JPH08226625A - Mixed combustion device for waste edible oil - Google Patents

Mixed combustion device for waste edible oil

Info

Publication number
JPH08226625A
JPH08226625A JP7059847A JP5984795A JPH08226625A JP H08226625 A JPH08226625 A JP H08226625A JP 7059847 A JP7059847 A JP 7059847A JP 5984795 A JP5984795 A JP 5984795A JP H08226625 A JPH08226625 A JP H08226625A
Authority
JP
Japan
Prior art keywords
oil
waste oil
waste
edible oil
tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP7059847A
Other languages
Japanese (ja)
Other versions
JP2756927B2 (en
Inventor
Yutaka Sasaki
豊 佐々木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
MITSUI KANKO KAIHATSU KK
Original Assignee
MITSUI KANKO KAIHATSU KK
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 MITSUI KANKO KAIHATSU KK filed Critical MITSUI KANKO KAIHATSU KK
Priority to JP7059847A priority Critical patent/JP2756927B2/en
Priority to PCT/JP1995/002710 priority patent/WO1996026394A1/en
Publication of JPH08226625A publication Critical patent/JPH08226625A/en
Application granted granted Critical
Publication of JP2756927B2 publication Critical patent/JP2756927B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00Feeding or distributing other fuel to combustion apparatus
    • F23K5/02Liquid fuel
    • F23K5/08Preparation of fuel
    • F23K5/10Mixing with other fluids
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/05Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste oils

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Filtration Of Liquid (AREA)
  • Combustion Of Fluid Fuel (AREA)

Abstract

PURPOSE: To permit the reutilization of used waste edible oil effectively as the fuel resource for a boiler and the like by a method wherein the proper amount of used waste edible oil in a reserving tank is mixed into fuel oil. CONSTITUTION: A mixed fuel combustion device for waste edible oil 11 is provided with a heavy oil supplying system 12, supplying heavy oil to a burner 111 from a service tank, and a waste oil supplying system 13, supplying waste edible oil to the burner 14 from a waste oil reserving tank 21, reserving used waste edible oil, while these oil supplying series 12, 13 are joined before a strainer 20 to mix the heavy oil and the waste edible oil. The mixing ratio between the heavy oil and the waste edible oil is specified so that 30% of waste edible oil is mixed into 70% of A-heavy oil, for example. The heavy oil and the waste edible oil are transferred by variable constant flow rate pumps 15, 16 provided in respective series 12, 13. Comparatively big foreign matters, mixed into the waste edible oil, are removed in the stage of throwing by a filter plate provided at the inlet port of the waste oil. According to this method, the used edible oil can be reutilized effectively as fuel resource for the boiler and the like.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は食用廃油混焼装置に係
り、特にボイラ等の燃料油に混合し燃焼させることによ
り食用廃油を処分する技術に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an edible waste oil mixing and burning apparatus, and more particularly to a technique for disposing of edible waste oil by mixing with fuel oil such as a boiler and burning it.

【0002】[0002]

【従来の技術】ホテルやレストラン等の厨房施設におい
ては、例えばてんぷらや揚げ物等、様々な調理に食用油
が使用され、使用後不要となった多量の食用油が排出さ
れる。このような食用廃油は従来、廃油処理業者によっ
て回収され、廃棄物として処分されている。
2. Description of the Related Art In kitchen facilities such as hotels and restaurants, edible oil is used for various cooking such as tempura and fried food, and a large amount of edible oil is discharged after use. Such edible waste oil is conventionally collected by a waste oil processing company and disposed of as waste.

【0003】一方、工業用鉱油の廃油については、例え
ばボイラ等の燃料として再利用する技術が近時提案され
ている。例えば特開昭52−34577号は、廃油を浄
化した後、熱源として再利用する装置に関するもので、
図10に示すように、貯留タンク1内の廃油を、沈澱分
離槽2,3および濾過槽4に順次導いて、含まれている
切屑や鋸屑等の金属その他の固形夾雑物を取り除き、同
時に水や石鹸分等を分離する。さらに濾過槽4を通過し
た廃油を、貯留タンク5を経て、ボイラ等の高熱排気を
通す別の配管7を設置した湯槽6内の配管8に導き、こ
の湯槽6で浄化後の廃油を加熱し、その粘度を低下させ
て流動性を増した後、バーナ9に導いて噴射燃焼させ
る。
On the other hand, for waste oil of industrial mineral oil, a technique of reusing it as fuel for boilers has been proposed recently. For example, JP-A-52-34577 relates to a device for purifying waste oil and then reusing it as a heat source.
As shown in FIG. 10, the waste oil in the storage tank 1 is sequentially introduced into the precipitation separation tanks 2 and 3 and the filtration tank 4 to remove the contained metal such as chips and sawdust and other solid contaminants, and at the same time to remove water. Separate soap and soap. Further, the waste oil that has passed through the filtration tank 4 is guided to a pipe 8 in a hot water tank 6 in which another pipe 7 for passing high-temperature exhaust gas such as a boiler is installed through a storage tank 5, and the waste oil after purification is heated in the hot water tank 6. After reducing its viscosity to increase its fluidity, it is led to the burner 9 to be injected and burned.

