JP2011056461A - Apparatus and method for reducing volume of sludge - Google Patents
Apparatus and method for reducing volume of sludge Download PDFInfo
- Publication number
- JP2011056461A JP2011056461A JP2009211589A JP2009211589A JP2011056461A JP 2011056461 A JP2011056461 A JP 2011056461A JP 2009211589 A JP2009211589 A JP 2009211589A JP 2009211589 A JP2009211589 A JP 2009211589A JP 2011056461 A JP2011056461 A JP 2011056461A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- sludge
- tank
- ozone treatment
- treatment tank
- 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
- 239000010802 sludge Substances 0.000 title claims abstract description 88
- 238000000034 method Methods 0.000 title abstract description 5
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 116
- 239000007787 solid Substances 0.000 claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 15
- 238000005273 aeration Methods 0.000 claims abstract description 13
- 238000007599 discharging Methods 0.000 claims description 3
- 230000001376 precipitating effect Effects 0.000 claims description 3
- 230000000630 rising effect Effects 0.000 claims description 2
- 230000003381 solubilizing effect Effects 0.000 claims description 2
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 abstract description 15
- 238000005063 solubilization Methods 0.000 abstract description 7
- 230000007928 solubilization Effects 0.000 abstract description 7
- 238000004062 sedimentation Methods 0.000 abstract description 3
- 239000003054 catalyst Substances 0.000 description 5
- 238000000354 decomposition reaction Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 210000002421 cell wall Anatomy 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 230000032683 aging Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 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
- Y02W10/20—Sludge processing
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
本発明は、汚泥減容化装置及び汚泥減容化方法に関する。より詳しく述べると、オゾン処理槽を利用した汚泥の減容化に関する。 The present invention relates to a sludge volume reduction device and a sludge volume reduction method. More specifically, it relates to volume reduction of sludge using an ozone treatment tank.
出願人は、現在、市町村規模での汚泥処理を行う施設を提供するために、特許出願をしている。その公開公報を先行技術文献に掲げる。以下、図４により従来の汚泥減容化システムの簡単なフローを説明する。まず、汚泥は流量調整槽２０１を経て曝気槽２０２で生物処理される。その後、処理液は、沈殿槽２０３で固液分離される。その後、汚泥の固体成分は、汚泥貯留槽２０４において貯留される。その後、汚泥は、オゾン処理槽２０５において可溶化される。ここで、オゾンは、汚泥の細胞を破壊し、可溶化を図るために用いられる。オゾン処理槽２０５で可溶化した汚泥は、循環槽２０６とオゾン処理槽２０５の間で循環されることによって、熟成する。そして、循環槽２０６で熟成した汚泥は、曝気槽２０２に戻され、再度生物処理に供される。この先行技術の特徴は、オゾン処理槽２０５と循環槽２０６の間を汚泥が循環することにより、熟成し、可溶化が促進することである。 The applicant is currently applying for a patent in order to provide a facility for sludge treatment on a municipal scale. The publication is listed in the prior art document. Hereinafter, a simple flow of the conventional sludge volume reduction system will be described with reference to FIG. First, the sludge is biologically processed in the aeration tank 202 through the flow rate adjustment tank 201. Thereafter, the treatment liquid is solid-liquid separated in the precipitation tank 203. Thereafter, the solid component of the sludge is stored in the sludge storage tank 204. Thereafter, the sludge is solubilized in the ozone treatment tank 205. Here, ozone is used to destroy sludge cells and solubilize. The sludge solubilized in the ozone treatment tank 205 is aged by being circulated between the circulation tank 206 and the ozone treatment tank 205. The sludge aged in the circulation tank 206 is returned to the aeration tank 202 and again subjected to biological treatment. The feature of this prior art is that the sludge circulates between the ozone treatment tank 205 and the circulation tank 206, thereby aging and promoting solubilization.
