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JP4157700B2 - Oil / water separator - Google Patents

Oil / water separator Download PDF

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Publication number
JP4157700B2
JP4157700B2 JP2001388842A JP2001388842A JP4157700B2 JP 4157700 B2 JP4157700 B2 JP 4157700B2 JP 2001388842 A JP2001388842 A JP 2001388842A JP 2001388842 A JP2001388842 A JP 2001388842A JP 4157700 B2 JP4157700 B2 JP 4157700B2
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Japan
Prior art keywords
tank
oil
water separation
fat
waste liquid
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JP2001388842A
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JP2003181204A (en
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秀雄 佐藤
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株式会社 大都技研
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Description

【0001】
【発明の属する技術分野】
本発明は、飲食店、ラーメン店等の厨房から排出される固形食品残滓と油脂を多量に含む廃液から油脂を分離回収する油水分離油脂回収装置において、流入廃液から固形食品残滓を分離する器具が備えられた組込型洗浄槽と油脂回収タンクを該装置上部に着脱自在に収納され、該装置下部は油水分離槽が形成され、該油水分離槽内には分離浮上した油脂を該油脂回収タンクへ汲上げるベルト式オイルスキマーが備えられている。下部構造として油水分離槽が、上部構造として組込型洗浄槽と油脂回収装置及び油脂回収タンクが一体化構成されている油水分離油脂回収装置に関する。
【0002】
【従来の技術】
飲食店、ラーメン店等の厨房から排出される食品残滓類は、固形食品残滓と多量の油脂を含む廃液から成る。この廃液から油脂を分離回収する装置類として、本発明者が提示した技術が有る。この装置は、油水分離油脂回収装置に組込型の洗浄槽が収納一体化され、上下位置関係にある組込型洗浄槽と油水分離槽の間に空隙が形成されず、油水分離槽の占有容積が最大限有効利用される形式で有る。
【0003】
厨房に設置された前記油水分離回収装置の組込型洗浄槽に設置されたストレーナにより廃液から大まかな固形食品残滓が捕捉除去された一次廃液は、前記洗浄槽からダクトを経由して前記油水分離槽へ流入し、前記油水分離槽に設置された補助分離器と比重差により油脂は一次廃液より分離され前記油水分離槽液面に浮上する、その後、前記油水分離槽内に設置された1台のベルト式オイルスキマーにより、油脂は汲上げられ回収タンクへ貯留される。
【0004】
【発明が解決しようとしている課題】
しかし、内蔵油水分離槽内に補助分離器を設け、一次廃液から比重差による油脂の分離浮上を促進させているが、一次廃液が過大量に流入すると筐体構造を採る油水分離槽の1区画では、油脂を分離浮上させる時間が不足し、油脂分離浮上が不十分な処理の状態で、一次廃液が該油水分離油脂回収装置から流出することがある。例え流出したとしても終末処理装置のグリース阻集器により油脂は一次廃液から分離回収されので、公共下水道、環境を悪化させることはないが、一次廃液から油脂を比重差により充分に分離浮上させる時間の確保、及び油脂回収能力を向上させ、廃水(油脂回収後の廃液)を該装置外に排水させる必要がある。
【0005】
また、漏斗状の油水分離槽々底下部に排出口が設けられている為、前記排出口と厨房床面との間隙が狭隘となる。その結果として前記排出口には大口径のバルブが取付けられず、油水分離槽に残留した微細固形食品残滓(味噌滓、香辛料等)を排出する際、排出口バルブが前記残滓により容易に閉塞される現象が発生する。その閉塞状態を解消する為、作業者は上部構成体の洗浄槽を取外し、手作業と流水で除去回収する効率的でない労力が要求された。
【0006】
【課題を解決する為の手段】
前記課題を解決するため、本発明に係わる油水分離油脂回収装置は、一次廃液から油脂を比重差により充分に分離浮上させる手段として、限られた容積内で流路の延長を図る目的で、該装置内蔵の油水分離槽は、上部開口面積と容量が小の第1槽とそれが共に大の第2槽に区画される。そして、前記第1槽と第2槽を区画する立隔壁の下部は、第2槽立壁の油水分離槽々底交接部近傍に設けられた微細固形食品残滓排出口に向って勾配を持つ多面体構造隔壁傾斜面が形成される。前記多面体構造隔壁傾斜面と前記排出口へ向って勾配を持つ前記槽底との交接部の一部分は第1槽と第2槽が通水する開口部が設けられ、下部隔壁の多面体構造隔壁傾斜面は、第1槽内を第1槽から第2槽へ向う流動一次廃液から、大部分の油脂が第1槽液面に集中して分離浮上させる機能を担い、更に、該排出口は、該第2槽下部立壁の槽底交接部に設置したことにより大口径バルブが取付けられることが可能となった。これにより、該装置の清掃、点検時に該第2槽底部に沈殿した微細固形食品残滓により該排出口は閉塞されず、微細固形食品残滓は速やかに排出される機能を併せ持つ手段を講じた。
【0007】
更に、本発明に係わる油水分離油脂回収装置は、内蔵油水分離槽が通水口で繋がる第1槽と第2槽に区画され、前記第2槽上面に廃液から固形食品残滓を分離するストレーナを持ち、そして一次廃液が前記第1槽に注水される流路を有する組込型洗浄槽と、主ベルト式オイルスキマーにより汲上げられる油脂を貯留する回収タンクが着脱自在に組込まれ、該第1槽には比重差により浮上分離される大部分の油脂を汲上げる常時稼動の主ベルト式オイルスキマーが設けられる。そして該第2槽には補助分離器と比重差により分離浮上された残余の油脂を汲上げ、該第1槽に戻す稼動サイクルが任意に調整可能な副ベルト式オイルスキマーが設けられている。
【0008】
その該第2槽に設けられた、稼動サイクルが任意に調整可能な、副ベルト式オイルスキマーにより汲上げられ該第1槽へ環流された油脂は、該第1槽液面浮上油脂層の容量嵩高を増大させ、それにより主ベルト式オイルスキマーの油脂吸着効果は高効率となり、究極的には廃液からの油脂回収効率が向上される。
【0009】
【発明の実施の形態】
以下、本発明の実施形態について図面を参照しながら詳細に説明する。
【0010】
図1は本発明の油水分離油脂回収装置1の外観図である。図2は組込型天板2、洗浄槽3及びストレーナ4の上部構成部品を取外した内部構造俯瞰図である。図3は図2の断面A−A図である。図4は図2の断面B−B図である。図5は、補助分離器の正面図である。
