JPH02218498A - Packing body for purifying tank - Google Patents
Packing body for purifying tankInfo
- Publication number
- JPH02218498A JPH02218498A JP1039001A JP3900189A JPH02218498A JP H02218498 A JPH02218498 A JP H02218498A JP 1039001 A JP1039001 A JP 1039001A JP 3900189 A JP3900189 A JP 3900189A JP H02218498 A JPH02218498 A JP H02218498A
- Authority
- JP
- Japan
- Prior art keywords
- phenol
- tank
- sludge
- packing body
- wastewater
- 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
- 238000012856 packing Methods 0.000 title claims abstract description 42
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims abstract description 43
- 239000002351 wastewater Substances 0.000 claims abstract description 38
- 239000002207 metabolite Substances 0.000 claims abstract description 23
- 150000001875 compounds Chemical class 0.000 claims abstract description 16
- 230000000813 microbial effect Effects 0.000 claims description 16
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical class O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 12
- 239000004575 stone Substances 0.000 claims description 9
- -1 andesite or rhyolite Chemical class 0.000 claims description 2
- 244000005700 microbiome Species 0.000 claims 1
- 239000010802 sludge Substances 0.000 abstract description 40
- 238000006243 chemical reaction Methods 0.000 abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 9
- 241000894006 Bacteria Species 0.000 abstract description 8
- 238000005273 aeration Methods 0.000 abstract description 6
- 238000004062 sedimentation Methods 0.000 abstract description 6
- 239000000126 substance Substances 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 2
- 239000003864 humus Substances 0.000 abstract 1
- 230000005012 migration Effects 0.000 abstract 1
- 238000013508 migration Methods 0.000 abstract 1
- 239000000945 filler Substances 0.000 description 14
- 241001148470 aerobic bacillus Species 0.000 description 6
- 239000005416 organic matter Substances 0.000 description 6
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 229920002521 macromolecule Polymers 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 230000001580 bacterial effect Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 235000019645 odor Nutrition 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 230000001617 migratory effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 239000005335 volcanic glass Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
-
- 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
- Life Sciences & Earth Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Biological Treatment Of Waste Water (AREA)
- Treatment Of Biological Wastes In General (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は浄化槽用充填体に関し、更に詳細には、有機物
を含む廃水の処理の際に、フェノール及び/又はフェノ
ール露出基のある化合物を含む微生物代謝産物若しくは
腐植物を利用する浄化槽用充填体に関する。Detailed Description of the Invention (Industrial Field of Application) The present invention relates to a packing for septic tanks, and more particularly, it relates to a packing for a septic tank, and more particularly, it is used to treat wastewater containing organic matter, and is used to fill a packing body containing phenol and/or a compound with a phenol-exposed group. The present invention relates to a packing for a septic tank that utilizes microbial metabolites or humic plants.
(従来技術)
河川汚染防止のため、家庭雑廃水、畜産廃水等の廃水を
処理する浄化槽が多く設置される様になってきている。(Prior Art) In order to prevent river pollution, many septic tanks are being installed to treat wastewater such as household wastewater and livestock wastewater.
かかる従来の浄化槽では、通常、廃水中の有機物を分解
し低分子化並びにガス化することを目的とする活性汚泥
法に基づく汚水処理法が採用されている。Such conventional septic tanks usually employ a sewage treatment method based on an activated sludge method, which aims to decompose organic matter in wastewater to convert it into low-molecular-weight molecules and gasify it.
この様な浄化槽においては、充分な有機物除去能力がな
く、且つ臭気が出るという基本的な問題がある。Such septic tanks have the basic problem of not having sufficient ability to remove organic matter and emitting odors.
この問題を解消すべく、特開昭61−33297号公報
及び特開昭61−260880号公報において、有機性
物質を含む廃水とフェノール及び/又はフェノール露出
基のある化合物を含む微生物代謝産物等とを混合する処
理方法が提案されている。In order to solve this problem, in JP-A-61-33297 and JP-A-61-260880, wastewater containing organic substances and microbial metabolites containing phenol and/or compounds with exposed phenol groups, etc. A processing method has been proposed that mixes the two.
