JP2009133173A - Grease trap device - Google Patents

Grease trap device Download PDF

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JP2009133173A
JP2009133173A JP2007328560A JP2007328560A JP2009133173A JP 2009133173 A JP2009133173 A JP 2009133173A JP 2007328560 A JP2007328560 A JP 2007328560A JP 2007328560 A JP2007328560 A JP 2007328560A JP 2009133173 A JP2009133173 A JP 2009133173A
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powder
oil
grease trap
trap device
tank
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Katsuo Suwada
勝男 諏訪田
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KANKYO SYSTEM KAIHATSU KK
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KANKYO SYSTEM KAIHATSU KK
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Treatment Of Biological Wastes In General (AREA)
  • Water Treatment By Sorption (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
  • Accessories For Mixers (AREA)
  • Sewage (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a grease trap device capable of surely removing oiliness even if the size of a treatment tank is small. <P>SOLUTION: This grease trap device comprises: the treatment tank 2 having a water inlet part 3 installed in a drain passage and having a foreign matter removing function of separating foreign matter in a drain, a stirring mechanism part (air jetting part 21) for stirring the stored drain from which foreign matter is removed, and a water outlet part 5 for discharging the stored drain from which solid matter is excluded; and an oil sucking and powder spraying mechanism 1. The oil sucking and powder spraying mechanism 1 comprises: a container-shaped powder storage part 11; a volumetric feeding part 12 operated by a rotary driving to the bottom side of the powder storage part; and a conveying part 13 which is connected to the volumetric feeding part and which has a supply pipe 131 having a front end port 133 facing the predetermined position of the treatment tank and a rear end connected to a blower 132. The volumetric feeding part and the blower are interlocked with each other at a proper interval. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、レストラン等からの排水のように、油性分を含む排水から油性分を除去するグリーストラップ装置及び油吸着粉末を供給する供給機構に関するものである。   The present invention relates to a grease trap device for removing oily components from wastewater containing oily components, such as wastewater from restaurants and the like, and a supply mechanism for supplying oil adsorbing powder.

レストラン等のように飲食物の調理を行っている厨房からの排水(食堂排水)には、通常、生ゴミの他にも調理用油が含まれていることが多く、そのまま下水道や河川などへの排水を行うと、油性分が固化して排水管や下水管に付着及び蓄積されて、詰まりの原因となったり、河川を汚染する虞がある。このため従前から油性分を含む食堂排水は、一旦厨房の床下等に設けられたグリーストラップ装置を通し、グリーストラップ装置内で排水中の油性分を分離し、その後放流するようにしている。   Drainage from kitchens where food and beverages are cooked like restaurants (dining room drainage) usually contains cooking oil in addition to raw garbage, and can be used directly to sewers and rivers. If drainage is performed, the oily component may solidify and adhere to and accumulate in the drainage pipe and sewer pipe, which may cause clogging and contaminate the river. For this reason, the cafeteria drainage containing oily components has been once passed through a grease trap device provided under the floor of the kitchen, etc., and the oily components in the drainage are separated in the grease trap device and then discharged.

グリーストラップ装置は、基本的に排水を一旦貯留し、水面上に溜まった油性分を定期的に機械又は手作業で汲み上げて除去するものであるが、除去作業が面倒であること、並びに油性分が貯留処理槽壁面に付着し、その油性分の酸化による悪臭が問題となる。そこで従前よりグリーストラップ装置内で油性分を処理することが種々提案されている。   The grease trap device basically stores the wastewater once, and periodically removes the oily component collected on the surface by machine or manual operation. However, the removal operation is troublesome and the oily component is removed. Adheres to the wall of the storage tank, and bad odor due to oxidation of the oily component becomes a problem. Therefore, various proposals have been made to treat oily components in a grease trap apparatus.

例えは特許文献1,2,3には、グリーストラップ装置の貯留処理槽に、油性分吸着体を配置し、当該吸着体に油性分を吸着させて排水から油性分を除去する手段が開示されている。また特許文献4には、油脂分解菌を使用し、分解槽(貯留処理槽)で油性分の生物分解を行なって油性分を除去する手段が開示されており、更に特許文献5には、鹸化剤を排水に添加して、油性分を石鹸化して除去する手段が開示されている。   For example, Patent Documents 1, 2, and 3 disclose means for disposing an oily component from a drainage by disposing an oily component adsorbent in a storage tank of a grease trap device and adsorbing the oily component to the adsorbent. ing. Patent Document 4 discloses means for removing oily components by using oil-degrading bacteria and performing biodegradation of oily components in a decomposition tank (storage treatment tank), and Patent Document 5 further discloses saponification. Means for adding an agent to waste water and soaping out oily components is disclosed.

特開2002−276019号公報。Japanese Patent Laid-Open No. 2002-276019. 特開2004−174346号公報。JP 2004-174346 A. 特開2004−66077号公報。JP 2004-66077 A. 特開2001−59262号公報。JP 2001-59262 A. 特開平9−150146号公報。Japanese Patent Laid-Open No. 9-150146.

前記のとおり従前より種々の油性分除去手段が提案されているが、油性分の生物分解は相応の時間を要するので、排水の分解槽(貯留処理槽)に大容積のものが必要になり、一般の食堂・レストランのような簡易で小容積のグリーストラップ装置を採用している場合には排水量に対して分解処理が追いつかないのが現状である。   As described above, various means for removing oily components have been proposed, but since biodegradation of oily components requires a certain amount of time, a wastewater decomposition tank (storage tank) requires a large volume, In the case where a simple and small-capacity grease trap device such as a general canteen or restaurant is adopted, the decomposition treatment cannot catch up with the amount of waste water.

また吸着体を採用する手段では、前記特許文献2に開示されているとおり、吸着材に油脂分解菌を含ませて、吸着した油性分の生物分解を行っているが、前述のとおり生物分解には時間を要し、更に吸着量の全てが分解されるまでに油性分の吸着量が限界となったり、吸着材の配置等によって、吸着体に吸着しない油性分が排出される虞も大きく、確実な油性分除去がなされない。   Moreover, in the means which employs an adsorbent, as disclosed in the above-mentioned Patent Document 2, the oil-degrading bacterium is included in the adsorbent and the adsorbed oil is biodegraded. Takes time, and the amount of oily component adsorbed is limited until all of the adsorbed amount is decomposed, or the oily component not adsorbed on the adsorbent is discharged due to the placement of the adsorbent, etc. Certain oil removal is not done.

また石鹸化においては、鹸化物質が必要であり、石鹸水の河川等への直接流出は、水性生物に影響を与え、また下水処理に際しては処理負担を大きくする問題がある。   In addition, soaping requires a saponification substance, and the direct outflow of soapy water into rivers and the like has a problem of affecting aquatic organisms and increases the treatment burden during sewage treatment.

