JPH0975982A - Mixed bed type anaerobic treatment device for organic waste water - Google Patents

Mixed bed type anaerobic treatment device for organic waste water

Info

Publication number
JPH0975982A
JPH0975982A JP23014995A JP23014995A JPH0975982A JP H0975982 A JPH0975982 A JP H0975982A JP 23014995 A JP23014995 A JP 23014995A JP 23014995 A JP23014995 A JP 23014995A JP H0975982 A JPH0975982 A JP H0975982A
Authority
JP
Japan
Prior art keywords
bed type
mixed bed
waste water
anaerobic treatment
treatment device
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
JP23014995A
Other languages
Japanese (ja)
Inventor
Nobuyuki Shima
宣行 志摩
Takashi Numa
隆志 沼
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.)
Nisshin Seito KK
Hitachi Zosen Corp
Original Assignee
Nisshin Seito KK
Hitachi Zosen 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 Nisshin Seito KK, Hitachi Zosen Corp filed Critical Nisshin Seito KK
Priority to JP23014995A priority Critical patent/JPH0975982A/en
Publication of JPH0975982A publication Critical patent/JPH0975982A/en
Pending legal-status Critical Current

Links

Classifications

    • Y02W10/12

Abstract

PROBLEM TO BE SOLVED: To provide a mixed bed type anaerobic treatment device for organic waste water enabling to treat SS-containing waste water at high speed and also to make the device compact. SOLUTION: In this mixed bed type anaerobic treatment device for organic waste water, a mixed bed type filling layer 7 in which a carrier 2 and granular sludge 3 are coexisted is filled in the reaction tank 1.

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】この発明は、食品産業廃水や
生活廃水などの高濃度の浮遊物質(SS)含有有機性廃
水のミックスベッド式嫌気性処理装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a mixed bed type anaerobic treatment apparatus for organic wastewater containing a high concentration of suspended solids (SS) such as food industry wastewater and domestic wastewater.

【0002】[0002]

【従来の技術】嫌気性処理には、メタン生成菌が凝集し
てなるグラニュール汚泥(図2参照)を用いる上向流式
嫌気性汚泥床法(UASB)法、消化汚泥をセラミック
スペレット担体に付着させ、この炉材を流動床または固
定床で用いる方法などが採用されている。
2. Description of the Related Art For anaerobic treatment, an upflow anaerobic sludge bed method (UASB) method using granulated sludge (see FIG. 2) formed by aggregating methanogens, and digested sludge as a ceramic pellet carrier. The method of adhering and using this furnace material in a fluidized bed or a fixed bed is adopted.

【0003】しかし、これらの方法は、個々には、高負
荷廃水の処理を行なえる機能や、SSの効率的な除去が
行なえるメリットをもつ反面、反応槽内でのSSの堆積
によるグラニュール汚泥の槽外流出や、処理水のSS通
過による処理水質の低下といった問題がある。
However, these methods have the function of treating high-load wastewater individually and the advantage of being able to remove SS efficiently, but on the other hand, they are granulated by the accumulation of SS in the reaction tank. There are problems such as sludge flowing out of the tank and deterioration of treated water quality due to passing of treated water through SS.

【0004】また、有機物濃度が低中濃度(COD:2
00〜2000mg/l)であるSS含有廃水は、立ち
上り運転に長期間を要する難点がある。
The organic matter concentration is low and medium (COD: 2).
The SS-containing wastewater of 0 to 2000 mg / l) has a drawback that it takes a long time to start up.

【0005】さらに、従来例として、グラニュール汚泥
を用いる部分と、無機担体の固定床を用いる部分とから
なるハイブリッド式反応槽も用いられていたが、この場
合、固定床を保持するための仕切り板や枠が必要であ
り、そのため反応槽の有効容積が大きくなる嫌いがあ
る。
Further, as a conventional example, a hybrid reaction tank comprising a part using granule sludge and a part using a fixed bed of an inorganic carrier was also used, but in this case, a partition for holding the fixed bed is used. Plates and frames are required, which tends to increase the effective volume of the reaction tank.