【0004】[0004]

【発明が解決しようとする課題】ところで、従来から行
われている食用廃油の処分には、廃油の輸送コストや処
理コストから、専用の設備を備えた処理業者に依頼する
場合であっても、相当の費用を要し、特に業務上多量の
食用油を日常的に使用する大規模なホテルやレストラ
ン、料理店等にとって、廃油の処分に要する経済的負担
は無視することが出来ないものとなっている。さらに、
かかる廃油は河川や湖沼、海洋の水質を汚濁し環境破壊
の原因ともなるから、環境保全の観点からも新たな処理
システムの提供が望まれる。
By the way, in the conventional disposal of edible waste oil, even if a processing company equipped with a dedicated facility is requested from the viewpoint of the transportation cost and processing cost of the waste oil, It costs a considerable amount of money, and especially for large-scale hotels, restaurants, restaurants, etc. that use a large amount of cooking oil on a daily basis, the financial burden of disposing of waste oil cannot be ignored. ing. further,
Since such waste oil pollutes the water quality of rivers, lakes and marshes and causes environmental damage, it is desired to provide a new treatment system from the viewpoint of environmental conservation.

【0005】一方、特開昭52−34577号は、廃油
をボイラ等で燃焼させることで、廃油の処分を行うと同
時に、燃料資源としての活用をも図るものであるが、か
かる装置には次のような問題があり、未だ改良の余地を
残している。すなわち、特開昭52−34577号の装
置は、バーナからの噴射燃焼を可能とするために、廃油
中に含まれる夾雑物の濾過を行っているが、濾過網を濾
過槽内に水平に配設した構造をとっている。このため、
濾過された夾雑物はすべて濾過網上に堆積することとな
り、濾過網が目詰まりを起こし易く、夾雑物の除去や濾
過網の交換等、頻繁なメンテナンスが必要となる。
On the other hand, Japanese Patent Laid-Open No. 34577/52 attempts to dispose of waste oil by burning the waste oil in a boiler or the like and at the same time to utilize it as a fuel resource. However, there is still room for improvement. That is, the device of JP-A-52-34577 filters impurities contained in the waste oil in order to enable injection combustion from the burner, but the filter net is horizontally arranged in the filter tank. The structure is set up. For this reason,
All the filtered impurities will be deposited on the filter net, and the filter net is likely to be clogged, and frequent maintenance such as removal of contaminants and replacement of the filter net is required.

【0006】また、この装置では、バーナからの噴射を
容易にするためにバーナ前段で廃油を加熱しているもの
の、廃油を浄化する沈澱分離槽や濾過槽は加熱手段を一
切備えていない。このため、特に廃油の温度が低下する
冬期間や寒冷地においては、粘度の増大および流動性の
低下に伴って、夾雑物の沈澱や濾過が難くなり、沈澱槽
や濾過槽における廃油の浄化能力が低下してしまう。ま
た残留夾雑物の多い廃油が沈澱槽から濾過槽に流入する
こととなれば、濾過槽の負担が増大し、前記濾過網の配
設構造と相俟って、濾過網の頻繁な清掃等が必要とな
る。さらにこの装置は、廃油タンク、沈澱槽(二槽)、
濾過槽、浄化油貯留タンク、並びに湯槽をそれぞれ別個
に形成した構造をとるから、装置が大型化し、広い設置
スペースが必要となるとの問題もある。
Further, in this apparatus, the waste oil is heated in the preceding stage of the burner in order to facilitate the injection from the burner, but the precipitation separation tank and the filtration tank for purifying the waste oil are not equipped with any heating means. Therefore, especially in winter and cold regions where the temperature of the waste oil decreases, it becomes difficult to precipitate and filter the contaminants due to the increase in viscosity and the decrease in fluidity, and the ability to purify the waste oil in the precipitation tank and the filtration tank is increased. Will decrease. Further, if waste oil with a large amount of residual contaminants flows into the filter tank from the settling tank, the load on the filter tank increases, and, in combination with the arrangement structure of the filter net, frequent cleaning of the filter net is not possible. Will be needed. In addition, this equipment is a waste oil tank, settling tank (two tanks),
Since the filter tank, the purified oil storage tank, and the hot water tank are separately formed, the device becomes large and a large installation space is required.

【0007】そこで本発明の目的は、第一に廃油、特に
食用廃油の処分とその有効な再利用を図ることにあり、
第二にその再利用に好適な装置構造を得ることにある。
Therefore, an object of the present invention is, firstly, to dispose of waste oil, particularly edible waste oil, and to effectively reuse it.
The second is to obtain a device structure suitable for reuse.

