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JP3049164U - Merged glass fiber reinforced plastic septic tank - Google Patents

Merged glass fiber reinforced plastic septic tank

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Publication number
JP3049164U
JP3049164U JP1997009324U JP932497U JP3049164U JP 3049164 U JP3049164 U JP 3049164U JP 1997009324 U JP1997009324 U JP 1997009324U JP 932497 U JP932497 U JP 932497U JP 3049164 U JP3049164 U JP 3049164U
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Japan
Prior art keywords
tank
sewage
plate
sedimentation
separation tank
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JP1997009324U
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Japanese (ja)
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坤池 楊
政諺 楊
程傑 楊
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坤池 楊
政諺 楊
程傑 楊
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Abstract

(57)【要約】 【課題】 効率的に汚水を処理する合併式ガラス繊維強
化浄化槽を提供する。 【解決手段】 合併式ガラス繊維強化浄化槽は、汚水入
口11、排気孔12、多くの気孔をもつ分解層13、お
よび大粒の浮き滓を下に沈殿させる導流板14をもつ第
一沈殿分離槽1と、第一沈殿分離槽1で沈殿する大粒の
汚物を中に沈殿させて菌床形成させ、初歩の嫌気分解さ
せる第二沈殿分離槽2と、固体液体分離板31、および
食い違って相向かう回流板32をもつ回流分離槽3と、
空気放出管、生物濾過材、および逆洗浄管をもつ空気さ
らし槽と、空気さらし槽から来る汚水を上から下に流さ
せる中空柱、流動面積を増加するための溢れ止め、浮遊
固形物を集中させる止め板、および底に沈積する汚泥を
第二沈殿分離槽に送り返す空気上昇ポンプをもつ沈殿槽
と、薬桶から消毒剤または塩素を吸取って汚水を消毒す
る消毒槽と、内部の掃除保養に供する掃除孔とを備え
る。
(57) [Summary] [PROBLEMS] To provide a combined glass fiber reinforced septic tank for efficiently treating wastewater. SOLUTION: A combined glass fiber reinforced septic tank is a first sedimentation separation tank having a sewage inlet 11, an exhaust hole 12, a decomposition layer 13 having many pores, and a flow guide plate 14 for sedimenting large scum. 1, a large sediment sedimented in the first sedimentation separation tank 1 is sedimented therein to form a bacterial bed, and a second sedimentation separation tank 2 for anaerobic decomposition at an elementary stage, a solid-liquid separation plate 31, and a contradictory difference A circulation separation tank 3 having a circulation plate 32;
Aeration tank with air discharge pipe, biological filter material, and backwash pipe, hollow column for draining wastewater coming from the aeration tank from top to bottom, overflow to increase flow area, concentration of suspended solids A sedimentation tank with an air lift pump that sends back sludge deposited on the bottom to the second sedimentation separation tank, a disinfectant tank that sucks disinfectant or chlorine from the vat to disinfect sewage, and a cleaning and maintenance of the inside. And a cleaning hole to be provided to the user.

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【考案の属する技術分野】[Technical field to which the invention belongs]

本考案は、汚水を処理するのに使用される合併式浄化槽に関し、特に合併式ガ ラス繊維強化プラスチック浄化槽(以下、「ガラス繊維強化プラスチック」をF RP(Fiberglass reinforced plastic)という )に関するものである。 The present invention relates to a combined-type septic tank used for treating sewage, and particularly to a combined-type glass fiber-reinforced plastic septic tank (hereinafter, “glass fiber-reinforced plastic” is referred to as FRP (Fiberglass reinforced plastic)). .

【0002】[0002]

【従来の技術】[Prior art]