【0006】[0006]

【発明が解決しようとする課題】この発明の課題は、上
記の点に鑑み、食品産業廃水や生活廃水などのSS含有
廃水を高速で嫌気処理することができると共に、装置の
コンパクト化を達成できる、有機性廃水のミックスベッ
ド式嫌気性処理装置を提供することにある。
SUMMARY OF THE INVENTION In view of the above points, an object of the present invention is to be able to anaerobically treat SS-containing wastewater such as food industry wastewater and domestic wastewater at a high speed, and also to make the apparatus compact. , To provide a mixed-bed type anaerobic treatment apparatus for organic wastewater.

【0007】[0007]

【課題を解決するための手段】この発明によるミックス
ベッド式嫌気性処理装置は、上記課題を解決すべく工夫
されたもので、反応槽(1) 内に、担体(2) とグラニュー
ル汚泥(3) が混在してなるミックスベッド式充填層(7)
が充填されていることを特徴とするものである。
Means for Solving the Problems The mixed bed type anaerobic treatment apparatus according to the present invention has been devised in order to solve the above-mentioned problems, and a carrier (2) and a granule sludge ( 3) Mixed bed type packed bed (7)
It is characterized by being filled.

【0008】担体(2) としてはセラミックスペレットか
らなるものがよく用いられるが、担体(2) はこれに限定
されない。グラニュール汚泥(3) はメタン生成菌が凝集
してなるものであって、市販品が使用できる。
The carrier (2) is often made of ceramic pellets, but the carrier (2) is not limited to this. The granulated sludge (3) is an aggregate of methanogens, and a commercially available product can be used.

【0009】担体(2) とグラニュール汚泥(3) からなる
ミックスベッド式充填層(7) は、たとえば、まず担体
(2) を、ついでグラニュール汚泥(3) を反応槽(1) 内に
投入し、廃水を所要時間塔内に流通させることによって
形成される。また、ミックスベッド式充填層(7) は、予
め担体(2) とグラニュール汚泥(3) の混合物を用意して
おき、これを槽内へ充填したものでもよい。
The mixed bed type packed bed (7) consisting of the carrier (2) and the granulated sludge (3) is, for example,
The (2) is formed by introducing the granulated sludge (3) into the reaction tank (1) and circulating the wastewater into the tower for a required time. The mixed bed type packed bed (7) may be prepared by preparing a mixture of the carrier (2) and granule sludge (3) in advance and filling the mixture into the tank.

【0010】[0010]

【発明の実施の形態】つぎに、図示の実施例に基づきこ
の発明を具体的に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Next, the present invention will be specifically described based on the illustrated embodiments.

【0011】図1において、約2リットルの反応槽(1)
内に、有効容積の65容量%の担体(2) と、有効容積の
35容量%のグラニュール汚泥(3) が混在してなるミッ
クスベッド式充填層(7) が充填されている。担体(2)
は、直径2mm×長さ6mmの円柱状セラミックスペレ
ットからなる。グラニュール汚泥(3) は、メタン生成菌
が凝集してなる直径1〜3mmのものである。ミックス
ベッド式充填層(7) は、まず円柱状セラミックスペレッ
ト担体(2) を、ついでグラニュール汚泥(3) を反応槽
(1) 内に投入し、廃水を1時間程度槽内に循環させるこ
とによって形成されたものである。
In FIG. 1, a reaction tank (1) of about 2 liters is provided.
A mixed bed type packed bed (7) in which a carrier (2) having an effective volume of 65% by volume and a granule sludge (3) having an effective volume of 35% by volume are mixed therein is filled therein. Carrier (2)
Is a cylindrical ceramic pellet having a diameter of 2 mm and a length of 6 mm. The granulated sludge (3) has a diameter of 1 to 3 mm formed by aggregation of methanogens. The mixed bed type packed bed (7) consists of the cylindrical ceramic pellet carrier (2) and then the granulated sludge (3) in the reaction tank.
(1) It is formed by pouring it into the inside and circulating the waste water in the tank for about 1 hour.

