JPH10500A - Sludge treatment method - Google Patents
Sludge treatment methodInfo
- Publication number
- JPH10500A JPH10500A JP8174382A JP17438296A JPH10500A JP H10500 A JPH10500 A JP H10500A JP 8174382 A JP8174382 A JP 8174382A JP 17438296 A JP17438296 A JP 17438296A JP H10500 A JPH10500 A JP H10500A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- mol
- mole
- group
- amphoteric polymer
- 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
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は新規な汚泥脱水方法
に関するものであり、特別な種類の高分子凝集剤を使用
する事により高効率の脱水を行い低添加量で高処理量の
脱水ケーキを得る事を目的とする。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a novel sludge dewatering method, which uses a special type of polymer flocculant to perform high-efficiency dewatering and to produce a high-throughput dewatered cake with a small amount of addition. The purpose is to gain.
【0002】[0002]
【従来の技術】これまでに各種の有機高分子凝集剤を用
いた汚泥脱水方法が提案されている。特開昭63−15
8200号公報にはカチオン当量値とアニオン当量値の
比が1.5〜8.0である両性高分子凝集剤を、無機凝
集剤添加後のpH値が5〜8である有機汚泥に添加し、
ついで脱水する事を特徴とする汚泥の脱水方法が記載さ
れている。 また特開昭60−248299号公報には
有機性汚泥に、アクリル酸ヒドラジド系高分子化合物と
アミノ基又は第四級アンモニウム塩を含有する高分子化
合物と、さらに酸又は酸性塩、中性塩およびアルカリ又
はアルカリ性塩から選ばれる少なくとも一種とを含有す
る溶液を添加することを特徴とする汚泥の処理方法が記
載されている。 ここに言うアミノ基又は第四級アンモ
ニウム塩を含有する高分子化合物は明細書中の発明の詳
細な説明の記載よりアクリル酸を含まぬポリマーである
事は明らかである。 また特開昭61−216800号
公報には有機性汚泥に金属塩を添加して攪拌したのち、
さらにアクリル酸ヒドラジド系高分子化合物とアミノ基
又は第四級アンモニウム塩を含有するカチオン系高分子
化合物とを添加して造粒することを特徴とする有機性汚
泥の凝集方法が記載されている。 また特開昭62−2
3500号公報には汚泥に金属塩を添加した後、濃縮
し、次いで濃縮汚泥にアクリル酸ヒドラジド系ポリマー
またはアクリル酸ヒドラジド系ポリマーとカチオン系ポ
リマーとを添加して脱水することを特徴とする汚泥の処
理方法が記載されている。2. Description of the Related Art A sludge dewatering method using various organic polymer flocculants has been proposed. JP-A-63-15
No. 8200 discloses that an amphoteric polymer flocculant having a ratio of cation equivalent value to anion equivalent value of 1.5 to 8.0 is added to an organic sludge having a pH value of 5 to 8 after addition of an inorganic flocculant. ,
Then, a method for dewatering sludge, which is characterized by dewatering, is described. JP-A-60-248299 discloses an organic sludge containing an acrylic acid hydrazide-based polymer compound and a polymer compound containing an amino group or a quaternary ammonium salt, and further containing an acid or acid salt, a neutral salt and A method for treating sludge, which comprises adding a solution containing at least one selected from alkalis and alkaline salts, is described. The high molecular compound containing an amino group or a quaternary ammonium salt mentioned herein is apparently a polymer containing no acrylic acid from the description of the detailed description of the invention in the specification. JP-A-61-216800 discloses that after adding a metal salt to organic sludge and stirring the mixture,
Furthermore, there is described a method for coagulating organic sludge, which comprises adding an acrylic acid hydrazide-based polymer compound and a cationic polymer compound containing an amino group or a quaternary ammonium salt to perform granulation. Further, Japanese Patent Application Laid-Open No. Sho 62-2
Japanese Patent No. 3500 discloses a sludge comprising adding a metal salt to a sludge, concentrating the sludge, and then adding an acrylic acid hydrazide-based polymer or an acrylic acid hydrazide-based polymer and a cationic polymer to the concentrated sludge for dehydration. A processing method is described.
