JP5444449B2 - Manure purification equipment - Google Patents

Manure purification equipment Download PDF

Info

Publication number
JP5444449B2
JP5444449B2 JP2012281800A JP2012281800A JP5444449B2 JP 5444449 B2 JP5444449 B2 JP 5444449B2 JP 2012281800 A JP2012281800 A JP 2012281800A JP 2012281800 A JP2012281800 A JP 2012281800A JP 5444449 B2 JP5444449 B2 JP 5444449B2
Authority
JP
Japan
Prior art keywords
chamber
treatment liquid
contact
pipe
manure
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
JP2012281800A
Other languages
Japanese (ja)
Other versions
JP2013099744A (en
Inventor
伸次郎 関根
勝 福田
浩三 後藤
Original Assignee
株式会社五光製作所
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 株式会社五光製作所 filed Critical 株式会社五光製作所
Priority to JP2012281800A priority Critical patent/JP5444449B2/en
Publication of JP2013099744A publication Critical patent/JP2013099744A/en
Application granted granted Critical
Publication of JP5444449B2 publication Critical patent/JP5444449B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Description

本発明はふん尿等浄化装置、特に船舶等に用いる海洋汚染を防止するための装置に関するものである。   The present invention relates to an apparatus for purifying manure, and more particularly to an apparatus for preventing marine pollution used in ships and the like.

図2は従来の船舶のふん尿等浄化装置を示し、1は船舶内に設置されたトイレなどからのふん尿等を処理する汚物タンク(汚水タンク)であり、上記汚物タンク1は、液の流れの方向(図中左から右方向)に沿って前処理室2と、接触酸化室3と、沈殿分離室4と、処理液室5とを順次連続した構成のものである。   FIG. 2 shows a conventional apparatus for purifying manure or the like of a ship, 1 is a waste tank (sewage tank) for treating manure or the like from a toilet installed in the ship, and the waste tank 1 has a liquid flow. The pretreatment chamber 2, the contact oxidation chamber 3, the precipitation separation chamber 4, and the treatment liquid chamber 5 are sequentially arranged along the direction (from left to right in the figure).

上記前処理室2は、トイレからのふん尿等を上記前処理室2内に導入する汚物管6と、上記汚物管6からのふん尿等をろ過するろ過器7と、暴気用空気管8とを有し、上記接触酸化室3は、塩化ビニルなどから成る接触酸化材9と、暴気用空気管10とを有し、上記処理液室5は、上記汚物タンク1の外部から上記処理液室5内に塩素剤を注入する消毒薬導入管11と、水位制御器12と、排水管13とよりなる。   The pretreatment chamber 2 includes a filth tube 6 for introducing manure from a toilet into the pretreatment chamber 2, a filter 7 for filtering the urine from the filth tube 6, and an air pipe for storm. The contact oxidation chamber 3 includes a contact oxidant 9 made of vinyl chloride and the like, and an air pipe 10 for turbulence, and the treatment liquid chamber 5 is formed from the outside of the waste tank 1 with the treatment liquid. It comprises a disinfectant introduction pipe 11 for injecting a chlorine agent into the chamber 5, a water level controller 12, and a drain pipe 13.

上記従来の船舶のふん尿等浄化装置においては、トイレからのふん尿等が上記汚物管6から上記前処理室2内に導入されて、大きな固体物は上記ろ過器7により除去され、小さな固体物は上記暴気用空気管8から噴出する気泡の暴気作用により粉砕され、固体と液体に分離され、その処理液が上記接触酸化室3に導入されて、多数のしわを有する接触酸化材9に膜状に形成された好気性微生物により上記処理液中の有機物が無機物に分解され、次に、その処理液が沈殿分離室4に導入されて、処理液中の固体部分を沈殿せしめて、液体部分のみを上記処理液室5に導入して、その処理液を、上記消毒薬導入管11より導入された塩素剤により消毒して貯蔵せしめ、その処理液が上記処理液室5内で所望の量貯まると上記水位制御器12がそれを検知して、上記排出管13を介して海水に自動排出していた。 In the conventional apparatus for purifying manure or the like in the conventional ship, manure or the like from a toilet is introduced into the pretreatment chamber 2 from the filth tube 6, large solids are removed by the filter 7, and small solids are Crushing is carried out by the turbulent action of the bubbles ejected from the aerating air pipe 8 and separated into a solid and a liquid, and the treatment liquid is introduced into the contact oxidation chamber 3 to form a contact oxidant 9 having a large number of wrinkles. The organic matter in the treatment liquid is decomposed into inorganic substances by the aerobic microorganisms formed in the form of a film, and then the treatment liquid is introduced into the precipitation separation chamber 4 to precipitate the solid portion in the treatment liquid. Only the portion is introduced into the treatment liquid chamber 5, and the treatment liquid is sterilized and stored with the chlorine agent introduced from the disinfectant introduction pipe 11, and the treatment liquid is desired in the treatment liquid chamber 5. When the amount is stored, the water level controller 12 Detects, were automatically discharged to sea via the discharge pipe 13.

