JPS6254072B2 - - Google Patents
Info
- Publication number
- JPS6254072B2 JPS6254072B2 JP1076982A JP1076982A JPS6254072B2 JP S6254072 B2 JPS6254072 B2 JP S6254072B2 JP 1076982 A JP1076982 A JP 1076982A JP 1076982 A JP1076982 A JP 1076982A JP S6254072 B2 JPS6254072 B2 JP S6254072B2
- Authority
- JP
- Japan
- Prior art keywords
- septic tank
- chamber
- human waste
- waste water
- flowing out
- 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.)
- Expired
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 35
- 239000010800 human waste Substances 0.000 claims description 27
- 239000002351 wastewater Substances 0.000 claims description 22
- 238000005273 aeration Methods 0.000 claims description 18
- 239000010865 sewage Substances 0.000 claims description 16
- 238000004659 sterilization and disinfection Methods 0.000 claims description 10
- 241001148470 aerobic bacillus Species 0.000 claims description 9
- 239000007924 injection Substances 0.000 claims description 9
- 238000002347 injection Methods 0.000 claims description 9
- 241001148471 unidentified anaerobic bacterium Species 0.000 claims description 8
- 210000002700 urine Anatomy 0.000 claims description 6
- 239000010802 sludge Substances 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 3
- 238000004062 sedimentation Methods 0.000 description 8
- 239000000306 component Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 235000014633 carbohydrates Nutrition 0.000 description 3
- 150000001720 carbohydrates Chemical class 0.000 description 3
- 230000000249 desinfective effect Effects 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 2
- 241000237502 Ostreidae Species 0.000 description 2
- CVSVTCORWBXHQV-UHFFFAOYSA-N creatine Chemical compound NC(=[NH2+])N(C)CC([O-])=O CVSVTCORWBXHQV-UHFFFAOYSA-N 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 206010012601 diabetes mellitus Diseases 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 235000020636 oyster Nutrition 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 235000000346 sugar Nutrition 0.000 description 2
- 229940030600 antihypertensive agent Drugs 0.000 description 1
- 239000002220 antihypertensive agent Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229960003624 creatine Drugs 0.000 description 1
- 239000006046 creatine Substances 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000005426 pharmaceutical component Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
Classifications
-
- 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
Description
この発明は難処理し尿汚水用浄化槽に関する。
従来、し尿汚水用浄化槽としては、第1図に示
すように、し尿汚水中の固形物を分離する分離室
A、該分離室Aから流出したし尿汚水に散気し、
好気性菌により処理を行う曝気室B、該曝気室B
から流出した処理水中の剥離汚泥等の浮遊物を沈
澱させる沈澱室C、該沈澱室Cから流出する処理
水を消毒し外部へ排出する消毒室Dを備えたもの
が一般的に知られている。
この種の汚水浄化槽は、通常一般的なし尿汚水
であれば、排出される汚水はほぼ完全に処理さ
れ、一般の下水道へも流出可能な程度に浄化され
るが、し尿汚水が難処理汚水の場合、特に糖尿性
し尿、あるいはビタミン剤、血圧降下剤等の薬剤
成分を含有するし尿汚水の場合は、し尿中に含ま
れる成分が完全に処理されず、排出基準に適合し
ないこととなる場合があつた。
この発明は、上記問題に鑑み、難処理であるし
尿汚水であつても、十分に浄化し得る浄化槽を提
供することを目的としてなされたものであつて、
流入口を有し、流入されたし尿汚水を静置し、嫌
気性菌により腐敗させる腐敗槽と、該腐敗槽から
流出するし尿汚水にアルカリ分(又は酸分)を付
加し、PHを調整するフイルター装置と、該フイル
ター装置を通して流出するし尿汚水を希釈する注
水装置と、希釈されて流出したし尿汚水に散気を
行い好気性菌により処理を行う接触曝気室と、該
接触曝気室から流出する処理水中の剥離汚泥等の
浮遊物を沈澱させる沈澱室と、該沈澱室から流出
する処理水を消毒する消毒室、並びに該消毒室に
設けた排出口とからなることを特徴とするもので
ある。
次に、この発明を実施例により説明する。
第2図はこの発明の実施例の断面を示す概念
図、第3図は一実施例の要部破断斜視図である。
この発明の難処理し尿汚水用浄化槽1は、し尿
汚水が流入される流入口2を有し、流入されたし
尿汚水Wを静置し、嫌気性菌により腐敗させる腐
敗槽3と、この腐敗槽3から流出するし尿汚水に
アルカリ分(又は酸分)を付加し、PHを調整す
る、例えば石灰石、牡蛎殻4Aを収納した網製容
器などからなるフイルター装置4と、このフイル
ター装置4を通して流出したし尿汚水を希釈する
注水装置5と、希釈汚水に散気を行い好気性菌に
より処理を行う接触曝気室6と、該接触曝気室6
から流出する処理水中の剥離汚泥等の浮遊物(図
示せず)を沈澱させる沈澱室7、この沈澱室7か