【0011】
廃液処理前準備として加熱ヒーター6により、油水分離槽8に貯留されている全一次廃液が、50〜60℃に予熱される。
【0012】
図1、図3及び図4において一次廃液は、上部構造のストレーナ4、洗浄槽3を経由して矢印(1)に示す様に、廃液受入れ皿11、廃液導通口23を経由し油水分離槽8内の第1槽9に流入する。
【0013】
図2に於て、第1槽9の上部は立隔壁で区画され上部に開口した筐体状に形成される、そして、第1槽9立隔壁下部は、多面体構造隔壁傾斜面14として第2槽側に張出した状態で形成されている。第1槽9の上部開口部面積と容積は、第2槽10のそれと比較すると共に小さい。
【0014】
油水分離槽8の槽底20は、図3、4に図示するように水平面と為す角度α、βの勾配を持ち、同じく多面体構造隔壁傾斜面14との交接部と形成する傾斜角γ、δを持つ勾配が形成される。
【0015】
第1槽9の上部開口部面積が第2槽10のそれに比較して小さく、第1槽9の下部多面体隔壁構造部容積が第1槽9の上部開口部容積より大きく形成される理由を説明する。
【0016】
その第一は、流入した一次廃液から分離浮上した油脂は、体積が一定である場合、開口部面積の大きな油水分離槽液面には油脂層嵩高が薄く拡散し、ベルト式オイルスキマーは油脂よりも廃液主成分の水分を多く汲上げることになる。この現象を避ける為、小さな開口面積を持つ第1槽液面に浮上させ、形成される油脂層嵩高を増すことにある。この結果、ベルト式オイルスキマー5が油脂を汲上げる効率を向上させる効果を得る。
【0017】
その第二は、或る量の冷温一次廃液が第1槽9の被予熱貯留一次廃液に注入されると、冷温一次廃液は被予熱貯留一次廃液より液温が低く、密度が大きい為、第1槽内を沈降する。沈降する低温一次廃液は第1槽9の多面体構造隔壁傾斜面14の内部で拡散し、第1槽9を取巻く大容量の第2槽被予熱貯留一次廃液から、多面体構造隔壁傾斜面を介して伝播する蓄熱を吸熱する。
熱移動を行う場合、低温側と高温側が接触する面積が大きい程、その速度は速い。その効果を得る為、区画隔壁下部は表面積増とする為、多面体傾斜面構造とし、最善の傾斜角γ、δが与えられる。
【0018】
その第三は、低温一次廃液が周囲の被予熱貯留一次廃液から吸熱し、熱移動が平衡状態になると、含有される油脂粒滴群は、比熱が水より小さい為、水より速く昇温し、体積が膨張する。その結果、油脂粒滴群は密度が低下し、分離浮上が促進される。その分離浮上する油脂粒滴群は、多面体構造隔壁傾斜面14に衝突し、表面張力により合体し粒滴が大きく成長し、浮力を増す。多面体構造隔壁傾斜面14はこの油滴の成長を促進させ、浮上させる効果がある。
【0019】
油水分離槽8を区画する隔壁材質は、オーステナイト系ステンレス鋼で形成されると、加工性、耐食性、熱伝導性の面で良好な結果を得る。多面体構造隔壁傾斜面14を構成する各面の境界部は、凹凸が無く、且つ、各面の表面が鏡面仕上げであるとより効果が増す。
【0020】
流入冷温一次廃液から、含有油脂が分離浮上する過程を説明する。
【0021】
矢印(1)に示す流れで或容量の一次廃液が、油水分離槽第1槽9に流入する。50〜60℃に予熱されている貯留一次廃液に冷温一次廃液が流入すると、冷温流入一次廃液は、被予熱貯留一次廃液の密度より大きく、流入一次廃液は、油水分離槽第1槽9内を沈降する。
【0022】
冷温一次廃液は、油水分離槽第1槽9内の多面体構造隔壁傾斜面域を沈降する過程で、被予熱全油水分離槽貯留一次廃液から吸熱し、熱移動が行われる。これを促進する為に、第1槽9の周囲を第2槽10が取囲み、第2槽10との接触面積が大となるように多面体構造隔壁傾斜面域14が設けられた。
【0023】
この影響により、第1槽9の多面体構造隔壁傾斜面域に沈降した冷温一次廃液は、前記隔壁傾斜面を介して被予熱貯留一次廃液から吸熱する。熱移動が平衡状態になると、含有する油脂粒滴群は、油脂の比熱は水より小さいことから、粒滴は水より先に吸熱しその体積が膨張し、密度が低下する。その結果として、一次廃液から分離浮上が促進される。
【0024】
通水口15に向う一次廃液の流れ矢印(2)から、吸熱により体積膨張し密度が低下した油脂粒滴群は比重差により浮上し、勾配を持つ鏡面状態の表面に仕上げられている多面体構造隔壁傾斜面14に衝突する。衝突した油脂粒滴群は表面張力により合体して大きな油滴に成長し、その浮力が増す。多面体構造隔壁傾斜部表面は鏡面状態である為、大きく成長した油滴は多面体構造隔壁傾斜部表面に付着することなく、前記隔壁表面に沿いながら、第1槽9の液面に向って浮上する。この過程が連続して行われ、粒滴が一次廃液より分離浮上する。
【0025】
このように多面体構造隔壁傾斜面14は、冷温一次廃液の滞留時間の延長と、冷温の流入一次廃液と被予熱貯留一次廃液の間で熱移動を速やかに行う必要から、立壁で区画されるより大きな表面積を得る傾斜面を持つ多面体隔壁構造を採用し、第2槽10から熱移動が迅速に行えるように為した、更に、一次廃液が含有する油脂粒滴群が比熱の関係で水より先に吸熱し、その体積が膨張することにより密度が低下し分離浮上するに伴い、浮上する油脂粒滴群の合体、油滴成長を促進する効果が得られる。この過程で、一次廃液から大部分の含有油脂を第1槽9の液面に分離浮上させる。
【0026】
以上が多面体構造隔壁傾斜面14によって得られる効果である。
【0027】
一次廃液から大部分の含有油脂分を第1槽9の液面に分離浮上させた二次廃液は、通水口15を経由し容積の大きい油水分離槽第2槽10に流入するが、通水口15の幅より幅方向に大きく広がる穏やかな流れになり、含有される残余の油脂粒滴群は比重差により第2槽10液面に浮上し、液面で合体成長し油脂層を形成する。
【0028】
油水分離槽第2槽10に気泡を発生させる手段、例えば、電気分解装置、或は、微小気泡を発生させるマイクロエアーノズル等を設置し、微細気泡を発生させ、貯留二次廃液に含まれる油脂粒滴に発生した前記微細気泡に付着させ液面に浮上させると、副ベルト式オイルスキマー13の油脂汲上げ効率が上昇する効果が得られる。
【0029】
第2槽10液面に浮上した油脂層は、第2槽10に設置された稼動サイクルが任意に調整可能な副ベルト式オイルスキマー13により、流動性を保つ為、二次廃液と共に戻り油脂受皿12へ汲上げられる。その戻り油脂受皿12は廃液受入れ皿11に連絡する、その汲上げられた油脂は油水分離槽第1槽9に、新たに流入する冷温一次廃液と共に注入される。
【0030】
第2槽10から汲上げられた油脂は、油滴が大きく成長しているので、冷温一次廃液と共に第1槽9に注入されても、前述した冷温一次廃液の流動に関係なく既存浮上油脂層に吸収され、その既存油脂層の嵩高を増やす。その結果、主ベルト式オイルスキマー5は油脂を汲上げる効率が上昇すると共に、油脂は回収タンク7に貯留される。回収された油脂は、肥料、飼料等を製造する二次資源として有効利用するに充分な純度を所有する。
【0031】
油水分離槽第2槽10に設けられている油水分離を促進する補助分離器16の流入口17が第2槽10の液面方向に上向きに設けられている効果で、補助分離器流入口17から二次廃液が流入しても、含有される油脂粒滴は、二次廃液の流れに逆らって第2槽10の液面に向って浮上する作用が妨げられることがない。