しかしながら、上記従来の船舶のふん尿等浄化装置では、塩素剤を使用しているため、残留塩素の除去調整管理が難しく、特に、平成22年から実施される国土交通省が発行する「海洋汚染防止設備、海洋汚染防止緊急措置手引書等及び大気汚染防止検査対象設備に関する技術上の基準等に関する省令の一部を改正する省令」に規定された残留塩素量と耐高温性大腸菌群数との両方を基準値以内に除去することが難しいという欠点があった。   However, since the above-mentioned conventional apparatus for purifying manure, etc. uses a chlorinating agent, it is difficult to control the removal and adjustment of residual chlorine. In particular, the “Prevention of Marine Pollution” issued by the Ministry of Land, Infrastructure, Transport and Tourism in 2010. Both the amount of residual chlorine and the number of high-temperature resistant Escherichia coli groups stipulated in `` Ministerial Ordinance Revising Part of Ministerial Ordinance on Technical Standards for Equipment, Marine Pollution Prevention Emergency Measures Manual, and Air Pollution Prevention Inspection Equipment '' There is a drawback that it is difficult to remove within the reference value.

本発明は上記の欠点を無くしたものである。   The present invention eliminates the above disadvantages.

本発明のふん尿等浄化装置は、トイレなどからのふん尿等を浄化処理する汚物タンクと、上記汚物タンク内で浄化処理した処理液を紫外線照射により殺菌処理する殺菌装置と、上記処理した処理液を例えば海水など上記汚物タンク外に放出する手段とよりなることを特徴とする。また、本発明のふん尿等浄化装置は、船舶内に設置されたトイレなどからのふん尿等を浄化処理する汚物タンクと、上記汚物タンク内で浄化処理した処理液を紫外線照射により殺菌処理する殺菌装置と、上記処理した処理液を船外に放出する手段とよりなることを特徴とする。   The apparatus for purifying manure, etc. of the present invention comprises a filth tank for purifying urine from a toilet, etc., a sterilizing apparatus for sterilizing the treatment liquid purified in the filth tank by ultraviolet irradiation, and the treated treatment liquid. For example, it comprises means for discharging out of the filth tank such as seawater. Moreover, the apparatus for purifying manure, etc. of the present invention includes a filth tank for purifying manure or the like from a toilet installed in a ship, and a sterilizing apparatus for sterilizing the treatment liquid purified in the filth tank by ultraviolet irradiation. And means for discharging the treated liquid to the outside of the ship.

また、上記汚物タンクが、接触酸化材と、暴気手段とを備えていることを特徴とする。   Further, the filth tank is provided with a contact oxidant and an air vent means.

また、上記汚物タンクが、液の流れの方向に沿って、1又は複数の接触酸化材と暴気手段とを有する前処理室と、1又は複数の接触酸化材と暴気手段とを有する接触酸化室と、処理液室とよりなり、上記接触酸化室からの処理液を上記殺菌装置に導入し、その処理液を上記処理液室に貯蔵せしめる手段を有することを特徴とする。   Further, the waste tank has a pretreatment chamber having one or more contact oxidizing materials and an air vent means, and one or more contact oxide materials and an air vent means along the liquid flow direction. It comprises an oxidation chamber and a treatment liquid chamber, and has means for introducing the treatment liquid from the contact oxidation chamber into the sterilizer and storing the treatment liquid in the treatment liquid chamber.

また、上記処理液室内の処理液を上記殺菌装置に導入し、その処理液を上記処理液室に貯蔵せしめる手段を更に有する。 The apparatus further includes means for introducing the treatment liquid in the treatment liquid chamber into the sterilizer and storing the treatment liquid in the treatment liquid chamber.