従来よく使用されている合併式汚水処理槽は、図1に示すように汚水を通過さ せるタンク9を含み、このタンク9は汚水入口90および汚水出口96を具備し 、汚水が汚水入口90から第一沈殿分離槽91の中に入ったとき、簡易浮き滓濾 過器911を通過して濾過されるが、これはただ浮き滓を濾過するだけにすぎず 、一歩進んだ分解作用をもたないので、濾過器911の小孔を容易に塞ぎ、濾過 器911の作用が失われ易い。甚だしくは全体の汚水処理系統が塞がれ、後日保 養修理上の困難を発生する。さらに、第一沈殿分離槽91に入っても、別に有効 な補助器材、例えば有機物を分解させて軟化させるとともに浮き滓の発生を抑制 する分解槽や、固体と液体と気体とを迅速に分離させる接触面積を増加し、滞留 時間を延長し、嫌気作用処理の効率を高め、メタン化作用による処理をさせて汚 水の中の比較的大粒の有機質を有効に分解させてから沈殿させ、第二沈殿分離槽 92の中に入らせるような有効な補助器材がなく、したがって汚水の経過する処 理工程が短く、そのため槽の中の比較的大粒の有機物は嫌気作用による有効な分 解ができず、沈殿分離槽の作用が果たされない。また、空気さらし槽93に入っ た汚水は、大量の空気を注入して汚水の中の粒を分解させなければならないので 動力を大きく使用し、エネルギーの浪費となる。さらに、排出された廃水の中の 生化学的酸素要求量(以下「生化学的酸素要求量」をBOD(Biochemi cal oxygen demand)という)および浮遊固形物(以下「浮遊 固形物」をSS(Suspended solid)という)の値が規定に符合 できず、汚泥の量が増加し、その処理は時間がかかる。次に、廃水は沈殿槽94 および消毒槽の中に入り、最後の沈殿および消毒の処理を受けた後、浄化された 汚水が汚水出口96から排出される。 Conventionally used combined sewage treatment tanks, as shown in FIG. 1, include a tank 9 for passing sewage, and this tank 9 has a sewage inlet 90 and a sewage outlet 96. When it enters the first sedimentation separation tank 91, it is filtered through a simple scum filter 911, but it only filters the scum and has an advanced decomposition action. Since there is no filter, the small hole of the filter 911 is easily closed, and the function of the filter 911 is easily lost. Severely, the entire sewage treatment system will be blocked, causing difficulty in maintenance and repair at a later date. Furthermore, even when entering the first sedimentation separation tank 91, other effective auxiliary equipment, for example, a decomposition tank for decomposing and softening organic substances and suppressing the generation of scum, and for rapidly separating solids, liquids and gases. The contact area is increased, the residence time is extended, the efficiency of the anaerobic treatment is increased, the treatment by methanation is performed, and the relatively large organic matter in the wastewater is effectively decomposed and then precipitated. There is no effective auxiliary equipment to allow the sedimentation separation tank 92 to enter, and therefore the treatment process in which sewage passes is short, so that relatively large organic matter in the tank cannot be effectively decomposed by anaerobic action. In addition, the function of the sedimentation separation tank is not performed. Further, the sewage that has entered the air release tank 93 requires a large amount of air to dissolve particles in the sewage, so that a large amount of power is used and energy is wasted. Furthermore, biochemical oxygen demand in the discharged wastewater (hereinafter “biochemical oxygen demand” is referred to as BOD (Biochemical oxygen demand)) and suspended solids (hereinafter “suspended solids” are referred to as SS (suspended). solid)) does not meet the requirements, the amount of sludge increases, and the processing takes time. Next, the wastewater enters the sedimentation tank 94 and the disinfection tank, and after having undergone the final sedimentation and disinfection treatment, the purified sewage is discharged from the sewage outlet 96.

【0003】[0003]

【考案が解決しようとする課題】[Problems to be solved by the invention]

しかしながら、上述の従来の合併式汚水処理槽は、浮き滓の除去分解設備がな いので、それを加設する必要があり、また回流板、および固体と液体との分離板 がないのでこれらを加設し、有効に嫌気作用を強化して比較的大きい有機物の粒 を分解させ、BODとSSの量を低下させて汚泥を減少させる必要がある。 However, the above-mentioned conventional combined sewage treatment tank does not have a facility for removing and decomposing floating slag, so it is necessary to add it.Moreover, since there is no circulating plate and a separating plate for solid and liquid, these must be added. In addition, it is necessary to effectively enhance the anaerobic action to break down relatively large organic matter particles, and to reduce the amount of BOD and SS to reduce sludge.

【0004】 したがって、本考案の主な目的は、効率的に汚水を処理する合併式FRP浄化 槽を提供することにある。Accordingly, a main object of the present invention is to provide a combined FRP purification tank that efficiently treats wastewater.