【0032】
油水分離槽第2槽10に設けられている補助分離器16の作用を説明する。
【0033】
前記補助分離器16の機能を図5を用いて説明する。図5に於て、16は補助分離器、この補助分離器16は排水管21に接続されると共に、旋回流と比重差で油水分離支援を行うトラップ17a、17b、19a、19bが設けられている。又、この補助分離器16は三重管構成の本管19と二重管構成の流入口17とで構成される。本管19と流入口17の下端との間を導管25で接続している。18は導管25の途中に設けられた枝管である。枝管18は、導管25を通水する二次廃液から分離浮上する油脂粒滴群を、枝管18の液面に逃す為に設けられる。
【0034】
二次廃液は、流入口17のトラップ17aから補助分離器16に流入する。矢印(8)の如く旋回しながら流入する。この過程においても残余の油脂粒滴群は液面に向け分離浮上する。その後矢印(9)に示すように導管25を経由しトラップ19aから補助分離器本管19に流入する。導管25を通過する間でも残余の油脂粒滴群は分離浮上し続け、油脂含有率は低下し続け、三次廃液となる。
【0035】
補助分離器本管19に流入した三次廃液は、矢印(10)に示すように旋回しながらトラップ19bを経由して、補助分離器本管19の枝管26の液位上限となる上端から矢印(11)に示すように溢水し、排水口21から終末処理装置のグリース阻集器へ排水される。
【0036】
補助分離器16に複数か所設けられる枝管には、二次廃液から微量の油脂が浮上し貯留されるが、定期的な点検・清掃時に貯留が確認できる程度の微量で、臭気等の害が発生しないことを開発段階の実験で確認している。
【0037】
図3、4に示すように油水分離槽8の槽底は、水平面と為す角度α、βの勾配を持ち、その勾配は、微細固形食品残滓排出口22に集中するように設けられている。
【0038】
微細固形食品残滓排出口22には、大口径のバルブが取付けられ、本装置の清掃、点検時に油水分離槽8に沈積した微細固形食品残滓を槽外に排出する際に、バルブの閉塞を招かない。また、油水分離槽8の槽底20は、微細固形食品残滓排出口22に集中するように勾配が設けられている為、貯留二次廃液と共に流勢を持って短時間で排出される。
【0039】
微細固形食品残滓排出口22は、床面と槽底20の間の狭隘となる区画に設けられていない。本装置と隣接して設置される機器、又は、建屋の壁との間の間隙に微細固形食品残滓排出口22が設けられている。この結果、作業者は容易にバルブ開閉操作が行え、微細固形食品残滓の排出状況を確認が行える。
【0040】
【発明の効果】
以上説明したように本発明の油水分離油脂回収装置は、内蔵する油水分離槽8が第1槽9と第2槽10に分割して設けられる。第1槽9の上部開口部面積と内容積が第2槽のそれと比較して小さく形成されることにより、次ぎの効果を所有する。
【0041】
その第一は、第1槽9と第2槽10を区画する立隔壁の下部を多面体構造隔壁傾斜面14としたことにより、冷温一次廃液が第1槽9の被予熱貯留一次廃液に注入されると、第1槽9内部で拡散し、第1槽9を取巻く大容量の第2槽被予熱貯留一次廃液から、大きな表面積を持つ多面体構造隔壁傾斜面14を介して蓄熱が伝播する。熱移動を行う場合、低温側と高温側が接触する面積が大きい程速く行える。しかも、油脂は水より比熱が小さく熱吸収が速く、一次廃液含有油脂粒滴は体積膨張し密度が低下する。その結果、油脂粒滴の分離浮上が迅速に行われる効果を得る。
【0042】
その第二は、低温一次廃液が周囲から分離浮上する油脂粒滴群は、第1槽9と第2槽10を区画する隔壁下部の多面体構造隔壁傾斜面14に衝突し、その箇所の隔壁表面では表面張力により合体し粒滴が大きく成長し、浮力を増す。多面体構造隔壁傾斜面14はこの油滴の成長を促進させ、一次廃液含有油脂の大部分を浮上させる効果を得る。
【0043】
その第三は、流入した一次廃液から分離浮上する大部分の油脂は、開口部面積の小さな第1槽9の液面に集積される。更に、第2槽10に浮上した油脂も副ベルト式オイルスキマー13により汲上げられ、第1槽9の液面に集約されることにより、第1槽9の油脂層が嵩高され、主ベルト式オイルスキマー5が油脂と接触する面積が増大し、油脂を汲上げる量と効率を向上させる効果を得る。
【図面の簡単な説明】
【図1】図1は本発明の油水分離油脂回収装置1の外観図である。
【図2】図2は組込型天板2、洗浄槽3及び金網4の上部構成部品を取外した内部構造俯瞰図である。
【図3】図3は図2の断面A−A図である。
【図4】図4は図2の断面B−B図である。
【図5】図5は、補助分離器の正面図である。
【符号の説明】
1 油水分離油脂回収装置 2 天板 3 洗浄槽
4 ストレーナ 5 主ベルト式オイルスキマー
6 ヒーター 6A ヒーターケース
7 回収タンク 8 油水分離槽 9 第1槽
10 第2槽 11 廃液受入れ皿
12 戻り油脂受皿 13 副ベルト式オイルスキマー
14 多面体構造隔壁傾斜面 15 通水口 16 補助分離器
17 補助分離器流入口 17a トラップ 17b トラップ
17c 流入口 17d 流入口枝管
18 補助分離器枝管 19 補助分離器本管
19a トラップ 19b トラップ 19c 流入口
20 油水分離槽々底 21 排水管
22 微細固形食品残滓排出口 23 廃液導通口
24 ガイド板 25 導管 26 本管枝管
[0001]
BACKGROUND OF THE INVENTION
The present invention provides an apparatus for separating solid food residue from inflow waste liquid in an oil / water separation oil / fat recovery apparatus that separates and recovers solid food residue discharged from kitchens such as restaurants and ramen shops and waste liquid containing a large amount of fat and oil. The built-in washing tank and the oil / fat recovery tank provided are detachably accommodated in the upper part of the apparatus, an oil / water separation tank is formed in the lower part of the apparatus, and the oil / fat separated and floated in the oil / water separation tank It is equipped with a belt type oil skimmer. The present invention relates to an oil / water separation tank in which an oil / water separation tank is integrated as a lower structure, and an embedded washing tank, an oil / fat recovery apparatus, and an oil / fat recovery tank are integrated as an upper structure.