また、本発明のふん尿等浄化装置は、液の流れの方向に沿って、1又は複数の接触酸化材と暴気手段とを有する前処理室と、1又は複数の接触酸化材と暴気手段とを有する接触酸化室と、処理液室とよりなる、トイレなどからのふん尿等を浄化処理する汚物タンクであることを特徴とする。また、本発明のふん尿等浄化装置は、液の流れの方向に沿って、1又は複数の接触酸化材と暴気手段とを有する前処理室と、1又は複数の接触酸化材と暴気手段とを有する接触酸化室と、処理液室とよりなる、船舶内に設置されたトイレなどからのふん尿等を浄化処理する汚物タンクであることを特徴とする。 Further, the apparatus for purifying manure, etc. of the present invention comprises a pretreatment chamber having one or a plurality of contact oxidants and aeration means along the direction of the liquid flow, one or a plurality of contact oxidants and aeration means. And a treatment liquid chamber, and a waste tank for purifying manure from a toilet or the like. Further, the apparatus for purifying manure, etc. of the present invention comprises a pretreatment chamber having one or a plurality of contact oxidants and aeration means along the direction of the liquid flow, one or a plurality of contact oxidants and aeration means. And a treatment liquid chamber, and a waste tank for purifying manure from a toilet or the like installed in a ship.

本発明のふん尿等浄化装置によれば、塩素剤を用いずに大腸菌を殺菌するので、残留塩素が出ず、平成22年から実施される国土交通省が発行する「海洋汚染防止設備、海洋汚染防止緊急措置手引書等及び大気汚染防止検査対象設備に関する技術上の基準等に関する省令の一部を改正する省令」に規定された残留塩素量と耐高温性大腸菌群数との両方を基準値以内に除去することが容易になるという大きな利益がある。   According to the apparatus for purifying manure or the like of the present invention, since E. coli is sterilized without using a chlorinating agent, no residual chlorine is produced. Both the amount of residual chlorine and the number of high-temperature resistant coliforms stipulated in the Ministry Ordinance for Revision of Part of the Ministerial Ordinance on Technical Standards for Equipment for Air Pollution Prevention Inspection etc. There is a great benefit that it is easy to remove.

また、本発明のふん尿等浄化装置によれば、前処理室内において、処理液が接触酸化材の多数のしわに接触することにより、固体と液体の分離を促進せしめ、かつ、接触酸化材に形成された微生物の作用により浄化処理を行なうことにより、TSSを著しく下げることができるなど、処理能力(効率)の向上を図ることができる。   Further, according to the apparatus for purifying manure or the like of the present invention, the treatment liquid contacts a large number of wrinkles of the contact oxidation material in the pretreatment chamber, thereby promoting the separation of the solid and the liquid and forming the contact oxidation material. By performing the purification treatment by the action of the microorganisms, it is possible to improve the processing capacity (efficiency), for example, TSS can be significantly reduced.

また、複数段の接触酸化材を用いることにより、浄化処理の効果を著しく上げることができる。 Moreover, the effect of the purification treatment can be remarkably enhanced by using a plurality of stages of contact oxidizing materials.

また、処理液室の処理液を再度殺菌装置に導入し、その処理液を再度処理液室に貯蔵せしめれば、殺菌効果のばらつきを少なくすることができる。 Further, if the treatment liquid in the treatment liquid chamber is introduced again into the sterilization apparatus and the treatment liquid is stored again in the treatment liquid chamber, the variation in the sterilization effect can be reduced.

図1は本発明のふん尿等浄化装置の説明図である。FIG. 1 is an explanatory view of an apparatus for purifying manure or the like according to the present invention. 図2は従来のふん尿等浄化装置の説明図である。FIG. 2 is an explanatory view of a conventional apparatus for purifying manure or the like.

以下、図面によって本発明の実施例を説明する。   Embodiments of the present invention will be described below with reference to the drawings.

本発明のふん尿等浄化装置は、図1に示すように、船舶内に設置されたトイレなどからのふん尿等を処理する汚物タンク14と殺菌装置15とよりなり、上記汚物タンク14は、流れの方向(図中左から右方向)に沿って、前処理室16と、接触酸化室17と、沈殿分離室18と、処理液室19とを順次連続した構成のものである。   As shown in FIG. 1, the apparatus for purifying manure of the present invention comprises a filth tank 14 and a sterilizer 15 for treating manure or the like from a toilet installed in a ship. A pretreatment chamber 16, a contact oxidation chamber 17, a precipitation separation chamber 18, and a treatment liquid chamber 19 are sequentially arranged along a direction (from left to right in the figure).