【0008】[0008]

【課題を解決するための手段】前記目的を達成して課題
を解決するため、本発明に係る食用廃油混焼装置は、燃
料油をノズルから噴射し燃焼させる燃焼器と、該燃焼器
に対して燃料油を供給する燃料油供給手段と、使用済み
の食用廃油を貯留する貯留槽と、該貯留槽内の食用廃油
を前記燃料油に対して適宜量混合する食用廃油混合手段
とを備えている。また、前記貯留槽は、食用廃油を投入
する廃油投入口と、食用廃油を排出する廃油排出口とを
備え、該廃油投入口と廃油排出口との間に、槽底から所
定の高さ寸法で起立する堰壁および該堰壁の頂上部に立
設したストレーナからなる隔壁を設け、さらに熱媒の貫
流により貯留廃油を加熱する熱配管を槽内に配設する場
合がある。
In order to achieve the above object and solve the problems, an edible waste oil mixed combustion apparatus according to the present invention is provided with a combustor for injecting fuel oil from a nozzle for combustion and a combustor for the combustor. A fuel oil supply means for supplying fuel oil, a storage tank for storing used edible waste oil, and an edible waste oil mixing means for appropriately mixing the edible waste oil in the storage tank with the fuel oil are provided. . Further, the storage tank includes a waste oil input port for inputting edible waste oil and a waste oil discharge port for discharging edible waste oil, and a predetermined height dimension from the bottom of the tank between the waste oil input port and the waste oil discharge port. In some cases, a partition wall including a weir wall standing upright and a strainer standing on the top of the weir wall is provided, and a heat pipe for heating the stored waste oil by the flow of the heat medium is provided in the tank.

【0009】[0009]

【作用】本発明に係る食用廃油混焼装置では、燃料油供
給手段により燃焼器に対して燃料油を供給する一方、該
燃料油に対して、食用廃油混合手段により食用廃油を混
合する。混合した廃油は燃焼器で燃料油とともに燃焼さ
れる。燃焼器としては、例えばボイラが備えるバーナが
好適である。すなわち本発明によれば、例えばホテルや
旅館等の厨房で排出される食用油の廃油を、暖房や給湯
用のボイラで燃焼し処分することが可能となる。しかも
単に廃油の処分が可能になるだけでなく、食用廃油をボ
イラの燃料資源として活用することができ、重油や灯油
等、ボイラの主燃料を節減することも可能となる。さら
に、食用油は硫黄分をほとんど含まないから、ボイラの
排気中に含まれる硫黄酸化物を低減させ、大気汚染の防
止にも寄与できる。
In the edible waste oil mixing / burning apparatus according to the present invention, while the fuel oil is supplied to the combustor by the fuel oil supply means, the edible waste oil is mixed with the fuel oil by the edible waste oil mixing means. The mixed waste oil is burned with the fuel oil in the combustor. As the combustor, for example, a burner included in a boiler is suitable. That is, according to the present invention, for example, waste oil of cooking oil discharged in a kitchen such as a hotel or an inn can be burned and disposed of in a boiler for heating or hot water supply. Moreover, not only is it possible to dispose of waste oil, but it is also possible to utilize edible waste oil as a fuel resource for the boiler, and it is also possible to save the main fuel of the boiler, such as heavy oil and kerosene. Further, since edible oil contains almost no sulfur content, it is possible to reduce the amount of sulfur oxides contained in the exhaust gas of the boiler and contribute to the prevention of air pollution.

【0010】ボイラの種類(構造)は特に限定されず、
例えば炉筒煙管ボイラや水管ボイラその他であって良
い。バーナも同様に、例えば高圧噴霧式のバーナや油圧
噴霧式バーナ、ロータリー式バーナ、低圧噴霧式バー
ナ、内部混合式バーナ等、その種類は特に問わない。ま
たボイラだけでなく、例えば加熱炉や溶融炉、窯業炉等
のいわゆる工業炉にも適用することが可能で、これらが
備える油バーナで食用廃油を混合し燃焼させても構わな
い。また燃料油には、これら燃焼器に使用される重油や
灯油、軽油等の各種の液体燃料が含まれる。尚、燃料油
と食用廃油との混合は、例えば、燃料油と食用廃油とを
別配管によって送油し、バーナ前で合流させてラインブ
レンダを通し混合を行っても良いし、混合用のタンクを
設け、該タンク内で撹拌し混合させるようにしても構わ
ない。
The type (structure) of the boiler is not particularly limited,
For example, it may be a fire tube boiler, a water tube boiler, or the like. Similarly, the burner may be of any type such as a high pressure spray burner, a hydraulic spray burner, a rotary burner, a low pressure spray burner, and an internal mixing burner. Further, not only the boiler but also a so-called industrial furnace such as a heating furnace, a melting furnace, a ceramic furnace, etc. can be applied, and edible waste oil may be mixed and burned by an oil burner provided therein. Further, the fuel oil includes various liquid fuels such as heavy oil, kerosene, and light oil used in these combustors. The fuel oil and the edible waste oil may be mixed, for example, by feeding the fuel oil and the edible waste oil through separate pipes, combining them in front of the burner, and mixing them through a line blender, or a mixing tank. May be provided, and the mixture may be stirred and mixed in the tank.