ら流出するし尿汚水を消毒する消毒室8、並びに
この消毒室8に設けられた排出口9とから構成さ
れている。
上記実施例において、腐敗槽3内に汚水を流入
させる流入管2Aとしては、腐敗槽3内の汚水中
にできるだけ空気の混入を防止するため、図示の
ように、管2Aの下端が汚水中の深い位置に開口
するようにし、汚水流入時に発生する気泡が槽3
内に広く拡散しないようにすることが望ましい。
又、腐敗槽3内の処理を確実に行わせるため、
図示のように、腐敗槽3内を、仕切壁3Aにより
いくつかに仕切り、汚水を矢印Pで示すように段
階的に移流していくようにすることが望ましい。
次に、この発明の実施例の作用を説明する。
難処理し尿汚水(糖尿性し尿の場合)が流入さ
れた腐敗槽3内においては、汚水中への酸素供給
が行われ難いこと及びし尿汚水は静置されるか
ら、汚水中に含まれる糖質成分等を好餌として嫌
気性菌が良好に繁殖し、嫌気性菌によつて糖質成
分等が分解される。
しかしながら、上記嫌気性菌による分解が行わ
れると、汚水中の糖や有機酸等により汚水のPH度
が異常に低下し、又、BOD値も極めて高い値と
なる。
これは、以後に行う好気性菌による分解処理に
不都合であるから、まずPH値を高めるため、フイ
ルター装置4を介し、次槽へ汚水を移流させるの
である。
このフイルター装置4により汚水のPH度は、4
より7程度にまで上げられる。特にフイルター装
置の下部からエアレーシヨンをする方がPHコント
ロールの効果が高まる(図示せず)。さらに、こ
の汚水は注水装置5より希釈され、次の曝気室6
へと移流される。この注水により、汚水はBOD
負荷が適正化され、次槽における処理が容易化さ
れる。
接触曝気室6内においては、散気室6Aより噴
出する気泡により汚水中に充分に空気が供給さ
れ、ここで育成された好気性菌により汚水中の有
機成分が分解される。
尚、曝気室6内における好気性菌、好気性微生
物の育成を助け、かつ、槽内の汚水の流れを整流
循環させるため、ハニカム状、ネツト状等の接触
材6Bが配置される。
この時点において、汚水中における有機成分
は、嫌気、好気性菌の両方によつて分解処理され
ている。
次いで、沈澱室7内において再び処理水は静置
され、この処理水中に含まれる剥離汚泥等の浮遊
物が沈澱除去される。上記浮遊物は主として接触
曝気室6内において育成された生物膜の剥離体で
ある。
そして、処理水は最終的に消毒室8で消毒さ
れ、排出口9より外部へ排出されるのである。
上記実施例は、浄化槽1として必要な室を当初
から一体に有したものの場合について示したが、
これにかかわらず、第1図に示したような従来例
の浄化槽であつても本発明の難処理用浄化槽とし
て使用することも可能である。
即ち、第4図は他の実施例の断面図を示すもの
であつて、従来の浄化槽1′における分離室A、
及び曝気室Bをそれぞれ腐敗槽3,3とし、沈澱
室C内に石灰石、牡蛎殻等を収納し、フイルター
装置4とし、消毒室Dを注水槽とし、ここに注水
装置5を設け、排出口9をもう一つの従来型の浄
化槽1″の流入口に接続し、この浄化槽1″により
曝気処理を行うようにしたものである。
又、第5図に示すように、従来型の浄化槽1′
全体を腐敗槽3として用い、この浄化槽1′の排
出口に、PHを調整するフイルター装置4、及び注
水装置5を一体に設けたコントロール槽45、及
び接触曝気型浄化槽1を順に接続することによ
つても同様に実施される。
ちなみに、本発明による浄化槽と、従来型の浄
化槽との浄化性能を比較したところ、下表のよう
結果が得られた。
し尿汚水の種類
1 尿中の糖が正常値の4〜10倍
2 尿の粘性が正常のものに比し高い
3 尿の比重が大きい
4 アセトン体、クレアチンが正常値より多い
上記のし尿汚水を本発明及び従来型の浄化槽に
流入させ、浄化後の排出液の水質を検査した。
The present invention relates to a septic tank for urine and sewage that is difficult to treat. Conventionally, as shown in Fig. 1, a septic tank for human waste sewage includes a separation chamber A for separating solid matter in the human waste water, a aeration system for the human waste water flowing out from the separation chamber A,
Aeration chamber B that performs treatment with aerobic bacteria;
It is generally known to have a sedimentation chamber C for precipitating suspended matter such as exfoliated sludge in the treated water flowing out from the sedimentation chamber C, and a disinfection chamber D for disinfecting the treated water flowing out from the sedimentation chamber C and discharging it to the outside. . This type of sewage septic tank normally treats the discharged sewage almost completely and purifies it to the extent that it can be discharged to the general sewer system, but human waste sewage is difficult to treat sewage. In some cases, especially in the case of diabetic human waste or human waste sewage containing pharmaceutical components such as vitamins and antihypertensive agents, the components contained in human waste may not be completely treated and may not meet the discharge standards. It was hot. In view of the above-mentioned problems, the present invention was made for the purpose of providing a septic tank that can sufficiently purify even human waste water, which is difficult to treat.