上記前処理室16は、汚物タンク14の図中左側壁20およびこれと対峙し、かつ上部と下部が開くと共に、その上端が上記汚物タンク14の天井付近まで延びる仕切板21と、上記仕切板21と対峙し、かつ上部が開き下部が閉じると共に、上端が上記仕切板21の上端より低く形成した仕切壁22とによって形成され、上記前処理室16の天井面に、トイレからのふん尿等を上記前処理室16内に導入する汚物管23と臭気抜管24を設け、また、上記左側壁20と上記仕切板21との間の上部に、上記汚物管23からのふん尿等をろ過するろ過器25と、その下部に、板状の塩化ビニル製などから成る第一の接触酸化材26を配設せしめ、また、上記仕切板21と上記仕切壁22との間に、上記第一の接触酸化材26よりも接触面積が大きい糸状の塩化ビニル製などからなる第二の接触酸化材27を配設せしめると共に、上記第一の接触酸化材26と第二の接触酸化材27の下方位置に、上記汚物タンク14の外部に設けたブロワ28にエアレーションパイプ29を介して接続され、かつ小穴を長手方向に多数配設した前後方向に伸びる暴気用空気管30を設ける。   The pretreatment chamber 16 includes a partition plate 21 facing the left side wall 20 of the waste tank 14 in the figure and the upper and lower portions thereof, and having an upper end extending to the vicinity of the ceiling of the waste tank 14, and the partition plate 21 is formed with a partition wall 22 having an upper portion opened and a lower portion closed, and an upper end formed lower than the upper end of the partition plate 21, and a manure from a toilet was placed on the ceiling surface of the pretreatment chamber 16. A filter for providing a filth tube 23 and an odor venting tube 24 to be introduced into the pretreatment chamber 16, and filtering manure from the filth tube 23 at the upper part between the left side wall 20 and the partition plate 21. 25, and a first contact oxidation material 26 made of a plate-like vinyl chloride or the like is disposed at the lower portion thereof, and the first contact oxidation is performed between the partition plate 21 and the partition wall 22. More contact area than material 26 A second contact oxidant 27 made of a thread-like vinyl chloride or the like is disposed, and at a position below the first contact oxidant 26 and the second contact oxidant 27 and outside the waste tank 14. A blower air pipe 30 is provided which is connected to the provided blower 28 via an aeration pipe 29 and which extends in the front-rear direction and includes a large number of small holes in the longitudinal direction.

上記接触酸化室17は、上記仕切壁22およびこれと対峙し、かつ上部と下部とが開くと共に、その上端が上記汚物タンク14の天井付近まで延びる仕切板31と、上記仕切板31と対峙し、かつ上部と下部が開くと共に、その上端が上記汚物タンク14の天井付近まで延びる仕切板32と、上記仕切板32と対峙し、かつ上部が開き下部が閉じると共に、上端が上記仕切壁22の上端より低く形成した仕切壁33とによって形成され、上記仕切壁22と上記仕切板31との間に上記第二の接触酸化材27よりも接触面積の大きいセラミックス製の第三の接触酸化材34を配設せしめると共に、上記第三の接触酸化材34の下方位置に、汚物タンク14の外部に設けたブロワ28にエアレーションパイプ29を介して接続され、かつ小穴を長手方向に多数配設した前後方向に伸びる暴気用空気管35を設ける。   The contact oxidation chamber 17 is opposed to the partition wall 22 and the partition plate 31 which is open at the top and bottom and whose upper end extends to the vicinity of the ceiling of the filth tank 14 and the partition plate 31. The upper and lower portions open, and the upper end of the partition plate 32 extends to the vicinity of the ceiling of the filth tank 14 and the partition plate 32. The upper portion opens, the lower portion closes, and the upper end of the partition wall 22 A third contact oxidant 34 made of a ceramic is formed by a partition wall 33 formed lower than the upper end and has a larger contact area than the second contact oxidant 27 between the partition wall 22 and the partition plate 31. Is connected to a blower 28 provided outside the filth tank 14 via an aeration pipe 29 at a position below the third contact oxidant 34 and has a small hole. Providing aeration air pipe 35 extending in the longitudinal direction and arranged in plural numbers in the direction.