【0011】食用廃油を貯留する貯留槽は、好ましくは
廃油投入口と廃油排出口との間に、槽底から所定の高さ
寸法で起立する堰壁と、該堰壁の頂上部に立設したスト
レーナとからなる隔壁を設けるとともに、貯留廃油を加
熱する熱配管を配設した構造とする。すなわち、このよ
うな貯留槽によれば、槽内に設けた堰壁が、廃油投入口
から廃油排出口に向け流れる廃油を堰止めて、その頂上
部を乗り越え流下する溢流(オーバーフロー)を形成す
る。そして、この溢流は堰壁の頂上部に立設したストレ
ーナを通過することになるから、廃油中に含まれる固形
の夾雑物がこのストレーナで除去されることとなる。さ
らに、廃油に含まれる水分は槽底に沈澱するが、堰壁が
この沈澱した水分の下流(廃油排出口側)への流下を阻
止するから、廃油から水分を分離することが可能とな
る。
The storage tank for storing the edible waste oil is preferably provided between the waste oil input port and the waste oil discharge port, and a weir wall standing upright at a predetermined height from the bottom of the tank, and standing on the top of the weir wall. And a heat pipe for heating the stored waste oil is provided. That is, according to such a storage tank, the weir wall provided in the tank blocks the waste oil flowing from the waste oil input port to the waste oil discharge port, and forms an overflow (overflow) that flows over the top of the waste oil and flows down. To do. Then, since this overflow passes through a strainer standing on the top of the weir wall, solid impurities contained in the waste oil are removed by this strainer. Further, the water contained in the waste oil precipitates on the bottom of the tank, but the weir wall prevents the precipitated water from flowing down (to the waste oil discharge port side), so that the water can be separated from the waste oil.

【0012】さらに本貯留槽では、冬期間や寒冷地にお
ける使用であっても、熱配管に熱媒を貫流させることに
より貯留廃油を加熱して廃油の粘度を低下させることが
出来るから、水分や夾雑物の濾過沈澱を容易にすること
が可能である。尚、廃油の温度が低下しない夏期等にお
いては、該熱配管による加熱を省いて構わない。
Further, in the present storage tank, even when used in winter or in cold regions, it is possible to heat the stored waste oil and reduce the viscosity of the waste oil by flowing the heat medium through the heat pipes, so that it is possible to reduce moisture and water content. It is possible to facilitate the filtration precipitation of contaminants. It should be noted that heating in the heat pipe may be omitted in the summer or the like when the temperature of the waste oil does not decrease.

【0013】[0013]

【実施例】以下、添付図面に基づいて本発明の実施例を
説明する。図1は本発明に係る食用廃油混焼装置の一例
を示す図である。図示のようにこの混焼装置11は、サ
ービスタンクからバーナ14(ボイラ)に対し重油を供
給する重油供給系統12と、食用廃油を貯留する廃油貯
留タンク21から食用廃油を供給する廃油供給系統13
とを備えており、これらの給油系統12,13をストレ
ーナ20の前で合流させることにより燃料油と食用廃油
との混合を行う。燃料油および食用廃油の移送は、各系
統に設けた可変式定流量ポンプ15および定流量ポンプ
16により行い、また各配管経路には、油量計や電磁弁
18,19を適宜設けてある。さらに廃油貯留タンク2
1には、貯留廃油の加熱を行う蒸気ドレイン22、およ
び油量が一定量以上となった場合に警報を行うランプ2
3を設けてある。廃油貯留タンク21の構造については
後述する。
Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is a view showing an example of an edible waste oil mixing and burning apparatus according to the present invention. As shown in the figure, this co-firing device 11 includes a heavy oil supply system 12 that supplies heavy oil from a service tank to a burner 14 (boiler), and a waste oil supply system 13 that supplies edible waste oil from a waste oil storage tank 21 that stores edible waste oil.
The fuel oil and the edible waste oil are mixed by merging these refueling systems 12 and 13 in front of the strainer 20. The transfer of the fuel oil and the edible waste oil is performed by the variable constant flow pump 15 and the constant flow pump 16 provided in each system, and an oil meter and solenoid valves 18 and 19 are appropriately provided in each piping path. Waste oil storage tank 2
1, a steam drain 22 for heating the stored waste oil, and a lamp 2 for issuing an alarm when the amount of oil exceeds a certain amount.
3 is provided. The structure of the waste oil storage tank 21 will be described later.

【0014】またこの装置は、廃油タンク21からヘッ
ダ17を介して複数(例えば3機)のボイラに対し食用
廃油を供給することが出来るように構成してある。尚、
この場合、各ボイラに対する重油の供給系に同様に食用
廃油を供給する。また本装置では、電磁弁18を閉止し
廃油供給系統13を遮断することにより、重油(燃料
油)のみによる運転を行うことも可能である。また、可
変式定流量ポンプ15による食用廃油の送油流量を変え
れば、燃料油と廃油との混合割合を変更することが出来
る。尚、例えばボイラの負荷が小さい夏期等において、
ボイラ(バーナ14)への重油の供給量を減少させるに
は、定流量ポンプ16による供給重油の一部を帰還系2
4を通じてサービスタンクに返送すれば良い。
Further, this apparatus is constructed so that the edible waste oil can be supplied from the waste oil tank 21 through the header 17 to a plurality of (for example, three) boilers. still,
In this case, edible waste oil is similarly supplied to the heavy oil supply system for each boiler. Further, in this device, it is also possible to operate only with heavy oil (fuel oil) by closing the solenoid valve 18 and shutting off the waste oil supply system 13. Further, by changing the oil supply flow rate of the edible waste oil by the variable constant flow pump 15, the mixing ratio of the fuel oil and the waste oil can be changed. In addition, for example, in the summer when the load on the boiler is small,
In order to reduce the amount of heavy oil supplied to the boiler (burner 14), part of the heavy oil supplied by the constant flow pump 16 is returned to the feedback system 2.
You can return it to the service tank through No. 4.