かかる方法によれば、廃水中の有機性物質(有機物)と
微生物代謝産物とを物理化学的に反応させることによっ
て、結合、粒子化、縦爪、縮合、重合を含む巨大分子化
並びに微細汚泥の巨大化を惹起させ、これを固液分離す
ることによって臭気の発生もなく容易に廃水を浄化する
ことができる。According to this method, by physicochemically reacting organic substances in wastewater with microbial metabolites, formation of macromolecules including bonding, granulation, vertical formation, condensation, and polymerization, and formation of fine sludge can be achieved. By inducing giant size and separating it into solid and liquid, wastewater can be easily purified without generating any odor.
本発明者は、先に特願昭62−257788号明細書に
おいて、前記処理方法を効率的に行うことができ、−辺
集合住宅或いは小規模下水道等に適用できる小型並びに
中型の浄化槽として、浄化槽内の廃水と接触する部位に
、フェノール及び/又はフェノール露出基のある化合物
を含む微生物代謝産物若しくは腐植物を充填した充填層
を予め固定しておくことを提案した。The present inventor previously disclosed in Japanese Patent Application No. 62-257788 a septic tank as a small- and medium-sized septic tank that can efficiently carry out the above-mentioned treatment method and can be applied to residential complexes or small-scale sewage systems. We proposed that a packed bed filled with microbial metabolites or humic plants containing phenol and/or compounds with phenol-exposed groups be fixed in advance in areas that come into contact with wastewater within the plant.
(発明が解決しようとする課題)
本発明者が先に提案した浄化槽によれば、廃水中及び汚
泥内の一最土壌細菌群のうちの好気性細菌及び通性嫌気
性細菌が、フェノール及び/又はフェノール露出基のあ
る化合物を含む微生物代謝産物若しくは腐植物からなる
充填物(以下、フェノール等の充填物と称することがあ
る)と接触し、その代謝産物中にフェノール及び/又は
フェノール露出基のある化合物を含むように馴致化され
るため、フェノール及び/又はフェノール露出基のある
化合物を含む微生物代謝産物の抽出が促進される。(Problems to be Solved by the Invention) According to the septic tank previously proposed by the present inventor, aerobic bacteria and facultative anaerobic bacteria, which are the most common soil bacterial groups in wastewater and sludge, or contact with a filling made of a microbial metabolite or humic plant containing a compound with a phenol-exposed group (hereinafter sometimes referred to as a filler of phenol, etc.), and the metabolite contains phenol and/or a phenol-exposed group. Being adapted to contain certain compounds facilitates the extraction of microbial metabolites containing phenols and/or compounds with phenol-exposed groups.
その結果、廃水処理機能の維持、促進がなされるため、
廃水処理を効率的に行うことができる。As a result, the wastewater treatment function is maintained and promoted.
Wastewater treatment can be carried out efficiently.
唯、予め浄化槽の廃水と接触する部位にフェノール等の
充填物を充填した充填層を固定しておく方法によれば、
汚泥等によって比較的短時間で充填層が閉塞する可能性
がある。However, according to the method of fixing a packed bed filled with a filler such as phenol in advance to the part of the septic tank that will come into contact with wastewater,
The packed bed may become clogged with sludge etc. in a relatively short period of time.
ところで、かかる充填層が閉塞すると、好気性細菌及び
通性嫌気性細菌とフェノール等の充填物との接触が有効
になされず、前記細菌の馴致化が容易になされないおそ
れがあるため、浄化槽の清掃周Jtllを比較的短期間
で行うことを要する。By the way, if such a packed bed is clogged, aerobic bacteria and facultative anaerobic bacteria will not come into contact with the filling such as phenol, and the bacteria may not be able to acclimatize easily. It is necessary to perform the cleaning cycle Jtll in a relatively short period of time.