【0005】[0005]

【課題を解決するための手段】[Means for Solving the Problems]

上記の課題を解決するための本考案の請求項1記載の合併式FRP浄化槽によ れば、その内部に第一沈殿分離槽と、第二沈殿分離槽と、回流分離槽と、空気さ らし槽と、沈殿槽と、消毒槽と、掃除孔とを備える。 第一沈殿分離槽は汚水入口と、排気孔と、多くの気孔をもつ分解槽と、傾斜し た大粒の浮き滓を下方に沈殿させて菌床を形成させる導流板をもつ。 According to the merged FRP purifying tank according to claim 1 of the present invention for solving the above-mentioned problems, the first sedimentation separation tank, the second sedimentation separation tank, the circulating separation tank, and the air separator are provided therein. A tank, a sedimentation tank, a disinfection tank, and a cleaning hole are provided. The first sedimentation separation tank has a sewage inlet, an exhaust port, a decomposition tank having many pores, and a flow guide plate that allows large inclined sludge to settle down to form a bacterial bed.

【0006】 第二沈殿分離槽は開き口を設け、第一沈殿分離槽で沈殿した大粒の汚物をその 中に入らせ、菌床を形成させて初歩の嫌気分解作用を進行させる。 回流分離槽は数個の固体液体分離板をもち、また数個の相互に食違って向かい 合う回流板を設け、汚水がこの槽の中に入ったとき、先に固体液体分離板に衝突 させて大粒の有機物を底部に沈殿させた後、嫌気作用により比較的小さい粒に分 解させ、これらの小粒は水と一緒に流れて一枚の回流板を経過した後、また別の 固体液体分離板に衝突してさらに小さい粒になり、この回流分離槽の中でこのよ うな同じ動作を数回繰返して最後に最少粒になる。The second sedimentation / separation tank is provided with an opening to allow the large filth settled in the first sedimentation / separation tank to enter therein to form a bacterial bed and to promote an elementary anaerobic decomposition action. The diversion tank has several solid-liquid separation plates, and several mutually opposite diversion plates are installed.When sewage enters this tank, it strikes the solid-liquid separation plate first. After the large organic matter settles to the bottom by anaerobic action, it is broken down into relatively small particles, and these small particles flow together with the water, pass through one circulation plate, and then separate into solid liquids. The particles collide with the plate and become smaller, and the same operation is repeated several times in this circulating separation tank, and finally the particles become the smallest.

【0007】 空気さらし槽は空気放出管をもち、またその内部上方に生物濾過材を設置し、 微生物酸化分解をする接触面積を増加し、また逆洗浄管を設け、この濾過材を逆 に水を吹きかけて洗い、その上に積もった厚い生物膜を洗い落とす。 次に、沈殿槽はその中に中空柱をもち、空気さらし槽から来る汚水を強制的に この中空柱の周囲壁の上から下に沿って流下させ、またさらに水位よりも少し低 い所に数個の溢れ止めを設けるほか、下部に傾斜した数個の止め板を設置し、汚 水の中のSSを下方に沈殿させ、空気上昇ポンプで底部に沈殿した汚泥を再び第 二沈殿槽の中に送り返す。[0007] The air release tank has an air discharge tube, and a biological filtration material is installed above the inside thereof to increase the contact area for oxidative decomposition of microorganisms. Spray to wash off the thick biofilm on it. Next, the sedimentation tank has a hollow column in it, forcing the sewage coming from the aeration tank to flow down from the top to the bottom of the surrounding wall of this hollow column, and further to a place slightly lower than the water level. In addition to providing several overflow stoppers, several inclined stopper plates are installed at the bottom, SS in the sewage is settled downward, and the sludge settled at the bottom by the air rising pump is returned to the second settling tank again. Send back inside.