特開２００８−３６５７１号
この開示された発明は、比較的大きい規模の施設で利用されるので、図４に示したオゾン処理槽２０５で可溶化できなかった汚泥を循環槽２０６に送り、更にオゾン処理槽２０５に戻し、循環させることで、可溶化を促進している。この装置によると、引き抜きが限りなくゼロに近づき、バキュームカーなどによる引き抜き処理が不要となり、環境にも優れている。
Since the disclosed invention is used in a relatively large scale facility, sludge that could not be solubilized in the ozone treatment tank 205 shown in FIG. Solubilization is promoted by returning to the treatment tank 205 and circulating it. According to this apparatus, the drawing is almost zero, and the drawing process using a vacuum car or the like is not necessary, and the environment is excellent.
近年、環境問題が提起され、各地方自治体においても、環境関連政策の一環として独自の条例が施行されている。その中で、飲食店などの特定施設においては、排水基準を満たすために、施設から出る排水を放流する前に排水の処理が課される例もある。このような排水処理を行うためには、上記の開示された発明とは異なり、汚泥をオゾン処理槽と循環槽の間で循環させる必要はない。そこで、飲食店などの施設を対象に、循環槽を用いずに、汚泥を減容化する装置を発明した。 In recent years, environmental issues have been raised, and each local government has its own regulations as part of its environmental policy. Among them, in particular facilities such as restaurants, there are cases where wastewater treatment is imposed before the wastewater discharged from the facility is discharged in order to satisfy the wastewater standards. In order to perform such wastewater treatment, unlike the above disclosed invention, it is not necessary to circulate sludge between the ozone treatment tank and the circulation tank. Therefore, an apparatus for reducing the volume of sludge was invented for facilities such as restaurants without using a circulation tank.
上記課題を解決する本発明は、次の項目に関する。
（１）汚泥の流量を調整するための流量調整槽１０１と、流量調整槽１０１から排出される汚泥を生物処理するための曝気槽１０２と、その後、液体と固体成分に分け液体は放流する一方で固体成分を沈殿しておく沈殿槽１０３と、固体成分を貯留するための汚泥貯留槽１０４と、汚泥貯留槽１０４に貯留された固体成分をオゾン処理して可溶化するオゾン処理槽１０５とからなる汚泥処理システムにおいて、オゾン処理槽１０５の本体１１の底面中央部に、オゾンが垂直方向に噴出されるようにオゾン供給配管１５の噴出口１５ａを設けたことを特徴とするオゾン処理システムである。
（２）オゾン供給配管１５より供給されたオゾンが、オゾン処理槽１０５の本体１１の底面中央部に設置されたオゾン噴出口１５ａから垂直方向に上昇し、オゾン処理槽１０５の本体１１の最上面に達した後、オゾンは３６０度の方向に拡散し、オゾン処理槽１０５の本体１１の側面に沿って下降し、オゾン処理槽１０５の本体１１の底面に達した後、オゾン処理槽１０５の本体１１の底面中央部に達し、オゾン処理槽１０５の本体１１の内部で循環を繰り返すことを特徴とするオゾン処理システムである。
（３）流量調整槽１０１において汚泥の流量を調整する工程と、流量調整槽１０１から排出される汚泥を曝気槽１０２において生物処理する工程と、その後、液体と固体成分に分け液体は放流する一方で固体成分を沈殿槽１０３において沈殿しておく工程と、固体成分を汚泥貯留槽１０４において貯留する工程と、汚泥貯留槽１０４に貯留された固体成分をオゾン処理槽１０５においてオゾン処理する工程とからなる汚泥処理方法において、オゾンと汚泥との接触率を上げるために、オゾン供給配管１５より供給されたオゾンが、オゾン処理槽１０５の本体１１の底面中央部に設置されたオゾン噴出口１５ａから垂直方向に上昇し、オゾン処理槽１０５の本体１１の最上面に達した後、オゾンは３６０度の方向に拡散し、オゾン処理槽１０５の本体１１の側面に沿って下降し、オゾン処理槽１０５の本体１１の底面に沿ってオゾン処理槽１０５の本体１１の底面中央部まで戻り、オゾン処理槽１０５の本体１１の内部で循環を繰り返す工程からなる汚泥の減容化方法である。
The present invention for solving the above problems relates to the following items.
