JPH06134496A - Dehydration of sludge in system to utilize sludge as resource - Google Patents
Dehydration of sludge in system to utilize sludge as resourceInfo
- Publication number
- JPH06134496A JPH06134496A JP4287883A JP28788392A JPH06134496A JP H06134496 A JPH06134496 A JP H06134496A JP 4287883 A JP4287883 A JP 4287883A JP 28788392 A JP28788392 A JP 28788392A JP H06134496 A JPH06134496 A JP H06134496A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- precoat
- supplied
- tank
- dehydration
- 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
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、例えば浄水場から発
生する汚泥や、河川、湖沼等に堆積した汚泥を、脱水し
た後、乾燥、造粒、焼成する汚泥資源化システムに関
し、さらに詳しくは、上記汚泥資源化システムにおける
汚泥の脱水方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sludge resource recycling system for dehydrating, drying, granulating and firing sludge generated from, for example, a water purification plant and sludge accumulated in rivers and lakes. The present invention relates to a sludge dewatering method in the sludge resource recycling system.
【0002】[0002]
【従来の技術】従来、浄水場・下水処理場から発生する
汚泥や、河川・湖沼から浚渫された汚泥(ヘドロ)は、
脱水処理が施された後、その大部分が埋立て処分されて
いた。しかし、汚泥処理量が増大し、埋立て地の確保も
困難になってきている実情に鑑みて、上記汚泥を原料と
して、これを造粒、乾燥、焼成することにより製品価値
の高い粒状焼成品を得る汚泥資源化システムが提案され
ている。2. Description of the Related Art Conventionally, sludge generated from water purification plants and sewage treatment plants and sludge dredged from rivers and lakes (sludge) are
After being dehydrated, most of it was landfilled. However, in view of the fact that the sludge treatment amount is increasing and it is becoming difficult to secure landfill, it is possible to granulate, dry, and calcine the above sludge as a raw material to obtain a granular product with high product value. A sludge resource recovery system for obtaining the above has been proposed.
【0003】ところで、上記汚泥資源化システムにあっ
ても、原料として使用される浄水場発生汚泥等の汚泥
を、まず脱水する必要があるが、その方法としては、デ
ハイドラム脱水機等の重力式脱水機によるもの、ベルト
プレス、フィルタープレス等の圧力式脱水機によるも
の、けいそう土等をプリコート材として使用するプリコ
ートフィルタ式脱水機によるもの等があった。By the way, even in the above sludge resource recycling system, it is necessary to first dehydrate sludge, such as sludge generated from a water purification plant, used as a raw material. As a method therefor, a gravity dehydration method such as a dehydration drum dehydrator is used. There were a machine, a pressure type dehydrator such as a belt press and a filter press, and a precoat filter type dehydrator using diatomaceous earth as a precoat material.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、上述し
た従来の汚泥の脱水方法には、次のような問題があっ
た。すなわち、まず、デハイドラム脱水機等の重力式脱
水機による方法は、脱水効率が低く、したがって、脱水
汚泥を後工程の乾燥工程で乾燥させるさいの負担が大き
く、熱効率的にも不経済であった。しかも、重力式脱水
機では、水ガラスや高分子系凝集剤を多量に投入して汚
泥を濃縮凝集させる必要があった。However, the above-mentioned conventional sludge dewatering method has the following problems. That is, first, the method using a gravity type dehydrator such as a dehydration drum dehydrator has a low dehydration efficiency, and therefore, a heavy burden is required when drying the dehydrated sludge in a subsequent drying step, and it is uneconomical in terms of thermal efficiency. . Moreover, in the gravity type dehydrator, it was necessary to add a large amount of water glass or a polymer-based coagulant to concentrate and coagulate the sludge.
【0005】ベルトプレス、フィルタープレス等の圧力
式脱水機を用いる場合、装置が高価であり、また脱水に
長時間を要するため経済的でなく、しかも、得られた脱
水汚泥(フィルターケーキ)が比較的大きな板状のもの
となるので、貯槽切出しが難しく、大きな開口と幅広の
切出し装置が必要となるとともに、造粒工程の前に脱水
汚泥またはその乾燥物を造粒に適した大きさに解砕する
工程を設ける必要があった。When a pressure type dehydrator such as a belt press and a filter press is used, the apparatus is expensive and it takes a long time to dehydrate, which is not economical, and the dehydrated sludge (filter cake) obtained is compared. Since it is a large plate, it is difficult to cut out the storage tank, a large opening and a wide cutting device are required, and the dehydrated sludge or its dried product is sized to be suitable for granulation before the granulation process. It was necessary to provide a crushing step.