【0008】 消毒槽は、前段からくる処理された汚水を消毒剤あるいは塩素で消毒する。 掃除孔は汚水処理槽の上方に数個設置し、以後の槽の孔部掃除に用いる丸い孔 である。 第一沈殿分離槽の中の分解層は、汚水の中の浮き滓を分解軟化させるとともに 、その再発生を抑制する。第二沈殿分離槽は、汚物の沈殿で菌床を形成させて初 歩の嫌気分解をさせる。回流分離槽は、その中で大粒の汚物に固体液体分離板、 回流板の順序で何回も衝突、沈殿および分解の作用を繰返させ、最後に大変小さ い粒にさせる作用をする。空気さらし槽の中では汚水の中に空気を吹込み、微生 物を生物濾過材に付着させ、汚水中のBODを低下させるほか、洗浄管で生物濾 過材の表面に蓄積される生物膜を定期的に洗い落とす。沈殿槽はSSをできるだ け沈殿させ、その沈殿した汚泥を再び第二沈殿分離槽に送り返し、再び処理させ る。また、排出標準に達した汚水は次の消毒槽に送られる。消毒槽は、この排出 標準に達した汚水を消毒材あるいは塩素で消毒してから外に排出する。[0008] The disinfection tank disinfects the treated wastewater coming from the preceding stage with a disinfectant or chlorine. Several cleaning holes are installed above the sewage treatment tank, and are round holes used for cleaning the holes in the tank. The decomposition layer in the first sedimentation separation tank decomposes and softens the scum in the sewage and suppresses its re-generation. The second sedimentation / separation tank forms a fungal bed with the sedimentation of filth, and performs elementary anaerobic decomposition. The circulating separation tank has the effect of repeatedly impacting, sedimenting, and decomposing large filths in the order of the solid-liquid separation plate and the circulating plate, and finally to very small particles. In the aeration tank, air is blown into the wastewater, causing microbes to adhere to the biological filtration material, lowering the BOD in the wastewater, and the biofilm accumulated on the surface of the biological filtration material in the washing pipe. Wash off regularly. In the sedimentation tank, SS is settled as much as possible, and the settled sludge is sent back to the second sedimentation separation tank again to be treated again. Sewage that has reached the discharge standard is sent to the next disinfection tank. The disinfection tank disinfects sewage that has reached this discharge standard with a disinfectant or chlorine before discharging it to the outside.

【0009】[0009]

【考案の実施の形態】[Embodiment of the invention]

以下、本考案の実施例を図面に基づいて説明する。 本実施例の合併式FRP浄化槽は、図2に示すように、その前段に第一沈殿分 離槽と、第二沈殿槽と、回流分離槽とを含有し、その後段に空気さらし槽と、沈 殿槽と、消毒槽とを含有する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. As shown in FIG. 2, the combined FRP purification tank of the present embodiment includes a first settling tank, a second settling tank, and a circulating separation tank in the preceding stage, and an air exposure tank in the subsequent stage. It contains a settling tank and a disinfection tank.

【0010】 第一沈殿分離槽1は大体その側面上方に汚水を流入させる汚水入口11をもち 、また側面上方に気体を排出させる排気孔12と、酸性および苛性に耐える材質 で作り、多くの気孔がある分離層13とを含有し、汚水入口11はこの分解層1 3を通り抜け、汚水は分解層13の下に排出される。分解層13は水位の下方に 位置し、浮き滓が浮上がるのを防止するとともに浮き滓を軟水化させてその増加 を抑制し、またさらに傾斜した大粒の有機物を下に沈殿させて菌床を形成させる 導流板14を含有する。The first sedimentation / separation tank 1 generally has a sewage inlet 11 for inflowing sewage above the side, an exhaust hole 12 for discharging gas above the side, and a material made of a material resistant to acid and caustic. The wastewater inlet 11 passes through the decomposition layer 13, and the wastewater is discharged under the decomposition layer 13. The decomposed layer 13 is located below the water level to prevent the floating of the scum and to soften the scum to suppress the increase, and to further precipitate the slanted large organic substances downward to form a fungal bed. A flow guide plate 14 to be formed is contained.

【0011】 第二沈殿分離槽2は、第一沈殿分離槽1との間に孔22をもつ止め板21が設 置され、第一沈殿分離槽1の導流板14に導引されて沈殿した大粒の汚物は、そ の止め板21の孔22から第二沈殿分離槽2の中に入って沈殿し、菌床を形成し て初歩の嫌気分解をなし、初歩分解した廃水は案内管23を経由して次の処理単 位に進入し、さらに進んだ処理を受ける。The second sedimentation / separation tank 2 is provided with a stopper plate 21 having a hole 22 between the second sedimentation / separation tank 1, and is guided by the flow guide plate 14 of the first sedimentation / separation tank 1 to settle the sedimentation. The large-sized waste particles enter the second sedimentation / separation tank 2 through the holes 22 of the stopper plate 21 and settle, forming a fungus bed to perform anaerobic decomposition at the elementary stage. Enters the next processing unit via, and receives further processing.

