JP2001062500A - Dehydrating method using carbonate sludge - Google Patents

Dehydrating method using carbonate sludge

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Publication number
JP2001062500A
JP2001062500A JP24414999A JP24414999A JP2001062500A JP 2001062500 A JP2001062500 A JP 2001062500A JP 24414999 A JP24414999 A JP 24414999A JP 24414999 A JP24414999 A JP 24414999A JP 2001062500 A JP2001062500 A JP 2001062500A
Authority
JP
Japan
Prior art keywords
sludge
carbonated
added
centrifugal dehydrator
sewage
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.)
Pending
Application number
JP24414999A
Other languages
Japanese (ja)
Inventor
Makoto Terunuma
誠 照沼
Hiroaki Miwa
宏明 三羽
Miyuki Fujiwara
幸 藤原
Hidekazu Shoji
英一 庄子
Yoshio Akazawa
義雄 赤澤
Tetsuji Mazaki
哲二 眞崎
Kenichi Kamiide
健一 上出
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP24414999A priority Critical patent/JP2001062500A/en
Publication of JP2001062500A publication Critical patent/JP2001062500A/en
Pending legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce the water content in a dehydrated cake and to decrease the quantity of the cake generated by carbonating sewage sludge, mixing the carbonated sludge having prescribed particle diameter with sewage sludge to be dehydrated and supplying a high molecular flocculant with the mixture to a centrifugal dehydrator or a belt type dehydrator to dehydrate. SOLUTION: The concentrated sludge 1 is stored in a sludge storing vessel 2 and the carbonated sludge 3 is added thereinto in a prescribed ratio. The concentrated sludge 1, in which the carbonated sludge 3 is added, is supplied to a centrifugal dehydrator 5 by a crushing pump 4. A polymer 6 of the high molecular flocculant is added into the centrifugal dehydrator 5 in a prescribed ratio. The carbonated sludge 3 acts as a nucleus at the time of forming floc in the flocculation of the sewage sludge by the polymer 6 to form large floc and to increase the flocculation effect. Because the flocculation effect is increased by the action of the carbonated sludge 3 in the centrifugal dehydrator 5, the sludge is easily settled and the dehydration property is improved, the water content in the dehydrated cake 7 is decreased and the stripping property to the filter cloth is improved.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、下水処理場におけ
る下水汚泥脱水の技術に係り、下水汚泥を炭化してなる
炭化汚泥を利用する脱水方法に関する。
The present invention relates to a technology for dewatering sewage sludge in a sewage treatment plant, and to a dewatering method using carbonized sludge obtained by carbonizing sewage sludge.

【0002】[0002]

【従来の技術】従来、下水処理場で発生する下水汚泥
は、脱水後の脱水ケーキの一部を溶融炉において溶融処
理して溶融スラグ化し、その有効利用を図っているが、
下水汚泥の全量を溶融処理できず、大部分を脱水ケーキ
として埋立処分している。しかし、近年においては最終
処分場を確保することが困難となっており、汚泥の減容
化と安定化が切望されるとともに、下水汚泥の有効利用
の推進が急務となっている。
2. Description of the Related Art Conventionally, sewage sludge generated in a sewage treatment plant has been subjected to a melting treatment of a part of a dewatered cake after dehydration in a melting furnace to form a molten slag for effective use.
The entire amount of sewage sludge cannot be melted and most of it is landfilled as dewatered cake. However, in recent years, it has become difficult to secure a final disposal site, and there is an urgent need to reduce and stabilize sludge, and there is an urgent need to promote the effective use of sewage sludge.

【0003】[0003]

【発明が解決しようとする課題】下水汚泥の脱水処理で
は、遠心脱水機、ベルトプレスにおける脱水助剤として
高分子凝集剤を下水汚泥に添加して脱水している。この
脱水機の性能および脱水ケーキ含水率はそれぞれ表1
(遠心脱水機)、表2(ベルトプレス)に示すようなもので
ある。
In the dewatering treatment of sewage sludge, a polymer flocculant is added to sewage sludge as a dewatering aid in a centrifugal dewatering machine and a belt press to dewater. Table 1 shows the performance of this dehydrator and the water content of the dehydrated cake.
(Centrifugal dehydrator), as shown in Table 2 (belt press).

【0004】[0004]

【表1】 [Table 1]

【0005】[0005]

【表2】 しかし、従来の高分子凝集剤だけでは、ケーキ含水率を
78%以下に低減できない問題があった。本発明は上記
した課題を解決するものであり、脱水ケーキの含水率を
低減し、含水率の低減によってケーキ発生量を低減でき
る炭化汚泥を利用する脱水方法を提供することを目的と
する。
[Table 2] However, there was a problem that the water content of the cake could not be reduced to 78% or less using only the conventional polymer flocculant. An object of the present invention is to solve the above-mentioned problems, and an object of the present invention is to provide a dewatering method using carbonized sludge that can reduce the water content of a dewatered cake and reduce the amount of cake generated by reducing the water content.