そこで、本発明の目的は、フェノール等の充填物が充填
されている充填層の比較的短時間での閉塞を防止し、好
気性細菌及び通性嫌気性細菌と前記充填物との接触を長
時間有効に保持することができる浄化槽用充填体を提供
することある。Therefore, an object of the present invention is to prevent a packed bed filled with a filler such as phenol from clogging in a relatively short period of time, and to prolong the contact between aerobic bacteria and facultative anaerobic bacteria and the filler. It is an object of the present invention to provide a filling body for a septic tank that can be effectively maintained for a long time.
(課題を解決するための手段)
浄化槽用充填体の汚泥等に因る比較的短時間に閉塞する
可能性は、下記の構成を有する本発明の浄化槽充填体に
よって防止することができる。(Means for Solving the Problems) The possibility that the septic tank packing body will be clogged with sludge or the like in a relatively short period of time can be prevented by the septic tank packing body of the present invention having the following configuration.
即ち、本発明は、浄化槽内の廃水と接触する部位に固定
することなく設けられる複数個の充填体であって、該充
填体の少なくとも一部には、フェノール及び/又はフェ
ノール露出基のある化合物を含む微生物代謝産物若しく
は腐植物が充填されていると共に、浮力調整部が併設さ
れていることを特徴とする浄化槽用充填体である。That is, the present invention provides a plurality of packing bodies that are provided without being fixed at a site in contact with wastewater in a septic tank, and at least a portion of the packing bodies contain phenol and/or a compound having a phenol-exposed group. This is a filling body for a septic tank, characterized in that it is filled with microbial metabolites or humic plants containing a buoyancy adjustment section.
かかる本発明において、前記微生物代謝産物しくは腐植
物が充填されている充填体と、安山岩質、流紋岩質等の
活性化されている珪酸分が含まれている砕石が充填され
ている充填体とが併用されていると、浄化槽における汚
泥の沈降性が極めて良好となり、容易に固液分離ができ
る。In the present invention, the filling body is filled with the microbial metabolite or humic plant, and the filling body is filled with crushed stone containing activated silicic acid such as andesite or rhyolite. When used in combination with sludge, the settling properties of sludge in the septic tank will be extremely good, and solid-liquid separation will be easy.
また、複数個の充填体が、廃水中において浮遊、回遊、
又は沈降する充填体が混在しているものであれば、充填
体が廃水の動きに従って容易に動き易いため、充填体の
閉塞を更に一層防止することができる。In addition, multiple packing bodies float, migrate, and
Alternatively, in the case where sedimentary filling bodies are mixed, the filling bodies can easily move according to the movement of waste water, so that clogging of the filling bodies can be further prevented.
尚、本発明においていう「フェノール露出基のある化合
物」とは、フェノール露出基をもつ有機物−最を指し、
特にフェノール露出基を有する酵素が有効である。In the present invention, the term "compound with a phenol exposed group" refers to an organic compound having a phenol exposed group,
Enzymes with exposed phenol groups are particularly effective.
また、「活性化された珪酸分」とは、安山岩質或いは流
紋岩質の組成を有し、且つ火山ガラス等の活性度の高い
不安定な物質を言う。Furthermore, the term "activated silicic acid content" refers to an unstable substance having an andesitic or rhyolitic composition and having a high activity such as volcanic glass.
(作用)
本発明によれば、廃水中の有機物はフェノール及び/又
はフェノール露出基めある化合物を含む微生物代謝物と
の接触によって、巨大分子化して浄化槽中に汚泥として
沈殿する。(Function) According to the present invention, organic matter in wastewater is converted into macromolecules by contact with microbial metabolites containing phenol and/or a compound having a phenol-exposed base, and is precipitated as sludge in a septic tank.
かかる汚泥は比鮫的沈降性が良く且つ充填体の表面を覆
っても粘着することがない。Such sludge has relatively good sedimentation properties and does not stick to the surface of the packing body.
しかも、充填体は、浄化槽内に固定されることなく設け
られ且つ浮力調整部が併設されている。ため、充填体が
廃水の動きに応じてその位置を変え易く、充填体の閉塞
を防止することができる。Furthermore, the filling body is provided without being fixed in the septic tank, and is also provided with a buoyancy adjustment section. Therefore, the filling body can easily change its position according to the movement of waste water, and clogging of the filling body can be prevented.