(1) A flow rate adjusting tank 101 for adjusting the flow rate of sludge, an aeration tank 102 for biologically treating the sludge discharged from the flow rate adjusting tank 101, and then dividing the liquid into solid components and releasing the liquid From a sedimentation tank 103 for precipitating the solid component, a sludge storage tank 104 for storing the solid component, and an ozone treatment tank 105 for solubilizing the solid component stored in the sludge storage tank 104 by ozone treatment. In the sludge treatment system, the ozone treatment system is characterized in that a jet outlet 15a of the ozone supply pipe 15 is provided at the center of the bottom surface of the main body 11 of the ozone treatment tank 105 so that ozone is jetted in the vertical direction. .
(2) The ozone supplied from the ozone supply pipe 15 rises in the vertical direction from the ozone outlet 15 a installed at the center of the bottom surface of the main body 11 of the ozone treatment tank 105, and the uppermost surface of the main body 11 of the ozone treatment tank 105. The ozone diffuses in the direction of 360 degrees, descends along the side surface of the main body 11 of the ozone treatment tank 105, reaches the bottom surface of the main body 11 of the ozone treatment tank 105, and then the main body of the ozone treatment tank 105. 11 is an ozone treatment system characterized in that it reaches the bottom center of 11 and repeats circulation inside the main body 11 of the ozone treatment tank 105.
(3) The step of adjusting the flow rate of sludge in the flow rate adjusting tank 101, the step of biologically treating the sludge discharged from the flow rate adjusting tank 101 in the aeration tank 102, and then dividing the liquid into solid components and discharging the liquid The solid component is precipitated in the sedimentation tank 103, the solid component is stored in the sludge storage tank 104, and the solid component stored in the sludge storage tank 104 is ozone-treated in the ozone treatment tank 105. In order to increase the contact rate between ozone and sludge, the ozone supplied from the ozone supply pipe 15 is perpendicular to the ozone outlet 15 a installed at the center of the bottom surface of the main body 11 of the ozone treatment tank 105. After rising in the direction and reaching the uppermost surface of the main body 11 of the ozone treatment tank 105, the ozone diffuses in the direction of 360 degrees, and the ozone treatment tank 105 The process of descending along the side surface of the main body 11, returning to the center of the bottom surface of the main body 11 of the ozone treatment tank 105 along the bottom surface of the main body 11 of the ozone treatment tank 105, and repeating the circulation inside the main body 11 of the ozone treatment tank 105. This is a method for reducing the volume of sludge.
本発明によると、汚泥の減容化に成功した結果、汚泥の引き抜きをしなくても良い効果がでた。 According to the present invention, as a result of succeeding in volume reduction of sludge, there is an effect that it is not necessary to extract sludge.
以下、本発明を添付図面に基づいて詳細に説明する。図１は、本発明の汚泥減容化システムを示すフローチャートであり、図２は、汚泥の分解の流れを示す模式図であり、図３は、本発明のオゾン処理槽を示す模式図であり、そして図４は、従来の汚泥減容化システムを示すフローチャートである。 Hereinafter, the present invention will be described in detail with reference to the accompanying drawings. FIG. 1 is a flowchart showing a sludge volume reduction system of the present invention, FIG. 2 is a schematic diagram showing a flow of sludge decomposition, and FIG. 3 is a schematic diagram showing an ozone treatment tank of the present invention. FIG. 4 is a flowchart showing a conventional sludge volume reduction system.
まず、図１に基づいて、本発明の汚泥減容化システムの流れを説明する。汚泥は、汚泥の流量を調整する流量調整槽１０１を経て曝気槽１０２で微生物により生物処理される。その後、処理液は、沈殿槽１０３で固液分離される。その後、汚泥の固体成分は、汚泥貯留槽１０４において貯留される。その後、汚泥は、オゾン処理槽１０５において可溶化される。可溶化した汚泥は、再度曝気槽１０２に戻され、生物処理に供される。 First, based on FIG. 1, the flow of the sludge volume reduction system of this invention is demonstrated. The sludge is biologically treated with microorganisms in the aeration tank 102 through the flow rate adjustment tank 101 for adjusting the flow rate of the sludge. Thereafter, the treatment liquid is solid-liquid separated in the precipitation tank 103. Thereafter, the solid component of the sludge is stored in the sludge storage tank 104. Thereafter, the sludge is solubilized in the ozone treatment tank 105. The solubilized sludge is returned again to the aeration tank 102 and used for biological treatment.