【0012】反応槽(1) のジャケット(4) に恒温水を流
しながら、廃水を廃水供給ポンプ(5) で反応槽(1) の底
部へ導入し、槽内のミックスベッド式充填層(7) 中を上
行させる。塔頂水を循環ポンプ(6) で抜き出して元の廃
水に合流させ、反応槽(1) の底部へ再送する。塔頂のオ
ーバーフロー水は処理水として塔頂部から排出する。廃
水の嫌気性処理によって生じたメタンガスおよび炭酸ガ
スは塔頂から抜き出す。
While flowing constant temperature water through the jacket (4) of the reaction tank (1), waste water was introduced into the bottom of the reaction tank (1) by a waste water supply pump (5), and a mixed bed type packed bed (7) ) Move up inside. The top water is extracted by the circulation pump (6), combined with the original wastewater, and re-sent to the bottom of the reaction tank (1). The overflow water at the top of the tower is discharged from the top of the tower as treated water. Methane gas and carbon dioxide gas generated by the anaerobic treatment of wastewater are extracted from the top of the tower.

【0013】表1に示す精製糖工場廃水を対象として連
続処理運転を行った。HRT(槽内の液滞留時間)が1
2Hrから2Hrになるように、段階的に通水量を増加
させた。処理液の全COD除去率およびSS除去率を測
定した。この結果は表2に示す通りである。
A continuous treatment operation was performed on the refined sugar factory wastewater shown in Table 1. HRT (liquid retention time in the tank) is 1
The water flow rate was increased stepwise so as to be changed from 2 hours to 2 hours. The total COD removal rate and SS removal rate of the treatment liquid were measured. The results are as shown in Table 2.

【0014】[0014]

【表1】 [Table 1]

【表2】 上記表から明らかなように、有機物濃度が低中濃度であ
るSS含有廃水を高速で嫌気処理することができる。
[Table 2] As is apparent from the above table, SS-containing wastewater having a low organic concentration is a high-speed anaerobic treatment.

【0015】[0015]

【発明の効果】この発明によるミックスベッド式嫌気性
廃水処理装置は、反応槽(1) 内に、担体(2) とグラニュ
ール汚泥(3) が混在状態で充填されてなるものであるの
で、産業廃水や生活廃水などのSS含有廃水を高速で嫌
気処理することができる。
The mixed bed type anaerobic wastewater treatment apparatus according to the present invention comprises the reaction tank (1) and the carrier (2) and the granulated sludge (3) in a mixed state. Anaerobic treatment of SS-containing wastewater such as industrial wastewater and domestic wastewater can be performed at high speed.

【0016】また、ミックスベッド式廃水処理装置は層
別をしないため、例えば容積比ではセラミックスペレッ
ト担体1にグラニュール汚泥1を加えると全体で約1で
すみ、装置のコンパクトを達成することができる。
Further, since the mixed bed type waste water treatment device does not perform stratification, for example, when the granule sludge 1 is added to the ceramic pellet carrier 1 in terms of volume ratio, it is only about 1 as a whole, and the compactness of the device can be achieved. .

【0017】この発明によるミックスベッド式嫌気性廃
水処理装置の効果を表3にまとめて示す。
The effects of the mixed bed type anaerobic wastewater treatment apparatus according to the present invention are summarized in Table 3.

【0018】[0018]

【表3】 [Table 3]

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

【図1】 ミックスベッド式嫌気性処理装置を示す概略
図である。
FIG. 1 is a schematic view showing a mixed bed type anaerobic treatment apparatus.

【図2】 グラニュール汚泥を示す概略図である。FIG. 2 is a schematic view showing granulated sludge.