(実施例) 本発明を図面を用いて説明する。(Example) The present invention will be explained using the drawings.
第1図は、本発明の充填体を用いた浄化槽の断面図であ
り、廃水は廃水流入バイブロから浄化槽の第1反応槽2
に流入し、第2反応槽3、沈殿槽4、及び放流槽5を経
由して清澄水が放流パイプ17から放流される。FIG. 1 is a sectional view of a septic tank using the packing body of the present invention, in which wastewater flows from the wastewater inflow vibro to the first reaction tank 2 of the septic tank.
Clear water flows through the second reaction tank 3, settling tank 4, and discharge tank 5, and is discharged from the discharge pipe 17.
尚、第1図の14は、第1反応槽2から第2反応槽3に
廃水を送液する送液管である。In addition, 14 in FIG. 1 is a liquid feeding pipe for feeding waste water from the first reaction tank 2 to the second reaction tank 3.
かかる浄化槽において、沈殿槽4で沈殿した汚泥は多少
の水と共に汚泥返送管13によって汚泥培養槽1に返送
される。この汚泥返送管13には、例えばエアポンプ(
図示せず)によって作動されるエアリフト構造のものが
採用されている。In such a septic tank, the sludge precipitated in the settling tank 4 is returned to the sludge culture tank 1 through the sludge return pipe 13 along with some water. For example, an air pump (
An air lift structure operated by a motor (not shown) is adopted.
これら汚泥培養槽1、及び第1〜2反応槽2.3の廃水
と接触する部位には、フェノール等の充填物が充填され
ている複数個の充填体と、安山岩質、流紋岩質等の活性
化されている珪酸分が含まれる砕石(以下、活性珪酸分
含有の砕石と称する。The parts of the sludge culture tank 1 and the first and second reaction tanks 2.3 that come into contact with wastewater are filled with a plurality of packing bodies filled with fillers such as phenol, andesitic, rhyolitic, etc. Crushed stone containing activated silicic acid (hereinafter referred to as crushed stone containing activated silicic acid).
ことがある)が充填されている複数個の充填体とが夫々
固定されることなく設けられている。A plurality of filling bodies each filled with (sometimes) are provided without being fixed to each other.
かかる複数個の充填体は、外形が略球形をしており、汚
泥培養槽1及び第1反応槽2においては、充填体と廃水
との接触を良好にし且つ充填体の流出を防止すべく、廃
水中に設けられているパンチングブレー、ト等の多孔板
8.8′及び槽の内壁によって囲まれている内に挿入さ
れている。The plurality of packing bodies have a substantially spherical outer shape, and in the sludge culture tank 1 and the first reaction tank 2, in order to improve the contact between the packing bodies and wastewater and to prevent the filling bodies from flowing out, A punching brake provided in the wastewater is inserted into a hole surrounded by a perforated plate 8.8' and the inner wall of the tank.
尚、第2反応槽3においては、槽下部の沈殿槽4との連
結部からの充填体の流出を防止すべく、多孔板8が槽内
壁にがら斜めに前記連結部を塞ぐ様に設けられている。In addition, in the second reaction tank 3, in order to prevent the filling material from flowing out from the connection part with the sedimentation tank 4 at the bottom of the tank, a perforated plate 8 is provided diagonally against the inner wall of the tank so as to block the connection part. ing.
この様な充填体のうち、汚魔培養槽1及び第1反応槽2
における充填体10は主として上方の多孔板8の近傍に
浮遊しており、充填体12は主として下方の多孔板8′
の近傍に沈降している。Among these packing bodies, the dirt culture tank 1 and the first reaction tank 2
The filling bodies 10 are mainly floating near the upper perforated plate 8, and the filling bodies 12 are mainly floating near the lower perforated plate 8'.
It is settling in the vicinity of.
また、充填体11は多孔板8と多孔板8′との間を昇降
しつつ廃水の動きに従って回遊する。Further, the filling body 11 moves up and down between the perforated plates 8 and 8' according to the movement of waste water.