【0015】図2乃至図4はそれぞれ廃油貯留タンクの
構造を示す正面断面図、平面図および側面図である。廃
油タンク21は、廃油の投入を行う廃油投入口25と廃
油を送出する廃油排出口26とを備え、投入口25と排
出口26との間に、3段の隔壁27,28,29を設け
てある。これらの隔壁は、槽底から所定の高さ寸法で起
立する堰壁30,31,32と、該堰壁の頂上部に立設
したストレーナ33〜38とからなる。堰壁30〜32
は、投入口側から排出口側へ向け廃油の流れをスムーズ
にし、また投入口側ほど沈澱分離される水分や夾雑物が
多いことを考慮し、上流側(投入口側)ほど高くしてあ
る。また、ストレーナ33〜38は下流(排出口側)に
向かうほど網目の細かいものを設置してあり、第一段ス
トレーナ33,34は例えば60メッシュ、第二段スト
レーナ35,36は例えば100メッシュ、第三段スト
レーナ37,38は例えば150(または120)メッ
シュとする。尚、これらのストレーナ33〜38は、い
ずれも図5に示すように上端部に把手39を備え、タン
クに対し装脱自在に設置してある。
2 to 4 are a front sectional view, a plan view and a side view showing the structure of the waste oil storage tank, respectively. The waste oil tank 21 includes a waste oil input port 25 for inputting waste oil and a waste oil discharge port 26 for sending out the waste oil, and three partition walls 27, 28, 29 are provided between the input port 25 and the discharge port 26. There is. These partition walls are composed of weir walls 30, 31, 32 standing upright from the bottom of the tank at a predetermined height, and strainers 33 to 38 standing on the top of the weir walls. Weir walls 30-32
Is made higher on the upstream side (input port side) in consideration of smoothing the flow of waste oil from the input port side to the discharge port side, and considering that the input port side has more water and impurities that precipitate and separate. . Further, the strainers 33 to 38 are installed such that the meshes are finer toward the downstream side (exhaust port side), the first stage strainers 33 and 34 are, for example, 60 mesh, the second stage strainers 35 and 36 are, for example, 100 mesh, The third-stage strainers 37 and 38 are, for example, 150 (or 120) mesh. It should be noted that each of these strainers 33 to 38 has a handle 39 at the upper end as shown in FIG. 5, and is installed detachably from the tank.

【0016】また、隔壁27〜29によって区切られた
各貯留室の底部(槽底)には、沈澱した水分や夾雑物を
排出するドレイン40を設けてある。またタンク21
は、底面に設けたキャスタ41により移動が可能であ
る。さらに図6に示すように、タンク21内には、貯留
廃油を加熱する熱配管22を、隔壁27〜29に沿って
蛇行させ配設してある。この熱配管22には、例えば蒸
気ドレインや厨房排気、ボイラ排気等の高温蒸気を熱媒
として貫流させる。尚、熱配管22の槽底からの配設高
さは、図2に示すように下流側(排出口側)ほど低く
し、各貯留室を通過する配管部の各々が、下流側の堰壁
以下の高さとなるようにすることが望ましい。廃油の貯
留量が少ない場合にも、各配管部が廃油中に位置するよ
うにして廃油の加熱効率を良好にするためであり、また
該配管が油液面から露出して管表面に付着した廃油が過
度に熱せられて不快臭を発するのを防止するためであ
る。尚、この実施例では、下流側堰壁上面と当該配管部
上面とが略同一高さとなるように配設した。
A drain 40 is provided at the bottom (tank bottom) of each of the storage chambers divided by the partitions 27 to 29 to discharge the precipitated water and foreign substances. Also the tank 21
Can be moved by the casters 41 provided on the bottom surface. Further, as shown in FIG. 6, a heat pipe 22 for heating the stored waste oil is arranged in the tank 21 in a meandering manner along the partition walls 27 to 29. High-temperature steam, such as steam drain, kitchen exhaust, and boiler exhaust, flows through the heat pipe 22 as a heat medium. As shown in FIG. 2, the height of the heat pipe 22 from the bottom of the tank is lowered toward the downstream side (exhaust port side), and each of the pipe portions passing through the respective storage chambers has a downstream weir wall. It is desirable that the height be as follows. Even if the amount of waste oil stored is small, this is because each pipe part is located in the waste oil to improve the heating efficiency of the waste oil, and the pipe is exposed from the oil liquid surface and adheres to the pipe surface. This is to prevent the waste oil from being overheated and generating an unpleasant odor. In this embodiment, the upper surface of the downstream weir wall and the upper surface of the piping portion are arranged at substantially the same height.