さらに、貯留処理槽に処理剤を供給する手段として、特許文献3は布裁断物であり、特別な供給機構は開示されていない。また特許文献4,5は、詳細な構造について説明はないが、構成図から液体の供給装置である。本発明は後述するように油吸着粉末を使用することを提案したもので、この油吸着粉末は、数十μmの顆粒の微粉末で、処理槽に対して油吸着粉末を効果的に供給する必要があるが、前記した従前の供給機構は採用することが出来ない。   Furthermore, as means for supplying the treatment agent to the storage treatment tank, Patent Document 3 is a cloth cut article, and no special supply mechanism is disclosed. Patent Documents 4 and 5 do not describe the detailed structure, but are liquid supply devices from the configuration diagram. The present invention proposes to use an oil adsorbing powder as will be described later, and this oil adsorbing powder is a fine powder of granules of several tens of μm, and effectively supplies the oil adsorbing powder to the treatment tank. Although necessary, the conventional supply mechanism described above cannot be employed.

本発明は、従前手段と異なる新規な油性分除去手段を備えたグリーストラップ装置を提案したものである。   The present invention proposes a grease trap device provided with a novel oily component removing means different from the conventional means.

本発明に係るグリーストラップ装置は、排水路途中に設け、排水中の夾雑物を分離する夾雑物除去機能を備えた入水部、及び夾雑物を除去した貯留排水を攪拌する攪拌機構部、及び固形分を除いて排出する出水部を付設した処理槽と、油性分を吸着して固形分とする油吸着粉末を処理槽上方から、適時散布する油吸着粉末散布機構とで構成してなることを特徴とするものである。   The grease trap device according to the present invention is provided in the middle of a drainage channel, and includes a water inlet portion having a contaminant removing function for separating contaminants in the wastewater, a stirring mechanism portion for stirring the stored wastewater from which the contaminants are removed, and a solid It is composed of a treatment tank with a water discharge section that discharges the water, and an oil-adsorbed powder spraying mechanism that spreads oil-adsorbed powder from the upper part of the treatment tank in a timely manner by adsorbing the oily component to form a solid content. It is a feature.

而して食堂排水は、入水部で夾雑物(野菜等の食材屑片)が除去され、夾雑物除去排水が処理槽に貯留されると、油吸着粉末散布機構から所定量の油吸着粉末が散布され、攪拌によって処理槽内排水と混合されると、排水中の油性分は当該粉末に吸着して塊状(固形分)となるので、排水部の固液分離によって固形分(油分)を含まない分離排水を処理槽から出水し、外部へ排出(放流)するものである。   Thus, the wastewater from the cafeteria is removed from the contaminants (food wastes such as vegetables) at the water inlet, and when the wastewater from the contaminants is stored in the treatment tank, a predetermined amount of oil-adsorbed powder is released from the oil-adsorbed powder spraying mechanism. When sprayed and mixed with wastewater in the treatment tank by stirring, the oily content in the wastewater is adsorbed to the powder and becomes a lump (solid content), so it contains solid content (oil content) by solid-liquid separation in the drainage section Unseparated wastewater is discharged from the treatment tank and discharged (discharged) to the outside.

また本発明(請求項2)は、前記グリーストラップ装置において、油吸着粉末散布機構が、容器状の粉末貯留部と、粉末貯留部の底方に回転駆動によって動作する定量供給部と、前記定量供給部と接続されると共に、先端口を処理槽の所定位置に臨ませ、基端を送風機と接続した供給管を備えた搬送部とで構成され、定量供給部と送風機とを適時間隔で連動させてなるもので、粉末貯留部内に所定の油吸着粉末(以下「粉体」という)を収納し、レストラン等の開店と共に作動すると、当該レストランの排水量並びに処理槽の容量に合わせて適宜間隔で、定量供給部と送風機とを連動させると、粉体の最適量を処理槽に散布することができるものである。   According to the present invention (Claim 2), in the grease trap device, the oil adsorbing powder spreading mechanism includes a container-shaped powder storage unit, a quantitative supply unit that operates by rotation driving to the bottom of the powder storage unit, and the quantitative determination unit. Consisting of a supply unit connected to the supply unit and a conveying unit equipped with a supply pipe with the distal end facing a predetermined position in the processing tank and the base end connected to the blower, the fixed-quantity supply unit and the blower are linked at appropriate intervals When a predetermined oil-adsorbing powder (hereinafter referred to as “powder”) is stored in the powder storage part and operated when the restaurant is opened, the drainage amount of the restaurant and the capacity of the processing tank are appropriately spaced. When the fixed amount supply unit and the blower are interlocked, the optimum amount of powder can be dispersed in the processing tank.

また本発明(請求項3)は、特に前記の油吸着粉末散布機構の定量供給部が、粉末貯留部の内底面に、回転外周近傍に供給口を開設した回転板を設け、粉末貯留部の底面に、前記供給口の通過位置に供給管と接続される排出口を有し、粉末貯留部の底方における前記排出口位置の回転方向側に障壁を設けてなるものである。   Further, in the present invention (Claim 3), in particular, the quantitative supply unit of the oil adsorbing powder spraying mechanism is provided with a rotating plate having a supply port in the vicinity of the rotating outer periphery on the inner bottom surface of the powder storing unit, The bottom surface has a discharge port connected to the supply pipe at a position where the supply port passes, and a barrier is provided on the rotational direction side of the discharge port position at the bottom of the powder reservoir.

而して、回転板を回転させると、回転板の供給口と排出口が重なる箇所で貯留部内の粉体が下方に落ち込み、特に排出口位置の回転方向側に障壁部を設けているので、回転板で回転方向に運ばれる粉体は、障壁に衝突して当該位置で止められ、盛り上がるので、前記の粉体の落下が確実に為される。そして供給管内に落下した粉体は、送風によって供給管内を搬送され、先端口から放出されて処理槽に供給散布される。   Thus, when the rotating plate is rotated, the powder in the storage portion falls downward at the location where the supply port and the discharge port of the rotating plate overlap, and in particular, the barrier portion is provided on the rotation direction side of the discharge port position. The powder conveyed in the rotation direction by the rotating plate collides with the barrier, stops at the position, and rises, so that the powder is surely dropped. And the powder which fell in the supply pipe | tube is conveyed in the supply pipe | tube by ventilation, is discharged | emitted from a front-end | tip opening, and is supplied and disperse | distributed to a processing tank.