かかる充填体は、第2図に示す様に、多孔の合成樹脂或
いは綱等で構成されており、その内部&qフェノール等
の充填物又は活性珪酸分含有の砕石が充填され、浮力調
整部が併設されているものである。As shown in Figure 2, such a packing body is made of porous synthetic resin or rope, etc., and the inside thereof is filled with a filler such as phenol or crushed stone containing active silicic acid, and a buoyancy adjustment section is attached. This is what is being done.
第2図の(1)は、第1図において充填体1゜として示
す浮遊タイプのものであり、充填体に浮力を付与するエ
アーバッグ20が設けられ、第2図の(2)は、第1図
において充填体12として示す沈降タイプのものであり
、充填体に沈降力を付与するサンドバッグ21が設けら
れている。(1) in FIG. 2 is a floating type shown as the filling body 1° in FIG. 1, and an air bag 20 is provided to give buoyancy to the filling body, It is of a settling type, shown as a filling body 12 in FIG. 1, and is provided with a sandbag 21 that applies a settling force to the filling body.
また、第2図の(3)は、第1図において充填体11と
して示す回遊タイプのものであり、エアーバッグ20と
サンドバッグ21とで浮力が調整されて廃水中を昇降し
つつ回遊するものである。Moreover, (3) in FIG. 2 is a migratory type shown as the filling body 11 in FIG. It is.
この様な充填体101.11.12の割合は、廃水の性
質等に応じて適宜変更することができ、第2反応槽3の
如く、回遊タイプである充填体11のみとすることがで
きるが、汚泥培養槽1及び第1反応槽2においては、浮
遊タイプである充填体10と沈降タイプである充填体1
2とをほぼ等しくし、回遊タイプである充填体11を前
記充填体の夫々よりも少なくすることが好ましい。The ratio of such packing bodies 101, 11, and 12 can be changed as appropriate depending on the properties of the wastewater, etc., and it is possible to use only the packing bodies 11 of the circulating type, such as in the second reaction tank 3. In the sludge culture tank 1 and the first reaction tank 2, a floating type packing body 10 and a settling type packing body 1 are used.
2 are approximately equal, and it is preferable that the number of migrating type filling bodies 11 be smaller than each of the above-mentioned filling bodies.
更に、フェノール等の充填物が充填されている充填体(
充填体A)と活性珪酸分含有の砕石が充填されている充
填体(充填体B)との比率も任意に変更できるが、充填
体Aを充填体Bよりも多くすることが好ましく、特に充
填体Aと充填体Bとの比率を3:1程度にすることが好
ましい。Furthermore, a packing body filled with fillers such as phenol (
Although the ratio of the filler A) to the filler filled with crushed stone containing active silicic acid (filler B) can be changed arbitrarily, it is preferable that the amount of filler A is larger than the filler B, and in particular It is preferable that the ratio of the body A and the filling body B be about 3:1.
本実施例においては、各種の下部に曝気装置9が設けら
れ、沈殿槽4に安山岩質、流紋岩質等の活性化されてい
る珪酸分が含まれている砕石を充填した充填層15が汚
泥との分離を完全にすべく設けられている。In this embodiment, an aeration device 9 is provided at each lower part, and a packed bed 15 filled with crushed stone containing activated silicic acid, such as andesite or rhyolite, is provided in the settling tank 4. It is provided to ensure complete separation from sludge.
かかる浄化槽に流入する廃水は、先ず別個所において設
けられている冬ット等を通過して夾雑物が取り除かれて
から第1反応槽2に流入する。この第1反応槽2の中で
廃水に含まれる有機物は廃水中のフ・エノール及び/又
はフェノール露出基のある化合物を含む微生物代謝産物
(以下、フェノール等の微生物代謝産物と称することが
ある)及び活性化した珪酸分等の作用によって凝集する
。The wastewater flowing into the septic tank first passes through a winter tank or the like provided at a separate location to remove impurities, and then flows into the first reaction tank 2. The organic matter contained in the wastewater in the first reaction tank 2 is a microbial metabolite containing phenol and/or a compound with a phenol-exposed group in the wastewater (hereinafter sometimes referred to as a microbial metabolite such as phenol). and aggregates due to the action of activated silicic acid components.