[0002]
[Prior art]
Food residues discharged from kitchens such as restaurants and ramen stores are composed of solid food residues and waste liquid containing a large amount of fats and oils. As an apparatus for separating and collecting oils and fats from this waste liquid, there is a technique presented by the present inventors. In this device, the built-in type washing tank is housed and integrated in the oil / water separation oil and fat recovery device, and no gap is formed between the built-in type washing tank and the oil / water separation tank in the vertical position, and the oil / water separation tank is occupied. There is a form in which the volume is utilized to the maximum extent.
[0003]
The primary waste liquid from which the rough solid food residue is captured and removed from the waste liquid by the strainer installed in the built-in type washing tank of the oil / water separation and recovery apparatus installed in the kitchen is separated from the washing tank through the duct. The oil flows into the tank, and the oil and fat is separated from the primary waste liquid due to the difference in specific gravity with the auxiliary separator installed in the oil / water separation tank, and floats on the liquid surface of the oil / water separation tank, and then installed in the oil / water separation tank Oil is pumped up and stored in a collection tank by the belt type oil skimmer.
[0004]
[Problems to be solved by the invention]
However, an auxiliary separator is provided in the built-in oil / water separation tank to promote the separation and floating of fats and oils due to the difference in specific gravity from the primary waste liquid, but one section of the oil / water separation tank adopts a housing structure when the primary waste liquid flows in excessively In such a case, the primary waste liquid may flow out of the oil / water separation oil / fat recovery apparatus in a state where the oil / fat is not sufficiently time to separate and float and the oil / fat separation / floating is insufficient. Even if it is spilled, the fat and oil is separated and recovered from the primary waste liquid by the grease interceptor of the end-of-life treatment equipment, so it does not deteriorate the public sewerage and the environment. It is necessary to secure and improve the ability to collect oil and fat, and drain waste water (waste liquid after collecting oil and fat) outside the apparatus.
[0005]
In addition, since a discharge port is provided at the bottom of the bottom of the funnel-shaped oil / water separation tank, the gap between the discharge port and the kitchen floor becomes narrow. As a result, a large-diameter valve is not attached to the discharge port, and when discharging a fine solid food residue (miso, spices, etc.) remaining in the oil-water separation tank, the discharge port valve is easily blocked by the residue. Occurs. In order to eliminate the blockage, the operator required an inefficient effort to remove the cleaning tank of the upper structure and remove and collect it manually and with running water.