【0003】[0003]
【発明の課題】しかしながら、これまで公知の方法では
デカンター脱水において、低添加量のポリマー消費によ
り単位時間あたりに多量の汚泥を効率良く脱水する方法
は知られていなかった。 本発明は効率よく上記問題を
解決する事を課題とする。However, in the method of decanter dehydration, a method of efficiently dehydrating a large amount of sludge per unit time by consuming a small amount of polymer has not been known. An object of the present invention is to solve the above problems efficiently.
【0004】[0004]
【課題を解決する為の手段】本願発明は上記課題を達成
するために次の用に構成される。請求項1の限定は有機
汚泥に無機凝集剤を添加混合した後に、下記式(1)で
表される両性高分子凝集剤(A)および式(2)で表さ
れる両性高分子凝集剤(B)を混合してなる汚泥脱水剤
の水溶液を機内薬注して、デカンター内にて該汚泥を凝
集させ、脱水する事を特徴とする汚泥の処理方法であ
る。機内薬注とは、高分子凝集剤水溶液と汚泥を二重配
管により回転軸部分からデカンター内に供給し、デカン
ターのボールの回転により混合する薬注方法を言う。Means for Solving the Problems In order to achieve the above object, the present invention is constituted as follows. The limitation of claim 1 is that after adding and mixing an inorganic flocculant to organic sludge, the amphoteric polymer flocculant (A) represented by the following formula (1) and the amphoteric polymer flocculant represented by the formula (2) ( This is a method for treating sludge, characterized by injecting an aqueous solution of a sludge dewatering agent obtained by mixing B) into an in-machine medicine, coagulating the sludge in a decanter, and dewatering the sludge. In-machine chemical injection refers to a chemical injection method in which a polymer flocculant aqueous solution and sludge are supplied from a rotating shaft portion into a decanter through a double pipe and mixed by rotation of a ball of the decanter.
【化3】 (式中R1 は水素原子またはメチル基、R2 はエチレン
基またはプロピレン基、R3 ,R4 はメチル基またはエ
チル基、R5 は水素原子, メチル基,エチル基またはベ
ンジル基、X- は対アニオンを表す。 またa+b+c
=100モル%,a=10〜50モル%,b=45〜8
5モル%,c=5〜50モル%の関係を有する。)Embedded image (Wherein R 1 is a hydrogen atom or a methyl group, R 2 is an ethylene group or a propylene group, R 3 and R 4 are a methyl group or an ethyl group, R 5 is a hydrogen atom , a methyl group, an ethyl group or a benzyl group, X − Represents a counter anion, and a + b + c
= 100 mol%, a = 10 to 50 mol%, b = 45 to 8
5 mol%, c = 5 to 50 mol%. )
【化4】 (d+e+f=約100モル%,d=10〜30モル
%,e=30〜80モル%,f=10〜40モル%の関
係を有する。) 請求項2の限定は両性高分子凝集剤(A)および両性高
分子凝集剤(B)を6:4〜8:2の比率で併用する事
を特徴とする請求項1に記載の汚泥の処理方法である。
請求項3の限定は無機凝集剤が鉄塩および/又はアルミ
ニウム塩である事を特徴とする請求項1ないし請求項2
に記載の汚泥の処理方法である。請求項4の限定は無機
凝集剤がポリ塩化アルミニウムである事を特徴とする請
求項1ないし請求項3に記載の汚泥の処理方法である。
請求項5の限定は有機汚泥が下水の嫌気性消化汚泥であ
ることを特徴とする請求項1ないし請求項4に記載の汚
泥の処理方法である。Embedded image (D + e + f = about 100 mol%, d = 10 to 30 mol%, e = 30 to 80 mol%, f = 10 to 40 mol%.) The limitation of claim 2 is the amphoteric polymer flocculant (A). ) And an amphoteric polymer flocculant (B) in a ratio of 6: 4 to 8: 2.