A septic tank with an inlet, where the inflowing human waste water is allowed to stand still and putrefied by anaerobic bacteria, and an alkaline content (or acid content) is added to the human waste waste water flowing out from the septic tank to adjust the pH. A filter device, a water injection device for diluting the human waste water flowing out through the filter device, a contact aeration chamber for aerating the diluted human waste water flowing out and treating it with aerobic bacteria, and a contact aeration chamber for dispersing the diluted human waste water flowing out and treating it with aerobic bacteria; It is characterized by consisting of a settling chamber for settling floating matter such as exfoliated sludge in the treated water, a disinfection chamber for disinfecting the treated water flowing out from the settling chamber, and an outlet provided in the disinfection chamber. . Next, the present invention will be explained using examples. FIG. 2 is a conceptual diagram showing a cross section of an embodiment of the present invention, and FIG. 3 is a cutaway perspective view of essential parts of one embodiment. A septic tank 1 for hard-to-treat night soil sewage according to the present invention has an inlet 2 through which the night soil sewage flows in, and a septic tank 3 in which the inflowed human waste sewage W is allowed to stand still and rotted by anaerobic bacteria, and this septic tank. A filter device 4 consisting of, for example, a mesh container containing limestone and oyster shells 4A is added to the human waste water flowing out from the filter device 4 to adjust the pH by adding alkalinity (or acid content) to the wastewater flowing out from the filter device 4. A water injection device 5 that dilutes human waste wastewater, a contact aeration chamber 6 that aerates the diluted wastewater and treats it with aerobic bacteria, and the contact aeration chamber 6
A sedimentation chamber 7 for precipitating suspended matter (not shown) such as exfoliated sludge in the treated water flowing out from the sedimentation chamber 7, a disinfection chamber 8 for disinfecting human waste water flowing out from this sedimentation chamber 7, and a drainage provided in this disinfection chamber 8. It consists of an exit 9. In the above embodiment, as for the inflow pipe 2A that flows the wastewater into the septic tank 3, in order to prevent air from being mixed into the wastewater in the septic tank 3 as much as possible, the lower end of the pipe 2A is inserted into the wastewater as shown in the figure. The opening is set at a deep position so that air bubbles generated when wastewater flows into tank 3
It is desirable to prevent it from spreading widely within the country. In addition, in order to ensure that the treatment inside the septic tank 3 is carried out,
As shown in the figure, it is desirable that the inside of the septic tank 3 be partitioned into several parts by partition walls 3A so that the sewage can be advected in stages as indicated by arrows P. Next, the operation of the embodiment of this invention will be explained. In the septic tank 3 into which difficult-to-treat human waste water (in the case of diabetic human waste) flows, it is difficult to supply oxygen to the waste water, and the human waste water is allowed to stand still, so the carbohydrates contained in the waste water are Anaerobic bacteria thrive on the ingredients, etc. as their favorite food, and the carbohydrate components, etc. are decomposed by the anaerobic bacteria. However, when decomposition by the above-mentioned anaerobic bacteria occurs, the PH degree of the wastewater is abnormally lowered due to sugars, organic acids, etc. in the wastewater, and the BOD value also becomes extremely high. Since this is inconvenient for the subsequent decomposition treatment by aerobic bacteria, the wastewater is advected to the next tank via the filter device 4 in order to increase the pH value. With this filter device 4, the pH level of the waste water is 4.