図２に示す汚泥の分解の流れでは、図１のオゾン処理槽１０５において、オゾンと接触した汚泥の細胞壁が傷付けられることによって分解が起こり、汚泥の内容物が流出し、可溶化状態になった後、図１の曝気槽１０２に戻され、生物分解される様子を示している。 In the sludge decomposition flow shown in FIG. 2, in the ozone treatment tank 105 of FIG. 1, the cell wall of the sludge in contact with ozone is damaged and the decomposition occurs, and the sludge contents flow out and become a solubilized state. Thereafter, the state is returned to the aeration tank 102 of FIG. 1 and biodegraded.
図４に示す従来の汚泥減容化システムでは、オゾン処理槽２０５で可溶化した汚泥は、循環槽２０６とオゾン処理槽２０５の間で循環されることによって、熟成する。そして、循環槽２０６で熟成した汚泥は、曝気槽２０２に戻され、再度生物処理に供される。大規模な施設では、オゾン処理槽２０５のみでは汚泥の可溶化が不十分であるため、循環槽２０６を用いて可溶化を完了することが不可欠である。 In the conventional sludge volume reduction system shown in FIG. 4, the sludge solubilized in the ozone treatment tank 205 is aged by being circulated between the circulation tank 206 and the ozone treatment tank 205. The sludge aged in the circulation tank 206 is returned to the aeration tank 202 and again subjected to biological treatment. In a large-scale facility, since the solubilization of sludge is insufficient only with the ozone treatment tank 205, it is essential to complete the solubilization using the circulation tank 206.
図３に示す本発明のオゾン処理槽１０５では、一日当たりの汚泥処理量を低減することによって、図４に示す従来の汚泥減容化システムから循環槽２０６を取り除いても、汚泥の引き抜きなしで汚泥の減容化が可能となる小規模施設用の汚泥減容システムである。 In the ozone treatment tank 105 of the present invention shown in FIG. 3, even if the circulation tank 206 is removed from the conventional sludge volume reduction system shown in FIG. 4 by reducing the amount of sludge treatment per day, the sludge is not extracted. This is a sludge volume reduction system for small-scale facilities that enables sludge volume reduction.
次に図３に示すオゾン処理槽１０５のしくみをより具体的に示す。汚泥貯留槽１０４から水中ポンプ１４を通して本体１１に流入した汚泥は、従来のオゾン処理槽２０５における流れと同様に、オゾン供給配管１５より供給されたオゾンと接触し、汚泥の細胞壁に傷が付けられ、浸透圧で内容物が流出し、可溶化状態になる。従来のオゾン処理槽２０５との相違点として、本発明においては、オゾンがオゾン処理槽１０５の内部で循環を繰り返す。まず、オゾン処理槽１０５の本体１１の底面中央部に設置されたオゾン供給配管１５のオゾン噴出口１５ａより噴出されたオゾンは、本体１１の底面中央部より垂直方向に上昇し、本体１１の最上面に達する。その後、３６０度の方向に拡散したオゾンは、本体１１の側面を伝って下降し、底面に達する。その後、オゾンは、底面を伝って再度本体１１の中央部に戻り、上昇する。この循環によって汚泥とオゾンの接触率が増し、可溶化がより効率良く促進されることになる。 Next, the mechanism of the ozone treatment tank 105 shown in FIG. 3 will be described more specifically. The sludge that flows into the main body 11 from the sludge storage tank 104 through the submersible pump 14 comes into contact with the ozone supplied from the ozone supply pipe 15 in the same manner as the flow in the conventional ozone treatment tank 205, and the cell wall of the sludge is damaged. The osmotic pressure causes the contents to flow out, resulting in a solubilized state. As a difference from the conventional ozone treatment tank 205, ozone repeats circulation inside the ozone treatment tank 105 in the present invention. First, the ozone ejected from the ozone outlet 15a of the ozone supply pipe 15 installed at the center of the bottom surface of the main body 11 of the ozone treatment tank 105 rises in the vertical direction from the center of the bottom surface of the main body 11, and reaches the top of the main body 11. Reach the top surface. Thereafter, the ozone diffused in the direction of 360 degrees descends along the side surface of the main body 11 and reaches the bottom surface. Then, ozone returns to the central part of the main body 11 again along the bottom surface and rises. This circulation increases the contact rate between sludge and ozone and promotes solubilization more efficiently.