上記沈殿分離室18は、上記仕切壁33およびこれと対峙し、かつ上部と下部が開くと共に、その上端が上記汚物タンク14の天井付近まで延びる仕切板36と、上記仕切板36に対峙し、かつ上部が開き下部が閉じると共に、その上端が上記汚物タンク14の天井付近まで延びる仕切壁37とよって形成され、上記仕切壁37の上方で、かつ上記仕切壁33の上端より低い位置に、上記沈殿分離室18内の処理液を上記殺菌装置15に導入する導入配管38を接続せしめる。   The sedimentation separation chamber 18 is opposed to the partition wall 33 and the partition plate 36 which is open at the top and bottom and whose upper end extends to the vicinity of the ceiling of the filth tank 14, and the partition plate 36. The upper portion is opened and the lower portion is closed, and the upper end thereof is formed by a partition wall 37 extending to the vicinity of the ceiling of the filth tank 14, and is located above the partition wall 37 and lower than the upper end of the partition wall 33. An introduction pipe 38 for introducing the processing liquid in the precipitation separation chamber 18 into the sterilizer 15 is connected.

上記殺菌装置15は、上記汚物タンク14の外部に設けた紫外線照射装置39を有する殺菌室40によって形成され、その入口に上記導入配管38を接続せしめ、出口に上記殺菌室15の処理液を上記処理液室19に排出するための排出配管41を接続せしめる。   The sterilizer 15 is formed by a sterilization chamber 40 having an ultraviolet irradiation device 39 provided outside the filth tank 14, the inlet pipe 38 is connected to the inlet, and the treatment liquid of the sterilizer 15 is connected to the outlet. A discharge pipe 41 for discharging to the processing liquid chamber 19 is connected.

上記処理液室19は、上記仕切壁37および汚物タンク14の図中右側壁42によって形成され、上記処理液室19内に水位制御器43を設け、また、上記右側壁42の、上記導入配管38が上記沈殿分離室18に接続された位置より低い位置に、上記排出配管44を接続せしめる。   The treatment liquid chamber 19 is formed by the partition wall 37 and the right side wall 42 in the figure of the filth tank 14. A water level controller 43 is provided in the treatment liquid chamber 19, and the introduction pipe of the right side wall 42 is provided. The discharge pipe 44 is connected to a position where 38 is lower than the position where the precipitation separation chamber 18 is connected.

また、上記右側壁42の、上記排出配管41接続口より下方に配管44を設け、その他端を循環ポンプ45を介して殺菌室40の入口側に接続せしめ、上記処理液室19内の処理液を、再度、上記殺菌装置15に導入せしめ、その処理液を上記処理液室19内に貯蔵せしめる。   Further, a pipe 44 is provided below the connection port of the discharge pipe 41 on the right side wall 42, and the other end is connected to the inlet side of the sterilization chamber 40 via the circulation pump 45, so that the processing liquid in the processing liquid chamber 19 is connected. Is again introduced into the sterilization apparatus 15 and the processing liquid is stored in the processing liquid chamber 19.

また、上記右側壁42の、上記配管44接続口より下方に処理水配管46を設ける。 Further, a treated water pipe 46 is provided below the right side wall 42 from the pipe 44 connection port.

また、上記処理液室19の天井面には臭気抜管47を設け、上記処理液室19の上記右側壁42上部にオーバフロー管48を設ける。   An odor vent pipe 47 is provided on the ceiling surface of the processing liquid chamber 19, and an overflow pipe 48 is provided on the right side wall 42 of the processing liquid chamber 19.

上記前処理室16、上記接触酸化室17、上記沈殿分離室18の各底部には、常時閉の排出弁49、50、51が設けられ、また、上記排出配管46には、常時開の排出弁52が設けられ、これが連結管53および常時開の弁54を介して排出ポンプ55に接続され、上記排出ポンプ55の出力側には、海水への排出用の排水管56が接続されている。   At the bottoms of the pretreatment chamber 16, the contact oxidation chamber 17, and the precipitation separation chamber 18, normally closed discharge valves 49, 50, 51 are provided, and the discharge pipe 46 has a normally open discharge. A valve 52 is provided, which is connected to a discharge pump 55 via a connecting pipe 53 and a normally open valve 54, and a drain pipe 56 for discharging to seawater is connected to the output side of the discharge pump 55. .

また、上記連結管53には上記弁54と流れ方向の反対位置に上記常時閉の弁57が設けられ、これが海水導入用の導入管58に接続されている。   The connecting pipe 53 is provided with the normally closed valve 57 at a position opposite to the valve 54 in the flow direction, and this is connected to an introduction pipe 58 for introducing seawater.