【0017】図7は廃油投入口を拡大して示す図であ
る。図示のように廃油投入口25は、開閉自在な蓋体4
2を備え、さらにパイプ格子43の下方に、廃油に混入
している比較的大きな夾雑物を投入段階で取り除くため
の二枚のフィルタ板44,45を有している。フィルタ
板44,45の網目は上段より下段を細かくしてあり、
上部フィルタ44は例えば30メッシュ、下部フィルタ
45は例えば60メッシュとする。尚、図8および図9
にパイプ格子43およびフィルタ板44(45)の一例
を示す。
FIG. 7 is an enlarged view of the waste oil input port. As shown, the waste oil input port 25 is provided with a lid 4 that can be opened and closed.
2, and further below the pipe grid 43, there are two filter plates 44 and 45 for removing relatively large contaminants mixed in the waste oil at the charging stage. The mesh of the filter plates 44 and 45 is made finer in the lower stage than in the upper stage.
The upper filter 44 is, for example, 30 mesh, and the lower filter 45 is, for example, 60 mesh. 8 and 9
An example of the pipe grating 43 and the filter plate 44 (45) is shown in FIG.

【0018】本貯留槽21によれば、槽内に多段に設け
た堰壁30〜32が、廃油投入口25から投入された廃
油を堰止め、その頂上部を乗り越え流下する溢流(オー
バーフロー)を形成するすることが出来る。そして、こ
の溢流は各堰壁の頂上部に立設したストレーナ33〜3
8を通過することになるから、廃油中に含まれる固形の
夾雑物はこれらのストレーナで捕捉され除去される。さ
らに廃油に含まれる水分は槽底に沈澱するが、堰壁30
〜32がこの沈澱した水分の廃油排出口側への流下を阻
止し、水分の分離除去を行う。尚、分離促進のために、
タンク内の廃油に対して水分分離剤(脱水剤)を適宜添
加しても構わない。
According to the present storage tank 21, the weir walls 30 to 32, which are provided in multiple stages in the tank, block the waste oil introduced from the waste oil inlet 25, and overflow the overflow (overflow) which flows over the top of the weir. Can be formed. And this overflow is a strainer 33-3 standing upright on the top of each weir wall.
Since it passes through No. 8, solid contaminants contained in the waste oil are captured and removed by these strainers. Further, the water contained in the waste oil settles at the bottom of the tank, but the weir wall 30
.About.32 prevent the precipitated water from flowing down to the waste oil discharge port side to separate and remove the water. In order to promote separation,
A water separating agent (dehydrating agent) may be appropriately added to the waste oil in the tank.

【0019】本装置によれば、例えばホテルや旅館等の
宿泊施設において、厨房から排出される食用廃油を暖房
用や給湯用のボイラで燃焼し、処分することが可能とな
る。しかも単に廃油の処分が可能になるだけでなく、食
用廃油をボイラの燃料資源として活用することができ、
重油や灯油等、ボイラの主燃料を節減することも出来
る。さらに、食用油は硫黄分をほとんど含まない(未使
用のものは全く含まず、使用済みの廃油でも0.01%
程度である)から、ボイラの排気中に含まれる硫黄酸化
物を低減させ、大気汚染の防止にも寄与できる。また、
本発明が提案する廃油貯留槽によれば、小さなスペース
で効率よく食用廃油の浄化を行うことが出来る。
According to this apparatus, for example, in an accommodation facility such as a hotel or an inn, edible waste oil discharged from the kitchen can be burned by a boiler for heating or hot water and disposed of. Moreover, not only is it possible to dispose of waste oil, but it is possible to utilize edible waste oil as a fuel resource for boilers,
It is also possible to save boiler main fuel such as heavy oil and kerosene. Furthermore, edible oil contains almost no sulfur (unused oil is not included, and used waste oil is 0.01%).
Therefore, it is possible to reduce sulfur oxides contained in the exhaust gas of the boiler and to contribute to the prevention of air pollution. Also,
According to the waste oil storage tank proposed by the present invention, edible waste oil can be efficiently purified in a small space.

【0020】尚、本発明は前記実施例に限定されるもの
ではない。例えば、実施例では廃油投入口と排出口との
間に3段の堰壁と6枚のストレーナを設けたが、堰壁の
数は1段あるいは2段であっても良いし、4段以上であ
っても構わない。同様にストレーナの数も例えば1枚乃
至5枚であっても良いし、7枚以上であっても構わな
い。尚、好ましくは前記実施例のように、各隔壁につい
て複数枚ずつ(実施例では2枚ずつ)のストレーナを設
置する。ストレーナを取り外す場合(例えばストレーナ
の清掃時)に、ストレーナを隔てて各貯留室内に貯留さ
れている廃油同士が混合してしまうのを防止するためで
ある。
The present invention is not limited to the above embodiment. For example, in the embodiment, three weir walls and six strainers are provided between the waste oil input port and the discharge port, but the number of weir walls may be one stage or two stages, or four or more stages. It doesn't matter. Similarly, the number of strainers may be, for example, 1 to 5, or 7 or more. In addition, preferably, a plurality of strainers (two in the embodiment) are installed for each partition wall as in the above embodiment. This is to prevent the waste oils stored in the respective storage chambers across the strainer from being mixed with each other when the strainer is removed (for example, when cleaning the strainer).