[0006]
[Means for solving the problems]
In order to solve the above-mentioned problems, the oil / water separation oil / fat recovery apparatus according to the present invention is a means for sufficiently separating and floating the oil / fat from the primary waste liquid due to the specific gravity difference, for the purpose of extending the flow path within a limited volume. The oil / water separation tank built in the apparatus is divided into a first tank having a small upper opening area and a small capacity and a second tank having a large capacity. And the lower part of the vertical partition which divides the said 1st tank and the 2nd tank has a polyhedral structure which has a gradient toward the fine solid food residue discharge port provided in the oil-water separation tank bottom vicinity joint part of the 2nd tank standing wall A partition inclined surface is formed. A part of the contact portion between the inclined surface of the polyhedral structure partition wall and the bottom of the tank having a gradient toward the discharge port is provided with an opening through which the first tank and the second tank pass water, and the polyhedral structure partition wall slope of the lower partition wall is provided. The surface is responsible for the function of causing most of the oil and fat to concentrate and float on the liquid surface of the first tank from the primary liquid waste flowing from the first tank to the second tank in the first tank. The large-diameter valve can be attached by installing the tank bottom joint portion of the second tank lower vertical wall. Thereby, the discharge port was not blocked by the fine solid food residue settled on the bottom of the second tank during the cleaning and inspection of the apparatus, and means for having a function of quickly discharging the fine solid food residue was taken.
[0007]
Further, the oil / water separation oil / fat recovery apparatus according to the present invention has a built-in oil / water separation tank divided into a first tank and a second tank connected by a water inlet, and has a strainer for separating solid food residue from waste liquid on the upper surface of the second tank. And a built-in cleaning tank having a flow path through which the primary waste liquid is poured into the first tank, and a recovery tank for storing oil pumped up by the main belt type oil skimmer are detachably incorporated, and the first tank Is equipped with a main belt type oil skimmer that is always in operation and pumps up most of the oil that floats and separates due to the difference in specific gravity. The second tank is provided with a sub-belt type oil skimmer that is capable of arbitrarily adjusting the operation cycle for pumping up residual oil separated and floated due to the difference in specific gravity from the auxiliary separator and returning it to the first tank.
[0008]
The oil and fat pumped up by the sub-belt type oil skimmer provided in the second tank and circulated back to the first tank is capable of adjusting the operation cycle arbitrarily. The bulkiness is increased, whereby the oil and fat adsorption effect of the main belt type oil skimmer becomes high efficiency, and ultimately the oil and fat recovery efficiency from the waste liquid is improved.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
[0010]
FIG. 1 is an external view of an oil / water separation oil / fat recovery apparatus 1 of the present invention. FIG. 2 is an overhead view of the internal structure with the built-in top plate 2, the cleaning tank 3, and the upper components of the strainer 4 removed. 3 is a cross-sectional view taken along the line AA of FIG. 4 is a cross-sectional view taken along the line BB in FIG. FIG. 5 is a front view of the auxiliary separator.
[0011]
As a preparation before waste liquid treatment, all the primary waste liquid stored in the oil / water separation tank 8 is preheated to 50 to 60 ° C. by the heater 6.
[0012]
1, 3, and 4, the primary waste liquid passes through the upper structure strainer 4 and the cleaning tank 3, and as shown by an arrow (1), passes through the waste liquid receiving tray 11 and the waste liquid conduction port 23, and the oil / water separation tank. It flows into the first tank 9 in 8.
[0013]
In FIG. 2, the upper part of the first tank 9 is formed in a casing shape that is partitioned by a standing partition wall and opened to the upper part, and the lower part of the first tank 9 standing partition wall is a polyhedral structure partition sloped surface 14. It is formed in a state of projecting to the tank side. The area and volume of the upper opening of the first tank 9 are small compared with that of the second tank 10.
[0014]
3 and 4, the tank bottom 20 of the oil / water separation tank 8 has inclinations of angles α and β formed with a horizontal plane, and the inclination angles γ and δ formed with the intersection with the polyhedral partition wall inclined surface 14 as well. A gradient with is formed.
[0015]
The reason why the upper opening area of the first tank 9 is smaller than that of the second tank 10 and the lower polyhedral partition structure volume of the first tank 9 is larger than the upper opening volume of the first tank 9 is explained. To do.
[0016]
First, when the oil and fat separated and floated from the primary waste liquid that flows in has a constant volume, the bulk of the oil and fat layer diffuses thinly on the liquid surface of the oil and water separation tank with a large opening area. However, it will pump up a lot of the main component of the waste liquid. In order to avoid this phenomenon, the surface of the first tank having a small opening area is floated to increase the bulk of the formed oil and fat layer. As a result, the belt-type oil skimmer 5 has an effect of improving the efficiency of pumping up fats and oils.
[0017]
Second, when a certain amount of cold primary waste liquid is injected into the preheated storage primary waste liquid in the first tank 9, the cold primary waste liquid has a lower liquid temperature and higher density than the preheated storage primary waste liquid. Settling in one tank. The low-temperature primary waste liquid that settles diffuses inside the polyhedral structure partition inclined surface 14 of the first tank 9, and passes from the large-capacity second tank preheated storage primary waste liquid surrounding the first tank 9 through the polyhedral structure partition inclined surface. Absorbs the stored heat.
When heat transfer is performed, the larger the contact area between the low temperature side and the high temperature side, the faster the speed. In order to obtain the effect, the lower surface of the partition wall is increased in surface area, so that it has a polyhedral inclined surface structure, and the best inclination angles γ and δ are given.
[0018]
The third is that when the low temperature primary waste liquid absorbs heat from the surrounding preheated primary waste liquid and the heat transfer is in an equilibrium state, the oil droplets contained will rise faster than water because the specific heat is smaller than that of water. , The volume expands. As a result, the fat and oil droplet group has a reduced density and promotes separation and levitation. The separated and levitated oil droplet group collides with the inclined surface 14 of the polyhedral structure partition wall, coalesces by the surface tension, and the particle droplet grows greatly to increase buoyancy. The polyhedral structure partition inclined surface 14 has an effect of promoting the growth of the oil droplets and floating.
[0019]
When the partition wall material partitioning the oil / water separation tank 8 is formed of austenitic stainless steel, good results are obtained in terms of workability, corrosion resistance, and thermal conductivity. The boundary portion of each surface constituting the polyhedral structure partition inclined surface 14 has no unevenness, and the effect is further enhanced when the surface of each surface is mirror-finished.
[0020]
The process in which the contained fats and oils separate and float from the inflow cold / hot primary waste liquid will be described.