The limitation of claim 3 is that the inorganic coagulant is an iron salt and / or an aluminum salt.
The method for treating sludge according to the above. The limitation of claim 4 is the method for treating sludge according to claims 1 to 3, wherein the inorganic coagulant is polyaluminum chloride.
The limitation of claim 5 is the sludge treatment method according to claims 1 to 4, wherein the organic sludge is anaerobic digestion sludge of sewage.
【0005】特開昭60−248299号公報には有機
性汚泥にアクリル酸ヒドラジド系高分子化合物とアミノ
基又は第四級アンモニウム塩を含有する高分子化合物
と、さらに酸又は酸性塩、中性塩およびアルカリ又はア
ルカリ性塩から選ばれる少なくとも一種とを含有する溶
液を添加することを特徴とする汚泥の処理方法が記載さ
れている。 ここに言うアミノ基又は第四級アンモニウ
ム塩を含有する高分子化合物は、明細書中の発明の詳細
な説明の記載にて、アクリル酸の生成を忌避している事
から、両性(メタ)アクリル系高分子凝集剤を想定して
いない事は明らかである。 また実施例に記載されたア
クリル酸ヒドラジド系高分子化合物の組成は本願発明の
ものとは異なる物質である。 すなわち本願発明のアク
リル酸ヒドラジド系高分子化合物は、ポリアクリルアミ
ドを無水ヒドラジンと反応させて得られた数十ppmか
ら数百ppmの架橋結合をした高分子であるため特殊な
凝集挙動を示し、両性(メタ)アクリレート高分子凝集
剤と相乗効果を発揮し強力な凝集効果を表す。(d+e
+f=約100モル%の記述は上記微量の架橋結合の存
在する結果による。) ポリマー混合比も特開昭60−
248299号公報実施例とは異なる範囲であり、該実
施例の評価方法もデカンターを想定したものでは無い。
すなわち特開昭60−248299号公報から本願発
明を成す事は困難であり、その進歩性ならびに新規性は
十分に特許に値するものと考える。 なお両性高分子
(A)および(B)の分子式から明らかな様に、両高分
子のカチオン性基は解離しアニオン性基は未解離であ
り、酸性状態にある事は自明である。本願発明に用いる
無機凝集剤としてはポリ塩化アルミニウム(PAC)あ
るいは含鉄PACが好ましく用いられる。 また本願発
明の対象とする有機汚泥は、都市下水の嫌気性消化汚泥
に対して特に有効である。 都市下水の嫌気性消化汚泥
は混合生汚泥に比し、繊維分少なく微細粒子が多くアル
カリ度が高く脱水性が悪く高分子凝集剤添加量が多めに
必要であり、デカンターの処理能力が低くならざるを得
ない。 かかる嫌気性消化汚泥に対して低添加量で有効
な高分子凝集剤の登場は画期的なことである。Japanese Patent Application Laid-Open No. 60-248299 discloses an organic sludge containing an acrylic acid hydrazide-based polymer compound, a polymer compound containing an amino group or a quaternary ammonium salt, and an acid or acid salt, and a neutral salt. And a solution containing at least one selected from alkali and alkaline salts are described. The high molecular compound containing an amino group or a quaternary ammonium salt mentioned here avoids the production of acrylic acid in the description of the detailed description of the invention in the specification. It is clear that no system polymer flocculant is assumed. The composition of the acrylic acid hydrazide polymer compound described in the examples is a substance different from that of the present invention. That is, the acrylic acid hydrazide polymer compound of the present invention is a polymer having a crosslinked bond of several tens ppm to several hundred ppm obtained by reacting polyacrylamide with anhydrous hydrazine, and thus exhibits a special aggregation behavior. It exhibits a synergistic effect with the (meth) acrylate polymer flocculant and shows a strong flocculating effect. (D + e
The description of + f = about 100 mol% is due to the result of the presence of the above trace amount of cross-linking. ) Polymer mixing ratio is also
The range is different from that of the embodiment of 248299, and the evaluation method of the embodiment does not assume a decanter.