この様に凝集して汚泥化した有機物は第2反応槽3に流
入し、再度フェノール等の微生物代謝産物及び活性化し
た珪酸分等と接触して巨大分子化し、沈殿槽4内で沈殿
する。The organic matter thus flocculated and turned into sludge flows into the second reaction tank 3, comes into contact with microbial metabolites such as phenol, activated silicic acid, etc. again, becomes macromolecules, and precipitates in the settling tank 4.
かかるフェノール等の微生物代謝産物は、主として廃水
中の好気性細菌及び通性嫌気性細菌の代謝によって供給
される。Microbial metabolites such as phenol are mainly supplied by the metabolism of aerobic bacteria and facultative anaerobic bacteria in wastewater.
この様に、前記細菌群を、その代謝産物中にフェノール
及び/又はフェノール露出基のある化合物を含む様に馴
致するため、フェノール等の充填物が充填されている充
填体を設け、フェノール等の微生物代謝産物を客用させ
て廃水中の雰囲気を調整しているのである。In this way, in order to acclimatize the bacterial group to include phenol and/or a compound with a phenol exposed group in its metabolites, a packing body filled with a filler such as phenol is provided. Microbial metabolites are used to adjust the atmosphere in wastewater.
この点、本実施例にお・ける充填体の夫々は、各種に設
けらている曝気装置9から放出される空気流によって流
動する廃水と共に動き汚泥等で閉塞されるおそれがなく
且つ廃水との接触面積も広くなるため、フェノール等の
微生物代謝物の客用が充分になされ一好気性細菌及び通
性嫌気性細菌がその代謝産物中にフェノール及び/又は
フェノール露出基のある化合物を含むように充分に馴致
することができる。In this respect, each of the packing bodies in this embodiment moves together with the wastewater flowing by the air flow released from the aeration device 9 provided in each type, and there is no risk of clogging with sludge etc. Since the contact area is also widened, microbial metabolites such as phenol can be used sufficiently, and aerobic bacteria and facultative anaerobic bacteria contain phenol and/or compounds with phenol-exposed groups in their metabolites. You can get used to it well.
更に、本実施例においては、沈降槽4で沈降した汚泥は
多少の水と共に汚泥返送管13を経由して汚泥培養槽1
に返送され、培養された後、廃水流入バイブロの汚泥流
入孔7から廃水中に混入され第1反応槽2に返送される
。Furthermore, in this embodiment, the sludge settled in the settling tank 4 is sent to the sludge culture tank 1 via the sludge return pipe 13 together with some water.
After being cultured, the sludge is mixed into the wastewater through the sludge inflow hole 7 of the wastewater inflow vibro, and is returned to the first reaction tank 2.
かかる汚泥培養槽1においても、フェノール等の充填物
が充填されている充填体と活性珪酸含有の砕石が充填さ
れている充填体とが槽内に設けられており、水及び汚泥
中の好気性細菌及び通性嫌気性細菌を前述した様に充分
に馴致し且つ汚泥自身を巨大分子化する。In this sludge culture tank 1, a packing body filled with a filler such as phenol and a packing body filled with crushed stone containing activated silicic acid are provided in the tank, and the aerobic conditions in water and sludge are As mentioned above, the bacteria and facultative anaerobic bacteria are sufficiently acclimatized and the sludge itself is converted into macromolecules.
この様に、充分に馴致された前記細菌群及び巨大分子化
した汚泥が廃水バイブロの汚泥流入孔7から浄化槽に流
入する廃水中に混入されるため、廃水中の好気性細菌及
び通性嫌気性細菌の馴致も行うことかで°きる。In this way, the bacteria group and macromolecularized sludge that have been sufficiently adapted are mixed into the wastewater that flows into the septic tank from the sludge inflow hole 7 of the wastewater vibro, so that the aerobic bacteria in the wastewater and the facultative anaerobic This can be done by acclimating the bacteria.