It can be raised to about 7. In particular, PH control is more effective when aeration is performed from the bottom of the filter device (not shown). Furthermore, this wastewater is diluted by the water injection device 5 and then transferred to the next aeration chamber 6.
is advected to. With this water injection, wastewater is reduced to BOD
The load is optimized and processing in the next tank is facilitated. In the contact aeration chamber 6, air is sufficiently supplied to the wastewater by bubbles ejected from the aeration chamber 6A, and organic components in the wastewater are decomposed by aerobic bacteria grown here. Note that a contact material 6B in the form of a honeycomb, a net, etc. is arranged to help the growth of aerobic bacteria and aerobic microorganisms in the aeration chamber 6, and to rectify and circulate the flow of wastewater in the tank. At this point, the organic components in the wastewater have been decomposed by both anaerobic and aerobic bacteria. Next, the treated water is allowed to stand still in the settling chamber 7 again, and suspended matter such as exfoliated sludge contained in the treated water is sedimented and removed. The above-mentioned floating matter is mainly a detached body of biofilm grown in the contact aeration chamber 6. The treated water is finally disinfected in the disinfection chamber 8 and discharged to the outside through the discharge port 9. The above embodiment has been shown in the case where the necessary chambers as the septic tank 1 were integrated from the beginning, but
Regardless of this, even a conventional septic tank as shown in FIG. 1 can be used as the difficult-to-treat septic tank of the present invention. That is, FIG. 4 shows a sectional view of another embodiment, in which the separation chamber A in the conventional septic tank 1',
and aeration chamber B are respectively used as septic tanks 3, 3, limestone, oyster shells, etc. are stored in sedimentation chamber C and used as a filter device 4, disinfection chamber D is used as a water injection tank, where a water injection device 5 is provided, and a discharge port is provided. 9 is connected to the inlet of another conventional septic tank 1'', and aeration processing is performed by this septic tank 1''. Furthermore, as shown in Fig. 5, the conventional septic tank 1'
The entire structure is used as a septic tank 3, and a filter device 4 for adjusting pH, a control tank 45 that is integrally equipped with a water injection device 5, and a contact aeration type septic tank 1 are connected in order to the outlet of this septic tank 1'. The same applies even if the By the way, when the purification performance of the septic tank according to the present invention and a conventional type septic tank was compared, the results shown in the table below were obtained. Types of human waste sewage 1 The sugar in the urine is 4 to 10 times the normal value 2 The viscosity of the urine is higher than normal 3 The specific gravity of the urine is large 4 The acetone body and creatine are higher than the normal value The above human waste sewage The water quality of the effluent after purification was examined by flowing it into the septic tanks of the present invention and the conventional type.
【表】
以上から明らかなように、本発明の難処理し尿
汚水用浄化槽は、従来、完全な処理が困難であつ
た糖質成分、あるいは他の薬品成分であつても、
嫌気性菌の作用により処理が可能であり、又、こ
の際に変化する汚水の水質特性を以後の処理が容
易なようにPH、及び濃度を適性化するため、処理
が確実かつ迅速に行えるのである。又、従来使用
されている浄化槽を組み合わせても実施できるか
ら、実施が容易であるなどの効果を有する。[Table] As is clear from the above, the difficult-to-treat human waste sewage septic tank of the present invention can handle carbohydrate components or other chemical components, which were conventionally difficult to completely treat.