【0006】[0006]

【課題解決するための手段】上記課題を解決するため
に、本発明の炭化汚泥を利用する脱水方法は、下水汚泥
を炭化して炭化汚泥を生成し、この所定粒径の炭化汚泥
を脱水対象の下水汚泥に添加して混合し、この混合物と
ともに高分子凝集剤を遠心脱水機もしくはベルトプレス
脱水機に供給して脱水するものである。
In order to solve the above-mentioned problems, a dewatering method using carbonized sludge according to the present invention is characterized in that sewage sludge is carbonized to form carbonized sludge, and the carbonized sludge having a predetermined particle size is subjected to dehydration. Is added to sewage sludge and mixed, and a polymer flocculant is supplied to a centrifugal dehydrator or a belt press dehydrator together with the mixture to be dehydrated.

【0007】上記した構成により、高分子凝集剤による
下水汚泥の凝集に際して炭化汚泥がフロック形成時に核
として作用し、大きなフロックを形成して凝集効果を高
める。このため、脱水性が向上して脱水ケーキの含水率
を低減することができ、含水率の低減によって脱水ケー
キの発生量を低減できる。また、炭化汚泥の吸着能によ
って脱水ケーキを脱臭して原臭濃度を低減でき、脱水ろ
液の清澄度を高めることができる。
[0007] With the above-described structure, carbonized sludge acts as a nucleus when flocs are formed during flocculation of sewage sludge by a polymer flocculant, and forms large flocs to enhance the flocculating effect. For this reason, the dewatering property can be improved and the water content of the dewatered cake can be reduced, and the amount of dewatered cake generated can be reduced by reducing the water content. Further, the dewatered cake can be deodorized by the adsorption ability of the carbonized sludge to reduce the original odor concentration, and the clarity of the dehydrated filtrate can be increased.

【0008】[0008]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。図1において、濃縮汚泥1は、下
水をオキシデーションディッチで処理して後に濃縮槽に
貯留し、重力沈降により濃縮したものである。この濃縮
汚泥1を汚泥貯留槽2に貯留し、炭化汚泥3を汚泥固形
物当り10〜30%の割合で添加する。炭化汚泥3の添
加は脱水を行なう前日ぐらいに投入するとより効果的で
ある。この炭化汚泥3を添加した濃縮汚泥1を破砕ポン
プ4によって遠心脱水機5へ供給する。
Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, concentrated sludge 1 is obtained by treating sewage by an oxidation ditch, storing the treated sewage in a concentration tank, and then concentrating by gravity sedimentation. This concentrated sludge 1 is stored in a sludge storage tank 2, and carbonized sludge 3 is added at a rate of 10 to 30% based on sludge solids. It is more effective to add the carbonized sludge 3 when the sludge is added about the day before dehydration. The concentrated sludge 1 to which the carbonized sludge 3 has been added is supplied to a centrifugal dehydrator 5 by a crushing pump 4.

【0009】遠心脱水機5には、高分子凝集剤であるポ
リマー6を汚泥固形物当り0.5〜1.2%の割合で添
加する。このとき、ポリマー6による下水汚泥の凝集に
際して炭化汚泥3がフロック形成時に核として作用し、
大きなフロックを形成して凝集効果を高める。このた
め、炭化汚泥3は1〜5mmφ程度の粒径を有する粒子
状が好適な形状である。
[0009] To the centrifugal dehydrator 5, a polymer 6 as a polymer flocculant is added at a ratio of 0.5 to 1.2% based on sludge solids. At this time, at the time of flocculation of sewage sludge by the polymer 6, the carbonized sludge 3 acts as a nucleus at the time of floc formation,
Form large flocs to enhance coagulation effect. Therefore, the carbonized sludge 3 is preferably in the form of particles having a particle size of about 1 to 5 mmφ.

【0010】この遠心脱水機5では、炭化汚泥3の作用
によって凝集効果が高まっているので、汚泥が沈降し易
く脱水性が向上し、脱水ケーキ7の含水率を低減するこ
とができ、かつ炭化汚泥粒子の存在によってろ布に対す
る剥離性が向上する。脱水ケーキ7はその一部もしくは
全量を炭化炉(図示省略)に投入して炭化し、生成する
炭化汚泥3を脱水性改善剤として循環利用する。
In the centrifugal dewatering machine 5, the effect of the carbonized sludge 3 enhances the coagulation effect, so that the sludge is liable to settle, the dewatering property is improved, and the water content of the dewatered cake 7 can be reduced. The presence of the sludge particles improves the releasability of the filter cloth. A part or all of the dewatered cake 7 is put into a carbonization furnace (not shown) and carbonized, and the generated carbonized sludge 3 is circulated and used as a dewatering property improving agent.