【符号の説明】 1:反応槽 2:セラミックスペレット担体 3:グラニュール汚泥 7:ミックスベッド式充填層[Explanation of reference symbols] 1: Reactor 2: Ceramic pellet carrier 3: Granule sludge 7: Mixed bed packed bed

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 反応槽(1) 内に、担体(2) とグラニュー
ル汚泥(3) が混在してなるミックスベッド式充填層(7)
が充填されていることを特徴とする、有機性廃水のミッ
クスベッド式嫌気性処理装置。
1. A mixed bed type packed bed (7) in which a carrier (2) and granulated sludge (3) are mixed in a reaction tank (1).
A mixed-bed type anaerobic treatment device for organic wastewater, which is filled with.
JP23014995A 1995-09-07 1995-09-07 Mixed bed type anaerobic treatment device for organic waste water Pending JPH0975982A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23014995A JPH0975982A (en) 1995-09-07 1995-09-07 Mixed bed type anaerobic treatment device for organic waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23014995A JPH0975982A (en) 1995-09-07 1995-09-07 Mixed bed type anaerobic treatment device for organic waste water

Publications (1)

Publication Number Publication Date
JPH0975982A true JPH0975982A (en) 1997-03-25

Family

ID=16903365

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23014995A Pending JPH0975982A (en) 1995-09-07 1995-09-07 Mixed bed type anaerobic treatment device for organic waste water

Country Status (1)

Country Link
JP (1) JPH0975982A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008510619A (en) * 2004-08-26 2008-04-10 カロロ エンジニアーズ, ピー・シー Anoxic biological reduction systems and methods
JP2009220076A (en) * 2008-03-18 2009-10-01 Chugoku Electric Power Co Inc:The Uasb reactor, biological nitrification and denitrification apparatus, and method for using the apparatus
JP2013027877A (en) * 2012-11-05 2013-02-07 Chugoku Electric Power Co Inc:The Uasb reactor and biological nitrification and denitrification apparatus
JP2014100677A (en) * 2012-11-21 2014-06-05 Kuraray Co Ltd Anaerobic wastewater treatment method using carrier
JP2014100679A (en) * 2012-11-21 2014-06-05 Kuraray Co Ltd Anaerobic wastewater treatment method using carrier
JP2014100680A (en) * 2012-11-21 2014-06-05 Kuraray Co Ltd Anaerobic wastewater treatment method using carrier
JP2014180622A (en) * 2013-03-19 2014-09-29 Sumitomo Heavy Industries Environment Co Ltd Anaerobic treatment apparatus
WO2014156216A1 (en) * 2013-03-27 2014-10-02 栗田工業株式会社 Anaerobic treatment method
US9096448B2 (en) 2010-11-24 2015-08-04 Kurita Water Industries Ltd. Anaerobic treatment method and apparatus

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008510619A (en) * 2004-08-26 2008-04-10 カロロ エンジニアーズ, ピー・シー Anoxic biological reduction systems and methods
JP2009220076A (en) * 2008-03-18 2009-10-01 Chugoku Electric Power Co Inc:The Uasb reactor, biological nitrification and denitrification apparatus, and method for using the apparatus
US9096448B2 (en) 2010-11-24 2015-08-04 Kurita Water Industries Ltd. Anaerobic treatment method and apparatus
KR20180113635A (en) 2010-11-24 2018-10-16 쿠리타 고교 가부시키가이샤 Method and apparatus for anaerobic treatment
JP2013027877A (en) * 2012-11-05 2013-02-07 Chugoku Electric Power Co Inc:The Uasb reactor and biological nitrification and denitrification apparatus
JP2014100677A (en) * 2012-11-21 2014-06-05 Kuraray Co Ltd Anaerobic wastewater treatment method using carrier
JP2014100679A (en) * 2012-11-21 2014-06-05 Kuraray Co Ltd Anaerobic wastewater treatment method using carrier
JP2014100680A (en) * 2012-11-21 2014-06-05 Kuraray Co Ltd Anaerobic wastewater treatment method using carrier
JP2014180622A (en) * 2013-03-19 2014-09-29 Sumitomo Heavy Industries Environment Co Ltd Anaerobic treatment apparatus
WO2014156216A1 (en) * 2013-03-27 2014-10-02 栗田工業株式会社 Anaerobic treatment method

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