Treatment is possible through the action of anaerobic bacteria, and the water quality characteristics of the wastewater change at this time, so that the pH and concentration are optimized for easy subsequent treatment, so treatment can be performed reliably and quickly. be. Moreover, since it can be carried out by combining conventionally used septic tanks, it has the advantage of being easy to carry out.
第1図は従来例の説明図、第2図はこの発明の
実施例の概念図、第3図は実施例の要部破断斜視
図、第4図、第5図は他の実施例の断面図であ
る。
1…難処理し尿汚水用浄化槽、2…流入口、3
…腐敗槽、4…フイルター装置、5…注水装置、
6…曝気室、7…沈澱室、8…消毒室、9…排出
口。
Fig. 1 is an explanatory diagram of a conventional example, Fig. 2 is a conceptual diagram of an embodiment of the present invention, Fig. 3 is a cutaway perspective view of the main part of the embodiment, and Figs. 4 and 5 are cross sections of other embodiments. It is a diagram. 1... Septic tank for difficult-to-treat urine sewage, 2... Inlet, 3
... Septic tank, 4... Filter device, 5... Water injection device,
6...Aeration chamber, 7...Sedimentation chamber, 8...Disinfection chamber, 9...Outlet.
Claims (1)
し、嫌気性菌により腐敗させる腐敗槽と、該腐敗
槽から流出するし尿汚水にアルカリ分(又は酸
分)を付加し、PHを調整するフイルター装置と、
該フイルター装置を通して流出するし尿汚水を希
釈する注水装置と、希釈されて流出したし尿汚水
に散気を行い好気性菌により処理を行う接触曝気
室と、該接触曝気室から流出する処理水中の剥離
汚泥等の浮遊物を沈澱させる沈澱室と、該沈澱室
から流出する処理水を消毒する消毒室、並びに該
消毒室に設けた排出口とからなることを特徴とす
る難処理し尿汚水用浄化槽。1. A septic tank with an inlet, where the inflowing human waste water is allowed to stand still and rotted by anaerobic bacteria, and an alkaline content (or acid content) is added to the human waste waste water flowing out from the septic tank to adjust the pH. a filter device to
A water injection device that dilutes the human waste water flowing out through the filter device, a contact aeration chamber that aerates the diluted human waste water that flows out and treats it with aerobic bacteria, and separation in the treated water that flows out from the contact aeration room. A septic tank for difficult-to-treat urine sewage characterized by comprising a settling chamber in which suspended matter such as sludge is settled, a disinfection chamber in which treated water flowing out from the settling chamber is disinfected, and an outlet provided in the disinfection chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57010769A JPS58128195A (en) | 1982-01-25 | 1982-01-25 | Septic tank of hardly disposable sewage of night soil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57010769A JPS58128195A (en) | 1982-01-25 | 1982-01-25 | Septic tank of hardly disposable sewage of night soil |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58128195A JPS58128195A (en) | 1983-07-30 |
JPS6254072B2 true JPS6254072B2 (en) | 1987-11-13 |
Family
ID=11759533
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57010769A Granted JPS58128195A (en) | 1982-01-25 | 1982-01-25 | Septic tank of hardly disposable sewage of night soil |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58128195A (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6257697A (en) * | 1985-09-04 | 1987-03-13 | Meidensha Electric Mfg Co Ltd | Waste water treatment device |
US5730305A (en) * | 1988-12-27 | 1998-03-24 | Kato Works Co., Ltd. | Crane safety apparatus |
US5468375A (en) * | 1994-05-09 | 1995-11-21 | Nova Power Systems, Ltd. | Wastewater pretreatment tank assembly |
GB2317169A (en) | 1996-09-13 | 1998-03-18 | Kvaerner Davy Ltd | Anoxic and aerobic metabolisation of waste |
GB9805714D0 (en) | 1998-03-17 | 1998-05-13 | Kvaerner Construction Limited | Liquid effluent treatment process and plant |
US6383372B1 (en) * | 2000-01-08 | 2002-05-07 | Michael H. Houck | Sequential flow filtration chamber for treatment of waste water and associated method |
CN112047581A (en) * | 2020-09-22 | 2020-12-08 | 广东帝亿建材科技有限公司 | Fecal sewage treatment's control system |
-
1982
- 1982-01-25 JP JP57010769A patent/JPS58128195A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS58128195A (en) | 1983-07-30 |
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