本発明のふん尿等浄化装置は上記のような構成であるから、トイレからのふん尿等が上記汚物管23から上記前処理室16内に導入され、大きな固体物は上記ろ過器25により除去され、上記ろ過された処理液は、エアーブローによる粉砕と、上記第一の接触酸化材26の多数のしわに接触することにより、固体と液体の分離が促進され、かつ、上記第一の接触酸化材26に膜状に形成された好気性微生物の作用により分解処理が行なわれ、さらに、その処理液を糸状の塩化ビニル製の第二の接触酸化材27に接触せしめることにより分解処理を進め、固液分離を促進せしめる。   Since the apparatus for purifying manure, etc. of the present invention is configured as described above, manure or the like from a toilet is introduced into the pretreatment chamber 16 from the waste pipe 23, and large solids are removed by the filter 25. The filtered treatment liquid is pulverized by air blow and brought into contact with a large number of wrinkles of the first contact oxidant 26 to promote separation of solid and liquid, and the first contact oxidant 26 is decomposed by the action of aerobic microorganisms formed in a film form, and the decomposition liquid is further brought into contact with the second contact oxidizing material 27 made of vinyl chloride to bring about the decomposition process. Promote liquid separation.

上記前処理室16の処理液は上記接触酸化室17に導入され、上記第一、第二の接触酸化材よりも接触面積の多い接触酸化材で微生物処理の効率をアップせしめ、その後、沈殿分離室18に導入されて、上記処理液の液体部分のみが上記導入配管38を介して殺菌装置15に導入され、紫外線が照射されることにより大腸菌が死滅し、その処理液は上記処理液室19内に貯蔵される。 The treatment liquid in the pretreatment chamber 16 is introduced into the contact oxidation chamber 17 to increase the efficiency of microbial treatment with a contact oxidant having a larger contact area than the first and second contact oxidants, and then precipitate separation. After being introduced into the chamber 18, only the liquid portion of the treatment liquid is introduced into the sterilizer 15 through the introduction pipe 38, and E. coli is killed by irradiation with ultraviolet rays, and the treatment liquid is treated with the treatment liquid chamber 19. Stored within.

また、上記処理液室19内の処理液は上記配管44、循環ポンプ45を介して、再度上記殺菌装置15に導入され、同様に紫外線が照射されることのより大腸菌が死滅し、その処理液は上記処理室19内に貯蔵される。 Further, the processing liquid in the processing liquid chamber 19 is again introduced into the sterilizer 15 through the pipe 44 and the circulation pump 45, and similarly, the E. coli is killed by being irradiated with ultraviolet rays. Is stored in the processing chamber 19.

上記処理液室19内の処理液は、上記処理液室19内で所望の量貯まると上記水位制御器43がそれを検知して、汚物排出ポンプ55により海水に自動排出される。 When a desired amount of the processing liquid in the processing liquid chamber 19 is stored in the processing liquid chamber 19, the water level controller 43 detects it and is automatically discharged to seawater by the filth discharge pump 55.

本発明のふん尿等浄化装置によれば、前処理室16内において、処理液が接触酸化材の多数のしわに接触することにより、固体と液体の分離を促進せしめ、かつ、接触酸化材に形成された微生物の作用により浄化処理を行なうことにより、TSSを著しく下げることができるなど、処理能力(効率)の向上を図ることができるという大きな利益がある。   According to the apparatus for purifying manure or the like of the present invention, the treatment liquid contacts a large number of wrinkles of the contact oxidant in the pretreatment chamber 16, thereby promoting the separation of the solid and the liquid and forming the contact oxidant. There is a great advantage that the treatment capacity (efficiency) can be improved, for example, TSS can be remarkably lowered by performing the purification treatment by the action of the microorganisms.

また、三段階の接触酸化材を用いることで、微生物処理の効果を著しく上げることができる。   Moreover, the effect of microorganism treatment can be remarkably improved by using a three-stage contact oxidizing material.