[0021]
A primary waste liquid having a volume indicated by the arrow (1) flows into the first oil-water separation tank 9. When the cold primary waste liquid flows into the stored primary waste liquid preheated to 50 to 60 ° C., the cold inflow primary waste liquid is larger than the density of the preheated stored primary waste liquid, and the inflow primary waste liquid passes through the first tank 9 in the oil / water separation tank. Settling.
[0022]
The cold / warm primary waste liquid absorbs heat from the preheated all-oil / water separation tank storage primary waste liquid in the process of sinking the inclined surface area of the polyhedral structure partition wall in the oil / water separation tank first tank 9, and heat transfer is performed. In order to promote this, the second tank 10 surrounds the first tank 9, and the polyhedral structure partition wall inclined surface area 14 is provided so that the contact area with the second tank 10 becomes large.
[0023]
Due to this influence, the cold and warm primary waste liquid that settles in the polyhedral structure partition inclined surface area of the first tank 9 absorbs heat from the preheated storage primary waste liquid through the partition inclined surface. When the heat transfer is in an equilibrium state, the fat and oil droplet group contained has a specific heat of fat and oil smaller than that of water, so that the droplet absorbs heat prior to water and expands its volume and the density decreases. As a result, separation and flotation are promoted from the primary waste liquid.
[0024]
From the flow arrow (2) of the primary waste liquid toward the water flow port 15, the oil droplets whose volume has expanded due to endothermic heat and whose density has been lowered floated due to the difference in specific gravity and are finished to a mirror-like surface with a gradient. Collides with the inclined surface 14. The collided groups of fat and oil droplets are united by surface tension to grow into large oil droplets, and the buoyancy is increased. Since the surface of the inclined surface of the polyhedral structure partition wall is in a mirror surface state, the oil droplets that have grown greatly float on the surface of the first tank 9 along the surface of the partition wall without adhering to the surface of the inclined surface of the partition wall structure. . This process is continuously performed, and the droplets are separated and floated from the primary waste liquid.
[0025]
In this way, the inclined surface 14 of the polyhedral structure partition wall is divided by the standing wall because it is necessary to extend the residence time of the cold primary waste liquid and to quickly transfer heat between the cold inflow primary waste liquid and the preheated storage primary waste liquid. A polyhedral partition wall structure having an inclined surface that obtains a large surface area has been adopted so that heat transfer can be performed quickly from the second tank 10, and the oil droplets contained in the primary waste liquid are ahead of the water due to the specific heat. As the volume is expanded and the volume expands, the density decreases and the particles float and separate, and the effect of accelerating the coalescence and oil droplet growth of the floating oil droplet groups is obtained. In this process, most of the contained fats and oils are separated and floated on the liquid surface of the first tank 9 from the primary waste liquid.
[0026]
The above is the effect obtained by the polyhedral structure partition inclined surface 14.
[0027]
The secondary waste liquid in which most of the contained fats and oils are separated and floated from the primary waste liquid to the liquid level of the first tank 9 flows into the second oil tank 10 having a large volume via the water inlet 15. It becomes a gentle flow that spreads in the width direction larger than the width of 15, and the remaining fat and oil droplet group contained floats on the liquid surface of the second tank 10 due to the difference in specific gravity, and coalesces and grows on the liquid surface to form an oil and fat layer.
[0028]
A means for generating bubbles in the second tank 10 for oil / water separation, for example, an electrolysis apparatus or a micro air nozzle for generating fine bubbles is installed to generate fine bubbles, and the fat and oil contained in the stored secondary waste liquid If it adheres to the fine bubbles generated in the droplets and floats on the liquid surface, an effect of increasing the oil and fat scavenging efficiency of the sub-belt type oil skimmer 13 can be obtained.
[0029]
The oil and fat layer that has floated on the liquid surface of the second tank 10 is returned to the oil receiving tray with the secondary waste liquid in order to maintain fluidity by the secondary belt-type oil skimmer 13 that can be arbitrarily adjusted in the operation cycle installed in the second tank 10. It is pumped up to 12. The return oil receiving tray 12 communicates with the waste liquid receiving tray 11, and the pumped oil and fat is injected into the first oil / water separation tank 9 together with the cold primary waste liquid flowing in.
[0030]
Since the oil and fat pumped up from the second tank 10 grows greatly in oil droplets, even if injected into the first tank 9 together with the cold and primary waste liquid, the existing floating oil and fat layer regardless of the flow of the cold and primary waste liquid described above. To increase the bulk of the existing fat layer. As a result, the efficiency with which the main belt type oil skimmer 5 pumps up oil and fats increases, and the oil and fats are stored in the recovery tank 7. The recovered fats and oils have sufficient purity to be effectively used as a secondary resource for producing fertilizers, feeds and the like.
[0031]
The auxiliary separator inlet 17 is provided by the effect that the inlet 17 of the auxiliary separator 16 that promotes oil / water separation provided in the second tank 10 is provided upward in the liquid surface direction of the second tank 10. Even if the secondary waste liquid flows in, the oil and fat droplets contained therein are not hindered from floating up toward the liquid surface of the second tank 10 against the flow of the secondary waste liquid.
[0032]
The operation of the auxiliary separator 16 provided in the oil / water separation tank second tank 10 will be described.
[0033]
The function of the auxiliary separator 16 will be described with reference to FIG. In FIG. 5, 16 is an auxiliary separator, and this auxiliary separator 16 is connected to a drain pipe 21 and provided with traps 17a, 17b, 19a, 19b for supporting oil / water separation by a swirling flow and specific gravity difference. Yes. The auxiliary separator 16 includes a main pipe 19 having a triple pipe structure and an inlet 17 having a double pipe structure. A conduit 25 connects the main pipe 19 and the lower end of the inlet 17. Reference numeral 18 denotes a branch pipe provided in the middle of the conduit 25. The branch pipe 18 is provided in order to allow the oil droplets separated from the secondary waste liquid flowing through the conduit 25 to escape to the liquid level of the branch pipe 18.