また本発明(請求項4)は、定量供給部を、ホッパー状の粉末貯留部の内底面に開口部を設け、柱状外周面に収納凹部を形成したロータリーバルブを、前記開口部に収納凹部が臨むように組み込み、開口部反対側の収納凹部に対面する箇所、供給管とを接続してなるもので、粉末貯留部内の粉体が収納凹部に入り、ロータリーバルブの回転によって収納凹部内の粉体が供給管内に落下し、送風によって供給管内を搬送され、先端口から放出され処理槽に供給散布される。   According to the present invention (Claim 4), the quantitative supply unit is provided with a rotary valve having an opening formed on the inner bottom surface of the hopper-shaped powder storage unit and a storage recess formed on the columnar outer peripheral surface. It is built so that it faces, the part facing the storage recess on the opposite side of the opening, and the supply pipe are connected. The powder in the powder storage part enters the storage recess and the powder in the storage recess is rotated by the rotation of the rotary valve. The body falls into the supply pipe, is transported through the supply pipe by air blowing, is discharged from the tip end, and is supplied and dispersed in the treatment tank.

また本発明(請求項5)は、前記のグリーストラップ装置において、処理槽内に網板又は濾過膜で仕切り部を設けて出水部における固形分分離機能を備えさせると共に、油吸着粉末供給機構の供給管先端を、前記仕切り部より入水部側に臨ませてなるもので、仕切り部の出水側は油分を含まない油分分離排水で満たされるので、この分離排水の自然放流がなされる。処理槽内の油分を吸着した固形分は、後述する手段で取り出して外部処理したり、処理槽に油分を分解する微生物を供給して自然分解を行なう。   Further, according to the present invention (Claim 5), in the grease trap apparatus, a partition portion is provided in the treatment tank with a mesh plate or a filtration membrane to provide a solid content separation function in the water discharge portion, and an oil adsorption powder supply mechanism is provided. The supply pipe tip is made to face the water inlet side from the partition part, and the water discharge side of the partition part is filled with oil-separated waste water that does not contain oil, so that the separated waste water is naturally discharged. The solid content adsorbing the oil in the treatment tank is taken out by means described later and externally treated, or the treatment tank is supplied with microorganisms that decompose the oil and is naturally decomposed.

また本発明(請求項6)は、前記のグリーストラップ装置において、処理槽内に沈殿物の取出用網容器を設けて固形分分離機能を備えさせると共に、油吸着粉末供給機構の供給管先端を、前記取出用網容器の上方に臨ませてなるもので、油分吸着固形分が取出用網容器内のみ存在することになるので、容器を処理槽から取り出して油分を吸着した固形分を容易に外部処理することができる。   According to the present invention (Claim 6), in the above grease trap apparatus, a deposit container is provided in the processing tank to provide a solids separation function, and the tip of the supply pipe of the oil adsorbing powder supply mechanism is provided. Since the oil adsorbing solid content is present only in the extraction net container, it is easy to remove the solid from the processing tank and adsorb the oil. Can be externally processed.

更に本発明(請求項7)は、固形分分離機能の付与構造として、貯留処理槽内の沈殿物・浮遊物を含んだ排水の汲み上げ機構と、汲み上げ排水の固形分を分離する分離部を備え、汲み上げた排水から固形分を除いた分離排水のみを排出する構造としたもので、沈殿物・浮遊物の汲み上げ分離及び油性分を含まない分離排水の外部排出(放流)が自動的に為されるものである。   Furthermore, the present invention (Claim 7) includes, as a structure for giving a solid content separation function, a pumping mechanism for drainage containing sediment / float in the storage tank and a separation unit for separating the solid content of the pumped wastewater. It is structured to discharge only the separated effluent from which the solid content is removed from the pumped effluent, and the pumping separation of sediment and suspended solids and the external discharge (release) of the separated effluent that does not contain oily components are performed automatically. Is.

また本発明(請求項8)は、前記装置において、油吸着粉末が、油吸着能力を有するバイオレメディエーション促進剤であるもので、分離固形物(油吸着物)をそのまま土壌に放置しても、効果的な生物分解が促進され、分離固形物の処理が容易になる。   Further, in the present invention (claim 8), in the apparatus, the oil adsorbing powder is a bioremediation accelerator having an oil adsorbing ability, and even if the separated solid (oil adsorbed material) is left as it is in the soil, Effective biodegradation is facilitated and the processing of separated solids is facilitated.

更に本発明(請求項9)は、前記装置において、攪拌機構が空気曝気機構であるので、排水中の油性分分解菌の働きも促進されると共に、滞留排水の好気発酵により悪臭の発生を抑制する。   Further, according to the present invention (Claim 9), in the apparatus, since the stirring mechanism is an air aeration mechanism, the action of oil-degrading bacteria in the waste water is promoted, and the generation of malodor by the aerobic fermentation of the accumulated waste water. Suppress.

本発明の構成は上記の通り、食堂排水の油性分除去を、処理対象排水に油吸着粉末を混合し、油分吸着後物質の排除という手段を採用したもので、グリーストラップ装置の貯留処理槽を大型化することなく、油性分を含まない分離排水を放流するもので、環境への影響を抑えた排水処理を実現したものである。   As described above, the configuration of the present invention employs a means for removing oily components from canteen wastewater, mixing oil-adsorbed powder with wastewater to be treated, and removing substances after oil adsorption. The wastewater treatment that does not contain oily components is discharged without increasing the size, and wastewater treatment with reduced environmental impact is realized.

また特に油分吸着粉末(粉体)の供給散布を確実に且つ所望量の供給を自動的に行なうことができたものでものである。   In particular, the oil adsorbed powder (powder) can be supplied and dispersed reliably and automatically in a desired amount.

次に本発明の実施形態について説明する。図1に示した第一の実施形態のグリーストラップ装置は、油吸着粉末散布機構1と、処理槽2で構成され、処理槽2には、入水部3と、攪拌機構部(曝気機構:噴気部21)と、固形分分離機能を果たす取出用網容器4と、出水部5を付設したものである。   Next, an embodiment of the present invention will be described. The grease trap apparatus according to the first embodiment shown in FIG. 1 includes an oil adsorbing powder spraying mechanism 1 and a processing tank 2. The processing tank 2 includes a water inlet 3 and a stirring mechanism (aeration mechanism: fuming air). Part 21), a net container 4 for taking out a solid content separation function, and a water discharge part 5 are provided.

油吸着粉末散布機構1は、容器状の粉末貯留部11と、粉末貯留部の底方に回転駆動によって動作する定量供給部12と、前記定量供給部12と接続されると共に、先端口を処理槽の所定位置に臨ませた搬送部13とで構成される。   The oil adsorbing powder spraying mechanism 1 is connected to a container-shaped powder storage unit 11, a quantitative supply unit 12 that operates by rotational driving at the bottom of the powder storage unit, and the quantitative supply unit 12, and also processes the front end port. It is comprised with the conveyance part 13 which faced the predetermined position of the tank.