【0012】 次の回流分離槽3は、適当な長さをもつ二片を縫合わせた導板を連結した水位 よりやや高い敷板の固体液体分離板31と、相互に食違って相向かった敷板の回 流板32とを含有し、図4に示すように、前記案内管23から来る汚水がこの回 流分離槽3に入って来たとき、先に前記固体液体分離板31に衝突し、この固体 液体分離板31は補捉分解の作用をもつので、大粒の有機物が固体液体分離板3 1に突当たったとき、速度が減少して底部に沈下し、この固体液体分離板31の 阻止により汚水の流速が減少し、底部に大粒の汚物が菌床を形成する。これらの 大粒の汚物は、嫌気作用により分解してもっと小さくなるとともに、メタンの泡 を発生し、比重が小さい粒となり、さらに水流に流されて回流板32を経由し、 また別の固体液体分離板31に衝突し、同じことを繰返す。このような沈殿→分 解→気泡を帯びた小粒の生成という再三の循環により、最小粒の有機物は水流と ともに流動し、案内管33を経由して次の処理単位に入る。この回流分離槽3は 、回流作用をもつとともに有効容積を増加し、その中での滞留時間と接触面積を 増加するほか、固体および液体の分離作用を高める。The next circulation separation tank 3 is composed of a solid liquid separation plate 31 slightly higher than the water level, which is obtained by connecting conductive plates obtained by sewing two pieces each having an appropriate length, and a floor plate which is staggered to face each other. As shown in FIG. 4, when the sewage coming from the guide tube 23 enters the flow separation tank 3, it collides with the solid / liquid separation plate 31 first, as shown in FIG. Since the solid-liquid separation plate 31 has the function of trapping and decomposing, when a large organic substance hits the solid-liquid separation plate 31, the speed decreases and sinks to the bottom, and the solid-liquid separation plate 31 is blocked. As a result, the flow rate of the sewage decreases, and large-sized filth forms a bed on the bottom. These large filths are decomposed by anaerobic action and become smaller, and at the same time, methane bubbles are generated, and the specific gravity becomes small. It collides with the plate 31 and repeats the same. Due to such repeated circulation of sedimentation → decomposition → generation of small particles with bubbles, the smallest organic matter flows together with the water flow and enters the next processing unit via the guide pipe 33. This circulating separation tank 3 has a circulating action and increases the effective volume, increases the residence time and contact area therein, and enhances the action of separating solids and liquids.

【0013】 図3に示すように、次の空気さらし槽4は、多くの空気孔をもち、気体を水中 に散布する空気放出管41を設け、微生物の酸化分解の接触面積を増加し、汚水 中のBODの値を低下させて排出標準に達成させるため、内部上方に生物濾過材 42を加設し、さらにこの生物濾過材42の上に長期使用により蓄積する厚い生 物膜を洗い落とすため、逆洗浄管43を設けて定期的に生物濾過材42を逆に洗 浄し、落ちた生物膜は案内管45から次の処理単位に送って処理させてこの生物 濾過材42の寿命を維持する。As shown in FIG. 3, the next air exposing tank 4 has many air holes, is provided with an air discharge pipe 41 for dispersing gas into water, increases the contact area for oxidative decomposition of microorganisms, and increases wastewater. In order to reduce the value of BOD in the medium and achieve the emission standard, a biological filter medium 42 is added above the inside, and in order to wash out the thick biofilm accumulated on the biological filter medium 42 due to long-term use, A backwashing pipe 43 is provided to periodically wash the biological filter medium 42 in reverse, and the dropped biofilm is sent from the guide pipe 45 to the next processing unit for processing to maintain the life of the biological filter medium 42. .