[0034]
The secondary waste liquid flows into the auxiliary separator 16 from the trap 17 a at the inlet 17. It flows while turning as shown by the arrow (8). Also in this process, the remaining oil droplet group is separated and floated toward the liquid surface. After that, as shown by an arrow (9), it flows into the auxiliary separator main pipe 19 from the trap 19a via the conduit 25. Even while passing through the conduit 25, the remaining oil droplet group continues to separate and float, the oil content continues to decrease, and becomes a tertiary waste liquid.
[0035]
The tertiary waste liquid that has flowed into the auxiliary separator main pipe 19 passes through the trap 19b while turning as indicated by an arrow (10), and the arrow starts from the upper end that becomes the upper liquid level of the branch pipe 26 of the auxiliary separator main pipe 19. As shown in (11), the water overflows and is drained from the drain port 21 to the grease interceptor of the terminal treatment apparatus.
[0036]
In the branch pipes provided at a plurality of locations in the auxiliary separator 16, a small amount of oil and fat floats from the secondary waste liquid and is stored. It has been confirmed through experiments at the development stage that no problem occurs.
[0037]
As shown in FIGS. 3 and 4, the bottom of the oil / water separation tank 8 has a gradient of angles α and β formed with a horizontal plane, and the gradient is provided so as to concentrate on the fine solid food residue discharge port 22.
[0038]
The fine solid food residue discharge port 22 is provided with a large-diameter valve, which causes the valve to be blocked when discharging the fine solid food residue deposited in the oil / water separation tank 8 during cleaning and inspection of the apparatus. No. Further, since the tank bottom 20 of the oil / water separation tank 8 is provided with a gradient so as to concentrate on the fine solid food residue discharge port 22, it is discharged in a short time with a flow along with the stored secondary waste liquid.
[0039]
The fine solid food residue discharge port 22 is not provided in a narrow space between the floor surface and the tank bottom 20. A fine solid food residue discharge port 22 is provided in a gap between the apparatus installed adjacent to the apparatus or the wall of the building. As a result, the operator can easily open and close the valve and check the discharge state of the fine solid food residue.
[0040]
【The invention's effect】
As described above, in the oil / water separation oil / fat recovery apparatus of the present invention, the built-in oil / water separation tank 8 is divided into the first tank 9 and the second tank 10. Since the upper opening area and the internal volume of the first tank 9 are formed smaller than that of the second tank, the following effects are possessed.
[0041]
The first is that the lower part of the vertical partition partitioning the first tank 9 and the second tank 10 is a polyhedral structure partition inclined surface 14, so that the cold primary waste liquid is injected into the preheated storage primary waste liquid in the first tank 9. Then, the heat storage propagates from the large-capacity second tank preheated storage primary waste liquid that diffuses inside the first tank 9 and surrounds the first tank 9 via the polyhedral structure partition wall inclined surface 14 having a large surface area. When heat transfer is performed, the heat transfer can be performed faster as the area of contact between the low temperature side and the high temperature side increases. In addition, fats and oils have a smaller specific heat than water and quick heat absorption, and the primary waste liquid-containing fat and oil droplets expand in volume and the density decreases. As a result, the effect of promptly separating and floating the fat droplets is obtained.
[0042]
Secondly, a group of oil droplets from which the low temperature primary waste liquid separates and floats from the surroundings collides with the polyhedral structure partition inclined surface 14 at the bottom of the partition partitioning the first tank 9 and the second tank 10, and the partition wall surface at that location Then, it coalesces by the surface tension, and the droplets grow large and increase buoyancy. The polyhedral structure partition inclined surface 14 promotes the growth of the oil droplets and obtains the effect of floating most of the primary waste liquid-containing oil and fat.
[0043]
Thirdly, most of the oil and fat that separates and floats from the inflowing primary waste liquid is collected on the liquid surface of the first tank 9 having a small opening area. Further, the oil and fat that has floated in the second tank 10 is also pumped up by the sub-belt type oil skimmer 13 and concentrated on the liquid surface of the first tank 9, so that the oil and fat layer in the first tank 9 becomes bulky, and the main belt type The area where the oil skimmer 5 comes into contact with the oil and fat increases, and the effect of improving the amount and efficiency of pumping up the oil and fat is obtained.
[Brief description of the drawings]
FIG. 1 is an external view of an oil / water separation oil collecting apparatus 1 of the present invention.
FIG. 2 is a top view of the internal structure with the built-in top plate 2, the cleaning tank 3 and the upper part of the wire mesh 4 removed.