【0021】また、重油と食用廃油の混合比は特に限定
されないが、例えばA重油(JIS1種重油)70%に
対して食用廃油を30%混合することが出来る。尚、こ
の混合比によれば、重油のJIS規格項目(反応、引火
点、粘度、流動点、硫黄分、残留炭素分、灰分および水
分)にも適合する。勿論この混合比は一例として示した
ものであって、適宜変更することが可能である。また、
燃料油として、B重油(2種重油)やC重油(3種重
油)、灯油や軽油を混合したいわゆる混合重油等を使用
しても構わない。
The mixing ratio of the heavy oil and the edible waste oil is not particularly limited. For example, 30% of the edible waste oil can be mixed with 70% of the A heavy oil (JIS type 1 heavy oil). According to this mixing ratio, it also complies with JIS standard items (reaction, flash point, viscosity, pour point, sulfur content, residual carbon content, ash content and water content) of heavy oil. Of course, this mixing ratio is shown as an example, and can be appropriately changed. Also,
As the fuel oil, B heavy oil (type 2 heavy oil), C heavy oil (type 3 heavy oil), so-called mixed heavy oil in which kerosene or light oil is mixed may be used.

【0022】さらに、本発明をボイラに使用する場合、
バーナとしては、例えばパイロット着火装置を備えたロ
ータリー式バーナを使用することが出来る。また、高圧
空気噴霧式のバーナや蒸気噴霧バーナ、油圧噴霧式バー
ナ、低圧噴霧式バーナ、内部混合式バーナ等を使用して
も構わない。また点火装置も、例えばダイレクト点火方
式による電気点火装置やその他の方式のものであっても
構わない。また、ボイラの構造も、例えば炉筒煙管ボイ
ラや水管ボイラ等、特に限定されない。さらに本発明は
ボイラのほか、例えば加熱炉や溶融炉、窯業炉等のいわ
ゆる工業炉やその他の油燃焼装置にも適用することが可
能で、これらの燃焼装置で食用廃油を混焼させることが
出来る。
Further, when the present invention is used in a boiler,
As the burner, for example, a rotary burner equipped with a pilot ignition device can be used. Further, a high-pressure air spray burner, a steam spray burner, a hydraulic spray burner, a low-pressure spray burner, an internal mixing burner, or the like may be used. Also, the ignition device may be, for example, an electric ignition device of a direct ignition type or another type. Further, the structure of the boiler is not particularly limited, for example, a tube smoke tube boiler or a water tube boiler. Furthermore, the present invention can be applied to so-called industrial furnaces such as heating furnaces, melting furnaces, and kilns, and other oil combustion devices in addition to boilers, and edible waste oil can be co-firing with these combustion devices. .

【0023】[0023]

【発明の効果】以上説明したように本発明に係る食用廃
油混焼装置によれば、食用廃油を処分することが出来る
と同時にボイラ等の燃料資源として有効に再利用するこ
とが可能となる。
As described above, according to the edible waste oil mixed burning apparatus according to the present invention, the edible waste oil can be disposed of, and at the same time, it can be effectively reused as a fuel resource such as a boiler.

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

【図1】本発明に係る食用廃油混焼装置の一例を示す図
である。
FIG. 1 is a diagram showing an example of an edible waste oil mixing and burning apparatus according to the present invention.

【図2】前記食用廃油混焼装置が備える廃油貯留タンク
の一例を示す正面断面図である。
FIG. 2 is a front cross-sectional view showing an example of a waste oil storage tank provided in the edible waste oil mixed combustion apparatus.

【図3】前記廃油貯留タンクの平面図である。FIG. 3 is a plan view of the waste oil storage tank.

【図4】前記廃油貯留タンクの側面図である。FIG. 4 is a side view of the waste oil storage tank.

【図5】前記廃油貯留タンクに設置するストレーナの一
例を示す図である。
FIG. 5 is a diagram showing an example of a strainer installed in the waste oil storage tank.

【図6】前記廃油貯留タンクに設置する熱配管の一例を
示す平面図である。
FIG. 6 is a plan view showing an example of a heat pipe installed in the waste oil storage tank.

【図7】前記廃油貯留タンクの廃油投入口を示す図であ
る。
FIG. 7 is a view showing a waste oil input port of the waste oil storage tank.

【図8】廃油投入口に設置するパイプを示す平面図であ
る。
FIG. 8 is a plan view showing a pipe installed at a waste oil input port.

【図9】同じく廃油投入口に設置するフィルタを示す平
面図である。
FIG. 9 is a plan view showing a filter similarly installed in the waste oil input port.

【図10】従来の廃油燃焼装置の一例を示す図である。FIG. 10 is a diagram showing an example of a conventional waste oil combustion device.