粉末貯留部11は、適宜容量の円筒状の容器体111と蓋体112を備え、容器体111の底面113の所定位置(後述する供給口123と対応する位置)に排出口114を形成し、更に前記排出口114の近傍位置に障壁115を設けたものである。   The powder storage unit 11 includes a cylindrical container body 111 and a lid body 112 having an appropriate capacity, and forms a discharge port 114 at a predetermined position (a position corresponding to a supply port 123 described later) on the bottom surface 113 of the container body 111. Further, a barrier 115 is provided in the vicinity of the discharge port 114.

定量供給部12は、回転板121と回転駆動部(モータ)122と、回転駆動部の制御部(図示せず)を備えたもので、回転板121は、容器体111の内底面で回転するように組み込んだもので、外周部分を回転中心部分より一段低い段差に形成すると共に、当該低段部分に供給口123を形成する。   The quantitative supply unit 12 includes a rotating plate 121, a rotation driving unit (motor) 122, and a control unit (not shown) of the rotation driving unit, and the rotating plate 121 rotates on the inner bottom surface of the container body 111. In this way, the outer peripheral portion is formed in a step that is one step lower than the rotation center portion, and the supply port 123 is formed in the low step portion.

尚障壁115は、回転板121の回転に支障が無いように回転板121の直上に設けたもので、特に前記段差に対応する形状で且つ排出口114の位置の回転方向側に設けたものである。   The barrier 115 is provided immediately above the rotating plate 121 so as not to hinder the rotation of the rotating plate 121, and is particularly provided in a shape corresponding to the step and on the rotational direction side of the position of the discharge port 114. is there.

搬送部13は、供給管131と送風機132を備えたもので、供給管131は、前記排出口114に接続され、先端口133を後述する処理槽2の所定位置(沈殿物等の取出用網容器4の上方)に望ませたもので、途中に横管134を接続し、当該横管134を送風機132に接続して送風搬送を実現するようにした。   The transport unit 13 includes a supply pipe 131 and a blower 132. The supply pipe 131 is connected to the discharge port 114, and a front end port 133 is disposed at a predetermined position (a net for taking out precipitates or the like) of the processing tank 2 described later. The horizontal pipe 134 is connected in the middle, and the horizontal pipe 134 is connected to the blower 132 so as to realize blown conveyance.

処理槽2は、通常のグリーストラップ装置と同様の容積の槽体で、エアポンプ6と処理槽2の底面に配置した噴気部(攪拌機構部)21によって空気曝気を行い、処理槽内の排水Bを攪拌するようにしたものである。   The processing tank 2 is a tank body having a volume similar to that of a normal grease trap device, and aeration unit (stirring mechanism unit) 21 disposed on the bottom surface of the air pump 6 and the processing tank 2 performs air aeration to discharge waste water B in the processing tank. Is agitated.

入水部3は、従前の装置と同様で、食堂排水Aの入水管31の出口に網状袋体(夾雑物除去部)32を着脱自在に取り付けたもので、更に網状袋体32を保持する保持部(穴開筒体)33を処理槽2内に配設してなるものである。   The water inlet 3 is the same as the previous device, and has a mesh bag body (contaminant remover) 32 detachably attached to the outlet of the water inlet pipe 31 of the canteen drainage A, and further holds the mesh bag body 32. A portion (perforated cylinder) 33 is disposed in the processing tank 2.

固形分分離機能は、沈殿物等の取出用網容器4によって実現しているもので、前記取出用網容器4は、適宜な網容器体で、処理槽2内に取り出し可能に設置するもので、なるべく前記の噴気部21の位置を避けて配置する。   The solid content separation function is realized by a net container 4 for taking out precipitates and the like, and the net container 4 for taking out is an appropriate net container body and is installed in the processing tank 2 so as to be removable. The position of the fusible portion 21 is avoided as much as possible.

出水部5は、処理槽2内の槽内排水Bから固形分(油分)が除去された油分分離排水Cを外部に放流するもので、処理槽2と接続して出水管51の開口部には適宜なフィルター52を設けておく。   The drainage section 5 discharges the oil separation drainage C from which the solid (oil) has been removed from the tank drainage B in the treatment tank 2 to the outside, and is connected to the treatment tank 2 to the opening of the drain pipe 51. A suitable filter 52 is provided.

上記構成のグリーストラップ装置は、従前どおりレストラン等のように飲食物の調理を行っている厨房からの排水(食堂排水)Aを下水に放流する間に介設して使用されるもので、予め容器体111内に油吸着粉末(市販の一剤タイプの油処理剤であって、油吸着能力を備えたバイオレメディエーション促進剤:例えば数十μmの顆粒で、水中で攪拌すると分散し、水中の油分を吸着し沈殿する商標名「ユトラスエースα」、三菱ガス化学株式会社販売)を、容器体111内に収納しておく。また回転駆動部122の動作制御は予め設定しておく。   The grease trap device having the above-described configuration is used while being drained from the kitchen (dining room drainage) A from the kitchen where food and drink are being cooked as in a restaurant, etc. Oil adsorbed powder in the container body 111 (commercially available one-component type oil treating agent, bioremediation accelerator with oil adsorbing ability: for example, granules of several tens of μm, dispersed when stirred in water, A trade name “Utras Ace α” (sold by Mitsubishi Gas Chemical Co., Ltd.) that adsorbs and precipitates oil is stored in the container body 111. The operation control of the rotation drive unit 122 is set in advance.

而して食堂排水Aは、入水管31から処理槽2内に流入するもので、流入に際して夾雑物除去部32を通過することで食堂排水A中の夾雑物が取り除かれる。この食堂排水Aは、夾雑物の他に油性分も含まれているが、油性分は前記夾雑物除去部32では除去されず、処理槽2内に貯留する排水(槽内排水B)に散在することになる。   Thus, the cafeteria drainage A flows into the treatment tank 2 from the water inlet pipe 31, and the contaminants in the cafeteria drainage A are removed by passing through the contaminant removal unit 32 during the inflow. This canal drainage A contains oily components in addition to contaminants, but the oily components are not removed by the contaminant removal unit 32 and are scattered in the wastewater stored in the treatment tank 2 (tank drainage B). Will do.