FIG. 3 is a cross-sectional view taken along the line AA in FIG. 2;
4 is a cross-sectional view taken along the line B-B in FIG. 2;
FIG. 5 is a front view of an auxiliary separator.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Oil-water separation fat collecting apparatus 2 Top plate 3 Washing tank 4 Strainer 5 Main belt type oil skimmer 6 Heater 6A Heater case 7 Collection tank 8 Oil water separation tank 9 1st tank 10 2nd tank 11 Waste liquid receiving tray 12 Return oil receiving tray 13 Sub Belt-type oil skimmer 14 Polyhedral structure partition inclined surface 15 Water inlet 16 Auxiliary separator 17 Auxiliary separator inlet 17 a Trap 17 b Trap 17 c Inlet 17 d Inlet branch pipe 18 Auxiliary separator branch pipe 19 Auxiliary separator main pipe 19 a Trap 19 b Trap 19c Inlet 20 Oil-water separation tank bottom 21 Drain pipe 22 Fine solid food residue outlet 23 Waste liquid outlet 24 Guide plate 25 Pipe 26 Main branch branch

Claims (3)

飲食店厨房内で使用される流し台と終末処理装置であるグリース阻集器までの経路中に設けられる油水分離油脂回収装置であって、該油水分離油脂回収装置内蔵油水分離槽は、上部開口面積と容積が小の第1槽とそれが共に大の第2槽とに立隔壁で区画され、その立隔壁下部構造は、前記第1槽から前記第2槽側へ張出す多面体構造の傾斜面を形成し、且つ、その多面体構造の傾斜面と微細固形食品残滓排出口に向う勾配を持つ油水分離槽々底との交接部の一部は、前記第1槽と前記第2槽との通水口が設けられ、前記第1槽から前記2槽へ流動する廃液から、多面体構造の傾斜面に沿って大部分の油脂が拡散されず、前記第1槽液面に分離浮上させる機能を所有する、内臓油水分離槽が前記第1槽と前記第2槽に区画される隔壁構造を持つことを特徴とする油水分離油脂回収装置。An oil / water separation oil / fat recovery device provided in a path to a sink used in a restaurant kitchen and a grease interceptor which is a terminal treatment device, and the oil / water separation tank with a built-in oil / water separation oil / fat recovery device has an upper opening area and The first tank having a small volume and the second tank having both of them are partitioned by a standing partition, and the lower structure of the standing partition has an inclined surface of a polyhedral structure projecting from the first tank to the second tank side. formed, and a portion of the mating portion of the oil-water separation tank s bottom with a gradient toward the inclined surface and the fine solid food residue outlet of the polyhedral structure, passing between the second tank and the first tank water inlet From the waste liquid flowing from the first tank to the two tanks, most of the oil and fat is not diffused along the inclined surface of the polyhedral structure, and possesses the function of separating and floating on the liquid surface of the first tank. A built-in oil / water separation tank has a partition structure that is divided into the first tank and the second tank. Oil-water separator oil recovery device characterized by and. 蔵油水分離槽を、上部開口面積と容量が小の第1槽とそれが大の第2槽とに区画する立隔壁下部構造であって、前記第1槽から前記第2槽側へ張出す傾斜面を持つ表面積大の多面体構造隔壁傾斜面は、前記第1槽に流入した冷温廃液へ前記第1槽を取囲む前記大容量の第2槽に貯留される被予熱廃液が持つ蓄熱を迅速に伝播する作用を行い、吸熱・昇温した冷温廃液含有油脂粒滴群は体積膨張と密度低下を誘引し、前記多面体構造隔壁傾斜面に沿いながら前記第1槽液面に浮上する効果を持つことを特徴とする請求項1記載の油水分離油脂回収装置に使用される多面体構造隔壁傾斜面を持つ立隔壁下部構造。 The built oil-water separation tank, an upper opening area and capacity a standing barrier rib substructure to which it and the first tank of small partitioned into a second tank of large, Zhang from the first tank to the second tank-side The polyhedral partition wall inclined surface having a large surface area with an inclined surface for discharging heat storage of the preheated waste liquid stored in the second large-capacity tank surrounding the first tank to the cold and waste liquid flowing into the first tank. The oil droplets containing cold waste liquid that has been rapidly propagated and endothermic / heated induces volume expansion and density reduction, and has the effect of floating on the first tank liquid surface along the inclined surface of the polyhedral structure partition wall. The standing partition lower part structure which has a polyhedral structure partition inclined surface used for the oil-water separation oil-fat collection | recovery apparatus of Claim 1 characterized by the above-mentioned. 請求項1記載の油水分離油脂回収装置に於て、内蔵油水分離槽の上面に、固形食品残滓屑と油脂を含む液体から固形食品残滓を分離するストレーナを持ち、廃液が前記油水分離槽第1槽に注水される流路を有する組込型洗浄槽と、主ベルト式オイルスキマーにより汲上げられる油脂を貯留する回収タンクが着脱自在に組込まれ収納されると共に、前記第1槽には分離浮上する大部分の油脂を汲上げる常時稼動の主ベルト式オイルスキマーが、前記第2槽には当該第2槽の液面方向に上向きに設けられた流入口を有する、油水分離を促進する補助分離器と比重差により廃液から分離浮上した残余の油脂を汲上げ前記第1槽に戻す、稼動サイクルが任意に調整可能な副ベルト式オイルスキマーが設けられ、廃液からの油脂回収効率向上が図れることを特徴とした、上部に組込型洗浄槽が下部に油水分離槽が一体収納された構造を持つ請求項1に記載の油水分離油脂回収装置。The oil / water separation oil / fat recovery apparatus according to claim 1, further comprising: a strainer for separating solid food residue from a liquid containing solid food residue and oil / fat on an upper surface of the built-in oil / water separation tank; A built-in cleaning tank having a flow path for water injection into the tank and a recovery tank for storing oil pumped up by the main belt type oil skimmer are detachably incorporated and stored, and separated and floated in the first tank. A main belt-type oil skimmer, which is always in operation to pump up most of the oil and fat, has an inlet provided in the second tank upward in the liquid surface direction of the second tank, and facilitates oil-water separation. returning the vessel and the specific gravity difference residual oil separated emerged from the waste liquid by the pumping said first tank, operating cycles arbitrarily adjustable auxiliary belt oil skimmer is provided, this which attained the oil recovery efficiency of the waste Was characterized, oil-water separation fat collecting apparatus according to claim 1 having the structure embedded cleaning tank at the top oil-water separation tank are integrally housed in the lower part.
JP2001388842A 2001-12-21 2001-12-21 Oil / water separator Expired - Fee Related JP4157700B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103183398A (en) * 2011-12-31 2013-07-03 华英伦水科技(宁波)有限公司 Oil-water separator and control method thereof

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JP2008000712A (en) * 2006-06-23 2008-01-10 Daitogiken Inc Oil/water separation fats and oils recovery apparatus
JP4928846B2 (en) * 2006-06-23 2012-05-09 株式会社 大都技研 Oil / water separation oil recovery system
CN101597094B (en) * 2009-04-28 2012-07-25 无锡荣和环保设备有限公司 Marine oil-water separator and separation method thereof
CN104086008B (en) * 2014-06-20 2018-02-23 广东嘉荣环保设备有限公司 Full-automatic whole kitchen oil water separator
CN107265760B (en) * 2017-06-28 2020-07-28 安徽理工大学 Catering swill treatment device
CN115557638B (en) * 2022-10-11 2023-08-01 南京环美科技股份有限公司 Landfill leachate concentrate processing apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103183398A (en) * 2011-12-31 2013-07-03 华英伦水科技(宁波)有限公司 Oil-water separator and control method thereof
CN103183398B (en) * 2011-12-31 2014-10-22 华英伦水科技(宁波)有限公司 Oil-water separator and control method thereof

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