【0011】表3に従来の構成と、本発明の炭化汚泥3
を脱水性改善剤として添加する構成との比較を示す。
Table 3 shows the conventional structure and the carbonized sludge 3 of the present invention.
Is shown in comparison with a configuration in which is added as a dehydration improver.

【0012】[0012]

【表3】 表3において、炭化汚泥3の投入により脱水ケーキ当り
で汚泥量が1.2倍となっているが、炭化汚泥3による
脱水性の向上によってケーキ含水率が65〜70%に低
下しているので、結果として脱水ケーキ7の発生量を低
減できる。脱水ケーキ7の一部を炭化汚泥3の原料とし
て使用することにより、搬出するケーキ量を削減でき、
脱水ケーキ7の全量を炭化汚泥3の原料とする場合に
は、搬出するケーキ量は無くなり、炭化汚泥3を燃料等
の有価物として貯留できる。炭化汚泥3はその吸着能に
より脱臭効果を発揮し、硫化水素:90%以上、硫化メ
チル:50%以上、メチルメルカプタン:80%以上の
除去効果を得ることができ、脱水ケーキの原臭濃度が低
下するので、後工程においける脱臭用薬剤の使用量の低
減、活性炭の長寿命化等の効果を得られる。また、炭化
汚泥3の吸着能により、脱水ろ液中のBODおよびCO
D濃度が低下するので、脱水ろ液の水処理におけるBO
D負荷を低減できる。
[Table 3] In Table 3, the sludge amount per dewatered cake was increased by 1.2 times by the introduction of the carbonized sludge 3, but the water content of the cake was reduced to 65 to 70% by the improvement of the dewatering property by the carbonized sludge 3. As a result, the amount of dewatered cake 7 generated can be reduced. By using a part of the dewatered cake 7 as a raw material of the carbonized sludge 3, the amount of cake to be carried out can be reduced,
When the entire amount of the dewatered cake 7 is used as a raw material of the carbonized sludge 3, the amount of cake to be carried out is eliminated, and the carbonized sludge 3 can be stored as a valuable material such as fuel. The carbonized sludge 3 exhibits a deodorizing effect due to its adsorption ability, and can obtain a removing effect of hydrogen sulfide: 90% or more, methyl sulfide: 50% or more, methyl mercaptan: 80% or more. Since the amount decreases, the effect of reducing the amount of the deodorizing agent used in the post-process and extending the life of the activated carbon can be obtained. In addition, BOD and CO in the dehydrated filtrate are determined by the adsorption capacity of the carbonized sludge 3.
As the D concentration decreases, BO in the water treatment of the dehydrated filtrate is reduced.
D load can be reduced.

【0013】図2に示すように、汚泥貯留槽2において
炭化汚泥3を添加した濃縮汚泥1は、高分子凝集剤であ
るポリマー6とともに、ベルトプレス脱水機8へ供給
し、脱水を行なうこともできる。この場合も、ポリマー
6は汚泥固形物当り0.5〜1.2%の割合で添加す
る。表4に従来の構成と、本発明の炭化汚泥3を脱水性
改善剤として添加する構成との比較を示す。
As shown in FIG. 2, the concentrated sludge 1 to which the carbonized sludge 3 has been added in the sludge storage tank 2 is supplied to a belt press dewatering machine 8 together with a polymer 6 which is a polymer flocculant, and may be dewatered. it can. Also in this case, the polymer 6 is added at a ratio of 0.5 to 1.2% based on the sludge solids. Table 4 shows a comparison between a conventional configuration and a configuration in which the carbonized sludge 3 of the present invention is added as a dewatering property improving agent.

【0014】[0014]

【表4】 [Table 4]

【0015】[0015]

【発明の効果】以上のように本発明によれば、炭化汚泥
がフロック形成時に核として作用して凝集効果を高める
ので、脱水性が向上して脱水ケーキの含水率を低減する
ことができ、含水率の低減によって脱水ケーキの発生量
を低減できる。また、炭化汚泥の吸着能によって脱水ケ
ーキを脱臭して原臭濃度を低減でき、脱水ろ液の清澄度
を高めることができる。
As described above, according to the present invention, the carbonized sludge acts as a nucleus at the time of floc formation and enhances the coagulation effect, so that the dewaterability is improved and the water content of the dewatered cake can be reduced. The amount of dewatered cake generated can be reduced by reducing the water content. Further, the dewatered cake can be deodorized by the adsorption ability of the carbonized sludge to reduce the original odor concentration, and the clarity of the dehydrated filtrate can be increased.