この汚泥培養槽1に設けられている充填体も、浮遊タイ
プの充填体10、回遊タイプの充填体11、及び沈降タ
イプの充填体12が混在し、槽下部に設けられている曝
気装置9から放出される空気流によって流動する水及び
汚泥等と共に動き、汚泥等によって充填体に充填されて
いる充填物を閉塞させることを防止する。The packing bodies provided in this sludge culture tank 1 are also a mixture of floating type packing bodies 10, migrating type packing bodies 11, and settling type packing bodies 12, and are separated from the aeration device 9 provided at the bottom of the tank. It moves together with the water, sludge, etc. that flow due to the discharged air flow, and prevents the filling filled in the packing body from being blocked by the sludge, etc.
尚、汚泥培養槽1の曝気装置9から噴出する空気量は槽
内の水及び汚泥を攪判する程度で充分であり、前記曝気
装置9への空気配管の途中に設けられているバルブ16
によって空気量を調整することができる。The amount of air ejected from the aeration device 9 of the sludge culture tank 1 is sufficient to agitate the water and sludge in the tank, and the valve 16 provided in the middle of the air piping to the aeration device 9 is sufficient to agitate the water and sludge in the tank.
The amount of air can be adjusted by
一方、この様な浄化槽の第1反応槽2、第2反応槽3、
及び沈降槽4を通過した清澄水は、放流槽5から放流さ
れる。この際、゛消毒薬等を、添加しても良い。On the other hand, the first reaction tank 2, the second reaction tank 3,
The clear water that has passed through the settling tank 4 is discharged from the discharge tank 5. At this time, a disinfectant or the like may be added.
尚、沈降槽4において活性珪酸含有の砕石が充填されて
いる充填層15は汚泥の分離を完全にすべく設けられて
いるものであるため、汚泥の分離が充分になされている
ならば、特に設ける必要はない。In addition, since the packed bed 15 filled with crushed stone containing activated silicic acid in the sedimentation tank 4 is provided to completely separate the sludge, if the sludge is sufficiently separated, There is no need to provide it.
また、本実施例における浄化槽は、FRP製で大量生産
が可能のものであるが、コンクリート製として組み立て
容易なプレハブとしてもよい。Further, the septic tank in this embodiment is made of FRP and can be mass-produced, but it may also be made of concrete and prefabricated for easy assembly.
更に、充填体の形状は球形に限定されず任意の形状、例
えば楕円球、立方体等であってもよい。Further, the shape of the filling body is not limited to a spherical shape, but may be any shape, such as an elliptical sphere or a cube.
(発明の効果)
本発明の浄化槽用充填体は、汚泥等によって閉塞され難
く廃水との接触を長時間良好に保持できるため、浄化槽
の清掃周期を長くすることができ、浄化槽の保守を簡素
化することができる。(Effects of the Invention) The septic tank filling body of the present invention is not easily blocked by sludge, etc. and can maintain good contact with wastewater for a long period of time, making it possible to lengthen the cleaning cycle of the septic tank and simplifying the maintenance of the septic tank. can do.