That is, it is difficult to make the invention of the present application based on Japanese Patent Application Laid-Open No. Sho 60-248299, and its inventive step and novelty are considered to be sufficiently worthy of a patent. As is apparent from the molecular formulas of the amphoteric polymers (A) and (B), it is obvious that the cationic groups of both polymers are dissociated and the anionic groups are not dissociated, and that they are in an acidic state. As the inorganic flocculant used in the present invention, polyaluminum chloride (PAC) or iron-containing PAC is preferably used. The organic sludge targeted by the present invention is particularly effective for anaerobic digested sludge of municipal sewage. Anaerobic digestion sludge from municipal sewage requires less fiber, more fine particles, higher alkalinity, poor dehydration, higher polymer coagulant addition, and lower decanter processing capacity than mixed raw sludge. I have no choice. The emergence of a high-polymer flocculant effective at a low addition amount for such anaerobic digested sludge is a breakthrough.
【0006】[0006]
【実施例】次に実施例によって、本発明を具体的に説明
するが、本発明はその要旨を超えない限り、以下の実施
例に制約されるものではない。EXAMPLES Next, the present invention will be described in detail with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist.
【0007】本願発明に用いる高分子凝集剤(A)は
(メタ)アクリレートカチオンモノマー,アクリルアミ
ド,アクリル酸を脱塩水に溶解し、脱酸素後に和光純薬
株式会社製水溶性アゾ系ラジカル発生剤V−50を添加
して重合を行い、ポリマー濃度0.2%の希釈水溶液と
して試験に供した。 PH調整のため対ポリマー5%の
塩酸を混合した。 本願発明に用いる高分子凝集剤
(B)はポリアクリルアミドの逆相乳化重合物を加熱脱
水した乾燥微粒分散液に無水ヒドラジンを加えて加熱反
応したのち、希塩酸水溶液に溶解して対イオンを含むポ
リマー濃度が0.2%水溶液となる様に希釈し、試験に
供した。 PH3とPH10におけるコロイド適定値に
よりカチオン量とアニオン量を求め組成を決定した。
高分子凝集剤(A)および高分子凝集剤(B)の固有粘
度は1規定食塩水中で25°Cにてオストワルド粘度計
によって還元粘度を測定し決定した。 高分子凝集剤
(A)の特性を表ー1に示す。The polymer coagulant (A) used in the present invention is obtained by dissolving a (meth) acrylate cationic monomer, acrylamide and acrylic acid in deionized water, and after deoxygenation, a water-soluble azo radical generator V manufactured by Wako Pure Chemical Industries, Ltd. Polymerization was carried out by adding -50, and the mixture was subjected to a test as a dilute aqueous solution having a polymer concentration of 0.2%. Hydrochloric acid of 5% with respect to the polymer was mixed for pH adjustment. The polymer flocculant (B) used in the present invention is a polymer containing a counter ion dissolved in a dilute hydrochloric acid aqueous solution after adding anhydrous hydrazine to a dry fine particle dispersion obtained by heating and dehydrating a reversed-phase emulsion polymer of polyacrylamide, and then dissolving in a dilute hydrochloric acid aqueous solution. It diluted so that it might become a 0.2% aqueous solution, and used for the test. The amounts of cations and anions were determined from the appropriate colloid values at PH3 and PH10 to determine the composition.
The intrinsic viscosities of the polymer flocculant (A) and the polymer flocculant (B) were determined by measuring the reduced viscosity with a Ostwald viscometer at 25 ° C. in 1N saline. Table 1 shows the characteristics of the polymer flocculant (A).
【表1】 同様に高分子凝集剤(B)の特性を表ー2に示す。[Table 1] Similarly, the properties of the polymer flocculant (B) are shown in Table-2.
【表2】 この両者を混合して試料を調整し効果試験に供した。[Table 2] These were mixed to prepare a sample, which was subjected to an effect test.
