 1 at a filling rate of 35%. The aeration tank 1 shown in Figure 1 is the riser pipe 2.
and a downcomer pipe 3, wastewater is injected from a wastewater outlet 4 and flows out from a treated water outlet 5. Air is sent from the air supply pipe 6, and the bubbles rise through the riser pipe 2, causing the wastewater treatment agent to flow due to the air lift effect, and come into contact with the wastewater to nitrify ammonia nitrogen compounds. NH4-Nl 5~30+n
g/1. (The results of treating D wastewater with a residence time of 6 hours are shown at 7 in Figure 2.
比較のため、従来法として、菌体濃度20001■/l
での浮遊型の活性汚泥法により前記の廃水と同じ廃水を
処理し、結果を第2図に8で示す。For comparison, as a conventional method, the bacterial cell concentration was 20001■/l.
The same wastewater as the one described above was treated by the floating activated sludge method, and the results are shown at 8 in Figure 2.
なお、第2図において9は原水のN114−N濃度を示
す。In addition, in FIG. 2, 9 indicates the N114-N concentration of the raw water.
第2図から判るように、従来法では運転20日口辺後に
糸ミミズが大量に発生し、硝化菌の量が減少し、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−C良好であった。As can be seen from Figure 2, in the conventional method, a large number of threadworms appeared after 20 days of operation, the amount of nitrifying bacteria decreased, and the quality of the treated water deteriorated. On the other hand, when the wastewater treatment agent of the present invention was used, even if threadworms were generated in the wastewater, the quality of the treated water was stable and -C was good.
実施例2
実施例1と同様にして硝化菌のフロックを作ったが、径
の異なるフロックを種々装造し、それぞれ実施例1と同
様に包括固定し、直径3++i、長さ“3 amの円柱
に成形した。得られた廃水処理剤の硝化菌の活性をII
I定し、結果を第3図に示す。Example 2 A floc of nitrifying bacteria was made in the same manner as in Example 1, but the flocs with different diameters were packed in various ways, and each was fixed in a package in the same manner as in Example 1 to form a cylinder with a diameter of 3++i and a length of 3 am. The activity of nitrifying bacteria in the obtained wastewater treatment agent was determined by II.
The results are shown in Figure 3.
硝化菌の活性は酸素摂取速度r y(mgo 2 /
h )で測定した。活性の残存率は包括固定する前の硝
化菌のγ、と包括固定した硝化菌のγ、との比率である
。The activity of nitrifying bacteria is determined by the oxygen uptake rate ry (mgo 2 /
h). The residual rate of activity is the ratio of γ of nitrifying bacteria before entrapping fixation to γ of nitrifying bacteria after entrapping fixation.
第3図から明らかなとおり、フロック径lOOμm未満
の硝化菌(高分子a集剤をlオ加しない)を包括固定し
た廃水処理剤の活性の残存率は10%以下であったが、
高分子凝集刑を添加し、フロック径を100μrn以上
とした凝集菌を包括固定゛した廃水処理剤の活性の残存
率は15〜40%であり、活性を大幅に向上できた。As is clear from Fig. 3, the residual activity of the wastewater treatment agent in which nitrifying bacteria with a floc diameter of less than 100 μm (without addition of 100% polymer a-collecting agent) was immobilized was less than 10%;
The residual activity of the wastewater treatment agent to which a polymer flocculant was added and flocculated bacteria with a floc diameter of 100 μrn or more was immobilized was 15 to 40%, and the activity was significantly improved.