【0006】けいそう土等をプリコート材として使用す
るプリコートフィルタ式脱水機による方法では、装置が
比較的低廉であるという利点があるが、プリコート材と
して多量に使用されるけいそう土等は高価なものであ
り、また汚泥資源化の目的によっては、けいそう土等の
プリコート材が汚泥中に混入するのが望ましくない場合
があった。The method using a precoat filter type dehydrator which uses diatomaceous earth or the like as a precoat material has an advantage that the apparatus is relatively inexpensive, but diatomaceous earth or the like used in large amounts as the precoat material is expensive. Depending on the purpose of recycling sludge, it may not be desirable to mix a precoat material such as diatomaceous earth into the sludge.
【0007】この発明は、上記実情に鑑みて、汚泥の脱
水を低コストで効率的に行なえるとともに、汚泥資源化
に望ましくない他物質が混入することのない汚泥資源化
システムにおける汚泥の脱水方法を提供することを目的
とする。[0007] In view of the above situation, the present invention is a method for dehydrating sludge in a sludge resource recovery system which can efficiently perform sludge dehydration at low cost and does not mix other substances undesired for sludge resource recovery. The purpose is to provide.
【0008】[0008]
【課題を解決するための手段及び作用】この発明による
汚泥資源化システムにおける汚泥の脱水方法は、上記の
目的を達成すべく工夫されたもので、汚泥を脱水した
後、造粒、乾燥、焼成する汚泥資源化システムにおい
て、脱水機としてプリコートフィルタ式脱水機を使用す
るとともに、そのプリコート材として、焼成廃ガス中の
集塵ダスト、細粒状焼成品および/または粗粒状焼成品
の粉砕物を使用することを特徴とするものである。Means and Actions for Solving the Problems The sludge dewatering method in the sludge resource recycling system according to the present invention is devised to achieve the above-mentioned object. After sludge is dehydrated, it is granulated, dried and fired. In the sludge resource recycling system, a pre-coat filter type dehydrator is used as the dehydrator, and dust collected in the firing waste gas, fine-grain burned products and / or crushed coarse-grain burned products are used as the pre-coat material. It is characterized by doing.
【0009】上記方法で得られた脱水汚泥の水分は、通
常60〜75重量%であり、これを造粒するには水分3
5〜45重量%まで乾燥することが好ましい。そのた
め、高熱効率の一次乾燥機により脱水汚泥を一次乾燥
し、その後に造粒が行なわれる。一次乾燥機としては、
高熱効率の間接式熱媒乾燥機が好適に用いられるが、熱
風式乾燥機を用いてもよい。また、上記方法で得られた
脱水汚泥は、比較的薄層であって、塊が小さいため、一
次乾燥機を経て、そのまま造粒機へ供給し、必要粒度に
造粒することができる。The water content of the dehydrated sludge obtained by the above method is usually 60 to 75% by weight.
It is preferable to dry to 5 to 45% by weight. Therefore, the dehydrated sludge is primarily dried by a highly efficient primary dryer, and then granulated. As a primary dryer,
An indirect heat medium dryer with high heat efficiency is preferably used, but a hot air dryer may be used. Further, since the dehydrated sludge obtained by the above method is a relatively thin layer and has a small lump, it can be directly supplied to the granulator through the primary dryer and granulated to a required particle size.
【0010】造粒された汚泥は、二次乾燥機を経て、焼
成機へ供給され、ここで焼成される。焼成温度は、一般
に800〜1200℃である。焼成廃ガスの排出路に
は、バグフィルタ等の集塵装置が設けられ、ここで回収
された集塵ダストが、プリコート材としてプリコートフ
ィルタ式脱水機に供給される。The granulated sludge is supplied to a calciner through a secondary dryer and calcined there. The firing temperature is generally 800 to 1200 ° C. A dust collecting device such as a bag filter is provided in the discharge path of the burning waste gas, and the dust collecting dust collected here is supplied to the precoat filter type dehydrator as a precoat material.