第1図は本発明の浄化槽用充填体を用いた浄化槽の断面
図、第2図は本発明の浄化槽用充填体の正面図を夫々示
す。
図において
1・・・汚泥培養槽、
2 ・
3 ・
4 ・
10 ・
11 ・
12・
20 ・
21 ・
第1反応槽、
第2反応槽、
沈降槽、
浮遊タイプの充填体、
回遊タイプの充填体、
沈降タイプの充填体、
浮力調整部(エアーバッグ)
浮力調整部(サンドバッグ)FIG. 1 is a sectional view of a septic tank using the septic tank filling body of the present invention, and FIG. 2 is a front view of the septic tank filling body of the present invention. In the figure, 1...sludge culture tank, 2, 3, 4, 10, 11, 12, 20, 21, first reaction tank, second reaction tank, sedimentation tank, floating type packing body, circulating type packing body , settling type packing, buoyancy adjustment section (air bag) buoyancy adjustment section (sandbag)
Claims (1)
設けられる複数個の充填体であつて、該充填体の少なく
とも一部には、フェノール及び/又はフェノール露出基
のある、化合物を含む微生物代謝産物若しくは腐植物が
充填されていると共に、浮力調整部が併設されているこ
とを特徴とする浄化槽用充填体。 2、充填体が、安山岩質、流紋岩質等の活性化されてい
る珪酸分が含まれている砕石が充填されている充填体と
、フェノール及び/又はフェノール露出基のある化合物
を含む微生物代謝産物若しくは腐植物が充填されている
充填体とからなる請求項第1項記載の浄化槽用充填体。 3、複数個の充填体が、廃水中において、浮遊、回遊、
又は沈降する充填体が混在している請求項第1項又は第
2項記載の浄化槽用充填体。[Scope of Claims] 1. A plurality of packing bodies provided without being fixed at a site in contact with wastewater in a septic tank, wherein at least a part of the packing bodies contains phenol and/or phenol-exposed groups. A filling body for a septic tank, characterized in that it is filled with a microbial metabolite containing a compound or a humic plant, and is also provided with a buoyancy adjustment section. 2. The filling body is filled with crushed stone containing activated silicic acid, such as andesite or rhyolite, and a microorganism containing phenol and/or a compound with a phenol exposed group. The filling body for a septic tank according to claim 1, comprising a filling body filled with a metabolite or a humic plant. 3. Multiple filling bodies float, migrate, and move in wastewater.
The filling body for a septic tank according to claim 1 or 2, wherein a filling body that settles or settles is mixed therein.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1039001A JPH0712480B2 (en) | 1989-02-17 | 1989-02-17 | Filler for septic tank |
| KR1019900001870A KR920005915B1 (en) | 1989-02-17 | 1990-02-16 | Waste water treating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1039001A JPH0712480B2 (en) | 1989-02-17 | 1989-02-17 | Filler for septic tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02218498A true JPH02218498A (en) | 1990-08-31 |
| JPH0712480B2 JPH0712480B2 (en) | 1995-02-15 |
Family
ID=12540886
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1039001A Expired - Lifetime JPH0712480B2 (en) | 1989-02-17 | 1989-02-17 | Filler for septic tank |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPH0712480B2 (en) |
| KR (1) | KR920005915B1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5976374A (en) * | 1995-04-07 | 1999-11-02 | Dowmus Pty Ltd | Self-cleansing filter |
| JP2006326387A (en) * | 2005-05-23 | 2006-12-07 | Waki Sangyo:Kk | Aeration tank structure |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105236589B (en) * | 2015-10-30 | 2017-06-09 | 天津市农业资源与环境研究所 | A kind of decentralized wastewater bioflocculation intensifying device and processing method |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61260880A (en) * | 1985-05-16 | 1986-11-19 | Mamoru Uchimizu | Method for cultivating bacterial group producing metabolite containing phenol or/and compound having exposed phenol group |
| JPS63232892A (en) * | 1987-03-19 | 1988-09-28 | Japan Organo Co Ltd | Dipping filter-bed biological treating device |
-
1989
- 1989-02-17 JP JP1039001A patent/JPH0712480B2/en not_active Expired - Lifetime
-
1990
- 1990-02-16 KR KR1019900001870A patent/KR920005915B1/en not_active Expired
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61260880A (en) * | 1985-05-16 | 1986-11-19 | Mamoru Uchimizu | Method for cultivating bacterial group producing metabolite containing phenol or/and compound having exposed phenol group |
| JPS63232892A (en) * | 1987-03-19 | 1988-09-28 | Japan Organo Co Ltd | Dipping filter-bed biological treating device |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5976374A (en) * | 1995-04-07 | 1999-11-02 | Dowmus Pty Ltd | Self-cleansing filter |
| CN1064560C (en) * | 1995-04-07 | 2001-04-18 | 陶玛斯有限公司 | Self-cleansing filter |
| JP2006326387A (en) * | 2005-05-23 | 2006-12-07 | Waki Sangyo:Kk | Aeration tank structure |
Also Published As
| Publication number | Publication date |
|---|---|
| KR920005915B1 (en) | 1992-07-24 |
| KR900012845A (en) | 1990-09-01 |
| JPH0712480B2 (en) | 1995-02-15 |
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