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アンモニ
ア態窒素化合物の濃度の経時変化図、第3図はフロック
径と硝化菌の活性の残存率との関係図である。
2・・・上昇管、3・・・下降管、6・・・送気管、7
・・・本発明の廃水処理剤での処理水のN II 4−
’ N 1iFj I!特HT1出願人
日立ブラント建設株式会社
第1図
0 10 20 30 40 50
覆@B数 (日)
第3図
)
ン
7r37りの1普 (、//)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 concentration of ammonia nitrogen compounds in the wastewater and treated water in Example 1 over time, and Figure 3 is the floc diameter. FIG. 2 is a relationship diagram between the residual rate of nitrifying bacteria activity and the residual rate of nitrifying bacteria activity. 2... Ascending pipe, 3... Descending pipe, 6... Air supply pipe, 7
... N II 4- of water treated with the wastewater treatment agent of the present invention
' N 1iFj I! Special HT1 Applicant: Hitachi Brandt Construction Co., Ltd. Figure 1 0 10 20 30 40 50 Number of covers@B (Japanese) Figure 3) N7r37Rino1P (,//)
Claims (3)
処理剤において、有機高分子凝集剤を用いて硝化菌をフ
ロック状に凝集させて得た凝集物をポリアクリルアミド
ゲル内部に包括固定化して成ることを特徴とする廃水処
理剤。(1) In a wastewater treatment agent that microbiologically nitrates nitrogen compounds in wastewater, an organic polymer flocculant is used to flocculate nitrifying bacteria into flocs, and the resulting flocs are entrapping and immobilized inside a polyacrylamide gel. A wastewater treatment agent characterized by comprising:
凝集させ、得られた凝集物をポリアクリルアミドゲル内
部に包括固定化することを特徴とする廃水処理剤の製造
方法。(2) A method for producing a wastewater treatment agent, which comprises aggregating nitrifying bacteria into flocs using an organic polymer flocculant and entrapping and immobilizing the resulting flocs inside a polyacrylamide gel.
ックに凝集させる特許請求の範囲第2項記載の方法。(3) The method according to claim 2, in which aggregates of nitrifying bacteria are aggregated into flocs with a size of 100 μm or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59009326A JPS60153998A (en) | 1984-01-20 | 1984-01-20 | Waste water treating agent and its preparation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59009326A JPS60153998A (en) | 1984-01-20 | 1984-01-20 | Waste water treating agent and its preparation |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60153998A true JPS60153998A (en) | 1985-08-13 |
JPH0137987B2 JPH0137987B2 (en) | 1989-08-10 |
Family
ID=11717347
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59009326A Granted JPS60153998A (en) | 1984-01-20 | 1984-01-20 | Waste water treating agent and its preparation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60153998A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63252591A (en) * | 1987-04-10 | 1988-10-19 | Nkk Corp | Treatment of sewage |
JPH02500729A (en) * | 1987-05-07 | 1990-03-15 | シエーリング アクチエンゲゼルシヤフト | How to purify wastewater |
JPH03143599A (en) * | 1989-10-26 | 1991-06-19 | Hitachi Plant Eng & Constr Co Ltd | Waste water treating device |
US5185415A (en) * | 1989-07-12 | 1993-02-09 | Japane Vilene Co., Ltd. | Adsorptive resin for microorganisms |
USRE34740E (en) * | 1989-07-12 | 1994-09-27 | Japane Vilkene Company, Ltd. | Adsorptive resin for microorganisms |
JP2003053385A (en) * | 2001-08-09 | 2003-02-25 | Kurita Water Ind Ltd | Biological denitrification equipment |
JP2009050850A (en) * | 2008-09-24 | 2009-03-12 | Hitachi Plant Technologies Ltd | Inclusion immobilization carrier and production process thereof |
CN110240720A (en) * | 2019-06-06 | 2019-09-17 | 南京农业大学 | A kind of methods and applications preparing polysaccharide composite film using thermostabilization recombinant bacteria laccase |
-
1984
- 1984-01-20 JP JP59009326A patent/JPS60153998A/en active Granted
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63252591A (en) * | 1987-04-10 | 1988-10-19 | Nkk Corp | Treatment of sewage |
JPH02500729A (en) * | 1987-05-07 | 1990-03-15 | シエーリング アクチエンゲゼルシヤフト | How to purify wastewater |
US5185415A (en) * | 1989-07-12 | 1993-02-09 | Japane Vilene Co., Ltd. | Adsorptive resin for microorganisms |
USRE34740E (en) * | 1989-07-12 | 1994-09-27 | Japane Vilkene Company, Ltd. | Adsorptive resin for microorganisms |
JPH03143599A (en) * | 1989-10-26 | 1991-06-19 | Hitachi Plant Eng & Constr Co Ltd | Waste water treating device |
JP2003053385A (en) * | 2001-08-09 | 2003-02-25 | Kurita Water Ind Ltd | Biological denitrification equipment |
JP2009050850A (en) * | 2008-09-24 | 2009-03-12 | Hitachi Plant Technologies Ltd | Inclusion immobilization carrier and production process thereof |
CN110240720A (en) * | 2019-06-06 | 2019-09-17 | 南京农业大学 | A kind of methods and applications preparing polysaccharide composite film using thermostabilization recombinant bacteria laccase |
Also Published As
Publication number | Publication date |
---|---|
JPH0137987B2 (en) | 1989-08-10 |
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