また、塩素剤を用いずに大腸菌を殺菌するので、残留塩素が出ず、平成22年から実施される国土交通省が発行する「海洋汚染防止設備、海洋汚染防止緊急措置手引書等及び大気汚染防止検査対象設備に関する技術上の基準等に関する省令の一部を改正する省令」に規定された残留塩素量と耐高温性大腸菌群数との両方を基準値以内に除去することが容易になる。 In addition, since Escherichia coli is sterilized without using a chlorinating agent, residual chlorine does not come out and issued by the Ministry of Land, Infrastructure, Transport and Tourism "Marine pollution prevention equipment, marine pollution prevention emergency measures manuals etc." It becomes easy to remove both the amount of residual chlorine and the number of high-temperature resistant coliforms specified in the “Ministerial Ordinance Revising a Part of the Ordinance on Technical Standards for Facilities to be Prevented and Inspected” within the standard value.

また、上記処理液室19内の処理液を再度殺菌装置15に循環することにより、殺菌効果のばらつきを少なくすることができる。 Further, by circulating the treatment liquid in the treatment liquid chamber 19 to the sterilization apparatus 15 again, the variation in the sterilization effect can be reduced.

本願発明はディスポーザ廃水などの生活液体廃棄物においても適用できる。 The present invention can also be applied to domestic liquid waste such as disposer wastewater.

1 汚物タンク
2 前処理室
3 接触酸化室
4 沈殿分離室
5 処理液室
6 汚物管
7 ろ過器
8 暴気用空気管
9 接触酸化材
10 暴気用空気管
11 消毒薬導入管
12 水位制御器
13 排水管
14 汚物タンク
15 殺菌装置
16 前処理室
17 接触酸化室
18 沈殿分離室
19 処理液室
20 左側壁
21 仕切板
22 仕切壁
23 汚物管
24 臭気抜管
25 ろ過器
26 接触酸化材
27 接触酸化材
28 ブロワ
29 エアレーションパイプ
30 暴気用空気管
31 仕切板
32 仕切板
33 仕切壁
34 接触酸化材
35 暴気用空気管
36 仕切板
37 仕切壁
38 導入配管
39 紫外線照射装置
40 殺菌室
41 排出配管
42 右側壁
43 水位制御器
44 配管
45 循環ポンプ
46 処理水配管
47 臭気抜管
48 オーバーフロー管
49 弁
50 弁
51 弁
52 弁
53 連結管
54 弁
55 排出ポンプ
56 排水管
57 弁
58 導入管
DESCRIPTION OF SYMBOLS 1 Dirty tank 2 Pretreatment chamber 3 Contact oxidation chamber 4 Precipitation separation chamber 5 Treatment liquid chamber 6 Filtrate tube 7 Filter 8 Air vent tube 9 Contact oxidizer 10 Air vent tube 11 Disinfectant introduction tube 12 Water level controller 13 Drainage pipe 14 Soil tank 15 Sterilizer 16 Pretreatment chamber 17 Contact oxidation chamber 18 Precipitation separation chamber 19 Treatment liquid chamber 20 Left side wall 21 Partition plate 22 Partition wall 23 Soil tube 24 Odor removal tube 25 Filter 26 Contact oxidation material 27 Contact oxidation Material 28 Blower 29 Aeration pipe 30 Air pipe 31 for aeration 31 Partition plate 32 Partition 33 Partition wall 34 Oxidizing material 35 Air pipe 36 for aeration 36 Partition wall 38 Introductory piping 39 Ultraviolet irradiation device 40 Sterilization chamber 41 Exhaust piping 42 Right side wall 43 Water level controller 44 Pipe 45 Circulating pump 46 Treated water pipe 47 Odor removal pipe 48 Overflow pipe 49 Valve 50 Valve 51 Valve 52 Valve 53 Connecting pipe 4 valve 55 discharge pump 56 drain pipe 57 valve 58 inlet tube

Claims (1)

船舶内に設置されたトイレなどからのふん尿等を浄化処理する汚物タンクと、上記汚物タンク内で浄化処理した処理液を紫外線照射により殺菌処理する殺菌装置と、上記処理した処理液を船外に放出する手段とよりなり、
上記汚物タンクが、液の流れの方向に沿って、前処理室と、接触酸化室と、処理液室とよりなり、
上記接触酸化室からの処理液を上記殺菌装置に導入し、その処理液を上記処理液室に貯蔵せしめる手段を有し、
上記処理液室内の処理液を上記殺菌装置に導入し、その処理液を上記処理液室に貯蔵せしめる手段を更に有することを特徴とするふん尿等浄化装置。
A filth tank that purifies manure from toilets installed in the ship, a sterilizer that sterilizes the treatment liquid purified in the filth tank by UV irradiation, and the treated liquid outside the ship. With the means to release,
The filth tank is composed of a pretreatment chamber, a contact oxidation chamber, and a treatment liquid chamber along the liquid flow direction,
Means for introducing the treatment liquid from the contact oxidation chamber into the sterilizer and storing the treatment liquid in the treatment liquid chamber;
An apparatus for purifying manure or the like, further comprising means for introducing the treatment liquid in the treatment liquid chamber into the sterilizer and storing the treatment liquid in the treatment liquid chamber.
JP2012281800A 2012-12-25 2012-12-25 Manure purification equipment Active JP5444449B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2012281800A JP5444449B2 (en) 2012-12-25 2012-12-25 Manure purification equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2012281800A JP5444449B2 (en) 2012-12-25 2012-12-25 Manure purification equipment