【0014】 さらに、次の沈殿槽5では、前記空気さらし槽4の中で処理された汚水の中に 未だ腐化しない汚物かあるいはSSがあるので、それらが案内管45を経由して 沈殿槽5の中に送られ、処理される。この沈殿槽5は中空柱51をもち、案内管 45と連接し、前記空気さらし槽4から来る汚水は、この中空柱51の周囲壁に 沿って上から下に流下し、不安定な流速によりSSの沈積が妨げられないように し、同時に水位よりやや低い場所に数個の溢れ止め52を設け、流体が経由する 表面積を増大して水流を安定させ、SSを自己の重力で沈下させ、さらに内部下 方に数個の傾斜した沈下止め板53を設置し、汚水中のSSをこの沈下止め板5 3に撞撃させてから下の方に集中させ、空気上昇ポンプ54でもって底部に沈積 した汚泥を第二沈殿分離槽2の中に送り返し、再び循環分解を進行させる。この ような工程を経過させて汚水中のSSを排出標準以下にさせてから、沈殿槽5の 上方に来る排出標準の汚水は、案内管55から次の処理単位の消毒槽6の中に送 られる。Further, in the next sedimentation tank 5, since there is filth not yet spoiled or SS in the sewage treated in the aeration tank 4, they are passed through the guide pipe 45 and settled in the sedimentation tank 5. Sent to and processed. The sedimentation tank 5 has a hollow column 51 and is connected to the guide pipe 45, and the sewage coming from the air exposing tank 4 flows down from the top along the peripheral wall of the hollow column 51 and has an unstable flow rate. To prevent the deposition of SS from being hindered, and at the same time, provide several overflow stops 52 slightly lower than the water level, increase the surface area through which the fluid passes, stabilize the water flow, and set the SS to sink by its own gravity. Further, several inclined settling stoppers 53 are installed in the lower part of the interior, and the SS in the sewage is caused to collide with the settling stoppers 53 and then concentrated downward. The deposited sludge is sent back into the second sedimentation separation tank 2, and the circulating decomposition proceeds again. After passing through such a process to reduce the SS in the wastewater to the discharge standard or less, the wastewater of the discharge standard coming above the sedimentation tank 5 is sent from the guide pipe 55 into the disinfection tank 6 of the next processing unit. Can be

【0015】 消毒槽6は前記沈殿槽5で処理された汚水を案内管55から受け入れ、薬桶6 1から消毒剤あるいは塩素を吸出し、汚水の中に混合させて消毒を施行し、消毒 された汚水は汚水出口62から排出される。以上でこの合併式FRP浄化槽の汚 水処理は完了する。 なお、この合併式FRP浄化槽の上方に数個の丸い掃除孔を設置し、槽内の掃 除を行うときに使用する。The disinfecting tank 6 receives the sewage treated in the sedimentation tank 5 from the guide pipe 55, sucks out a disinfectant or chlorine from the chemical trough 61, mixes it into the sewage, performs disinfection, and is disinfected. The sewage is discharged from a sewage outlet 62. This completes the wastewater treatment of this combined FRP septic tank. In addition, several round cleaning holes are installed above this combined FRP septic tank and used when cleaning the inside of the tank.

【0016】 本考案の分解層により、嫌気分解作用を高めて粒状の汚物を有効に微粒化させ るほか、固体液体分離板により汚水中の粒状汚物が衝突する動作が何回も繰返さ れるので、その粒が次第に小さくなるほか、沈殿と嫌気分解の反復により汚水中 のBODおよびSSが徹底的に低下できる効果がある。[0016] The decomposition layer of the present invention enhances the anaerobic decomposition action to effectively atomize the granular waste, and the operation of colliding the granular waste in the wastewater by the solid-liquid separation plate is repeated many times. In addition to gradually reducing the size of the grains, BOD and SS in wastewater can be thoroughly reduced by repeated precipitation and anaerobic decomposition.

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

【図1】従来の合併式汚水処理槽の斜視図である。FIG. 1 is a perspective view of a conventional merged sewage treatment tank.

【図2】本考案の実施例による合併式FRP浄化槽の前
段部の斜視図である。
FIG. 2 is a perspective view of a front part of the combined FRP septic tank according to the embodiment of the present invention.

【図3】本考案の実施例による合併式FRP浄化槽の後
段部の斜視図である。
FIG. 3 is a perspective view of a rear part of the combined FRP septic tank according to the embodiment of the present invention.