【0011】焼成により得られた粒状焼成品は、スクリ
ーンにかけられて、適宜の粒度を有する焼成品ごとに選
り分けられる。そのうち、細粒状焼成品はそのまま、比
較的粒度の大きい粗粒状焼成品は粉砕機により粉砕され
たのち、プリコート材としてプリコートフィルタ式脱水
機に供給される。The granular fired products obtained by firing are screened and selected according to the fired product having an appropriate particle size. Among them, the fine-granular baked product is kept as it is, and the coarse-granular baked product having a relatively large particle size is pulverized by a pulverizer and then supplied as a precoat material to a precoat filter type dehydrator.
【0012】したがって、上記方法によれば、プリコー
トフィルタ式脱水機のプリコート材として、高価なけい
そう土等の代わりに、焼成廃ガス中の集塵ダスト、細粒
状焼成品および/または粗粒状焼成品の粉砕物を使用す
るため、汚泥の脱水を低コストで効率的に行なうことが
でき、しかも汚泥の資源化に望ましくない場合があるけ
いそう土等の他物質が汚泥中に混入することがないの
で、用途開発を行ない易いという利点がある。Therefore, according to the above method, as the precoat material for the precoat filter type dehydrator, instead of expensive diatomaceous earth or the like, dust collected in the firing waste gas, fine-grain fired product and / or coarse-grain fired Since crushed products are used, sludge can be dehydrated efficiently at low cost, and other substances such as diatomaceous earth that may not be desirable for recycling sludge can be mixed into sludge. Since it does not exist, there is an advantage that application development is easy.
【0013】[0013]
【実施例】以下、この発明の一実施例を図面を参照なが
ら説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.
【0014】この実施例は、浄水場発生汚泥を原料とし
て園芸用土等に利用できる粒状焼成品を製造する汚泥資
源化システムである。浄水場においては、河川から引き
込まれた原水を、沈殿池等に導くとともに、これに凝集
剤を投入して、原水中に含まれる土砂等を凝集沈殿さ
せ、更にこれを濃縮槽に導き、高濃度の汚泥を得る。This embodiment is a sludge resource recycling system for producing granular fired products that can be used as horticultural soil, etc., using the sludge generated in the water purification plant as a raw material. At the water treatment plant, the raw water drawn from the river is guided to a settling basin, etc., and a coagulant is added to this to coagulate and sediment the sediment contained in the raw water, which is then guided to a concentrating tank. Obtain a concentration of sludge.
【0015】得られた高濃度の汚泥は、プリコートフィ
ルタ式脱水機(1) の原液槽(11)に供給される。一方、後
述する焼成廃ガス排出路中に設けられた集塵装置(7) か
らの集塵ダストと、焼成によって得られた粒状焼成品の
うち粗粒状焼成品の粉砕機(8) による粉砕物とが、プリ
コートフィルタ式脱水機(1) のプリコート槽(12)に、そ
れぞれプリコート材として供給され、ここで清水と混合
されてプリコート液が得られる。The obtained high-concentration sludge is supplied to the stock solution tank (11) of the precoat filter type dehydrator (1). On the other hand, the dust collected from the dust collector (7) provided in the burning waste gas discharge passage described later and the pulverized product of the coarse-grained calcinated product of the pulverized product obtained by calcination by the crusher (8) Are supplied as precoat materials to the precoat tank (12) of the precoat filter type dehydrator (1), and are mixed there with fresh water to obtain a precoat liquid.
【0016】そして、まずプリコートフィルタ(13)のタ
ンク(14)内に、プリコート液を供給するとともに、タン
ク(14)内にその下端部が浸された濾過円筒(15)を回転さ
せることにより、濾過円筒(15)の表面に、集塵ダストお
よび粗粒状焼成品の粉砕物よりなるプリコート材の薄層
が形成される。Then, first, while supplying the precoat liquid into the tank (14) of the precoat filter (13), the filtration cylinder (15) having its lower end immersed in the tank (14) is rotated, On the surface of the filtration cylinder (15), a thin layer of the pre-coat material composed of dust collected dust and a crushed product of the coarse-grain fired product is formed.