なお、汚泥の上部にはオゾンの気泡が発生し、これがオゾン処理槽１０５の本体１１の上部に設置された触媒反応槽１６まで到達すると、触媒が濡れることによって、触媒の働きが弱くなる。これを防ぐため、汚泥の液面とオゾン処理槽１０５の本体１１の最上面までの長さが３０cm以上に保たれるようにし、かつ発生したオゾンの気泡の層の最上面とオゾン処理槽１０５の本体１１の最上面までの長さが１５cm以上に保たれるようにした。 Note that ozone bubbles are generated in the upper part of the sludge, and when this reaches the catalyst reaction tank 16 installed in the upper part of the main body 11 of the ozone treatment tank 105, the catalyst is weakened to weaken the function of the catalyst. In order to prevent this, the length from the sludge liquid surface to the top surface of the main body 11 of the ozone treatment tank 105 is kept at 30 cm or more, and the top surface of the generated ozone bubble layer and the ozone treatment tank 105 are maintained. The length to the top surface of the main body 11 was kept at 15 cm or more.
表１に示す本発明の実施例１では、オゾン処理槽１０５の汚泥処理量を一日当たり５０m3、容量を３７５L、オゾンの発生量を１時間当たり４５g、オゾン濃度を７５g/Nm3、及び流量を１時間当たり０．６Nm3と限定した。 In Example 1 of the present invention shown in Table 1, the amount of sludge treated in the ozone treatment tank 105 is 50 m 3 per day, the volume is 375 L, the amount of ozone generated is 45 g per hour, the ozone concentration is 75 g / Nm 3 , and the flow rate. Was limited to 0.6 Nm 3 per hour.
また、表１に示す本発明の実施例２では、より小規模な施設のために、オゾン処理槽１０５の汚泥処理量を一日当たり１５m3、容量を１１２．５L、オゾンの発生量を１時間当たり１３．５g、オゾン濃度を７５g/Nm3、及び流量を１時間当たり０．１８Nm3と限定した。 In Example 2 of the present invention shown in Table 1, for a smaller facility, the sludge treatment amount of the ozone treatment tank 105 is 15 m 3 per day, the capacity is 112.5 L, and the generation amount of ozone is one hour. per 13.5 g, with limited ozone concentration 75 g / Nm 3, and the flow rate per hour 0.18 nm 3.
また、オゾン処理槽１０５の本体１１の上部に設置された触媒反応槽１６にヒーター１２を用いて、触媒を露点温度以上に保つようにした。さらに、オゾン処理槽１０５の本体１１に断熱カバー１３をかけることによって、外気温度の変化がオゾン処理槽１０５の働きに与える影響を最小限に留めるようにした。 In addition, the catalyst was kept at the dew point temperature or higher by using the heater 12 in the catalyst reaction tank 16 installed in the upper part of the main body 11 of the ozone treatment tank 105. Furthermore, by applying the heat insulating cover 13 to the main body 11 of the ozone treatment tank 105, the influence of changes in the outside air temperature on the function of the ozone treatment tank 105 is kept to a minimum.
本発明の好ましい形態として、オゾン処理装置１０５の本体１１は垂直方向に長いほど、オゾンの循環時に、オゾンと汚泥の接触率が増し、汚泥の可溶化がより促進される。 As a preferred embodiment of the present invention, the longer the main body 11 of the ozone treatment apparatus 105 is in the vertical direction, the greater the contact rate between ozone and sludge during the circulation of ozone, and the more solubilization of sludge is promoted.