【0008】[0008]
効果試験−1 都市下水汚泥の嫌気性消化汚泥(SS:9000pp
m,PH:7.35)にポリ塩化アルミニウムをアルミ
ナ(Al2 O3 )換算対SS3%を添加混合後、高分子
凝集剤を機内薬注により添加混合し、デカンターにより
脱水した。 脱水試験の結果を表ー3に示す。 薬注量
は98%以上の回収率が得られる量とする。Effect test-1 Anaerobic digestion sludge of municipal sewage sludge (SS: 9000 pp)
m, PH: 7.35), polyaluminum chloride was added and mixed with 3 % of SS (alumina (Al 2 O 3 ) in terms of Al 2 O 3 ), and then a polymer flocculant was added and mixed by in-machine injection, followed by dehydration with a decanter. Table 3 shows the results of the dehydration test. The chemical injection amount is an amount that can obtain a recovery rate of 98% or more.
【表3】 本願発明の薬注量低下効果は顕著であり経費削減に有効
である。なお、特開昭60−248299号公報実施例
に記載されたと同等のポリアクリルアミドのマンニッヒ
変性物と高分子凝集剤(B)各例との等量混合物は回収
率95%以上に成らなかった。 効果試験−2 効果試験−1に用いた汚泥にポリ塩化アルミニウムをア
ルミナ(Al2 O3 )換算対SS3%を添加混合後、凝
集槽に高分子凝集剤を添加混合しフロックを形成したの
ちデカンターに供給したところ、効果試験−1の各添加
量において全て回収率は70%以下であった。 この事
から本願発明のポリマー添加は機内薬注が絶対必要条件
であることがわかる。[Table 3] The effect of the present invention on reducing the amount of injected medicine is remarkable and is effective for cost reduction. Incidentally, an equivalent mixture of the Mannich-modified polyacrylamide and each of the examples of the polymer flocculant (B) equivalent to those described in the examples of JP-A-60-248299 did not achieve a recovery rate of 95% or more. Effect Test -2 effect test sludge on polyaluminum chloride used -1 alumina (Al 2 O 3) after adding and mixing a conversion pair SS3%, decanter after forming the floc was added and mixed polymeric flocculant flocculation tank , The recovery rate was 70% or less for each addition amount of the effect test-1. From this fact, it is understood that in-flight injection is an absolutely necessary condition for the addition of the polymer of the present invention.
Claims (5)
に、下記式(1)で表される両性高分子凝集剤(A)お
よび式(2)で表される両性高分子凝集剤(B)を混合
してなる汚泥脱水剤の水溶液を機内薬注して、デカンタ
ー内にて該汚泥を凝集させ、脱水する事を特徴とする汚
泥の処理方法。 【化1】 (式中R1 は水素原子またはメチル基、R2 はエチレン
基またはプロピレン基、R3 ,R4 はメチル基またはエ
チル基、R5 は水素原子, メチル基,エチル基またはベ
ンジル基、X- は対アニオンを表す。 またa+b+c
=100モル%,a=10〜50モル%,b=45〜8
5モル%,c=5〜50モル%の関係を有する。) 【化2】 (d+e+f=約100モル%,d=10〜30モル
%,e=30〜80モル%,f=10〜40モル%の関
係を有する。)An amphoteric polymer flocculant (A) represented by the following formula (1) and an amphoteric polymer flocculant (B) represented by the following formula (2) after adding and mixing an inorganic flocculant to the organic sludge. ), Wherein an aqueous solution of a sludge dewatering agent obtained by mixing the sludge is injected into the machine, the sludge is coagulated in a decanter, and the sludge is dewatered. Embedded image (Wherein R 1 is a hydrogen atom or a methyl group, R 2 is an ethylene group or a propylene group, R 3 and R 4 are a methyl group or an ethyl group, R 5 is a hydrogen atom , a methyl group, an ethyl group or a benzyl group, X − Represents a counter anion, and a + b + c
= 100 mol%, a = 10 to 50 mol%, b = 45 to 8
5 mol%, c = 5 to 50 mol%. ) (D + e + f = about 100 mol%, d = 10 to 30 mol%, e = 30 to 80 mol%, and f = 10 to 40 mol%)
子凝集剤(B)を6:4〜8:2の比率で併用する事を
特徴とする請求項1に記載の汚泥の処理方法。2. The method for treating sludge according to claim 1, wherein the amphoteric polymer flocculant (A) and the amphoteric polymer flocculant (B) are used together in a ratio of 6: 4 to 8: 2. .