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

【図1】本発明の実施の形態における脱水のフローシー
トである。
FIG. 1 is a dehydration flow sheet according to an embodiment of the present invention.

【図2】本発明の他の実施の形態における脱水のフロー
シートである。
FIG. 2 is a dehydration flow sheet according to another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 濃縮汚泥 2 汚泥貯留槽 3 炭化汚泥 4 破砕ポンプ 5 遠心脱水機 6 ポリマー 7 脱水ケーキ DESCRIPTION OF SYMBOLS 1 Condensed sludge 2 Sludge storage tank 3 Carbonized sludge 4 Crushing pump 5 Centrifugal dehydrator 6 Polymer 7 Dehydration cake

───────────────────────────────────────────────────── フロントページの続き (72)発明者 三羽 宏明 愛知県名古屋市守山区白山1丁目811番地 (72)発明者 藤原 幸 秋田県由利郡大内町葛岡字宮ノ前31番地 (72)発明者 庄子 英一 北海道虻田郡豊浦町字東雲町48番地8 (72)発明者 赤澤 義雄 埼玉県浦和市宮本2−8−34 (72)発明者 眞崎 哲二 東京都板橋区徳丸8−25−13 メゾン ア ジュール205 (72)発明者 上出 健一 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 Fターム(参考) 4D059 AA03 BB05 BE08 BE16 BE38 BE56 BE64 BK02 CA24 CC05 CC06 DA70 DB40  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Hiroaki Miwa 1-811 Hakusan, Moriyama-ku, Nagoya-shi, Aichi Prefecture (72) Inventor Sachi Fujiwara 31 Miyano-mae, Kuzuoka, Ouchi-cho, Yuri-gun, Akita Prefecture (72) Inventor Eiichi Shoko 48-8 Shinonome-cho, Toyoura-cho, Abuta-gun, Hokkaido (72) Inventor Yoshio Akazawa 2-8-34 Miyamoto, Urawa-shi, Saitama (72) Inventor Tetsuji Masaki 8-25-13 Maison A, Itabashi-ku, Tokyo Jules 205 (72) Inventor Kenichi Ude 2-4-147 Shizitsuhigashi, Naniwa-ku, Osaka-shi

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 下水汚泥を炭化して炭化汚泥を生成し、
この所定粒径の炭化汚泥を脱水対象の下水汚泥に添加し
て混合し、この混合物とともに高分子凝集剤を遠心脱水
機もしくはベルトプレス脱水機に供給して脱水すること
を特徴とする炭化汚泥を利用する脱水方法。
Claims: 1. Sewage sludge is carbonized to produce carbonized sludge,
The carbonized sludge having the predetermined particle size is added to and mixed with the sewage sludge to be dewatered. Dehydration method used.
JP24414999A 1999-08-31 1999-08-31 Dehydrating method using carbonate sludge Pending JP2001062500A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24414999A JP2001062500A (en) 1999-08-31 1999-08-31 Dehydrating method using carbonate sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24414999A JP2001062500A (en) 1999-08-31 1999-08-31 Dehydrating method using carbonate sludge

Publications (1)

Publication Number Publication Date
JP2001062500A true JP2001062500A (en) 2001-03-13

Family

ID=17114499

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24414999A Pending JP2001062500A (en) 1999-08-31 1999-08-31 Dehydrating method using carbonate sludge

Country Status (1)

Country Link
JP (1) JP2001062500A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008229414A (en) * 2007-03-16 2008-10-02 Makikatsu Takahashi Method and system for preventing generation of odor material
JP4478804B1 (en) * 2009-03-31 2010-06-09 学校法人東邦大学 Organic sludge treatment method
CN102923928A (en) * 2012-10-24 2013-02-13 广东工业大学 Method for improving dehydration performance of sludge by adding tannery sludge incineration bottom ash

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008229414A (en) * 2007-03-16 2008-10-02 Makikatsu Takahashi Method and system for preventing generation of odor material
JP4478804B1 (en) * 2009-03-31 2010-06-09 学校法人東邦大学 Organic sludge treatment method
JP2010234233A (en) * 2009-03-31 2010-10-21 Toho Univ Foundation Organic sludge treatment method
CN102923928A (en) * 2012-10-24 2013-02-13 广东工业大学 Method for improving dehydration performance of sludge by adding tannery sludge incineration bottom ash

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