１１ 本体
１２ ヒーター
１３ 断熱カバー
１４ 水中ポンプ
１５ オゾン供給配管
１５ａ オゾン噴出口
１６ 触媒反応槽
１０１ 流量調整槽
１０２ 曝気槽
１０３ 沈殿槽
１０４ 汚泥貯留槽
１０５ オゾン処理槽
２０１ 流量調整槽
２０２ 曝気槽
２０３ 沈殿槽
２０４ 汚泥貯留槽
２０５ オゾン処理槽
２０６ 循環槽
DESCRIPTION OF SYMBOLS 11 Main body 12 Heater 13 Heat insulation cover 14 Submersible pump 15 Ozone supply piping 15a Ozone jet 16 Catalytic reaction tank 101 Flow rate adjustment tank 102 Aeration tank 103 Precipitation tank 104 Sludge storage tank 105 Ozone treatment tank 201 Flow rate adjustment tank 202 Aeration tank 203 Precipitation tank 204 Sludge storage tank 205 Ozone treatment tank 206 Circulation tank
Claims (3)
前記流量調整槽から排出される前記汚泥を生物処理するための曝気槽と、
その後、液体と固体成分に分け前記液体は放流する一方で前記固体成分を沈殿しておく沈殿槽と、
前記固体成分を貯留するための汚泥貯留槽と、
前記汚泥貯留槽に貯留された前記固体成分をオゾン処理して可溶化するオゾン処理槽と、
からなる汚泥処理システムにおいて、前記オゾン処理槽の本体底面中央部に、オゾンが垂直方向に噴出されるようにオゾン供給配管の噴出口を設けたことを特徴とするオゾン処理システム。 A flow rate adjusting tank for adjusting the flow rate of sludge;
An aeration tank for biologically treating the sludge discharged from the flow rate adjustment tank;
Thereafter, a settling tank for separating the liquid into solid components and discharging the liquid while precipitating the solid components;
A sludge storage tank for storing the solid component;
An ozone treatment tank for solubilizing the solid component stored in the sludge storage tank by ozone treatment;
In the sludge treatment system comprising the ozone treatment system, an ozone supply piping outlet is provided at the center of the bottom of the main body of the ozone treatment tank so that ozone is jetted in the vertical direction.
前記流量調整槽から排出される前記汚泥を曝気槽において生物処理する工程と、
その後、液体と固体成分に分け前記液体は放流する一方で前記固体成分を沈殿槽において沈殿しておく工程と、
前記固体成分を汚泥貯留槽において貯留する工程と、
前記汚泥貯留槽に貯留された前記固体成分をオゾン処理槽においてオゾン処理する工程と、
からなる汚泥処理方法において、オゾンと汚泥との接触率を上げるために、オゾン供給配管より供給されたオゾンが、前記オゾン処理槽の本体底面中央部に設置された前記オゾン供給配管の噴出口から垂直方向に上昇し、前記オゾン処理槽の本体最上面に達した後、前記オゾンは３６０度の方向に拡散し、前記オゾン処理槽の本体側面に沿って下降し、前記オゾン処理槽の本体底面に達した後、前記オゾン処理槽の本体底面中央部に達し、前記オゾン処理槽内で循環を繰り返す工程からなる汚泥の減容化方法。 Adjusting the flow rate of sludge in the flow rate adjustment tank;
Biologically treating the sludge discharged from the flow rate adjustment tank in an aeration tank;
Thereafter, dividing the liquid into solid components and discharging the liquid while precipitating the solid components in a settling tank;
Storing the solid component in a sludge storage tank;
A step of ozone-treating the solid component stored in the sludge storage tank in an ozone treatment tank;
In order to increase the contact rate between ozone and sludge, the ozone supplied from the ozone supply pipe is discharged from the outlet of the ozone supply pipe installed at the center bottom of the main body of the ozone treatment tank. After rising in the vertical direction and reaching the top surface of the main body of the ozone treatment tank, the ozone diffuses in the direction of 360 degrees, descends along the side surface of the main body of the ozone treatment tank, and the bottom surface of the main body of the ozone treatment tank Is reached, the bottom of the main body bottom of the ozone treatment tank is reached, and the volume of sludge is reduced by repeating the circulation in the ozone treatment tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2009211589A JP5497387B2 (en) | 2009-09-14 | 2009-09-14 | Sludge volume reduction device and sludge volume reduction method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2009211589A JP5497387B2 (en) | 2009-09-14 | 2009-09-14 | Sludge volume reduction device and sludge volume reduction method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2011056461A true JP2011056461A (en) | 2011-03-24 |
| JP5497387B2 JP5497387B2 (en) | 2014-05-21 |
Family
ID=43944741