ウム塩である事を特徴とする請求項1ないし請求項2に
記載の汚泥の処理方法。3. The method for treating sludge according to claim 1, wherein the inorganic coagulant is an iron salt and / or an aluminum salt.
る事を特徴とする請求項1ないし請求項3に記載の汚泥
の処理方法。4. The method for treating sludge according to claim 1, wherein the inorganic flocculant is polyaluminum chloride.
ことを特徴とする請求項1ないし請求項4に記載の汚泥
の処理方法。5. The method for treating sludge according to claim 1, wherein the organic sludge is anaerobic digestion sludge of sewage.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17438296A JP3633726B2 (en) | 1996-06-14 | 1996-06-14 | Sludge treatment method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17438296A JP3633726B2 (en) | 1996-06-14 | 1996-06-14 | Sludge treatment method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10500A true JPH10500A (en) | 1998-01-06 |
JP3633726B2 JP3633726B2 (en) | 2005-03-30 |
Family
ID=15977647
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17438296A Expired - Fee Related JP3633726B2 (en) | 1996-06-14 | 1996-06-14 | Sludge treatment method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3633726B2 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002100944A1 (en) * | 2001-06-11 | 2002-12-19 | Hymo Corporation | Amphoteric water-soluble polymer dispersion and use thereof |
JP2003117309A (en) * | 2001-10-11 | 2003-04-22 | Toagosei Co Ltd | Composition, amphoteric polymer coagulant and dehydration method of sludge |
JP2003175302A (en) * | 2001-09-04 | 2003-06-24 | Toagosei Co Ltd | Composition, amphoteric polymeric flocculant and use of them |
US7141181B2 (en) * | 2001-09-04 | 2006-11-28 | Toagosei Co., Ltd. | Composition comprising amphoteric polymeric flocculants |
JP2007061773A (en) * | 2005-09-01 | 2007-03-15 | Kobelco Eco-Solutions Co Ltd | Organic sludge treatment method and apparatus |
JP4894264B2 (en) * | 2004-01-20 | 2012-03-14 | 東亞合成株式会社 | Composition comprising amphoteric water-soluble polymer |
CN105551534A (en) * | 2015-11-13 | 2016-05-04 | 中国核动力研究设计院 | Reactor coolant chemical and volume control system and control method thereof |
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1996
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Cited By (8)
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WO2002100944A1 (en) * | 2001-06-11 | 2002-12-19 | Hymo Corporation | Amphoteric water-soluble polymer dispersion and use thereof |
US7250462B2 (en) | 2001-06-11 | 2007-07-31 | Hymo Corporation | Amphoteric water-soluble polymer dispersion and use thereof |
JP2003175302A (en) * | 2001-09-04 | 2003-06-24 | Toagosei Co Ltd | Composition, amphoteric polymeric flocculant and use of them |
US7141181B2 (en) * | 2001-09-04 | 2006-11-28 | Toagosei Co., Ltd. | Composition comprising amphoteric polymeric flocculants |
JP2003117309A (en) * | 2001-10-11 | 2003-04-22 | Toagosei Co Ltd | Composition, amphoteric polymer coagulant and dehydration method of sludge |
JP4894264B2 (en) * | 2004-01-20 | 2012-03-14 | 東亞合成株式会社 | Composition comprising amphoteric water-soluble polymer |
JP2007061773A (en) * | 2005-09-01 | 2007-03-15 | Kobelco Eco-Solutions Co Ltd | Organic sludge treatment method and apparatus |
CN105551534A (en) * | 2015-11-13 | 2016-05-04 | 中国核动力研究设计院 | Reactor coolant chemical and volume control system and control method thereof |
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