【図4】本考案の実施例による合併式FRP浄化槽の回
流分離槽の断面図である。
FIG. 4 is a cross-sectional view of the circulation separation tank of the combined FRP purification tank according to the embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 第一沈殿分離槽 2 第二沈殿分離槽 3 回流分離槽 4 空気さらし槽 5 沈殿槽 6 消毒槽 11 汚水入口 12 排気孔 13 分解層 14 導流板 21 止め板 22 孔 23、33、45、55 案内管 31 固体液体分離板 32 回流板 41 空気放出管 42 生物濾過材 43 逆洗浄管 51 中空柱 52 溢れ止め 53 沈下止め板 54 空気上昇ポンプ 61 薬桶 62 汚水出口 DESCRIPTION OF SYMBOLS 1 First sedimentation separation tank 2 Second sedimentation separation tank 3 Round flow separation tank 4 Air exposure tank 5 Sedimentation tank 6 Disinfection tank 11 Sewage water inlet 12 Exhaust hole 13 Decomposition layer 14 Flow guide plate 21 Stop plate 22 Hole 23, 33, 45, 55 Guide tube 31 Solid liquid separation plate 32 Flow plate 41 Air release tube 42 Biological filtration material 43 Backwash tube 51 Hollow column 52 Overflow stop 53 Settlement stop plate 54 Air rising pump 61 Chemical trough 62 Sewage outlet

───────────────────────────────────────────────────── フロントページの続き (72)考案者 楊 政諺 台湾屏東県東港鎮船頭路4之27号 (72)考案者 楊 程傑 台湾屏東県東港鎮船頭路4之27号 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Yang Masa proverb No. 27, Donggang Township, Pingtung County, Taiwan No. 27 (72) Inventor Yang Chengjie No. 27, Donggang Township, Pingtung County, Taiwan

Claims (1)