そこで回転駆動部122及び送風機132を同時に作動させると、回転板121が回転し、回転板121の供給口123と、排出口114が重なる箇所で粉末貯留部11内の油吸着粉末(粉体)aが下方に落下する。特に障壁115に回転板121で回転方向に運ばれる粉体aが衝突し、粉体aの落下が確実に為される。   Therefore, when the rotation driving unit 122 and the blower 132 are operated simultaneously, the rotating plate 121 rotates, and the oil adsorbed powder (powder) in the powder storage unit 11 at a place where the supply port 123 and the discharge port 114 of the rotating plate 121 overlap. a falls downward. In particular, the powder a carried in the rotation direction by the rotating plate 121 collides with the barrier 115, and the powder a is surely dropped.

そして落下した粉体aは、送風bによって横管134内を搬送され、先端口133から放出され、取出用網容器4に向って供給散布される。   The fallen powder a is conveyed through the horizontal tube 134 by the air b, discharged from the front end port 133, and supplied and dispersed toward the extraction net container 4.

槽内排水Bは、エアポンプ6の作動で、曝気されながら攪拌するので、散布された粉体aは、槽内排水Bと共にかき混ぜられることで、槽内排水Bに含まれる油性分を吸着し、油性分は混濁状態から分離して沈殿物や浮遊物となる。   The tank drainage B is stirred while being aerated by the operation of the air pump 6, so that the dispersed powder a is mixed with the tank drainage B to adsorb the oily component contained in the tank drainage B, The oily component separates from the turbid state and becomes a precipitate or suspended matter.

特に粉体aの供給散布が取出用網容器4に向って為されるので、主として前記の容器4内において油分を吸着した粉体が沈殿物・浮遊物(分離油性分)Dとして容器4内に残ることになる。   In particular, since the supply and dispersion of the powder a is directed toward the extraction net container 4, the powder that has adsorbed oil mainly in the container 4 is deposited in the container 4 as a precipitate / floating matter (separated oily component) D. Will remain.

そして油性分を除去された処理済の槽内排水Bは、出水管51から下水などに放流されるものである。また取出用網容器4に溜まった沈殿物・浮遊物(分離油性分)Dは、容器4を処理槽2から取り出し、廃棄される。   The treated in-tank waste water B from which the oily component has been removed is discharged from the drain pipe 51 into sewage or the like. Further, the sediment / floating matter (separated oil component) D accumulated in the extraction net container 4 is taken out of the processing tank 2 and discarded.

従って例えば食堂開店と当時に油吸着粉末散布機構1の動作スイッチを入れ、回転板121及び送風機132の駆動間隔時間を予め設定しておくと、処理槽2内への粉体aの供給量を決定することができるので、使用箇所の食堂排水Aの排水量、油分の混入割合、処理槽2の容量等を基準として、最適な粉体供給を実現できたものである。   Therefore, for example, when the restaurant is opened and the operation switch of the oil adsorbing powder spraying mechanism 1 is turned on at that time, and the drive interval time of the rotating plate 121 and the blower 132 is set in advance, the amount of powder a supplied into the processing tank 2 is reduced. Since it can be determined, the optimum powder supply can be realized on the basis of the drainage amount of the canteen drainage A at the use location, the mixing ratio of oil, the capacity of the treatment tank 2, and the like.

また本発明装置に油吸着粉末散布機構は、図4に示すような別構造を採用しても良い。図4に例示した油吸着粉末散布機構1aは、粉末貯留部11aをホッパー状に形成し、粉末貯留部11aの内底面に開口部116を設け、当該開口部116の下方に定量供給部12aを接続して設けたものである。   Moreover, you may employ | adopt another structure as shown in FIG. The oil adsorbing powder spreading mechanism 1a illustrated in FIG. 4 has a powder storage part 11a formed in a hopper shape, an opening 116 is provided on the inner bottom surface of the powder storage part 11a, and a quantitative supply part 12a is provided below the opening 116. They are connected.

定量供給部12aは、所謂ロータリーバルブで、筒型弁箱124内に回転作動する柱状の弁本体125を組み込むと共に、弁本体125の外周面に収納凹部126を形成した、弁箱124の下方部分を供給管131と接続してなるものである。他の構成は前記した第一実施形態の油吸着粉末散布機構1と同様である。   The fixed amount supply unit 12a is a so-called rotary valve, and incorporates a columnar valve body 125 that rotates in a cylindrical valve box 124, and has a housing recess 126 formed on the outer peripheral surface of the valve body 125. Is connected to the supply pipe 131. Other configurations are the same as those of the oil adsorbing powder spreading mechanism 1 of the first embodiment described above.

前記の油吸着粉末散布機構1aは、弁本体125を180度回転させると、収納凹部126に存在する粉体aは、供給管131に落下し、同時に作動させる送風機132による送風bで横管134内を搬送され、先端口133から放出され、処理槽2の所定位置に向って供給散布される。   In the oil adsorbing powder spreading mechanism 1a, when the valve body 125 is rotated 180 degrees, the powder a existing in the storage recess 126 falls into the supply pipe 131 and is blown by the blower 132 that is operated simultaneously. The inside is conveyed, discharged from the front end port 133, and supplied and dispersed toward a predetermined position of the processing tank 2.

従って弁本体125の180度の回転動作を、適時な間隔や、処理槽2に付設した水位センサの検知結果に基づいて動作制御を行なうことで、所望量の粉体散布を実現できるものである。   Therefore, a desired amount of powder can be dispersed by controlling the rotation of the valve body 125 based on the timely interval and the detection result of the water level sensor attached to the treatment tank 2. .

また図5には本発明の第二の実施形態を示したもので、この実施形態は、沈殿物・浮遊物(分離油性分)Dの確実な取り出しを実現するために、汲み上げ機構4aを採用したものである。   FIG. 5 shows a second embodiment of the present invention. This embodiment employs a pumping mechanism 4a in order to realize reliable removal of the precipitate / float (separated oil component) D. It is what.

汲み上げ機構4aは、処理槽2の底面近傍或いは適宜な水位位置に汲み上げ口41を備え、処理槽2内の上部に排出口42を設けた汲上管43に、エアポンプ6からの空気放出を行うようにして、エアリフトポンプを構成したもので、排出口42に油を吸着した沈殿物・浮遊物Dを濾過できるフィルター44とフィルター受け皿45を設けてなるものである。   The pumping mechanism 4a has a pumping port 41 in the vicinity of the bottom surface of the processing tank 2 or at an appropriate water level, and discharges air from the air pump 6 to a pumping pipe 43 provided with a discharge port 42 in the upper part of the processing tank 2. Thus, an air lift pump is configured, and a filter 44 and a filter tray 45 that can filter the sediment / floating matter D adsorbing oil to the discharge port 42 are provided.