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2009211589A Expired - Fee Related JP5497387B2 (en) | 2009-09-14 | 2009-09-14 | Sludge volume reduction device and sludge volume reduction method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP5497387B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103265155A (en) * | 2013-05-17 | 2013-08-28 | 桂林理工大学 | Method for quickly proliferating and nitrifying sludge |
Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5823630U (en) * | 1981-08-07 | 1983-02-15 | バブコツク日立株式会社 | mixer |
| JPH02251295A (en) * | 1989-03-24 | 1990-10-09 | Fuji Electric Co Ltd | Apparatus for treating waste water with ozone |
| JPH05131195A (en) * | 1991-03-22 | 1993-05-28 | Senichi Masuda | Purification using ozone in water tank and its device |
| JPH07299477A (en) * | 1994-05-10 | 1995-11-14 | Fuji Electric Co Ltd | Descending dissolution type ozone reactor |
| JPH08252593A (en) * | 1995-03-20 | 1996-10-01 | Kurita Water Ind Ltd | Aerobic treatment of organic waste liquid |
| JPH09206780A (en) * | 1996-02-01 | 1997-08-12 | Kurita Water Ind Ltd | Aerobic biological treating device |
| WO1998003437A1 (en) * | 1996-07-19 | 1998-01-29 | Kurita Water Industries Ltd. | Method and apparatus for biological treatment of waste organic liquid |
| JP2001070958A (en) * | 1999-09-07 | 2001-03-21 | Hitachi Plant Eng & Constr Co Ltd | Partitioned type ozone/ultraviolet circulating oxidation treatment apparatus |
| JP2002336890A (en) * | 2001-05-18 | 2002-11-26 | Ebara Corp | Method and device for treating organic effluent |
| JP2003190976A (en) * | 2001-12-27 | 2003-07-08 | Toray Ind Inc | Apparatus and method for treating wastewater |
| JP2006055737A (en) * | 2004-08-19 | 2006-03-02 | Diamond Engineering Kk | Sludge treatment method and sludge treatment apparatus |
| JP2008012233A (en) * | 2006-06-30 | 2008-01-24 | Akio Tsubota | Ultrasonic ozone water sterilization and cleaning apparatus |
| JP2008036571A (en) * | 2006-08-09 | 2008-02-21 | Fuji Koki Kk | Volume reduction apparatus of waste sludge, and volume reduction methode of waste sludge |
| JP2008212890A (en) * | 2007-03-07 | 2008-09-18 | Fuji Koki Kk | Surplus sludge solubilization apparatus and ozone treatment tank for the surplus sludge solubilization apparatus |
| JP2009018223A (en) * | 2007-07-10 | 2009-01-29 | Japan Science & Technology Agency | Method for treating dredged bottom sludge |
-
2009
- 2009-09-14 JP JP2009211589A patent/JP5497387B2/en not_active Expired - Fee Related
Patent Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5823630U (en) * | 1981-08-07 | 1983-02-15 | バブコツク日立株式会社 | mixer |
| JPH02251295A (en) * | 1989-03-24 | 1990-10-09 | Fuji Electric Co Ltd | Apparatus for treating waste water with ozone |
| JPH05131195A (en) * | 1991-03-22 | 1993-05-28 | Senichi Masuda | Purification using ozone in water tank and its device |
| JPH07299477A (en) * | 1994-05-10 | 1995-11-14 | Fuji Electric Co Ltd | Descending dissolution type ozone reactor |
| JPH08252593A (en) * | 1995-03-20 | 1996-10-01 | Kurita Water Ind Ltd | Aerobic treatment of organic waste liquid |
| JPH09206780A (en) * | 1996-02-01 | 1997-08-12 | Kurita Water Ind Ltd | Aerobic biological treating device |
| WO1998003437A1 (en) * | 1996-07-19 | 1998-01-29 | Kurita Water Industries Ltd. | Method and apparatus for biological treatment of waste organic liquid |
| JP2001070958A (en) * | 1999-09-07 | 2001-03-21 | Hitachi Plant Eng & Constr Co Ltd | Partitioned type ozone/ultraviolet circulating oxidation treatment apparatus |
| JP2002336890A (en) * | 2001-05-18 | 2002-11-26 | Ebara Corp | Method and device for treating organic effluent |
| JP2003190976A (en) * | 2001-12-27 | 2003-07-08 | Toray Ind Inc | Apparatus and method for treating wastewater |
| JP2006055737A (en) * | 2004-08-19 | 2006-03-02 | Diamond Engineering Kk | Sludge treatment method and sludge treatment apparatus |