【符号の説明】[Explanation of symbols]

11 混焼装置 12 重油供給系統 13 廃油供給系統 14 バーナ(ボイラ) 15,16 可変式定流量ポンプ 17 廃油ヘッダ 18,19 電磁弁 20 ストレーナ 21 廃油貯留タンク 22 熱配管 23 警報ランプ 24 重油帰還系 25 廃油投入口 26 廃油排出口 27,28,29 隔壁 30,31,32 堰壁 33〜38 ストレーナ 39 把手 40 ドレイン 41 キャスタ 42 蓋体 43 パイプ格子 44,45 フィルタ板 11 Mixed Burning Device 12 Heavy Oil Supply System 13 Waste Oil Supply System 14 Burner (Boiler) 15, 16 Variable Constant Flow Pump 17 Waste Oil Header 18, 19 Solenoid Valve 20 Strainer 21 Waste Oil Storage Tank 22 Heat Piping 23 Warning Lamp 24 Heavy Oil Return System 25 Waste Oil Input port 26 Waste oil discharge port 27, 28, 29 Partition wall 30, 31, 32 Weir wall 33-38 Strainer 39 Handle 40 Drain 41 Castor 42 Lid 43 Pipe lattice 44, 45 Filter plate

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 燃料油をノズルから噴射し燃焼させる燃
焼器と、 該燃焼器に対して燃料油を供給する燃料油供給手段と、 使用済みの食用廃油を貯留する貯留槽と、 該貯留槽内の食用廃油を前記燃料油に対して適宜量混合
する食用廃油混合手段とを備えたことを特徴とする食用
廃油混焼装置。
1. A combustor for injecting and burning fuel oil from a nozzle, a fuel oil supply means for supplying fuel oil to the combustor, a storage tank for storing used edible waste oil, and the storage tank. And an edible waste oil mixing means for mixing an appropriate amount of edible waste oil therein to the fuel oil.
【請求項2】 前記貯留槽は、 食用廃油を投入する廃油投入口と、 食用廃油を排出する廃油排出口とを備え、 該廃油投入口と廃油排出口との間に、槽底から所定の高
さ寸法で起立する堰壁および該堰壁の頂上部に立設した
ストレーナからなる隔壁を設け、 さらに熱媒の貫流により貯留廃油を加熱する熱配管を配
設したものであることを特徴とする請求項1に記載の食
用廃油混焼装置。
2. The storage tank is provided with a waste oil input port for inputting edible waste oil and a waste oil discharge port for discharging edible waste oil, and between the waste oil input port and the waste oil discharge port, a predetermined amount is provided from the bottom of the tank. A partition wall composed of a weir wall standing upright in a height dimension and a strainer standing on the top of the weir wall is provided, and a heat pipe for heating the stored waste oil by the flow of the heat medium is further arranged. The edible waste oil mixed firing apparatus according to claim 1.
JP7059847A 1995-02-22 1995-02-22 Edible waste oil co-firing equipment Expired - Fee Related JP2756927B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP7059847A JP2756927B2 (en) 1995-02-22 1995-02-22 Edible waste oil co-firing equipment
PCT/JP1995/002710 WO1996026394A1 (en) 1995-02-22 1995-12-27 Equipment for burning waste edible oil mixture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7059847A JP2756927B2 (en) 1995-02-22 1995-02-22 Edible waste oil co-firing equipment

Publications (2)

Publication Number Publication Date
JPH08226625A true JPH08226625A (en) 1996-09-03
JP2756927B2 JP2756927B2 (en) 1998-05-25

Family

ID=13125014

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7059847A Expired - Fee Related JP2756927B2 (en) 1995-02-22 1995-02-22 Edible waste oil co-firing equipment

Country Status (2)

Country Link
JP (1) JP2756927B2 (en)
WO (1) WO1996026394A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008051431A (en) * 2006-08-25 2008-03-06 Shinko Plantech Co Ltd Byproduct oil treatment apparatus and byproduct oil treatment method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0560923U (en) * 1992-01-27 1993-08-10 株式会社豊田自動織機製作所 Fuel tank multilayer filter structure
JPH05271672A (en) * 1992-03-25 1993-10-19 Sanai Fujita Apparatus for producing fuel

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56112441U (en) * 1980-01-30 1981-08-31
JPS6232565Y2 (en) * 1980-02-29 1987-08-20
JPH02108711U (en) * 1989-02-16 1990-08-29
JPH07107442B2 (en) * 1991-01-30 1995-11-15 加藤 護 Combustion equipment for animal and vegetable oil and waste oil

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0560923U (en) * 1992-01-27 1993-08-10 株式会社豊田自動織機製作所 Fuel tank multilayer filter structure
JPH05271672A (en) * 1992-03-25 1993-10-19 Sanai Fujita Apparatus for producing fuel

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008051431A (en) * 2006-08-25 2008-03-06 Shinko Plantech Co Ltd Byproduct oil treatment apparatus and byproduct oil treatment method

Also Published As

Publication number Publication date
JP2756927B2 (en) 1998-05-25
WO1996026394A1 (en) 1996-08-29

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