また出水部5aは、フィルター44で固液分離された排水(処理済排水)Cを受け止めて装置外に放流する出水管51と、前記出水管51と処理槽2との間に設けた濾過膜53で構成される。   Moreover, the water discharge part 5a receives the waste_water | drain (processed waste_water | drain) C solid-liquid-separated by the filter 44, and the drain membrane 51 provided between the said water discharge pipe 51 and the processing tank 2 which discharges | emits out of the apparatus. 53.

上記構成のグリーストラップ装置は、第一実施形態と同様に、従前どおりレストラン等のように飲食物の調理を行っている厨房からの排水(食堂排水)Aを下水に放流する間に介設して使用されるもので、食堂排水Aは、入水管31から処理槽2内に流入し、流入に際して網状袋体32を通過することで食堂排水A中の夾雑物が取り除かれる。   As in the first embodiment, the grease trap apparatus having the above-described configuration is provided while draining water (canteen drainage) A from a kitchen where food and drink are being cooked as in a restaurant, etc., as before. The canteen drainage A flows into the treatment tank 2 from the water inlet pipe 31 and passes through the mesh bag 32 during the inflow to remove impurities in the canteen drainage A.

そして処理槽内排水Bの水位が処理水位(高水位)Hに達すると、油吸着粉末散布機構1が作動して所定量(処理槽2の容積に対応した量:高水位H時の処理槽内排水量に対応した量)の油吸着粉末aを処理槽2内に供給散布する。   When the water level of the waste water B in the treatment tank reaches the treatment water level (high water level) H, the oil adsorbing powder spraying mechanism 1 is activated and a predetermined amount (amount corresponding to the volume of the treatment tank 2: treatment tank at the high water level H). The amount of oil adsorbed powder a) corresponding to the amount of internal wastewater is supplied and dispersed in the treatment tank 2.

同時若しくはそれ以前(排水中の油性分分解菌の働きを促進し、処理槽内排水Bの好気発酵により悪臭の発生を抑制する)からエアポンプ6を作動して処理槽内排水Bを曝気して攪拌する。処理槽内排水Bに散布された油吸着粉末aは、処理槽内排水Bと共にかき混ぜられて、処理槽内排水Bに含まれる油性分を吸着し、油性分は混濁状態から塊状態で分離して沈殿・浮遊する。   At the same time or earlier (accelerating the action of oil-degrading bacteria in the wastewater and suppressing the generation of malodor by aerobic fermentation of the wastewater B in the treatment tank), the air pump 6 is operated to aerate the wastewater B in the treatment tank. And stir. The oil adsorbed powder a sprayed on the waste water B in the treatment tank is stirred together with the waste water B in the treatment tank to adsorb the oily content contained in the waste water B in the treatment tank, and the oily content is separated from the turbid state in a lump state. Precipitate and float.

そこで曝気攪拌を中止し、汲上管43内にエアポンプ6から空気を送り出してエアリフト作用によって沈殿物(分離油性分)Dを、フィルター44上に汲み上げ、固液分離を行なう。   Therefore, aeration and agitation are stopped, air is sent out from the air pump 6 into the pumping pipe 43, and the precipitate (separated oil component) D is pumped up on the filter 44 by the air lift action to perform solid-liquid separation.

分離された固形分(分離油性分)Dは、フィルター44に溜まり、油性分を除去された処理済排水Cは、出水管51から下水などに放流されるものである。同時に濾過膜53で固形分の通過が阻止され、油性分を含まない処理済排水Cのみが通過して出水管51から放流される。   The separated solid content (separated oily content) D is accumulated in the filter 44, and the treated wastewater C from which the oily content has been removed is discharged from the outlet pipe 51 into sewage or the like. At the same time, the filtration membrane 53 prevents solids from passing, and only the treated waste water C that does not contain oily components passes through and is discharged from the drain pipe 51.

更にフィルター44に溜められた分離油性分Dは、そのまま土壌に放置するだけで、生物分解され、自然に帰るものである。特に油吸着粉末aが、バイオレメディエーション促進剤であるから、前記の生物分解も効果的に行なわれることになる。   Furthermore, the separated oily component D stored in the filter 44 is biodegraded simply by leaving it in the soil as it is, and returns naturally. In particular, since the oil adsorbed powder a is a bioremediation promoter, the above-described biodegradation is also effectively performed.

図6は、処理槽2aの他に受入槽7を設け、透過膜53を備えない出水部5aを採用した第三実施形態を示したものである。   FIG. 6 shows a third embodiment in which a receiving tank 7 is provided in addition to the processing tank 2 a and a water discharge part 5 a that does not include the permeable membrane 53 is adopted.

受入槽7は、入水管71と接続し、更に入水管71に夾雑物除去部72を設けると共に、曝気機構を付設し、更に処理槽2aとの間に水門部8を設けたものである。この水門部8は、処理槽2aの水位に応じて処理槽への流入制御をなすようにしたものである。   The receiving tank 7 is connected to the water inlet pipe 71, further provided with a contaminant removing part 72 in the water inlet pipe 71, and provided with an aeration mechanism, and further provided with a sluice part 8 between the processing tank 2a. The sluice part 8 is configured to perform inflow control to the treatment tank according to the water level of the treatment tank 2a.

出水部5aは、汲み上げ機構4aの汲上管43の排出口42、及びフィルター44とフィルター受け皿45を上方に配置したもので、出水管51を連設したものである。   The water discharge section 5a is configured such that the discharge port 42 of the pumping pipe 43 of the pumping mechanism 4a, the filter 44, and the filter tray 45 are disposed above, and the water discharge pipe 51 is provided continuously.

而して前記の第三実施形態も第一実施形態と同様に食堂排水Aの油性分除去を行なうもので、食堂排水Aは、入水管71から受入槽7内に流入するもので、流入に際して夾雑物除去部(網状袋体)72を通過することで食堂排水A中の夾雑物が取り除かれて受入槽7内に一時滞留する。   Thus, the third embodiment also removes the oily content of the canteen drainage A in the same manner as the first embodiment, and the canteen drainage A flows into the receiving tank 7 from the inlet pipe 71. By passing through the foreign matter removing section (reticulated bag) 72, the foreign matter in the canteen drainage A is removed and temporarily stays in the receiving tank 7.

処理槽2aにおいて、所定の低水位Lに至ると水門部8が開き、受入槽7内の夾雑物除去排水Eが、処理槽2a内に流入する。   In the treatment tank 2a, when the predetermined low water level L is reached, the sluice part 8 opens, and the contaminant removal waste water E in the receiving tank 7 flows into the treatment tank 2a.

水門部8は、一定時間又は所定の高水位Hに達すると閉じ、そして処理槽2aにおいては、油吸着粉末散布機構1が作動して所定量の油吸着粉末aが散布され、同時に曝気によって攪拌される。   The sluice unit 8 is closed for a certain time or when a predetermined high water level H is reached, and in the treatment tank 2a, the oil adsorbing powder spraying mechanism 1 is activated to spray a predetermined amount of the oil adsorbing powder a, and at the same time agitated by aeration. Is done.