【実用新案登録請求の範囲】[Utility model registration claims] 【請求項1】 上方に形成する汚水入口、上方に形成す
る排気孔、耐酸性および耐苛性の材質で作られ、複数の
気孔を有し、水位の下方に位置する分解層、および大粒
の有機物を下向きに沈殿させて菌床を形成する傾斜した
導流板を有し、前記汚水入口は前記分解層を貫通してそ
の下方に汚水を排出し、浮き滓は前記分解層に補捉さ
れ、水に軟化分解される第一沈殿分離槽と、 前記第一沈殿分離槽で沈殿した粒状汚物が、第一沈殿分
離槽の次に設置される止め板の孔から入り、内部で沈殿
して初歩の嫌気分解をする菌床を形成し、初歩的分解を
した汚水は案内管から次の処理単位に流入する第二沈殿
分離槽と、 内部に、二個の適当な長さをもつ縫合された導板で接連
される敷板の固体液体分離板、および相互に食違って相
向かう敷板の回流板を含有し、前記固体液体分離板は所
定の水位より高く、前記案内管から汚水が入ってきたと
き、先に前記固体液体分離板に衝突し、大粒の汚物は減
速して底部に阻止され、流速は減少して菌床を形成し、
粒状汚物は再び嫌気作用を発生して分解し、その粒はさ
らに小さくかつ気泡を帯びて比重がより小さくなり、こ
れらの粒はまた水流に携帯され、前記回流板を通過し、
また別の固体液体分離板と衝突し、上述と同じ作用を繰
返し、最後に最少粒となって水流と一緒に流動する回流
分離槽と、 複数の気孔を有し、平均的に気体を水中に放出する空気
放出管、上方に設けられ、微生物酸化分解をする接触面
積を増加させる生物濾過材、この生物濾過材の上に蓄積
する厚い生物膜を洗浄してはぎ落とすため、定期的に逆
の洗浄を行って前記生物濾過材の寿命を維持再生させる
逆洗浄管、および次の処理単位に汚水を送る案内管を含
有する空気さらし槽と、 前記案内管と連結され、前記空気さらし槽から流入する
汚水を周囲壁の上方から下方に沿って流させる中空柱、
水位からやや低い位置に水流面積を増加させ、水流を安
定させて浮遊固形物を分離させ、自身の重力で沈下させ
るようにする複数の傾斜した止め板、底に沈積した汚泥
を前記第二沈殿分離槽に再び送り返す空気上昇ポンプ、
およびすでに排出標準に合う汚水を次の処理単位に送る
案内管とを有する沈殿槽と、 前記沈殿槽から来る排出標準に合う汚水を前記案内管か
ら受け入れ、薬桶から消毒剤や塩素を吸取り、汚水の中
に混合させて消毒し、その汚水を外に排出する汚水出口
を有する消毒槽と、 上方に設置して内部の掃除保養工作ができる複数の掃除
孔とを備えることを特徴とする合併式ガラス繊維強化プ
ラスチック浄化槽。
1. An upwardly formed sewage inlet, an upwardly formed exhaust hole, a decomposition layer made of an acid and rust resistant material, having a plurality of pores, located below a water level, and a large organic substance. Having an inclined flow guide plate that precipitates downward to form a bacterial bed, the sewage inlet penetrates the decomposition layer and discharges sewage below the decomposition layer, and the scum is trapped by the decomposition layer, The first sedimentation separation tank that is softened and decomposed into water, and the particulate waste deposited in the first sedimentation separation tank enters through the hole of the stop plate that is installed next to the first sedimentation separation tank, and precipitates inside, and the first step The sewage, which forms a fungal bed that decomposes anaerobically, and the rudimentary decomposed sewage flows into the next treatment unit from the guide tube, and is internally sewn with two appropriate lengths Solid liquid separation plate of floor plate connected with conductive plate, and circulating plate of floor plate facing each other staggeredly Containing, the solid liquid separation plate is higher than a predetermined water level, and when sewage enters from the guide pipe, it first collides with the solid liquid separation plate, and large filth is decelerated and stopped at the bottom, Decreases to form a bacterial bed,
The granular waste again degrades by generating anaerobic action, the grains become smaller and more air-bubble and have a lower specific gravity, these grains are also carried in the water stream and pass through the circulating plate,
In addition, it collides with another solid liquid separation plate, repeats the same operation as above, and finally has a circulating separation tank that becomes the smallest particle and flows together with the water flow, and has a plurality of pores, and on average gas is put into water An air discharge pipe that discharges, a biofilter that is installed above and increases the contact area for microbial oxidative degradation, and is periodically turned upside down to wash and remove thick biofilm that accumulates on the biofilter. A backwash tube for washing and maintaining and regenerating the life of the biological filtration material, and an air-exposed tank containing a guide tube for sending sewage to the next processing unit; and an inflow tank connected to the guide tube and flowing from the air-exposed tank. A hollow column that allows sewage water to flow downward from above the surrounding wall,
Increasing the water flow area to a position slightly lower than the water level, stabilizing the water flow and separating suspended solids, a plurality of inclined stopper plates to settle by its own gravity, the sludge deposited at the bottom of the second settling An air lift pump that is sent back to the separation tank,
And a sedimentation tank having a guide pipe for sending sewage that already meets the discharge standard to the next processing unit, receiving the sewage that meets the discharge standard coming from the sedimentation tank from the guide pipe, sucking up a disinfectant and chlorine from a chemical vat, A merger comprising a disinfection tank having a sewage outlet that mixes and disinfects sewage and discharges the sewage to the outside, and a plurality of cleaning holes that are installed above and that can be used for internal cleaning work. Glass fiber reinforced plastic septic tank.
JP1997009324U 1997-10-21 1997-10-21 Merged glass fiber reinforced plastic septic tank Expired - Lifetime JP3049164U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1997009324U JP3049164U (en) 1997-10-21 1997-10-21 Merged glass fiber reinforced plastic septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1997009324U JP3049164U (en) 1997-10-21 1997-10-21 Merged glass fiber reinforced plastic septic tank

Publications (1)

Publication Number Publication Date
JP3049164U true JP3049164U (en) 1998-06-02

Family

ID=43183417

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1997009324U Expired - Lifetime JP3049164U (en) 1997-10-21 1997-10-21 Merged glass fiber reinforced plastic septic tank

Country Status (1)

Country Link
JP (1) JP3049164U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116768352A (en) * 2023-05-20 2023-09-19 天津大学建筑设计规划研究总院有限公司 Rural sewage treatment plant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116768352A (en) * 2023-05-20 2023-09-19 天津大学建筑设计规划研究总院有限公司 Rural sewage treatment plant

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