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP2009279948A Division JP5171800B2 (en) 2009-12-09 2009-12-09 Manure purification equipment

Publications (2)

Publication Number Publication Date
JP2013099744A JP2013099744A (en) 2013-05-23
JP5444449B2 true JP5444449B2 (en) 2014-03-19

Family

ID=48620937

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2012281800A Active JP5444449B2 (en) 2012-12-25 2012-12-25 Manure purification equipment

Country Status (1)

Country Link
JP (1) JP5444449B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7028640B2 (en) * 2017-12-28 2022-03-02 ニシム電子工業株式会社 Bio toilet system

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3425673B2 (en) * 1992-06-01 2003-07-14 財団法人鉄道総合技術研究所 Vehicle toilet equipment
JPH07214053A (en) * 1994-02-07 1995-08-15 Nippondenso Co Ltd Water purifier
JPH1150509A (en) * 1997-08-04 1999-02-23 Nippon Light Metal Co Ltd Treated-water-recycling-type flush toilet with waste water treatment vessel
FI20010628A (en) * 2001-03-27 2002-09-28 Evac Int Oy Device for cleaning waste
US7211187B2 (en) * 2004-10-29 2007-05-01 Steven Lumbert Mobile or stationary modular self-contained dehydration toilet, dehydration engine, and gray water recovery system
JP4589203B2 (en) * 2005-08-26 2010-12-01 株式会社五光製作所 Liquid waste treatment equipment for ship life

Also Published As

Publication number Publication date
JP2013099744A (en) 2013-05-23

Similar Documents

Publication Publication Date Title
JP3204678U (en) Domestic sewage treatment equipment
KR100938463B1 (en) Biochemical sewage treatment system for marine use
KR101226547B1 (en) Sewage treatment system for marine use
KR101638970B1 (en) Apparatus for sewage treatment of ship using moving bed bio reactor
KR102054625B1 (en) Waste water treatment apparatus
KR101217165B1 (en) System and method of natural flow-type rainwater treatment using non-motorized early rainwater exclusion device
JP5171800B2 (en) Manure purification equipment
KR100789955B1 (en) High density sludge and waste water treatment apparatus
KR101210536B1 (en) Sewage treat device for marine use
JP5444449B2 (en) Manure purification equipment
KR20140103609A (en) Apparatus for treating sewage in ship and fish farm
CN209178185U (en) A kind of anaerobism, aerobic, stripping reflux sewage-treatment plant
CN108423883B (en) Method and device for degrading and mineralizing quinolone antibiotics by hydroxyl radicals
KR101162150B1 (en) Waste food treating apparatus including bod removing device
KR101671199B1 (en) Apparatus for on-site treating night soil in vessels
CN108585285A (en) The processing system and its processing method of antibiotic in hydroxyl radical free radical mineralized drinking water
JP2007054789A (en) Apparatus for treating daily liquid waste material of vessel
CN209974525U (en) System for black and odorous waste water based on microorganism and ultraviolet sterilization
CN113860649A (en) Treatment equipment and treatment process for domestic sewage
RU2355648C1 (en) Drinking water preparation plant
KR100469317B1 (en) System for Advanced Wastewater Treatment using ozone
CN206244587U (en) Compact high efficient biochemistry ozone oxidation sewage treatment unit
CN105347630B (en) A kind of MBR embrane methods marine domestic sewage processing system
KR102437141B1 (en) Apparatus for separating solid and liquid using micro-bubble and System for waste water treatment using micro-bubble
RU156852U1 (en) MOBILE WATER TREATMENT STATION

Legal Events

Date Code Title Description
TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20131129

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20131220

R150 Certificate of patent or registration of utility model

Ref document number: 5444449

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250