従って処理槽内排水Bは、散布された油吸着粉末aによって、油性分は混濁状態から分離して塊状で沈殿・浮遊するので、曝気攪拌を中止後、汲上管43でフィルター44に送り込み、フィルター44で固液分離され、油性分を除去された処理済排水Cは、出水管51から下水等に放流される。   Therefore, the waste water B in the treatment tank is separated from the turbid state by the sprayed oil adsorbing powder a, and settles and floats in a lump, so after aeration stirring is stopped, it is sent to the filter 44 through the pumping pipe 43. The treated waste water C that has been subjected to solid-liquid separation at 44 and from which oily components have been removed is discharged from the drain pipe 51 into sewage or the like.

従って前記第三実施形態は、食堂排水Aに変動があったとしても、一旦受入槽7に貯留することができるので、処理槽2aでの油吸着粉末aの散布並びに沈殿物分離を効率的に行うことができるものである。   Therefore, since the third embodiment can be temporarily stored in the receiving tank 7 even if there is a change in the canteen drainage A, it is possible to efficiently disperse the oil adsorbed powder a and separate the precipitate in the processing tank 2a. Is something that can be done.

尚発明は前記の実施形態に限定されるものではなく、最も単純な構成は、例えば図7に例示する第四実施形態のように油吸着粉末散布機構1と、処理槽2bで構成され、処理槽2bには、夾雑物除去用の網状袋体32を備えた入水部3を接続し、攪拌機構部22を内設し、固形分分離機能を果たす網状の仕切り部23を設け、この網状仕切り部23の下流側に出水部5を付設するのみで良く、油分を吸着した沈殿物・浮遊物は、適宜汲み上げたり、生物分解するのみで良い。   The invention is not limited to the above-described embodiment, and the simplest configuration includes an oil adsorbing powder spraying mechanism 1 and a processing tank 2b as in the fourth embodiment illustrated in FIG. The tank 2b is connected to a water inlet 3 having a mesh bag body 32 for removing contaminants, provided with a stirring mechanism 22 and provided with a mesh partition 23 for performing a solid content separation function. It is only necessary to attach the water discharge part 5 to the downstream side of the part 23, and the sediment / floating matter adsorbing the oil may be appropriately pumped up or biodegraded.

本発明の第一実施形態の全体の構成図。The whole block diagram of 1st embodiment of this invention. 同油吸着粉末散布機構の全体の構成図。The whole block diagram of the oil adsorption powder spreading mechanism. 同動作説明図。FIG. 同油吸着粉末散布機構の別例の全体の構成図。The whole block diagram of the other example of the oil adsorption powder distribution mechanism. 本発明の第二実施形態の全体の構成図。The whole block diagram of 2nd embodiment of this invention. 本発明の第三実施形態の全体の構成図。The whole block diagram of 3rd embodiment of this invention. 本発明の第四実施形態の全体の構成図。The whole block diagram of 4th embodiment of this invention.

符号の説明Explanation of symbols

1,1a 油吸着粉末散布機構
11,11a 粉末貯留部
111 容器体
112 蓋体
113 底面
114 排出口
115 障壁
116 開口部
12,12a 定量供給部
121 回転板
122 回転駆動部(モータ)
123 供給口
124 弁箱
125 弁本体
126 収納凹部
13 搬送部
131 供給管
132 送風機
133 先端口
134 横管
2,2a,2b 処理槽
21 噴気部
22 攪拌機構部
23 仕切り部
3 入水部
31 入水管
32,72 網状袋体(夾雑物除去部)
33 保持部(穴開筒体)
4 取出用網容器
4a 汲み上げ機構
41 汲み上げ口
42 排出口
43 汲上管
44 フィルター
45 フィルター受け皿
5,5a 出水部
51,71 出水管
52 フィルター
53 濾過膜
6 エアポンプ
7 受入槽
8 水門部
A 食堂排水
B 処理槽内排水
C 処理済排水(油分分離排水)
D 沈殿物・浮遊物(分離油性分)
E 夾雑物除去排水
a 油吸着粉末(粉体)
b 送風
1, 1a Oil adsorbing powder spraying mechanism 11, 11a powder reservoir
111 Container
112 lid
113 Bottom surface 114 Discharge port 115 Barrier 116 Opening part 12, 12 a Fixed amount supply part 121 Rotating plate 122 Rotation drive part (motor)
123 Supply port 124 Valve box 125 Valve body 126 Storage recess 13 Conveying part 131 Supply pipe 132 Blower 133 Front end port 134 Horizontal pipes 2, 2a, 2b Treatment tank 21 Foaming part 22 Stirring mechanism part 23 Partition part 3 Incoming part 31 Incoming part 32 , 72 Mesh bag (contaminant removal part)
33 Holding part (perforated cylinder)
4 Extraction net container 4a Pumping mechanism 41 Pumping port 42 Discharge port 43 Pumping pipe 44 Filter 45 Filter tray 5, 5a Drain part 51, 71 Drain pipe 52 Filter 53 Filtration membrane 6 Air pump 7 Receiving tank 8 Wastewater in tank C Treated wastewater (oil separation wastewater)
D Precipitate / Float (separated oil)
E Debris removal wastewater a Oil adsorbed powder (powder)
b Blower

Claims (9)