【0017】次いで、原液槽(11)から汚泥よりなる原液
をタンク(14)に供給し、真空ポンプ(16)を作動させて濾
過円筒(15)内を減圧しながら、濾過円筒(15)を回転さ
せ、汚泥の脱水濾過を行なう。Then, the stock solution consisting of sludge is supplied from the stock solution tank (11) to the tank (14), and the vacuum pump (16) is operated to reduce the pressure in the filter cylinder (15) while the filter cylinder (15) is opened. Rotate and dehydrate and filter sludge.
【0018】脱水濾過により濾過円筒(15)の表面に付着
した水分含量約65重量%の脱水汚泥は、スクレーパ等
によって除滓されて、高熱効率の間接式熱媒式乾燥機よ
りなる一次乾燥機(2) に供給され、ここで乾燥される。The dehydrated sludge having a water content of about 65% by weight attached to the surface of the filtration cylinder (15) by dehydration filtration is removed by a scraper or the like, and a primary dryer composed of an indirect heat medium dryer having high heat efficiency. It is fed to (2) and dried there.
【0019】得られた水分含量約45重量%の乾燥品
は、造粒機(3) へ送られる。The dried product having a water content of about 45% by weight is sent to the granulator (3).
【0020】得られた水分含量約45重量%の汚泥造粒
品は、次いで二次乾燥機(4) へ供給され、ここでさらに
乾燥される。The sludge granulation product having a water content of about 45% by weight is then fed to the secondary dryer (4), where it is further dried.
【0021】得られた水分含量約10重量%の乾燥品
は、焼成機(5) へ送られ、ここで焼成せられる。焼成機
(5) から出た焼成廃ガスは、バグフィルタよりなる集塵
装置(7) に送られ、ここで回収された集塵ダストがプリ
コートフィルタ式脱水機(1) のプリコート槽(12)へ送ら
れる。The dried product having a water content of about 10% by weight is sent to a calciner (5) where it is calcined. Firing machine
The burning waste gas from (5) is sent to the dust collector (7) consisting of a bag filter, and the dust collected here is sent to the precoat tank (12) of the precoat filter dehydrator (1). To be
【0022】焼成により得られた粒状焼成品は、冷却
後、スクリーン(6) に送られて、粒度毎に選り分けられ
る。そして、粒度15mm以上の粗粒状焼成品が、粉砕
機(8)に供給されてここで粉砕され、得られた粉砕物
が、プリコートフィルタ式脱水機(1) のプリコート槽(1
2)へ送られる。The granular fired product obtained by firing is sent to a screen (6) after cooling and is sorted according to the particle size. Then, the coarse-grained fired product having a particle size of 15 mm or more is supplied to the pulverizer (8) and pulverized there, and the obtained pulverized product is the precoat tank (1
Sent to 2).
【0023】[0023]
【発明の効果】この発明によれば、汚泥を脱水した後、
造粒、乾燥、焼成する汚泥資源化システムにおいて、脱
水機としてプリコートフィルタ式脱水機を使用するとと
もに、そのプリコート材として、従来の高価なけいそう
土等を使用する代わりに、焼成廃ガス中の集塵ダスト、
細粒状焼成品および/または粗粒状焼成品の粉砕物を使
用するので、汚泥の脱水を低コストで効率的に行なうこ
とができ、しかも汚泥の資源化に望ましくない場合があ
るけいそう土等の他物質が汚泥中に混入することがない
ので、用途開発を行ない易いという利点がある。According to the present invention, after dewatering sludge,
In a sludge resource recycling system for granulating, drying and firing, a precoat filter type dehydrator is used as the dehydrator, and as the precoat material, instead of using conventional expensive diatomaceous earth, etc., Dust collection dust,
Since finely pulverized and / or coarsely pulverized pulverized products are used, sludge can be dehydrated efficiently at low cost, and it may not be desirable for sludge to be recycled as diatomaceous earth. Since other substances are not mixed in the sludge, there is an advantage that the application can be easily developed.