| JP2008012233A (en) * | 2006-06-30 | 2008-01-24 | Akio Tsubota | Ultrasonic ozone water sterilization and cleaning apparatus |
| JP2008036571A (en) * | 2006-08-09 | 2008-02-21 | Fuji Koki Kk | Volume reduction apparatus of waste sludge, and volume reduction methode of waste sludge |
| JP2008212890A (en) * | 2007-03-07 | 2008-09-18 | Fuji Koki Kk | Surplus sludge solubilization apparatus and ozone treatment tank for the surplus sludge solubilization apparatus |
| JP2009018223A (en) * | 2007-07-10 | 2009-01-29 | Japan Science & Technology Agency | Method for treating dredged bottom sludge |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103265155A (en) * | 2013-05-17 | 2013-08-28 | 桂林理工大学 | Method for quickly proliferating and nitrifying sludge |
Also Published As
| Publication number | Publication date |
|---|---|
| JP5497387B2 (en) | 2014-05-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP2008055291A (en) | Water treating device | |
| KR101437816B1 (en) | Method for Treating Wastewater, System for Treating Wastewater and BENZENE's Separating and Eliminating Apparatus used for the same | |
| KR101742557B1 (en) | Water treatment apparatus and method using ozone reaction | |
| JP2011072939A (en) | Membrane treatment equipment | |
| JP5497387B2 (en) | Sludge volume reduction device and sludge volume reduction method | |
| JP3731806B2 (en) | Organic wastewater treatment method and apparatus | |
| JP6656138B2 (en) | Water treatment system and water treatment method | |
| JP4861383B2 (en) | Organic sludge ozone treatment equipment | |
| JP4240655B2 (en) | Organic sludge ozone treatment equipment | |
| JP2014133206A (en) | Waste water treatment apparatus, and update/modification method thereof | |
| JP2012106211A (en) | Drainage pretreatment method utilizing foam separation, and drainage pretreatment device using the method | |
| JP2016049512A (en) | Anaerobic ammonia oxidation treatment method, anaerobic ammonia oxidation treatment apparatus, and denitrification method of organic waste water | |
| JP5269331B2 (en) | Waste water treatment equipment | |
| JP2008036571A (en) | Volume reduction apparatus of waste sludge, and volume reduction methode of waste sludge | |
| JP2012106214A (en) | Method for producing organic substance sludge and organic substance produced by the producing method | |
| JP2017104780A (en) | Conversion method and renewal method of biological treatment apparatus | |
| JP4011431B2 (en) | Ozone treatment method | |
| JP3087914B2 (en) | Aeration treatment equipment | |
| JP2007117867A (en) | Method and equipment for treating organic solid | |
| JP6447302B2 (en) | Water treatment system | |
| JP6924812B2 (en) | Water treatment equipment and water treatment method | |
| JP4425288B2 (en) | Surplus sludge solubilizer and ozone treatment tank for surplus sludge solubilizer | |
| JP4854706B2 (en) | Organic wastewater treatment method and treatment apparatus | |
| JP5600525B2 (en) | Upflow type reaction tank, water treatment method using the reaction tank, and water treatment apparatus provided with the reaction tank | |
| JP2018514375A (en) | Biological wastewater purification method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20120330 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20130408 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20130822 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20130902 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20131031 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20140224 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20140306 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 5497387 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| LAPS | Cancellation because of no payment of annual fees |