排水路途中に設け、排水中の夾雑物を分離する夾雑物除去機能を備えた入水部、及び夾雑物を除去した貯留排水を攪拌する攪拌機構部、及び固形分を除いて排出する出水部を付設した処理槽と、油性分を吸着して固形分とする油吸着粉末を処理槽上方から、適時散布する油吸着粉末散布機構とで構成してなることを特徴とするグリーストラップ装置。   Provided in the middle of the drainage channel, a water intake part equipped with a contaminant removal function for separating the contaminants in the drainage, a stirring mechanism part for stirring the stored wastewater from which the contaminants have been removed, and a water discharge part that discharges the solids except for the solids A grease trap device comprising: an attached processing tank; and an oil-adsorbing powder spraying mechanism for spraying oil-adsorbed powder that absorbs oily components to form a solid content from above the processing tank. 油吸着粉末散布機構が、容器状の粉末貯留部と、粉末貯留部の底方に回転駆動によって動作する定量供給部と、前記定量供給部と接続されると共に、先端口を処理槽の所定位置に臨ませ、基端を送風機と接続した供給管を備えた搬送部とで構成され、定量供給部と送風機とを適時間隔で連動させてなる請求項1記載のグリーストラップ装置。   The oil-adsorbing powder spraying mechanism is connected to the container-shaped powder storage unit, the quantitative supply unit that operates by rotational driving at the bottom of the powder storage unit, and the fixed-quantity supply unit. The grease trap device according to claim 1, wherein the grease trap device is configured by a conveying unit including a supply pipe having a base end connected to a blower, the fixed supply unit and the blower being interlocked at a timely interval. 定量供給部が、粉末貯留部の内底面に、回転外周近傍に供給口を開設した回転板を設け、粉末貯留部の底面に、前記供給口の通過位置に供給管と接続される排出口を有し、粉末貯留部の底方における前記排出口位置の回転方向側に障壁を設けてなる請求項2記載のグリーストラップ装置。   The fixed amount supply unit is provided with a rotating plate having a supply port in the vicinity of the rotating outer periphery on the inner bottom surface of the powder storage unit, and a discharge port connected to the supply pipe at a position where the supply port passes on the bottom surface of the powder storage unit. The grease trap apparatus according to claim 2, further comprising a barrier provided on a rotation direction side of the discharge port position at the bottom of the powder storage unit. 定量供給部が、ホッパー状の粉末貯留部の内底面に開口部を設け、柱状外周面に収納凹部を形成したロータリーバルブを、前記開口部に収納凹部が臨むように組み込み、開口部反対側の収納凹部に対面する箇所と、供給管とを接続してなる請求項2記載のグリーストラップ装置。   The fixed amount supply unit is equipped with a rotary valve having an opening on the inner bottom surface of the hopper-shaped powder storage unit and a storage recess formed on the columnar outer peripheral surface so that the storage recess faces the opening. The grease trap device according to claim 2, wherein a portion facing the storage recess is connected to the supply pipe. 処理槽内に網板又は透過膜で仕切りを設けて出水部における固形分分離機能を備えさせると共に、油吸着粉末散布機構の供給管先端を、前記仕切り部より入水部側に臨ませてなる請求項2乃至4記載の何れかのグリーストラップ装置。   A partition provided with a mesh plate or a permeable membrane in the treatment tank to provide a solid content separation function in the water discharge part, and a supply pipe tip of the oil adsorbing powder spraying mechanism facing the water inlet part side from the partition part Item 5. The grease trap device according to any one of Items 2 to 4. 処理槽内に沈殿物の取出用網容器を設けて固形分分離機能を備えさせると共に、油吸着粉末散布機構の供給管先端を、前記取出用網容器の上方に臨ませてなる請求項2乃至4記載の何れかのグリーストラップ装置。   A deposit container for removing precipitates is provided in the treatment tank so as to have a solid content separation function, and the tip of the supply pipe of the oil adsorbing powder spraying mechanism faces the upper part of the extractor container. 5. The grease trap device according to any one of 4 above. 処理槽に、貯留槽沈殿物を汲み上げて固形分を分離する汲み上げ機構を設けて固形分分離機能を備えさせてなる請求項2乃至4記載の何れかのグリーストラップ装置。   The grease trap apparatus according to any one of claims 2 to 4, wherein a pumping mechanism for pumping the storage tank deposit to separate the solid content is provided in the processing tank to provide a solid content separation function. 油吸着粉末が、油吸着能力を有するバイオレメディエーション促進剤である請求項1乃至7記載の何れかのグリーストラップ装置。   The grease trap device according to any one of claims 1 to 7, wherein the oil adsorbing powder is a bioremediation accelerator having oil adsorbing ability. 攪拌機構が空気曝気機構である請求項1乃至8記載の何れかのグリーストラップ装置。   9. The grease trap device according to claim 1, wherein the stirring mechanism is an air aeration mechanism.
JP2007328560A 2007-09-19 2007-12-20 Grease trap device Pending JP2009133173A (en)

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JP2014177342A (en) * 2013-03-15 2014-09-25 Cci Corp Powder supply device
JP2018187573A (en) * 2017-05-09 2018-11-29 五一 深町 Drainage treatment method for grease trap and drainage treatment apparatus
US10208210B2 (en) 2014-07-30 2019-02-19 Mitsubishi Materials Corporation Hydrophilic oil repellent and production method of same, surface coating material, coating film, resin composition, oil-water separation filter material, and porous body
US10294125B2 (en) 2014-07-30 2019-05-21 Mitsubishi Materials Corporation Filter medium, method for producing filter medium, water treatment module, and water treatment device
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US10399868B2 (en) 2014-07-30 2019-09-03 Mitsubishi Materials Corporation Oil-water separation apparatus and drainage system
CN112592822A (en) * 2020-12-30 2021-04-02 山东民和生物科技股份有限公司 Treatment system and method for producing biogas by co-fermentation of livestock and poultry breeding waste
CN112850863A (en) * 2019-11-27 2021-05-28 上海凯泉泵业(集团)有限公司 Automatic quantitative dosing and disinfecting device for sewage treatment
CN113896343A (en) * 2021-11-01 2022-01-07 南京一阳环保科技有限公司 Integrated high-concentration wastewater treatment method and treatment assembly line thereof

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014177342A (en) * 2013-03-15 2014-09-25 Cci Corp Powder supply device
US10208210B2 (en) 2014-07-30 2019-02-19 Mitsubishi Materials Corporation Hydrophilic oil repellent and production method of same, surface coating material, coating film, resin composition, oil-water separation filter material, and porous body
US10294125B2 (en) 2014-07-30 2019-05-21 Mitsubishi Materials Corporation Filter medium, method for producing filter medium, water treatment module, and water treatment device
US10364360B2 (en) 2014-07-30 2019-07-30 Mitsubishi Materials Corporation Surface coating material, coating film, and hydrophilic oil repellent member
US10399868B2 (en) 2014-07-30 2019-09-03 Mitsubishi Materials Corporation Oil-water separation apparatus and drainage system
JP2018187573A (en) * 2017-05-09 2018-11-29 五一 深町 Drainage treatment method for grease trap and drainage treatment apparatus
CN112850863A (en) * 2019-11-27 2021-05-28 上海凯泉泵业(集团)有限公司 Automatic quantitative dosing and disinfecting device for sewage treatment
CN112592822A (en) * 2020-12-30 2021-04-02 山东民和生物科技股份有限公司 Treatment system and method for producing biogas by co-fermentation of livestock and poultry breeding waste
CN112592822B (en) * 2020-12-30 2022-01-14 山东民和生物科技股份有限公司 Treatment system and method for producing biogas by co-fermentation of livestock and poultry breeding waste
CN113896343A (en) * 2021-11-01 2022-01-07 南京一阳环保科技有限公司 Integrated high-concentration wastewater treatment method and treatment assembly line thereof

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