【図1】この発明の実施例を示すフローシートである。FIG. 1 is a flow sheet showing an embodiment of the present invention.
(1) …… プリコートフィルタ式脱水機 (2) …… 一次乾燥機 (3) …… 造粒機 (4) …… 二次乾燥機 (5) …… 焼成機 (6) …… スクリーン (7) …… 集塵装置 (8) …… 粉砕機 (1) …… Pre-coated filter dehydrator (2) …… Primary dryer (3) …… Granulator (4) …… Secondary dryer (5) …… Firing machine (6) …… Screen (7) ) …… Dust collector (8) …… Crusher
Claims (1)
汚泥資源化システムにおいて、脱水機としてプリコート
フィルタ式脱水機を使用するとともに、そのプリコート
材として、焼成廃ガス中の集塵ダスト、細粒状焼成品お
よび/または粗粒状焼成品の粉砕物を使用することを特
徴とする、汚泥資源化システムにおける汚泥の脱水方
法。1. A sludge resource recycling system in which sludge is dehydrated, then granulated, dried and fired, and a precoat filter type dehydrator is used as the dehydrator, and dust collected in the firing waste gas is used as the precoat material. A method for dewatering sludge in a sludge recycling system, characterized by using a pulverized product of a fine-grain baked product and / or a coarse-grain baked product.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4287883A JP2779887B2 (en) | 1992-10-26 | 1992-10-26 | Sludge dewatering method in sludge recycling system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4287883A JP2779887B2 (en) | 1992-10-26 | 1992-10-26 | Sludge dewatering method in sludge recycling system |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06134496A true JPH06134496A (en) | 1994-05-17 |
JP2779887B2 JP2779887B2 (en) | 1998-07-23 |
Family
ID=17722963
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4287883A Expired - Fee Related JP2779887B2 (en) | 1992-10-26 | 1992-10-26 | Sludge dewatering method in sludge recycling system |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2779887B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0782879A1 (en) * | 1995-12-21 | 1997-07-09 | Altenburger Electronic GmbH | Process and apparatus for the micro- and ultrafiltration of suspensions |
KR20010083023A (en) * | 2000-04-01 | 2001-08-31 | 차상태 | System of filtering wastewater and method thereof |
JP4478804B1 (en) * | 2009-03-31 | 2010-06-09 | 学校法人東邦大学 | Organic sludge treatment method |
CN105859100A (en) * | 2016-05-30 | 2016-08-17 | 葛洲坝中固科技股份有限公司 | Cement kiln/sludge deep dewatering synergic sludge integrated treatment method and system |
JP2016532553A (en) * | 2013-08-19 | 2016-10-20 | ポール コーニグ, | Waste treatment system |
CN111253040A (en) * | 2020-03-07 | 2020-06-09 | 福建省明能新型建材有限公司 | Domestic sludge rapid drying equipment for ceramsite production |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5334176A (en) * | 1976-09-13 | 1978-03-30 | Suido Kiko Kk | Filter medium |
-
1992
- 1992-10-26 JP JP4287883A patent/JP2779887B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5334176A (en) * | 1976-09-13 | 1978-03-30 | Suido Kiko Kk | Filter medium |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0782879A1 (en) * | 1995-12-21 | 1997-07-09 | Altenburger Electronic GmbH | Process and apparatus for the micro- and ultrafiltration of suspensions |
KR20010083023A (en) * | 2000-04-01 | 2001-08-31 | 차상태 | System of filtering wastewater and method thereof |
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 |
JP2016532553A (en) * | 2013-08-19 | 2016-10-20 | ポール コーニグ, | Waste treatment system |
US10195552B2 (en) | 2013-08-19 | 2019-02-05 | Paul KOENIG | Waste processing system |
CN105859100A (en) * | 2016-05-30 | 2016-08-17 | 葛洲坝中固科技股份有限公司 | Cement kiln/sludge deep dewatering synergic sludge integrated treatment method and system |
CN111253040A (en) * | 2020-03-07 | 2020-06-09 | 福建省明能新型建材有限公司 | Domestic sludge rapid drying equipment for ceramsite production |
Also Published As
Publication number | Publication date |
---|---|
JP2779887B2 (en) | 1998-07-23 |
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